WO2008103450A2 - Three dimensional printing material system and method using plasticizer-assisted sintering - Google Patents
Three dimensional printing material system and method using plasticizer-assisted sintering Download PDFInfo
- Publication number
- WO2008103450A2 WO2008103450A2 PCT/US2008/002362 US2008002362W WO2008103450A2 WO 2008103450 A2 WO2008103450 A2 WO 2008103450A2 US 2008002362 W US2008002362 W US 2008002362W WO 2008103450 A2 WO2008103450 A2 WO 2008103450A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- particulate material
- article
- aqueous
- plasticizer
- kit
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C64/00—Additive manufacturing, i.e. manufacturing of three-dimensional [3D] objects by additive deposition, additive agglomeration or additive layering, e.g. by 3D printing, stereolithography or selective laser sintering
- B29C64/10—Processes of additive manufacturing
- B29C64/165—Processes of additive manufacturing using a combination of solid and fluid materials, e.g. a powder selectively bound by a liquid binder, catalyst, inhibitor or energy absorber
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C64/00—Additive manufacturing, i.e. manufacturing of three-dimensional [3D] objects by additive deposition, additive agglomeration or additive layering, e.g. by 3D printing, stereolithography or selective laser sintering
- B29C64/10—Processes of additive manufacturing
- B29C64/188—Processes of additive manufacturing involving additional operations performed on the added layers, e.g. smoothing, grinding or thickness control
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B33—ADDITIVE MANUFACTURING TECHNOLOGY
- B33Y—ADDITIVE MANUFACTURING, i.e. MANUFACTURING OF THREE-DIMENSIONAL [3-D] OBJECTS BY ADDITIVE DEPOSITION, ADDITIVE AGGLOMERATION OR ADDITIVE LAYERING, e.g. BY 3-D PRINTING, STEREOLITHOGRAPHY OR SELECTIVE LASER SINTERING
- B33Y10/00—Processes of additive manufacturing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B33—ADDITIVE MANUFACTURING TECHNOLOGY
- B33Y—ADDITIVE MANUFACTURING, i.e. MANUFACTURING OF THREE-DIMENSIONAL [3-D] OBJECTS BY ADDITIVE DEPOSITION, ADDITIVE AGGLOMERATION OR ADDITIVE LAYERING, e.g. BY 3-D PRINTING, STEREOLITHOGRAPHY OR SELECTIVE LASER SINTERING
- B33Y70/00—Materials specially adapted for additive manufacturing
- B33Y70/10—Composites of different types of material, e.g. mixtures of ceramics and polymers or mixtures of metals and biomaterials
Definitions
- This invention relates generally to rapid prototyping techniques and, more particularly, to a three-dimensional printing material and method using plasticizer-assisted sintering.
- three dimensional printing can be quicker and less expensive than machining of prototype parts or production of cast or molded parts by conventional "hard” or “soft” tooling techniques, that can take from a few weeks to several months, depending on the complexity of the item.
- An early three dimensional printing technique described in U.S. Patent No.
- the three-dimensional ink-jet printing technique or liquid binder method involves applying a layer of a powdered material to a surface using a counter-roller. After the powdered material is applied to the surface, the ink-jet printhead delivers a liquid binder in a predetermined pattern to the layer of powder. The binder infiltrates into gaps in the powder material and hardens to bond the powder material into a solidified layer. The hardened binder also bonds each layer to the previous layer.
- an adhesive can be suspended in a carrier that evaporates, leaving the hardened adhesive behind.
- the powdered material may be ceramic, metal, plastic or a composite material, and may also include fibers.
- the liquid binder material may be organic or inorganic. Typical organic binder materials used are polymeric resins or ceramic precursors, such as polycarbosilazane. Inorganic binders are used where the binder is incorporated into the final articles; silica is typically used in such an application. [0006] As described in U.S. Patent No. 6.007,318, incorporated herein by reference in its entirety, printed articles may be dipped or painted with a solution that infiltrates the article by capillary actions. This processing may improve handling properties of the article and prevent its decay.
- a strong printed article may be made by three dimensional printing over a substantially dry particulate material build material including an aqueous- insoluble thermoplastic particulate material.
- the printed article is further post-processed by infiltrating a liquid medium into the article.
- the liquid medium selectively plasticizes the aqueous-insoluble thermoplastic particulate material, lowering the thermoplastic's glass transition temperature. This facilitates sintering of the thermoplastic particulate material to bond together the matrix of the article, thereby increasing the article's durability.
- Typical existing printing processes include a post-processing infiltration step to increase the strength of the printed article using two-component casting resins and/or adhesives or one-component cyanoacrylate adhesives to achieve greater durability to a three-dimensional article.
- Articles printed with the particulate material build material described herein and further infiltrated with a liquid plasticizer have strengths comparable to that of articles formed with cyanoacrylate adhesive, e.g., about 20 MPa, which has historically been proven to be sufficient for most concept modeling applications.
- the infiltrant materials used for plasticized sintering may provide some advantages over other build materials.
- Using two-component casting resins such as epoxy-amine, isocyanate-amines, and/or isocyanate-polyol systems decreases the ease-of-use by the end-user by incorporating extra mixing steps, imposing pot-life constraints, and giving rise to safety, health, and environmental issues.
- One-component cyanoacrylate adhesives typically offer better ease-of-use because these materials do not require mixing, but they may create safety, heath, and environment issues such as fumes, irritation, and adhesion to skin and may not be stable when exposed to the open atmosphere for long periods of time.
- the plasticized assisted sintering of a build material consisting of a thermoplastic particulate increases ease of use by offering a method in which the process can be automated or semi-automated whereby the article is immersed in a stable, one component liquid medium for a predetermined amount of time and allowed to cool to a handling temperature.
- Stable refers to maintaining a consistent viscosity at a predetermined temperature when exposed to the open atmosphere for a long period of time, i.e., on the order of months.
- an embodiment of the invention features a powder material system for three dimensional printing including a substantially dry particulate material including an aqueous-insoluble thermoplastic particulate material, plaster, and a water-soluble adhesive.
- the dry particulate material is suitable for use in three dimensional printing to form an article comprising a plurality of layers, the layers including a reaction product of the particulate material and an aqueous fluid that contacts the particulate material during three dimensional printing.
- a static and a dynamic friction coefficient of the particulate material possess a relationship defined by a Bredt parameter having a value in excess of 0.1.
- An internal angle of friction may be selected from a range of 40° and 70°.
- the particulate material may include about 5% - 50% by weight of the aqueous- insoluble thermoplastic, about 25 - 90% by weight of the plaster, and about 5 - 30 % by weight - A -
- the aqueous-insoluble thermoplastic may include or consist essentially of high molecular weight polyethylene, polyamide, poly-cyclic-olefins, and/or combinations thereof.
- the particulate material may further include a processing aid, e.g., the particulate material may include about 0.01 - 2.0 % by weight of the processing aid.
- the processing aid may include or consist essentially of mineral oil, propylene glycol di(caprylate/caprate), petroleum jelly, propylene glycol, di-isobutyl phthalate, di-isononyl phthalate, polyalkyleneoxide modified heptamethyltrisiloxanes, polyalkyleneoxide modified polydimethylsiloxanes, and/or combinations thereof.
- an embodiment of the invention features a kit including a substantially dry particulate material including an aqueous-insoluble thermoplastic particulate material, plaster, and a water-soluble adhesive.
- the kit also includes an aqueous fluid binder and an infiltrant.
- the infiltrant may include 0- 99.99% by weight hydroxylated hydrocarbon, 0-99.99% by weight a solid wax, 0-99.99% by weigh a plasticizer, and 0.01-5% by weight a stabilizer.
- the hydroxylated hydrocarbon may include a hydrocarbon diol with a molecular weight greater than 118 g/mol, a melting point greater than 3O 0 C, and a kinematic viscosity of 150 centiStokes or less, preferably 50 centiStokes or less, at a temperature of at least 5O 0 C.
- the hydrocarbon diol may include or consist essentially of octane diol and/or decane diol.
- the infiltrant may include hydroxylated hydrocarbon that includes (i) a hydrocarbon diol with a molecular weight greater than 1 18 g/mol and a melting point greater than 30 0 C and (ii) a plasticizer.
- the hydroxylated hydrocarbon may include decane diol.
- the plasticizer may include or consist essentially of benzene sulfonamide and/or propylene carbonate.
- the hydroxylated hydrocarbon may include an alcohol with boiling point selected from a range of 25°C to 100 0 C, and the plasticizer may have a boiling point selected from a range of 25°C to 100 0 C.
- the alcohol may include or consist essentially of isopropanol.
- an embodiment of the invention includes a method for forming an article by three dimensional printing.
- the method includes (i) providing a particulate material comprising a plurality of adjacent particles, the particulate material comprising an aqueous-insoluble thermoplastic; (ii) applying to at least some of the plurality of particles an aqueous fluid binder in an amount sufficient to bond those particles together to define the article; and (iii) immersing the article in a liquid infiltrant medium.
- the liquid infiltrant medium may include a hydroxylated hydrocarbon.
- the liquid infiltrant medium may also include a plasticizer.
- the particulate material may further include at least one of plaster, a water-soluble adhesive, a retarder, an accelerator, and a processing aid.
- an embodiment of the invention features an essentially solid article manufactured by a three-dimensional printing process, the essentially solid article comprising a product of a reaction between (i) a substantially dry particulate material including an aqueous- insoluble thermoplastic particulate material, plaster, and a water-soluble adhesive; (ii) an aqueous fluid comprising water, a humectant, a rheology modifier, a surfactant, a preservative, and an optical brightening agent; and (iii) an infiltrant including a hydroxylated hydrocarbon, a wax, a plasticizer, and a stabilizer.
- the aqueous-insoluble thermoplastic particulate material material is plasticized by the infiltrant.
- an article in still another embodiment, includes a product of (i) a substantially dry particulate material including an aqueous-insoluble thermoplastic particulate material, plaster, and a water-soluble adhesive; and (ii) an infiltrant.
- the article preferably has a strength of at least 5 megapascal (MPa), more preferably at least 15 MPa, and most preferably at least 20 MPa.
- Figure 1 is a schematic view of a first layer of a mixture of particulate material of an embodiment of the invention deposited onto a downwardly movable surface of a container on which an article is to be built, before any fluid has been delivered;
- Figure 2 is a schematic view of an ink-jet nozzle delivering a fluid to a portion of the layer of particulate material of Figure 1 in a predetermined pattern
- Figure 3 is a schematic view of a final article of an embodiment of the invention enclosed in the container, the article made by a series of steps illustrated in Figure 2 and still immersed in the loose unactivated particles;
- Figure 4 is a schematic view of the final article of Figure 3;
- Figure 5 is a graph illustrating an estimated solubility range of TROGAMID T-5000;
- Figure 6 is a schematic illustration of a circulating spreader bead
- Figures 7a, 7b, and 8 are graphs illustrating the forces acting on a particle during three dimensional printing
- Figure 9a is a CAD drawing of the article portion printed in Figures 9b and 9c;
- Figures 9b and 9c are laser profilometer images comparing the effect of particulate materials with high internal angle of friction on finished article properties;
- Figure 10a is a CAD drawing of the article portion printed in Figures 10b and 10c; and Figure 10b and 10c are laser profilometer images comparing the effect of particulate material with low internal angle of friction on finished article properties.
- the layer or film of particulate material 20 may be formed in any suitable manner, for example using a counter-roller.
- the particulate material 20 applied to the surface includes an aqueous-insoluble thermoplastic particulate material, plaster, and a water-soluble adhesive.
- the particulate material 20 may also include a filler material, a processing aid material, and/or a fibrous material.
- an ink-jet style nozzle 28 delivers an activating fluid 26, i.e., an aqueous fluid described below, to at least a portion 30 of the layer or film of the particulate mixture 20 in a two-dimensional pattern.
- the fluid 26 is delivered to the layer or film of particulate material 20 in any predetermined two-dimensional pattern (circular, in the figures, for purposes of illustration only), using any convenient mechanism, such as a drop-on-demand (DOD) printhead driven by software in accordance with article model data from a computer-assisted-design (CAD) system.
- DOD drop-on-demand
- CAD computer-assisted-design
- the first portion 30 of the particulate mixture is activated by the fluid 26, causing the activated particles to adhere together to form a conglomerate of the particulate material 20 (powder) and fluid 26.
- the conglomerate defines an essentially solid circular layer that becomes a cross-sectional portion of an intermediate article 38 (see, e.g., Figures 3 and 4).
- activates is meant to define a change in state from essentially inert to adhesive. This definition encompasses the activation of the adhesive particulate material to bond the absorbent filler particulate material.
- a typical droplet of activating fluid has a volume of about 40 picoliters (pi), and spreads to a diameter of about 100 ⁇ m after coming into contact with the particulate mixture.
- pi picoliters
- the fluid viscosity increases dramatically, arresting further migration of the fluid from the initial point of impact.
- the fluid with adhesive dissolved therein infiltrates the less soluble and slightly porous particles, forming adhesive bonds between the absorbent filler particulate material as well as between the additional filler and the fiber.
- the activating fluid is capable of bonding together an amount of the particulate mixture that is several times the mass of a droplet of the fluid.
- the adhesive bonds harden, joining the absorbent filler particulate material and, optionally, additional filler and fiber particulates into a rigid structure, which becomes a cross-sectional portion of the final article 40.
- the layers include a reaction product of the particulate material and the activiating fluid, e.g., an aqueous fluid.
- any unactivated particulate mixture 32 that was not exposed to the fluid remains loose and free-flowing on the movable surface 22.
- the unactivated particulate mixture is typically left in place until formation of the intermediate article 38 is complete. Leaving the unactivated, loose particulate mixture in place ensures that the intermediate article 38 is fully supported during processing, allowing features such as overhangs, undercuts, and cavities to be defined and formed without the need to use supplemental support structures.
- the movable surface 22 is indexed downwardly, in this embodiment, and the process is repeated.
- a second film or layer of the particulate mixture is then applied over the first layer, covering both the rigid first cross- sectional portion, and any proximate loose particulate mixture.
- a second application of fluid follows in the manner described above, dissolving the adhesive and forming adhesive bonds between at least a portion of the previous cross-sectional formed portion, the absorbent filler particulate material, and, optionally, additional filler and fiber of the second layer, and hardening to form a second rigid cross-sectional portion added to the first rigid cross-sectional portion of the final article.
- the movable surface 22 is again indexed downward.
- the previous steps of applying a layer of particulate mixture, including the adhesive, applying the activating fluid, and indexing the movable surface 22 downward are repeated until the intermediate article 38 is completed.
- the intermediate article 38 may be any shape, such as cylindrical. At the end of the process, only a top surface 34 of the intermediate article 38 is visible in the container 24.
- the intermediate article 38 is typically completely immersed in a surrounding bed 36 of unactivated particulate material.
- an article could be formed in layers upward from an immovable platform, by successively depositing, smoothing, and printing a series of such layers.
- the unactivated particulate material may be removed from the intermediate article 38 by pressurized air flow or a vacuum.
- a post-processing treatment may be performed, such as cleaning, infiltration with stabilizing materials, painting, etc. to define a final article 40, having the same shape as intermediate article 38, but with additional desired characteristics, such as a stiffness, strength, and flexibility.
- a particularly suitable infiltration method for the particulate material described herein includes immersing a finished article into a liquid infiltrant medium, i.e., a plasticizer, to increase the strength and toughness of the article. After the article is formed, it may be submerged in a liquid material and then heated to a sintering temperature. Alternatively, it may be submerged into a preheated plasticizer bath, causing in-situ diffusion and sintering. [0033] Preferably the article is completely immersed into the liquid or molten material.
- a liquid infiltrant medium i.e., a plasticizer
- the material may be melted by placing the material in a polypropylene container in an oven, e.g., a Blue M oven or a Cole Palmer StableTemp mechanically convected oven model 52100-00, with the oven temperature being sufficiently high to melt the material.
- the container is preferably sufficiently large for the article to be completely submerged into a liquid disposed therein.
- the material may be melted by exposure to microwaves.
- the article is completely submerged until substantially all of the entrapped air rises to the liquid's surface in the form of air bubbles.
- the resulting essentially solid article may be the product of the reaction of (i) a substantially dry particulate material including an aqueous-insoluble thermoplastic particulate material, plaster, and a water-soluble adhesive; (ii) an aqueous fluid comprising water, a humectant, a rheology modifier, a surfactant, a preservative, and an optical brightening agent; and (iii) an infiltrant comprising a hydroxylated hydrocarbon, a wax, a plasticizer, and a stabilizer, with the aqueous-insoluble thermoplastic particulate material being plasticized by the infiltrant.
- a substantially dry particulate material including an aqueous-insoluble thermoplastic particulate material, plaster, and a water-soluble adhesive
- an aqueous fluid comprising water, a humectant, a rheology modifier, a surfactant, a preservative, and an optical brightening agent
- an infiltrant compris
- An article may be the product of a substantially dry particulate material including an aqueous-insoluble thermoplastic particulate material, plaster, and a water-soluble adhesive, and an infiltrant.
- the article may have a strength of at least 5 MPa, preferably at least 15 MPa, and most preferably at least 20 MPa.
- a particulate material i.e., a substantially dry particulate material, includes or consists essentially of: an aqueous-insoluble thermoplastic particulate material 5 - 50 wt% plaster (calcium hemihydrate) 25 - 90 wt% water-soluble adhesive 5 - 30 wt% retarder 0.01 - 5 wt% accelerator 0.01 - 5 wt% processing aids 0.01 - 2.0 wt% [0037]
- An example of a preferred particulate composition is: an aqueous-insoluble thermoplastic particulate material 15 - 35 wt% plaster (calcium hemihydrate) 50 - 80 wt% water-soluble adhesive 5 - 15 wt% retarder 0.01 - 5 wt% accelerator 0.01 - 3 wt% processing aids 0.01 - 2.0 wt%
- a preferred particle size of components of the particulate material is an average particle diameter of less than 125 microns and greater than 10 microns.
- the aqueous-insoluble thermoplastic particulate material provides extra durability and increased strength when it sinters together after being plasticized by the liquid medium.
- a suitable aqueous-insoluble thermoplastic has a particle size greater than 20 microns and less than 100 microns, and has a glass transition temperature greater than 45°C.
- the aqueous- insoluble thermoplastic particulate material also is soluble and/or permeable with certain nonaqueous solvents, waxes, or hydrocarbon diols that can act as plasticizers.
- aqueous-insoluble thermoplastic particulate material is a polyamide 6-3 and terphthalic acid copolymer, available under the trade name of TROGAMID, such as TROGAMID T5000 from Degussa based in Germany. According to its technical data sheet, TROGAMID T5000 exhibits a resistance to most chemicals; however, it lacks chemical resistance to certain hydroxylated hydrocarbons like ethanol, propylene glycol, and pentanediol.
- TROGAMID T5000 also has decreased chemical resistance against, e.g., methanol, 1-propanol, pentanol, allyl alcohol, aniline, crotonaldehyde, dimethylformamide, and glacial acetic acid.
- TROGAMID T5000's weakness to these types of chemicals makes it possible to use these hydroxylated hydrocarbons as plasticizers with TROGAMID T5000 to reduce its glass transition temperature to a point where it sinters together in the matrix of the three-dimensional article.
- aqueous-insoluble thermoplastic particulate materials are high molecular weight polyethylene like GUR from Ticona USA based in Florence, KY and cyclic polyolefins like TOPAS from TOPAS Advanced Polymers. These particular thermoplastics lack chemical resistance to aliphatic and/or aromatic solvents, and/or paraffin based oils and waxes, rendering these materials suitable for use as plasticizers for these thermoplastic materials. Yet other examples of aqueous-insoluble thermoplastic particulate materials include polyamide and poly-cyclic-olefins.
- the plaster provides dimensional stability and adhesion for strength of an article formed from the particulate material.
- a suitable plaster for use with embodiments of the invention is calcium hemihydrate having a particle size distribution ranging from greater than 20 microns to less than 125 microns.
- An example of such plaster is HYDROCAL, available from USG based in Chicago, IL.
- Another suitable plaster product that is whiter than HYDROCAL is the SSS Brand from San Esu based in Suita, Osaka, Japan. The whiter product imparts a more neutral color to articles than HYDROCAL, which may be desirable for attaining a wider color gamut.
- the water-soluble adhesive provides adhesive strength in the system and helps to control bleed or pooling of fluid binder in selectively printed areas.
- a suitable water-soluble adhesive is a polymer with an average molecular weight from a range of 10,000 to 200,000 g/mol with hydrolysis greater than 85% and less than 90% and a particle size distribution ranging from greater than 5 micron to less than 125 microns.
- a water-soluble adhesive is a polyvinyl alcohol such as CELVOL 203 S available from Celanese from Dallas, TX.
- Another suitable resin is a maltodextrin such as STAR-DRI- 1, available from A.E. Staley based in Decatur, IL. Maltodextrin may be used to improve the stiffness of the article as it is drying and during the post processing with a liquid medium infiltrant.
- a retarder may be included, such as borax.
- borax After an aqueous binder is deposited onto a plaster-containing particulate material, calcium sulfate dihydrate crystals form during gypsum setting. Retarders help decrease the growth rate of calcium sulfate dihydrate crystals, thus reducing a distortion effect known as arching in three dimensional printing. Arching is a distortion defect in which flat bottom surfaces exhibit concavity from successive layers expanding too fast.
- An accelerator may be included, such as potassium sulfate, potassium aluminum sulfate, sodium sulfate, calcium sulfate dihydrate, or aluminum sulfate.
- the accelerator helps increase the precipitation rate of aqueous calcium sulfate into calcium sulfate dihydrate to gain an appreciable early handling strength.
- processing aids include propylene glycol di(caprylate/caprate), petroleum jelly, propylene glycol, di-isobutyl phthalate, di-isononyl phthalate, polyalkyleneoxide modified heptamethyltrisiloxanes, polyalkyleneoxide modified polydimethylsiloxanes, and combinations thereof.
- a fluid binder is an aqueous fluid that includes or consists essentially of: water 70 - 90 wt% humectant l - 10 wt% preservative 0.05 - 5 wt% surfactant 0 - 2 wt% optical brightening agent 0 - 5 wt%
- humectants examples include Glycerol and other diols from 3 - 10 carbons long; many other examples of humectants are known in the art. Printing may be successful with humectant levels from 1 - 20%, depending on the binder formulation.
- Surfactants are typically used to control the surface tension of the aqueous fluid. Proper surface tension helps ensure that the droplets being ejected from a print head are formed with a consistent volume, depart from the print head at the appropriate vector, and do not form satellite drops. Very high surface tension may create poor wetting when the binder impacts loose powder. Low surface tension may create poor droplet formation at the face of the print head. Surface tensions of suitable binders for use with an HP 11 print head (from Hewlett- Packard) range from 30 dynes/cm to 36 dynes/cm.
- a liquid infiltrant includes or consists essentially of: a hydroxylated hydrocarbon 0 - 99.99 wt% a wax (solid at room temperature) 0 - 99.99 wt% a plasticizer 0 - 99.99 wt% stabilizer 0.01 - 5 wt%
- the liquid infiltrant may include or consist essentially of: a hydroxylated hydrocarbon (solid at room temperature) 69.99 - 99.99 wt% a plasticizer 0 - 30 wt% stabilizer 0.01 - 5 wt%
- a liquid infiltrant may include or consists essentially of: a paraffin wax (solid at room temperature) 79.99 - 99.99 wt% a plasticizer 0 - 20 wt% stabilizer 0.01 - 5 wt%
- the hydroxylated hydrocarbon may be the primary plasticizer that reduces the glass transition temperature of the aqueous-insoluble thermoplastic particulate material.
- the hydroxylated hydrocarbon may also be the carrier of a secondary plasticizer that is soluble in the hydroxylated hydrocarbon and more effective in plasticizing the aqueous-insoluble thermoplastic, and where the hydroxylated hydrocarbon is less effective in plasticizing the aqueous-insoluble thermoplastic.
- Suitable hydroxylated hydrocarbons are ethanol, pentane- diol, octane-diol, and decanediol.
- Ethanol having a boiling point below 100°C, is a suitable fugitive plasticizer for the TROGAMID T5000; ethanol evaporates away from the printed article after infiltrating the article, with the TROGAMID T5000 sintering together within the matrix of the article. Ethanol may be too effective in plasticizing TROGAMID T5000 to an extent that an article may distort and collapse under its own weight. The plasticizing effect of ethanol may be reduced by adding another miscible hydroxylated hydrocarbon having a boiling point less than 100°C such as isopropanol.
- Isopropanol does not exhibit the same plasticizing effect on TROGAMID T5000, and is fugitive as well having a boiling point well below 100 0 C.
- the addition of isopropanol to ethanol may decrease the hydrogen bonding forces of the ethanol, thereby possibly decreasing the plasticization effect of the alcohol mixture on TROGAMID T5000.
- the use of hydroxy lated hydrocarbons with boiling points less than 100 0 C may raise concerns of flammability and end-user safety.
- Octane diol and decane diols are generally more preferred hydroxylated hydrocarbons because they have higher flashpoints than ethanol, and are solid at room temperature and are liquid with a kinematic viscosity of 150 centiStokes or less, more preferably 50 centiStokes or less at temperatures greater than 50°C.
- a solid wax having a melting point greater than 30°C may be the primary plasticizer to reduce the glass transition temperature (T g ) of the aqueous-insoluble thermoplastic, or may be the carrier of a secondary plasticr that is soluble in the solid wax when in a melted, liquid state at temperatures above 50 0 C if the solid wax is not effective in lowering the T g of the aqueous-insoluble thermoplastic alone.
- Suitable waxes that plasticize TROGAMID T5000 are hydrocarbon diols with molecular weights greater than 118 g/mol, such as octane diol and decane diol.
- paraffin wax such as Paraplast X-Tra available from McCormick Scientific based in St. Louis, MO, which is suitable for plasticizing both polyethylene thermoplastics like GUR and cyclic-poly-olef ⁇ ns like TOPAS.
- the wax may have a kinematic viscosity of 150 centiStokes or less, preferably 50 centiStokes or less, to ensure a fast infiltration rate and deep penetration into an immersed article; and to facilitate easier drainage and removal of excess liquid infiltrant from the article when the article is extracted from the liquid infiltrant, thereby reducing pooling and drip defects on the article as the wax solidifies.
- the plasticizer may be the sole ingredient or an additive in either a hydroxylated hydrocarbon and/or a solid wax to enhance the plasticization of the aqueous-insoluble thermoplastic particulate material.
- the plasticizer may be the sole ingredient that is in a liquid state when infiltrating a three dimensional article.
- Suitable sole plasticizers are, for example, ethanol, octane diol, and decane diol for reducing the T g of TROGAMID T5000.
- Paraffin waxes and mineral oil may also be suitable as sole plasticizers for polyethene and poly-cyclic poly olefins such as GUR and TOPAS respectively.
- Stabilizers may be added to the liquid infiltrant medium to decrease oxidation that may lead to the discoloration of the liquid infiltrant medium when kept at temperatures above 50°C for prolonged periods of time.
- Suitable stabilizers are antioxidants such as butylated hydroxytoluene.
- a summary of a printing/infiltration process is as follows: a) a layer is formed of a substantially dry particulate material containing thermoplastic particulate, a plaster, and/or a water-soluble polymer such as a water-soluble adhesive; b) an aqueous fluid binder is applied to the layer of dry particulate material in a predetermined pattern to cause binding in the areas to which the binder is applied; c) steps (a) and (b) are repeated sequentially to define a three-dimensional article; d) after complete setting of the thermoplastic, plaster, or water-soluble polymer, the three-dimensional article is removed from the build, i.e., from the stack of dry particulate material layers; e) the three-dimensional article is submerged in the plasticizer or its solution, i.e., the liquid infiltrant medium, at ambient or elevated temperature; and f) optionally, the particulate material is exposed to additional energy in the form of conventional heat, visible or infrared light, microwave, or radio
- articles are submerged into a liquid infiltrant medium and heated to the sintering temperature.
- articles may be submerged in a preheated plasticizer bath causing in-situ diffusion and sintering. The sintering may be performed without application of additional pressure, i.e., the sintering may be substantially pressure-free.
- the plasticizer may be a component of the particulate composition.
- the article may be placed in a heated chamber filled with plasticizer in the gaseous phase.
- the particulate composition may include an inert absorbent filler is saturated with plasticizer.
- plasticizer migrates into the polymer matrix during heat treatment.
- the plasticizer may be applied as a pure substance, solution or emulsion. It may also contain solvents, surfactants, viscosity modifiers, dyes, and/or pigments.
- the plasticizer may be liquid or solid at room temperature. Solid plasticizer may be applied to the particulate composition in the molten form. Use of plasticizers with high melting point typically diminishes or prevents their migration during the lifetime of an article. Liquid plasticizer may be dissolved in a high melt temperature inert solid carrier, creating material that is solid at room temperature.
- One of the advantages of the processes described herein is that one may produce both rigid and rubbery articles from the same particulate composition by employing a different plasticizer system or a system that contains different concentrations of the same plasticizers.
- uniformly colored articles may be produced by dissolving dyes in the liquid or solid plasticizer systems.
- Solubility of the plasticizer in the polymer matrix of the article is determined by the polymer system, and depends on three major parameters. These parameters are: interaction between plasticizer molecules; the molecular interaction between the polymer molecules; and the mutual interaction of the polymer molecules when mixed.
- Hansen solubility parameters allow for accurate estimation of solubility and swelling of the polymers in solvents, or in this case plasticizers.
- the Hansen solubility parameters represent the following intermolecular forces, the so-called Van der Waals forces: dispersion forces ( ⁇ d ), dipole - dipole interactions ( ⁇ p ) and hydrogen bonding forces ( ⁇ h ). The total
- plasticizer material may be preferably selected from materials that have low solubility at room temperature but greater solubility at higher temperatures.
- the plasticizer may be diluted either by the solvent that is removed after sintering or inert solid material that may remain in the three dimensional article after cooling.
- any solvent within a radius of 5 (MPa) 1/2 of a polymer's solubility parameter location on the ⁇ h vs ( ⁇ d 2 + ⁇ p 2 ) 1/2 plot is to be considered a solvent that will interact with the polymer, and any solvent outside that radius typically does not have any effect.
- the solubility parameters for TROGAMID T5000 in this example may also be estimated from the Hoy contribution method.
- solvents that have no effect lie at or beyond the radius of interaction (indicated by a large oval), while solvents that affect the polymer (represented by o and ⁇ , as well as octanediol and decanediol) fall within the radius with some extending upwards outside the radius as the hydrogen bonding forces increase. This suggests that solvents with high hydrogen bonding forces are more significant in polymer-solvent interaction for this particular example.
- hydroxylated hydrocarbons of interest i.e., decanediol and octanediol
- decanediol and octanediol are plotted using the Hoy contribution method, one can see that they fall within the radius of interaction of TROGAMID T5000, and may, therefore, impart the desired plasticizing effect.
- Flexural strength test bars 50 mm long, 5 mm wide, and 5.7 mm tall were printed on Z310 using zb58 binder with a-binder-to-volume ratio of 0.10. The test bars were dried for 2 hours at 38 0 C in an oven. Sequentially, test bars were infiltrated by dipping them in different alcohols (solvents) for 15 seconds at room temperature, removing them from the solvents, and placing them in an oven (Cole Palmer StableTemp mechanically convected oven model 52100-00) preheated to 75 0 C for 3 hours. After the test bars were cooled at ambient conditions for 1 hour, they were placed and supported on a 2-point span spaced at 40 mm.
- solvents solvents
- Powdered material was prepared according to the procedure described in Example 1 , using the materials and ratios shown below in Table 4.
- Flexural strength test bars describe in Example 1 were printed on Z310 particulate material using zb58 binder with a binder to volume ratio of 0.25. Parts were dried for 2 hours at 38 0 C in an oven. Sequentially, parts were infiltrated by dipping them in different liquids for 15 seconds at room temperature. Then parts were removed from the solvent and placed in a microwave oven (Sharp Carousel model R2A57 700W). Parts were micro waved for 5 minutes at "High" settings. After parts cooled at ambient conditions for 1 hour, the flexural strengths were acquired as described in Example 1, and are reported in Table 5.
- Example 3 Powdered material was prepared according to the procedure described in the Example 1 using the materials and ratios shown below in Table 6.
- Flexural strength test bars described in Example 1 were printed on Z310 particulate material using zb58 binder with a binder to volume ratio of 0.23. Parts were dried for 2 hours at 38 0 C in an oven. Parts were completely dipped in the heated bath containing molten materials for 10 seconds, removed from the molten material and placed in the oven. The flexural strength results are indicated in Table 7.
- a powdered material may be prepared according to the procedure described in the
- Example 1 using the materials and ratios shown below in Table 8.
- Articles may be created from the particulate material formulation listed in Table 8 using zb58 aqueous fluid binder with a Z310 printer. The article may then be removed from the Z310 printer 2 hours after printing has been completed and the article placed in a mechanical convection oven set between 75°C to 100°C for 0.5 to 2 hours to melt the hydrocarbon diol within the article, to plasticize the plastic and facilitate sintering.
- a preferred kit includes a powder adapted for three dimensional printing, an aqueous fluid for activating water soluble components of the three-dimensional printing powder, and an inf ⁇ ltrant suitable for plasticizing an aqueous-insoluble thermoplastic component of the particulate material.
- the powder may include a loose, dry, and substantially free-flowing particulate mixture including an aqueous-insoluble thermoplastic particulate material, plaster (calcium hemihydrate), water-soluble adhesive, and, optionally, a retarder, accelerator, and/or processing aids.
- the aqueous fluid binder may include water, a humectant, a preservative, and, optionally, a surfactant, and/or an optical brightening agent.
- the infiltrant may include a hydroxylated hydrocarbon, a solid wax, a plasticizer, and a stabilizer.
- the particulate material is adapted for use in three dimensional printing to form an article comprising a plurality of layers, the layers including a reaction product of the particulate material and the aqueous fluid that contacts the particulate material during three dimensional printing.
- the aqueous fluid may be substantially clear, have a viscosity selected from a range of 1-1.35 cps, a surface tension selected from a range of 30-36 dynes/cm, and a pH selected from a range 4.9 to 10.3.
- the infiltrant may be adapted to plasticize the aqueous-insoluble thermoplastic particulate material by lowering the glass transition temperature of the aqueous- insoluble thermoplastic particulate to allow the sintering of those particulates.
- the kit may also include a combination of aqueous fluids comprising cyan, magenta, and yellow colorants.
- the aqueous binder may be selected such that it is capable of hydrating the plaster (calcium hemihydrate) and initiating the precipitation into a gypsum cement.
- the binder is applied onto the substantially dry particulate material so as to occupy from 10% to 35% of the volume defined by the selectively printed area at a predetermined layer thickness, typically 100 microns.
- the printed area is then allowed to set to attain a flexural strength of at least 1 MPa, for example after 2 hours from the time the last layer was printed.
- An infiltrant that is selected to plasticize the aqueous-insoluble thermoplastic particulate material is preferably clear and translucent to allow the natural lightness and color of the powder to show through.
- compositions have been disclosed above that relate to the control of the flow properties of the build material in three-dimensional printers.
- the three principle methods flow property control are the addition of liquid "processing aids," control of grain size distribution, and the addition of solid fillers that contribute to the frictional behavior of the build material.
- Many candidate materials have been disclosed previously, for example, in U.S. Patent Publication Number 2005/0003189, incorporated herein by reference in its entirety. Previously, however, the exact implementation of these methods has been by trial and error.
- some mechanical properties of dry particulate build materials are disclosed that are particularly suited for use in three dimensional printing, especially in contrast to other formulations of similar materials for other uses that may not require special flow characteristics of the raw materials.
- dry, free- flowing particulate build material is spread by a rotating spreader rod 500.
- the rod rotates in a direction counter to the direction of motion of the spreading mechanism.
- a circulating bead 510 of build material 32 is pushed in front of a moving rod over a stationary bed.
- the system is shown in the frame of the rod with a moving bed 520 and stationary bead. The bed is assumed to approach the spreader, and the bead of build material circulates around a nearly stationary center.
- the direction of the flow of the build material reverses close to a nip 540, i.e., an interface between the spreading roller 500 and the moving bed 520.
- a nip 540 i.e., an interface between the spreading roller 500 and the moving bed 520.
- the equilibrium of a small printed feature as it passes directly underneath the spreader rod is analyzed.
- the thickness t of a single printed layer of build material 32 is approximately Vioo the radius of the spreader rod.
- the spreader exerts a compressive stress ⁇ ⁇ and a shear stress ⁇ xz on the build material directly underneath it.
- the feature is assumed to leave a wake 1620 behind it where build material, after being swept along the upper surface, is unable to wrap around the downstream corner and establish a stress analogous to hydrostatic pressure against the right surface.
- the horizontal stress applied to the left may be opposed by a shear stress along the bottom surface.
- a free body diagram of the feature is shown in Figure 7b, including a hollow cavity 630 formed in the feature wake 620.
- Bredt flow parameter (Br) is herein defined, expressing, in general, the propensity for printed features to shift in the build area of a three-dimensional printer during spreading of build material:
- ⁇ / ⁇ xx Br > t / L * 0.1 (2)
- the ratio t/L is slightly arbitrary. One may assume for practical purposes that features with a length at least several times the layer thickness ( L ⁇ 10 times t) are those that are preferably considered in this model. Layers with thickness of 100 ⁇ m are standard in three- dimensional printing machines that are currently available, and instability of isolated patches smaller than 1.0 mm may have a minimally discernable effect on the appearance of an article.
- the build material is non-cohesive, i.e., the cohesion of the particulate material is much less than the dynamic pressure of material in flow. Using reasonable values for the bulk density of the build material and spreading speed in a standard ZPrinter®310 three-dimensional printer, one obtains an order of magnitude estimate :
- a material having shear strength of this magnitude is a weak gel, such as yogurt. While it is not “strong” in any sense of the word, it is by no means "free-flowing."
- the bead of free- flowing particulate build material may be in a state of yielding at the bottom of the pile when the counter-roller begins to move it across the build area. In a ZPrinter®310 three-dimensional printer, the bead is approximately 1 cm tall. Accordingly, we require the following inequality to hold:
- Equation 7 expresses a vitally important feature of free-flowing particulate build materials that are suitable for use in three-dimensional printing machines.
- the quantity on the left, Br nc is termed the "Bredt flow parameter for noncohesive particulate materials," and it preferably has a value greater than about V 10 for small printed features to remain stationary during spreading.
- the device then applies a gradually increasing transverse shearing force until it detects slip in the sample of material. It performs this measurement across a range of applied loads to develop a yield locus analogous to those pictured in Figure 8. Since the instrument measures the shear stress at the instant of rupture, this is the "static" friction in the particulate material.
- An approximate laboratory procedure may provide estimates of the flow parameter for non-cohesive particulate build materials. This may be done by measuring the angle of repose of a pile of a particulate material under static and dynamic conditions. The procedure is executed as follows. On an unpolished type 304 stainless steel sheet with a 2B mill finish and a dimension of 12 inches square by 0.060 inches in thickness available from McMaster-Carr based in Elmhurst , IL, a conical pile is formed from a particulate material sample by sprinkling particles very slowly at a bulk volumetric flow rate of 30 ⁇ 15 mL per minute over one point using a 385 mL stainless steel funnel available from Lab Safety Supply in Janesville, WI from a height of about 1 cm above the growing top of the pile. The height of the pile is chosen such that gh « (u+ ⁇ a) 2
- Neobee M20 was used to coat glass beads. Neobee M20 from Stepan Industries
- glass spheres alone had the poorest performance, with a flow parameter of only about 0.05. This, too, is supported by qualitative experience: glass beads alone are unsuitable for three dimensional printing from the standpoint of spreading. However, glass beads may be mixed with various processing aids and with other particulate materials that may be finer or equal to in particle size having a non-spherical and irregular particle shape to achieve a desirable Bredt parameter greater than 0.10, thereby being suitable for use in three dimensional printing.
- processing aids To illustrate the extreme sensitivity of particulate behavior with even small additions of certain chemicals, generally referred to as "processing aids," a series of data were taken in which tiny (10 ppm) increments of a low- viscosity emulsifier are added to a sample of glass spheres. The flow parameter rises quickly, peaks, and falls away even more quickly even though both the static and dynamic friction angles increase through the series. The critical point occurs when the dynamic angle of repose transitions from a nearly constant value to a linearly increasing value. This shows that there can be rather sharp optima in composition to obtain useful spreading characteristics. [0109] This test is a fairly useful technique for identifying relative performance properties between different candidate materials.
- the preferred method for evaluating flow properties of candidate build materials during formal optimization after the initial selection period is to test samples of the material on a working three-dimensional printer.
- Certain pathological geometries are known to those experienced in the art, and they can be evaluated either qualitatively or quantitatively.
- One particularly useful geometry for observing stability during spreading is a flat plate studded with pegs that are oriented downward during the build. During printing, the earliest layers addressed are a series of disconnected patches that are relatively free to shift in the build material. After these have been formed, a plate is printed that joins all of the pegs together in a single object. One can easily examine whether the pegs are uniform and straight, and one can evaluate the quality of spreading on that basis.
- compositions relate to control of the flow properties of the build material in three-dimensional printers.
- the three principal methods are the addition of liquid "processing aids," control of grain size distribution, and the addition of solid fillers that contribute to the frictional behavior of the build material.
- Many candidate materials have been disclosed previously, for example, in U.S. Patent Publication Number 2005/0003189.
- Some mechanical properties of dry particulate build materials are disclosed in the following discussion that are particularly suited for use in three dimensional printing, especially in contrast to other formulations of similar materials for other uses that do not require special flow characteristics of the raw materials.
- a method that may be used to quantify a particulate material's suitability for three dimensional printing includes placing 1 liter in bulk volume of a particulate material in a metal cylinder with an inside dimension of 6.1 inches, and inside height of 6.2 inches so that the height of the powder is between 2.5 to 3.0 inches when the cylinder is capped with a translucent cover and laid on its side (i.e., the height of the cylinder is horizontal).
- the drum is then slowly rolled with a rotational velocity of 2.5 rotations/min ⁇ 0.5 rotations/min until the powder reaches an angle where it avalanches upon itself.
- the distance that the drum rolled, s, is recorded and the angle, ⁇ , can be determined from equation 8:
- Figure 9a is an exemplary CAD drawing of a test geometry that exhibits the distortion caused by the dragging of an article in a powder that is too flowable.
- Figures 9b and 9c are surface finish scans from a VIKING laser profilometer from Solarius. The figures show a 3D topographical representation of articles formed by three dimensional printing. In Figure 9b, a scan of an article made with zpl31 from Z Corporation exhibits smooth, even contours that closely follow the intended CAD data.
- Figure 9c is a scan of a typically "too flowable" powder with an internal friction angle ⁇ 40°; the powder is too flowable and unable to resist the spreading forces causing previously printed layers to be displaced, resulting in an article that has a rough and uneven surface finish, or even has displaced artifacts missing from the surface of the article.
- the arrow in Figure 9c shows where geometry has shifted during printing.
- Figure 10a is a CAD drawing of the formed article illustrated in Figures 10b and 10c.
- a particulate material with an internal angle of friction that is between 40° and 70° e.g., zpl31
- a particulate material with an internal angle of friction greater than 70° Figure 10c
- This test i.e., determination of an internal angle of friction, is a useful technique for identifying relative performance properties between different candidate materials.
- the preferred method for evaluating flow properties of candidate build materials during formal optimization after initial selection is to test samples of the material on a working three- dimensional printer. Certain pathological geometries are known to those experienced in the art, and they can be evaluated either qualitatively or quantitatively.
- One particularly useful article for observing stability during spreading is a flat plate studded with pegs that are oriented downward during the build. During printing, the earliest layers addressed are a series of disconnected patches that are relatively free to shift in the build material. After these have been formed, a plate is printed that joins all of the pegs together in a single object.
Abstract
Materials system, kit, and methods are provided to enable the formation of articles by three dimensional printing. The kit includes (i) a substantially dry particulate material including an aqueous-insoluble thermoplastic particulate material, plaster, and a water-soluble adhesive; (ii) an aqueous fluid binder, and (iii) an infiltrant.
Description
THREE DIMENSIONAL PRINTING MATERIAL SYSTEM AND METHOD USING
PLASTICIZER-ASSISTED SINTERING
Related Application
[0001] This application claims priority to U.S. Provisional Patent Application Serial No. 60/902,782, filed February 22, 2007, the disclosure of which is hereby incorporated by reference in its entirety.
Technical Field [0002] This invention relates generally to rapid prototyping techniques and, more particularly, to a three-dimensional printing material and method using plasticizer-assisted sintering.
Background [0003] The field of rapid prototyping involves the production of prototype articles and small quantities of functional parts, as well as structural ceramics and ceramic shell molds for metal casting, directly from computer-generated design data.
[0004] Two well-known methods for rapid prototyping include a selective laser sintering process and a liquid binder three dimensional printing process. These techniques are similar, to the extent that they both use layering techniques to build three-dimensional articles. Both methods form successive thin cross-sections of the desired article. The individual cross- sections are formed by bonding together adjacent grains of a granular, i.e. particulate material on a generally planar surface of a bed of the granular material. Each layer is bonded to a previously formed layer to form the desired three-dimensional article at the same time as the grains of each layer are bonded together. The laser-sintering and liquid binder techniques are advantageous, because they create parts directly from computer-generated design data and can produce parts having complex geometries. Moreover, three dimensional printing can be quicker and less expensive than machining of prototype parts or production of cast or molded parts by conventional "hard" or "soft" tooling techniques, that can take from a few weeks to several months, depending on the complexity of the item. [0005] An early three dimensional printing technique, described in U.S. Patent No.
5,204,055, incorporated herein by reference in its entirety, describes the use of an ink-jet style printing head to deliver a liquid or colloidal binder material to sequentially applied layers of
powdered material. The three-dimensional ink-jet printing technique or liquid binder method involves applying a layer of a powdered material to a surface using a counter-roller. After the powdered material is applied to the surface, the ink-jet printhead delivers a liquid binder in a predetermined pattern to the layer of powder. The binder infiltrates into gaps in the powder material and hardens to bond the powder material into a solidified layer. The hardened binder also bonds each layer to the previous layer. After the first cross-sectional portion is formed, the previous steps are repeated, building successive cross-sectional portions until the final article is formed. Optionally, an adhesive can be suspended in a carrier that evaporates, leaving the hardened adhesive behind. The powdered material may be ceramic, metal, plastic or a composite material, and may also include fibers. The liquid binder material may be organic or inorganic. Typical organic binder materials used are polymeric resins or ceramic precursors, such as polycarbosilazane. Inorganic binders are used where the binder is incorporated into the final articles; silica is typically used in such an application. [0006] As described in U.S. Patent No. 6.007,318, incorporated herein by reference in its entirety, printed articles may be dipped or painted with a solution that infiltrates the article by capillary actions. This processing may improve handling properties of the article and prevent its decay.
[0007] The use of an absorbent filler to facilitate infiltrant absorption is described in U. S. Patent Application 2005/0059757, incorporated herein by reference in its entirety. That application describes the incorporation of thermoplastic fillers in a powder, with the activating or infiltration material being a solvent.
Summary
[0008] In an embodiment, a strong printed article may be made by three dimensional printing over a substantially dry particulate material build material including an aqueous- insoluble thermoplastic particulate material. The printed article is further post-processed by infiltrating a liquid medium into the article. The liquid medium selectively plasticizes the aqueous-insoluble thermoplastic particulate material, lowering the thermoplastic's glass transition temperature. This facilitates sintering of the thermoplastic particulate material to bond together the matrix of the article, thereby increasing the article's durability.
[0009] Typical existing printing processes include a post-processing infiltration step to increase the strength of the printed article using two-component casting resins and/or adhesives or one-component cyanoacrylate adhesives to achieve greater durability to a three-dimensional article. Articles printed with the particulate material build material described herein and further infiltrated with a liquid plasticizer have strengths comparable to that of articles formed with cyanoacrylate adhesive, e.g., about 20 MPa, which has historically been proven to be sufficient for most concept modeling applications.
[0010] The infiltrant materials used for plasticized sintering may provide some advantages over other build materials. Using two-component casting resins such as epoxy-amine, isocyanate-amines, and/or isocyanate-polyol systems decreases the ease-of-use by the end-user by incorporating extra mixing steps, imposing pot-life constraints, and giving rise to safety, health, and environmental issues. One-component cyanoacrylate adhesives typically offer better ease-of-use because these materials do not require mixing, but they may create safety, heath, and environment issues such as fumes, irritation, and adhesion to skin and may not be stable when exposed to the open atmosphere for long periods of time. The plasticized assisted sintering of a build material consisting of a thermoplastic particulate increases ease of use by offering a method in which the process can be automated or semi-automated whereby the article is immersed in a stable, one component liquid medium for a predetermined amount of time and allowed to cool to a handling temperature. Stable, as used herein, refers to maintaining a consistent viscosity at a predetermined temperature when exposed to the open atmosphere for a long period of time, i.e., on the order of months.
[0011] In an aspect, an embodiment of the invention features a powder material system for three dimensional printing including a substantially dry particulate material including an aqueous-insoluble thermoplastic particulate material, plaster, and a water-soluble adhesive. The dry particulate material is suitable for use in three dimensional printing to form an article comprising a plurality of layers, the layers including a reaction product of the particulate material and an aqueous fluid that contacts the particulate material during three dimensional printing. [0012] One or more of the following features may be included. A static and a dynamic friction coefficient of the particulate material possess a relationship defined by a Bredt parameter having a value in excess of 0.1. An internal angle of friction may be selected from a range of 40° and 70°. The particulate material may include about 5% - 50% by weight of the aqueous- insoluble thermoplastic, about 25 - 90% by weight of the plaster, and about 5 - 30 % by weight
- A -
of a water-soluble adhesive. The aqueous-insoluble thermoplastic may include or consist essentially of high molecular weight polyethylene, polyamide, poly-cyclic-olefins, and/or combinations thereof.
[0013] The particulate material may further include a processing aid, e.g., the particulate material may include about 0.01 - 2.0 % by weight of the processing aid. The processing aid may include or consist essentially of mineral oil, propylene glycol di(caprylate/caprate), petroleum jelly, propylene glycol, di-isobutyl phthalate, di-isononyl phthalate, polyalkyleneoxide modified heptamethyltrisiloxanes, polyalkyleneoxide modified polydimethylsiloxanes, and/or combinations thereof. [0014] In another aspect, an embodiment of the invention features a kit including a substantially dry particulate material including an aqueous-insoluble thermoplastic particulate material, plaster, and a water-soluble adhesive. The kit also includes an aqueous fluid binder and an infiltrant. [0015] One or more of the following features may be included. The infiltrant may include 0- 99.99% by weight hydroxylated hydrocarbon, 0-99.99% by weight a solid wax, 0-99.99% by weigh a plasticizer, and 0.01-5% by weight a stabilizer.
[0016] The hydroxylated hydrocarbon may include a hydrocarbon diol with a molecular weight greater than 118 g/mol, a melting point greater than 3O0C, and a kinematic viscosity of 150 centiStokes or less, preferably 50 centiStokes or less, at a temperature of at least 5O0C. The hydrocarbon diol may include or consist essentially of octane diol and/or decane diol.
[0017] The infiltrant may include hydroxylated hydrocarbon that includes (i) a hydrocarbon diol with a molecular weight greater than 1 18 g/mol and a melting point greater than 300C and (ii) a plasticizer. The hydroxylated hydrocarbon may include decane diol. The plasticizer may include or consist essentially of benzene sulfonamide and/or propylene carbonate. [0018] The hydroxylated hydrocarbon may include an alcohol with boiling point selected from a range of 25°C to 1000C, and the plasticizer may have a boiling point selected from a range of 25°C to 1000C. The alcohol may include or consist essentially of isopropanol. The plasticizer may include or consist essentially of ethanol. [0019] In yet another aspect, an embodiment of the invention includes a method for forming an article by three dimensional printing. The method includes (i) providing a particulate material comprising a plurality of adjacent particles, the particulate material comprising an aqueous-insoluble thermoplastic; (ii) applying to at least some of the plurality of particles an
aqueous fluid binder in an amount sufficient to bond those particles together to define the article; and (iii) immersing the article in a liquid infiltrant medium.
[0020] One or more of the following features may be included. The liquid infiltrant medium may include a hydroxylated hydrocarbon. The liquid infiltrant medium may also include a plasticizer. The particulate material may further include at least one of plaster, a water-soluble adhesive, a retarder, an accelerator, and a processing aid.
[0021] In another aspect, an embodiment of the invention features an essentially solid article manufactured by a three-dimensional printing process, the essentially solid article comprising a product of a reaction between (i) a substantially dry particulate material including an aqueous- insoluble thermoplastic particulate material, plaster, and a water-soluble adhesive; (ii) an aqueous fluid comprising water, a humectant, a rheology modifier, a surfactant, a preservative, and an optical brightening agent; and (iii) an infiltrant including a hydroxylated hydrocarbon, a wax, a plasticizer, and a stabilizer. The aqueous-insoluble thermoplastic particulate material material is plasticized by the infiltrant. [0022] In still another embodiment, an article includes a product of (i) a substantially dry particulate material including an aqueous-insoluble thermoplastic particulate material, plaster, and a water-soluble adhesive; and (ii) an infiltrant.
[0023] The article preferably has a strength of at least 5 megapascal (MPa), more preferably at least 15 MPa, and most preferably at least 20 MPa.
Brief Description of the Figures
[0024] The following drawings are not necessarily to scale, emphasis instead being placed generally upon illustrating the principles of the invention. The foregoing and other features and advantages of the present invention, as well as the invention itself, will be more fully understood from the following description of exemplary and preferred embodiments, when read together with the accompanying drawings, in which:
Figure 1 is a schematic view of a first layer of a mixture of particulate material of an embodiment of the invention deposited onto a downwardly movable surface of a container on which an article is to be built, before any fluid has been delivered;
Figure 2 is a schematic view of an ink-jet nozzle delivering a fluid to a portion of the layer of particulate material of Figure 1 in a predetermined pattern;
Figure 3 is a schematic view of a final article of an embodiment of the invention enclosed in the container, the article made by a series of steps illustrated in Figure 2 and still immersed in the loose unactivated particles;
Figure 4 is a schematic view of the final article of Figure 3; Figure 5 is a graph illustrating an estimated solubility range of TROGAMID T-5000;
Figure 6 is a schematic illustration of a circulating spreader bead; Figures 7a, 7b, and 8 are graphs illustrating the forces acting on a particle during three dimensional printing;
Figure 9a is a CAD drawing of the article portion printed in Figures 9b and 9c; Figures 9b and 9c are laser profilometer images comparing the effect of particulate materials with high internal angle of friction on finished article properties;
Figure 10a is a CAD drawing of the article portion printed in Figures 10b and 10c; and Figure 10b and 10c are laser profilometer images comparing the effect of particulate material with low internal angle of friction on finished article properties.
Detailed Description
Three Dimensional Printing
[0025] Referring to Figure 1 , in accordance with a printing method using the materials system of the present invention, a layer or film of a particulate material 20, i.e., a powder, is applied on a linearly movable surface 22 of a container 24. The layer or film of particulate material 20 may be formed in any suitable manner, for example using a counter-roller. The particulate material 20 applied to the surface includes an aqueous-insoluble thermoplastic particulate material, plaster, and a water-soluble adhesive. The particulate material 20 may also include a filler material, a processing aid material, and/or a fibrous material. [0026] Referring to Figure 2, an ink-jet style nozzle 28 delivers an activating fluid 26, i.e., an aqueous fluid described below, to at least a portion 30 of the layer or film of the particulate mixture 20 in a two-dimensional pattern. According to the printing method, the fluid 26 is delivered to the layer or film of particulate material 20 in any predetermined two-dimensional pattern (circular, in the figures, for purposes of illustration only), using any convenient mechanism, such as a drop-on-demand (DOD) printhead driven by software in accordance with article model data from a computer-assisted-design (CAD) system.
[0027] The first portion 30 of the particulate mixture is activated by the fluid 26, causing the activated particles to adhere together to form a conglomerate of the particulate material 20 (powder) and fluid 26. The conglomerate defines an essentially solid circular layer that becomes a cross-sectional portion of an intermediate article 38 (see, e.g., Figures 3 and 4). As used herein, "activates" is meant to define a change in state from essentially inert to adhesive. This definition encompasses the activation of the adhesive particulate material to bond the absorbent filler particulate material. When the fluid initially comes into contact with the particulate mixture, it immediately flows outwardly (on a microscopic scale) from the point of impact by capillary suction, dissolving the adhesive within a relatively short time period, such as the first few seconds. A typical droplet of activating fluid has a volume of about 40 picoliters (pi), and spreads to a diameter of about 100 μm after coming into contact with the particulate mixture. As the solvent dissolves the adhesive, the fluid viscosity increases dramatically, arresting further migration of the fluid from the initial point of impact. Within a few minutes, the fluid with adhesive dissolved therein infiltrates the less soluble and slightly porous particles, forming adhesive bonds between the absorbent filler particulate material as well as between the additional filler and the fiber. The activating fluid is capable of bonding together an amount of the particulate mixture that is several times the mass of a droplet of the fluid. As volatile components of the fluid evaporate, the adhesive bonds harden, joining the absorbent filler particulate material and, optionally, additional filler and fiber particulates into a rigid structure, which becomes a cross-sectional portion of the final article 40. Thus, the layers include a reaction product of the particulate material and the activiating fluid, e.g., an aqueous fluid.
[0028] Any unactivated particulate mixture 32 that was not exposed to the fluid remains loose and free-flowing on the movable surface 22. The unactivated particulate mixture is typically left in place until formation of the intermediate article 38 is complete. Leaving the unactivated, loose particulate mixture in place ensures that the intermediate article 38 is fully supported during processing, allowing features such as overhangs, undercuts, and cavities to be defined and formed without the need to use supplemental support structures. After formation of the first cross-sectional portion of the intermediate article 38, the movable surface 22 is indexed downwardly, in this embodiment, and the process is repeated.
[0029] Using, for example, a counter-rolling mechanism, a second film or layer of the particulate mixture is then applied over the first layer, covering both the rigid first cross- sectional portion, and any proximate loose particulate mixture. A second application of fluid follows in the manner described above, dissolving the adhesive and forming adhesive bonds between at least a portion of the previous cross-sectional formed portion, the absorbent filler particulate material, and, optionally, additional filler and fiber of the second layer, and hardening to form a second rigid cross-sectional portion added to the first rigid cross-sectional portion of the final article. The movable surface 22 is again indexed downward. [0030] The previous steps of applying a layer of particulate mixture, including the adhesive, applying the activating fluid, and indexing the movable surface 22 downward are repeated until the intermediate article 38 is completed. Referring to Figure 3, the intermediate article 38 may be any shape, such as cylindrical. At the end of the process, only a top surface 34 of the intermediate article 38 is visible in the container 24. The intermediate article 38 is typically completely immersed in a surrounding bed 36 of unactivated particulate material. Alternatively, an article could be formed in layers upward from an immovable platform, by successively depositing, smoothing, and printing a series of such layers. [0031] Referring to Figure 4, the unactivated particulate material may be removed from the intermediate article 38 by pressurized air flow or a vacuum. After removal of the unactivated particulate material from the intermediate article 38, a post-processing treatment may be performed, such as cleaning, infiltration with stabilizing materials, painting, etc. to define a final article 40, having the same shape as intermediate article 38, but with additional desired characteristics, such as a stiffness, strength, and flexibility.
[0032] A particularly suitable infiltration method for the particulate material described herein includes immersing a finished article into a liquid infiltrant medium, i.e., a plasticizer, to increase the strength and toughness of the article. After the article is formed, it may be submerged in a liquid material and then heated to a sintering temperature. Alternatively, it may be submerged into a preheated plasticizer bath, causing in-situ diffusion and sintering. [0033] Preferably the article is completely immersed into the liquid or molten material. The material may be melted by placing the material in a polypropylene container in an oven, e.g., a Blue M oven or a Cole Palmer StableTemp mechanically convected oven model 52100-00, with the oven temperature being sufficiently high to melt the material. The container is preferably sufficiently large for the article to be completely submerged into a liquid disposed
therein. Alternatively, the material may be melted by exposure to microwaves. In a preferred embodiment, the article is completely submerged until substantially all of the entrapped air rises to the liquid's surface in the form of air bubbles.
[0034] Alternatively, liquid or molten material may be sprayed onto the article using spray bottles, nozzles, pumps or other means to completely cover the surface of the article.
[0035] The resulting essentially solid article may be the product of the reaction of (i) a substantially dry particulate material including an aqueous-insoluble thermoplastic particulate material, plaster, and a water-soluble adhesive; (ii) an aqueous fluid comprising water, a humectant, a rheology modifier, a surfactant, a preservative, and an optical brightening agent; and (iii) an infiltrant comprising a hydroxylated hydrocarbon, a wax, a plasticizer, and a stabilizer, with the aqueous-insoluble thermoplastic particulate material being plasticized by the infiltrant. An article may be the product of a substantially dry particulate material including an aqueous-insoluble thermoplastic particulate material, plaster, and a water-soluble adhesive, and an infiltrant. The article may have a strength of at least 5 MPa, preferably at least 15 MPa, and most preferably at least 20 MPa.
Particulate material
[0036] In a preferred embodiment, a particulate material, i.e., a substantially dry particulate material, includes or consists essentially of: an aqueous-insoluble thermoplastic particulate material 5 - 50 wt% plaster (calcium hemihydrate) 25 - 90 wt% water-soluble adhesive 5 - 30 wt% retarder 0.01 - 5 wt% accelerator 0.01 - 5 wt% processing aids 0.01 - 2.0 wt%
[0037] An example of a preferred particulate composition is: an aqueous-insoluble thermoplastic particulate material 15 - 35 wt% plaster (calcium hemihydrate) 50 - 80 wt% water-soluble adhesive 5 - 15 wt% retarder 0.01 - 5 wt% accelerator 0.01 - 3 wt% processing aids 0.01 - 2.0 wt%
[0038] A preferred particle size of components of the particulate material is an average particle diameter of less than 125 microns and greater than 10 microns.
[0039] The aqueous-insoluble thermoplastic particulate material provides extra durability and increased strength when it sinters together after being plasticized by the liquid medium. A suitable aqueous-insoluble thermoplastic has a particle size greater than 20 microns and less than 100 microns, and has a glass transition temperature greater than 45°C. The aqueous- insoluble thermoplastic particulate material also is soluble and/or permeable with certain nonaqueous solvents, waxes, or hydrocarbon diols that can act as plasticizers. [0040] An example of an appropriate aqueous-insoluble thermoplastic particulate material is a polyamide 6-3 and terphthalic acid copolymer, available under the trade name of TROGAMID, such as TROGAMID T5000 from Degussa based in Germany. According to its technical data sheet, TROGAMID T5000 exhibits a resistance to most chemicals; however, it lacks chemical resistance to certain hydroxylated hydrocarbons like ethanol, propylene glycol, and pentanediol. TROGAMID T5000 also has decreased chemical resistance against, e.g., methanol, 1-propanol, pentanol, allyl alcohol, aniline, crotonaldehyde, dimethylformamide, and glacial acetic acid. TROGAMID T5000's weakness to these types of chemicals makes it possible to use these hydroxylated hydrocarbons as plasticizers with TROGAMID T5000 to reduce its glass transition temperature to a point where it sinters together in the matrix of the three-dimensional article.
[0041] Other suitable aqueous-insoluble thermoplastic particulate materials are high molecular weight polyethylene like GUR from Ticona USA based in Florence, KY and cyclic polyolefins like TOPAS from TOPAS Advanced Polymers. These particular thermoplastics lack chemical resistance to aliphatic and/or aromatic solvents, and/or paraffin based oils and
waxes, rendering these materials suitable for use as plasticizers for these thermoplastic materials. Yet other examples of aqueous-insoluble thermoplastic particulate materials include polyamide and poly-cyclic-olefins.
[0042] The plaster provides dimensional stability and adhesion for strength of an article formed from the particulate material. A suitable plaster for use with embodiments of the invention is calcium hemihydrate having a particle size distribution ranging from greater than 20 microns to less than 125 microns. An example of such plaster is HYDROCAL, available from USG based in Chicago, IL. Another suitable plaster product that is whiter than HYDROCAL is the SSS Brand from San Esu based in Suita, Osaka, Japan. The whiter product imparts a more neutral color to articles than HYDROCAL, which may be desirable for attaining a wider color gamut.
[0043] The water-soluble adhesive provides adhesive strength in the system and helps to control bleed or pooling of fluid binder in selectively printed areas. A suitable water-soluble adhesive is a polymer with an average molecular weight from a range of 10,000 to 200,000 g/mol with hydrolysis greater than 85% and less than 90% and a particle size distribution ranging from greater than 5 micron to less than 125 microns. A water-soluble adhesive is a polyvinyl alcohol such as CELVOL 203 S available from Celanese from Dallas, TX. Another suitable resin is a maltodextrin such as STAR-DRI- 1, available from A.E. Staley based in Decatur, IL. Maltodextrin may be used to improve the stiffness of the article as it is drying and during the post processing with a liquid medium infiltrant.
[0044] A retarder may be included, such as borax. After an aqueous binder is deposited onto a plaster-containing particulate material, calcium sulfate dihydrate crystals form during gypsum setting. Retarders help decrease the growth rate of calcium sulfate dihydrate crystals, thus reducing a distortion effect known as arching in three dimensional printing. Arching is a distortion defect in which flat bottom surfaces exhibit concavity from successive layers expanding too fast.
[0045] An accelerator may be included, such as potassium sulfate, potassium aluminum sulfate, sodium sulfate, calcium sulfate dihydrate, or aluminum sulfate. The accelerator helps increase the precipitation rate of aqueous calcium sulfate into calcium sulfate dihydrate to gain an appreciable early handling strength.
[0046] Processing aids may be used to affect particulate material spreading characteristics to achieve a desirable Bredt parameter (see discussion below) and to reduce dust becoming
airborne while the powder is being used. Mineral oil is a typical processing aid that affects the Bredt parameter of the particulate material. Mineral oil from Sigma- Aldrich may provide a good balance of particulate cohesion and low plasticizing of the aqueous-insoluble filler. Other examples of processing aids include propylene glycol di(caprylate/caprate), petroleum jelly, propylene glycol, di-isobutyl phthalate, di-isononyl phthalate, polyalkyleneoxide modified heptamethyltrisiloxanes, polyalkyleneoxide modified polydimethylsiloxanes, and combinations thereof.
Fluid binder
[0047] In a preferred embodiment, a fluid binder is an aqueous fluid that includes or consists essentially of: water 70 - 90 wt% humectant l - 10 wt% preservative 0.05 - 5 wt% surfactant 0 - 2 wt% optical brightening agent 0 - 5 wt%
The aqueous fluid may also include rheology modifiers at a concentration of 0.01 - 5 wt%. As discussed below, the aqueous fluid may include a fluorescent brightener based on stilbene chemistry or distyrylbiphenyl. [0048] Humectants may serve to keep the nozzles of the print head from drying out and forming a crust when uncapped, such as during the period when the print head is not firing droplets but moving over the build area to a new position. The type and concentration of a humectant may also influence the dynamics of droplet formation, the consistency of drop trajectory, and the curing of the article formed by three dimensional printing. Examples of suitable humectants include Glycerol and other diols from 3 - 10 carbons long; many other examples of humectants are known in the art. Printing may be successful with humectant levels from 1 - 20%, depending on the binder formulation.
[0049] The preservative may serve to prolong the shelf life of the fluid as manufactured, as well as to extend its useful life in the machine. Preservatives may have detrimental effects on print quality, and in some cases on the appearance or curing of the article being formed by three dimensional printing. It is generally desirable to choose environmentally friendly, stable, and substantially clear preservatives. An example of a suitable preservative includes Proxel GXL,
manufactured by Arch Chemical. Many other suitable preservatives are available in the industry.
[0050] Surfactants are typically used to control the surface tension of the aqueous fluid. Proper surface tension helps ensure that the droplets being ejected from a print head are formed with a consistent volume, depart from the print head at the appropriate vector, and do not form satellite drops. Very high surface tension may create poor wetting when the binder impacts loose powder. Low surface tension may create poor droplet formation at the face of the print head. Surface tensions of suitable binders for use with an HP 11 print head (from Hewlett- Packard) range from 30 dynes/cm to 36 dynes/cm. Suitable surfactants include Surfynol CT- 171, Surfynol 465, and Surfynol 485 in ranges from 0.24 wt% to 1.5 wt%. Such products are available from Air Products. The range of viscosities of the aqueous fluid suitable for use with HPl 1 print heads is 1 - 1.35 cps. pH of the fluid may also influence the safety of the product, the effect of the binder on the reaction rate of the plaster, and the compatibility of the fluid with the materials from which the machine is constructed. An acceptable range of pH for the aqueous fluid described herein is, e.g., from 4.9 to 10.3.
[0051] The aqueous fluid may be used for three dimensional printing, such that an article printed with the aqueous fluid including the optical brightening agent has a lower chroma C* than an article printed with the aqueous fluid without the optical brightening agent. Optical brighteners are used to color correct the whiteness of a three-dimensional printed part. Optical brightening agents increase the perceived whiteness of a part by absorbing ultra violet light having a wavelength <400 nanometers (nm) and re-emitting blue light with a wavelength typically selected from a range of 400 to 450 nm, increasing the reflected light in the visible spectrum. The blue fluorescence of the optical brightener helps to overcomes the natural yellowness of the other raw materials. Quantitatively, this may be expressed as higher emission in the blue reflectance. Liquid infiltrant medium
[0052] In one preferred embodiment, a liquid infiltrant includes or consists essentially of: a hydroxylated hydrocarbon 0 - 99.99 wt% a wax (solid at room temperature) 0 - 99.99 wt% a plasticizer 0 - 99.99 wt% stabilizer 0.01 - 5 wt%
[0053] For example, the liquid infiltrant may include or consist essentially of: a hydroxylated hydrocarbon (solid at room temperature) 69.99 - 99.99 wt% a plasticizer 0 - 30 wt% stabilizer 0.01 - 5 wt%
[0054] In another embodiment, a liquid infiltrant may include or consists essentially of: a paraffin wax (solid at room temperature) 79.99 - 99.99 wt% a plasticizer 0 - 20 wt% stabilizer 0.01 - 5 wt%
[0055] In another preferred embodiment, a liquid infiltrant includes or consists essentially of: a fugitive hydroxylated hydrocarbon (liquid at room temperature) 30 - 100 wt% a solvent 0 - 50 wt% a plasticizer 0 - 30 wt%
[0056] The hydroxylated hydrocarbon may be the primary plasticizer that reduces the glass transition temperature of the aqueous-insoluble thermoplastic particulate material. The hydroxylated hydrocarbon may also be the carrier of a secondary plasticizer that is soluble in the hydroxylated hydrocarbon and more effective in plasticizing the aqueous-insoluble thermoplastic, and where the hydroxylated hydrocarbon is less effective in plasticizing the aqueous-insoluble thermoplastic. Suitable hydroxylated hydrocarbons are ethanol, pentane- diol, octane-diol, and decanediol.
[0057] Ethanol, having a boiling point below 100°C, is a suitable fugitive plasticizer for the TROGAMID T5000; ethanol evaporates away from the printed article after infiltrating the article, with the TROGAMID T5000 sintering together within the matrix of the article. Ethanol may be too effective in plasticizing TROGAMID T5000 to an extent that an article may distort and collapse under its own weight. The plasticizing effect of ethanol may be reduced by adding another miscible hydroxylated hydrocarbon having a boiling point less than 100°C such as isopropanol. Isopropanol does not exhibit the same plasticizing effect on TROGAMID T5000, and is fugitive as well having a boiling point well below 1000C. The addition of isopropanol to ethanol may decrease the hydrogen bonding forces of the ethanol, thereby
possibly decreasing the plasticization effect of the alcohol mixture on TROGAMID T5000. However, the use of hydroxy lated hydrocarbons with boiling points less than 1000C may raise concerns of flammability and end-user safety. Octane diol and decane diols are generally more preferred hydroxylated hydrocarbons because they have higher flashpoints than ethanol, and are solid at room temperature and are liquid with a kinematic viscosity of 150 centiStokes or less, more preferably 50 centiStokes or less at temperatures greater than 50°C. [0058] A solid wax having a melting point greater than 30°C may be the primary plasticizer to reduce the glass transition temperature (Tg) of the aqueous-insoluble thermoplastic, or may be the carrier of a secondary plasticr that is soluble in the solid wax when in a melted, liquid state at temperatures above 500C if the solid wax is not effective in lowering the Tg of the aqueous-insoluble thermoplastic alone. Suitable waxes that plasticize TROGAMID T5000 are hydrocarbon diols with molecular weights greater than 118 g/mol, such as octane diol and decane diol. Another suitable solid wax is paraffin wax such as Paraplast X-Tra available from McCormick Scientific based in St. Louis, MO, which is suitable for plasticizing both polyethylene thermoplastics like GUR and cyclic-poly-olefϊns like TOPAS. At a temperature of at least 5O0C, the wax may have a kinematic viscosity of 150 centiStokes or less, preferably 50 centiStokes or less, to ensure a fast infiltration rate and deep penetration into an immersed article; and to facilitate easier drainage and removal of excess liquid infiltrant from the article when the article is extracted from the liquid infiltrant, thereby reducing pooling and drip defects on the article as the wax solidifies.
[0059] The plasticizer may be the sole ingredient or an additive in either a hydroxylated hydrocarbon and/or a solid wax to enhance the plasticization of the aqueous-insoluble thermoplastic particulate material. The plasticizer may be the sole ingredient that is in a liquid state when infiltrating a three dimensional article. Suitable sole plasticizers are, for example, ethanol, octane diol, and decane diol for reducing the Tg of TROGAMID T5000. Paraffin waxes and mineral oil may also be suitable as sole plasticizers for polyethene and poly-cyclic poly olefins such as GUR and TOPAS respectively. A suitable mineral oil for use with an embodiment of this invention is supplied by Aldrich based in Milwaukee, WI. The plasticizer may be used as an additive when supplied in a soluble carrier at a concentration less than 20% by weight. A suitable plasticizer used as an additive may be ethanol carried in isopropanol, or, more preferably, benzene sulfonamide carried in decane diol to assist the plasticization of
TROGAMID T5000. Other suitable plasticizer additives may be used, such as ones based on carbonates, succinates, phthalates, adipates, and phosphates.
[0060] Stabilizers may be added to the liquid infiltrant medium to decrease oxidation that may lead to the discoloration of the liquid infiltrant medium when kept at temperatures above 50°C for prolonged periods of time. Suitable stabilizers are antioxidants such as butylated hydroxytoluene.
Mechanisms of plasticizer-assisted sintering
[0061] A summary of a printing/infiltration process is as follows: a) a layer is formed of a substantially dry particulate material containing thermoplastic particulate, a plaster, and/or a water-soluble polymer such as a water-soluble adhesive; b) an aqueous fluid binder is applied to the layer of dry particulate material in a predetermined pattern to cause binding in the areas to which the binder is applied; c) steps (a) and (b) are repeated sequentially to define a three-dimensional article; d) after complete setting of the thermoplastic, plaster, or water-soluble polymer, the three-dimensional article is removed from the build, i.e., from the stack of dry particulate material layers; e) the three-dimensional article is submerged in the plasticizer or its solution, i.e., the liquid infiltrant medium, at ambient or elevated temperature; and f) optionally, the particulate material is exposed to additional energy in the form of conventional heat, visible or infrared light, microwave, or radio-frequency, for additional sintering of particulate material.
[0062] The use of certain infiltrant materials (such as plasticizers) described herein allows selective diffusion into the polymer matrix during infiltration to reduce the glass transition temperature and to increase the melt flow of the aqueous-insoluble polymer. This also results in the reduction of the inert, non- water-soluble polymer concentration in order to achieve good green strength and sagging resistance.
[0063] In an embodiment, articles are submerged into a liquid infiltrant medium and heated to the sintering temperature. In another embodiment, articles may be submerged in a preheated plasticizer bath causing in-situ diffusion and sintering. The sintering may be performed without application of additional pressure, i.e., the sintering may be substantially pressure-free.
[0064] In yet another embodiment, rather than being provided as a liquid infiltrant, the plasticizer may be a component of the particulate composition. Alternatively , the article may be placed in a heated chamber filled with plasticizer in the gaseous phase.
[0065] The particulate composition may include an inert absorbent filler is saturated with plasticizer. Here, after an article is printed, the plasticizer migrates into the polymer matrix during heat treatment.
[0066] The plasticizer may be applied as a pure substance, solution or emulsion. It may also contain solvents, surfactants, viscosity modifiers, dyes, and/or pigments.
[0067] The plasticizer may be liquid or solid at room temperature. Solid plasticizer may be applied to the particulate composition in the molten form. Use of plasticizers with high melting point typically diminishes or prevents their migration during the lifetime of an article. Liquid plasticizer may be dissolved in a high melt temperature inert solid carrier, creating material that is solid at room temperature.
[0068] One of the advantages of the processes described herein is that one may produce both rigid and rubbery articles from the same particulate composition by employing a different plasticizer system or a system that contains different concentrations of the same plasticizers.
Also, uniformly colored articles may be produced by dissolving dyes in the liquid or solid plasticizer systems.
[0069] Solubility of the plasticizer in the polymer matrix of the article is determined by the polymer system, and depends on three major parameters. These parameters are: interaction between plasticizer molecules; the molecular interaction between the polymer molecules; and the mutual interaction of the polymer molecules when mixed.
[0070] Most commonly, those interactions may be calculated using the Hansen solubility parameters. These parameters allow for accurate estimation of solubility and swelling of the polymers in solvents, or in this case plasticizers. In particular, the Hansen solubility parameters represent the following intermolecular forces, the so-called Van der Waals forces: dispersion forces (δd), dipole - dipole interactions (δp) and hydrogen bonding forces (δh). The total
Hildebrand solubility parameter (δ) may be calculated with these components as follows: δ = ( δd 2 + δp 2 + δh 2 )1/2 [0071] The concepts presented here regarding the Hildebrand and Hansen solubility parameters may be found in the Polymer Handbook, Brandup, J. et. al., John Wiley & Sons,
Inc., 1999, the disclosure of which is incorporated herein by reference in its entirety. A close
quantitative agreement between the Hansen solubility parameters of the polymer and the Hansen solubility parameters of the plasticizer implies greater solubility of the plasticizer into the polymer, thus lowering the energy typically required for sintering. [0072] Extremely high solubility of the polymer in plasticizer may be undesirable because this may result in over-plasticization or the dissolution of the thermoplastic additive. In that case, the glass transition temperature may be close or below room temperature, which may cause distortion and weak particle bonding. In some embodiments, plasticizer material may be preferably selected from materials that have low solubility at room temperature but greater solubility at higher temperatures.
[0073] To reduce solubility, the plasticizer may be diluted either by the solvent that is removed after sintering or inert solid material that may remain in the three dimensional article after cooling.
[0074] As an example of how one may select a plasticizing solvent, chemical resistance data was acquired from Degussa's TROGAMID T5000 product literature and the Hansen solubility parameters of the solvents were estimated using the Hoy group contribution method as described in the Polymer Handbook, to produce the data given in Table 1 :
Table 1
[0075] From this table, one can plot a solubility range for TROGAMID T5000 by plotting the hydrogen bonding forces, δh, against the combined value of the dispersion and polar forces, (δd 2 + δp 2)1/2, as shown in Figure 5. In accordance with a heuristic, any solvent within a radius of 5 (MPa)1/2 of a polymer's solubility parameter location on the δh vs (δd2 + δp 2)1/2 plot is to be considered a solvent that will interact with the polymer, and any solvent outside that radius typically does not have any effect. The solubility parameters for TROGAMID T5000 in this example may also be estimated from the Hoy contribution method. One can see in Figure 5
that solvents that have no effect (represented by X), as indicated in the TROGAMID T5000 product literature, lie at or beyond the radius of interaction (indicated by a large oval), while solvents that affect the polymer (represented by o and π, as well as octanediol and decanediol) fall within the radius with some extending upwards outside the radius as the hydrogen bonding forces increase. This suggests that solvents with high hydrogen bonding forces are more significant in polymer-solvent interaction for this particular example. When the hydroxylated hydrocarbons of interest in certain embodiment, i.e., decanediol and octanediol, are plotted using the Hoy contribution method, one can see that they fall within the radius of interaction of TROGAMID T5000, and may, therefore, impart the desired plasticizing effect.
Examples Example 1
[0076] One kilogram of particulate material was prepared using the materials and ratios shown below in Table 2. The mixture was placed in a Kitchen Aid Professional 600 Mixer and mixed for about 20 minutes. The resulting blended mixture was then sieved through a 50 mesh screen to remove clumps.
Table 2
Flexural strength test bars 50 mm long, 5 mm wide, and 5.7 mm tall were printed on Z310 using zb58 binder with a-binder-to-volume ratio of 0.10. The test bars were dried for 2 hours at 38 0C in an oven. Sequentially, test bars were infiltrated by dipping them in different alcohols (solvents) for 15 seconds at room temperature, removing them from the solvents, and placing them in an oven (Cole Palmer StableTemp mechanically convected oven model 52100-00) preheated to 750C for 3 hours. After the test bars were cooled at ambient conditions for 1 hour,
they were placed and supported on a 2-point span spaced at 40 mm. A force was applied on the top of the bar at the center of the 40 mm span using a Texture Analyzer TA-XT2 from Texture technologies (Scottsdale, NY). The maximum force applied at which the bars break was recorded and used to calculate the measured bar strengths given in Table 3. As one can see from the table, the use of an infiltrant greatly increased the resulting bar strength.
Table 3 Example 2
[0077] Powdered material was prepared according to the procedure described in Example 1 , using the materials and ratios shown below in Table 4.
Table 4
[0078] Flexural strength test bars describe in Example 1 were printed on Z310 particulate material using zb58 binder with a binder to volume ratio of 0.25. Parts were dried for 2 hours at 38 0C in an oven. Sequentially, parts were infiltrated by dipping them in different liquids for 15 seconds at room temperature. Then parts were removed from the solvent and placed in a microwave oven (Sharp Carousel model R2A57 700W). Parts were micro waved for 5 minutes
at "High" settings. After parts cooled at ambient conditions for 1 hour, the flexural strengths were acquired as described in Example 1, and are reported in Table 5.
Table 5
[0079] The same dry uninfϊltrated flexural strength test bars were placed in a preheated bath contained 1,10-decanediol preheated to 85 0C for 10 seconds, removed and left for 16 hours in the oven at 85 0C. The flexural strength test indicated a strength of 28.1 MPa.
Example 3 [0080] Powdered material was prepared according to the procedure described in the Example 1 using the materials and ratios shown below in Table 6.
Table 6
[0081] Flexural strength test bars described in Example 1 were printed on Z310 particulate material using zb58 binder with a binder to volume ratio of 0.23. Parts were dried for 2 hours at 38 0C in an oven. Parts were completely dipped in the heated bath containing molten materials for 10 seconds, removed from the molten material and placed in the oven. The flexural strength results are indicated in Table 7.
Table 7
Example 4
[0082] A powdered material may be prepared according to the procedure described in the
Example 1 using the materials and ratios shown below in Table 8.
Table 8
[0083] Articles may be created from the particulate material formulation listed in Table 8 using zb58 aqueous fluid binder with a Z310 printer. The article may then be removed from the Z310 printer 2 hours after printing has been completed and the article placed in a mechanical convection oven set between 75°C to 100°C for 0.5 to 2 hours to melt the hydrocarbon diol within the article, to plasticize the plastic and facilitate sintering.
Kits
[0084] A preferred kit includes a powder adapted for three dimensional printing, an aqueous fluid for activating water soluble components of the three-dimensional printing powder, and an infϊltrant suitable for plasticizing an aqueous-insoluble thermoplastic component of the particulate material. The powder may include a loose, dry, and substantially free-flowing particulate mixture including an aqueous-insoluble thermoplastic particulate material, plaster (calcium hemihydrate), water-soluble adhesive, and, optionally, a retarder, accelerator, and/or processing aids. The aqueous fluid binder may include water, a humectant, a preservative, and, optionally, a surfactant, and/or an optical brightening agent. The infiltrant may include a hydroxylated hydrocarbon, a solid wax, a plasticizer, and a stabilizer. [0085] The particulate material is adapted for use in three dimensional printing to form an article comprising a plurality of layers, the layers including a reaction product of the particulate material and the aqueous fluid that contacts the particulate material during three dimensional printing. The aqueous fluid may be substantially clear, have a viscosity selected from a range of 1-1.35 cps, a surface tension selected from a range of 30-36 dynes/cm, and a pH selected from a range 4.9 to 10.3. The infiltrant may be adapted to plasticize the aqueous-insoluble thermoplastic particulate material by lowering the glass transition temperature of the aqueous- insoluble thermoplastic particulate to allow the sintering of those particulates. The kit may also include a combination of aqueous fluids comprising cyan, magenta, and yellow colorants.
[0086] The aqueous binder may be selected such that it is capable of hydrating the plaster (calcium hemihydrate) and initiating the precipitation into a gypsum cement. The binder is applied onto the substantially dry particulate material so as to occupy from 10% to 35% of the volume defined by the selectively printed area at a predetermined layer thickness, typically 100 microns. The printed area is then allowed to set to attain a flexural strength of at least 1 MPa, for example after 2 hours from the time the last layer was printed.
[0087] An infiltrant that is selected to plasticize the aqueous-insoluble thermoplastic particulate material is preferably clear and translucent to allow the natural lightness and color of the powder to show through. The infiltrant may also be selected so as to not interact with the selectively printed areas where aqueous fluid colorants were applied so that the colors do not migrate out of or through the article. The infiltrant may be selected to have a kinematic viscosity of 150 centiStokes or less when in a liquid state at a predetermined temperature.
Flow Properties of Build Materials
[0088] Compositions have been disclosed above that relate to the control of the flow properties of the build material in three-dimensional printers. The three principle methods flow property control are the addition of liquid "processing aids," control of grain size distribution, and the addition of solid fillers that contribute to the frictional behavior of the build material. Many candidate materials have been disclosed previously, for example, in U.S. Patent Publication Number 2005/0003189, incorporated herein by reference in its entirety. Previously, however, the exact implementation of these methods has been by trial and error. Here, some mechanical properties of dry particulate build materials are disclosed that are particularly suited for use in three dimensional printing, especially in contrast to other formulations of similar materials for other uses that may not require special flow characteristics of the raw materials. [0089] Referring to Figure 6, in an embodiment of a three-dimensional printer, dry, free- flowing particulate build material is spread by a rotating spreader rod 500. The rod rotates in a direction counter to the direction of motion of the spreading mechanism. A circulating bead 510 of build material 32 is pushed in front of a moving rod over a stationary bed. For the sake of convenience, the system is shown in the frame of the rod with a moving bed 520 and stationary bead. The bed is assumed to approach the spreader, and the bead of build material circulates around a nearly stationary center. One may assume that the build material is lifted by the leading surface of the spreader rod because it adheres to the rod surface 530. The direction of the flow of the build material reverses close to a nip 540, i.e., an interface between the spreading roller 500 and the moving bed 520. [0090] The equilibrium of a small printed feature as it passes directly underneath the spreader rod is analyzed. On typical three-dimensional printers, the thickness t of a single printed layer of build material 32 is approximately Vioo the radius of the spreader rod.
Referring to Figure 7a, the spreader exerts a compressive stress σ∞ and a shear stress τxz on the build material directly underneath it. There is also a horizontal stress component σxx. [0091] One may assume that the horizontal stress applied to the left edge 600 of the feature is not opposed by another stress on the right edge 610. The feature is assumed to leave a wake 1620 behind it where build material, after being swept along the upper surface, is unable to wrap around the downstream corner and establish a stress analogous to hydrostatic pressure against the right surface. The horizontal stress applied to the left may be opposed by a shear stress along the bottom surface. A free body diagram of the feature is shown in Figure 7b, including a hollow cavity 630 formed in the feature wake 620. [0092] It is assumed here that dry, free-flowing particulate build material in motion possesses a different shear strength than build material that has been allowed to rest for a time. In general, one may expect a different yield locus for build material in different states of motion. For purposes of this derivation, this is expressed here as two different sets of yield parameters, "static" and "dynamic" values of the cohesion and friction angle. [0093] These properties of particulate materials are amply supported in the literature. See, for example, B.M. Das, Advanced Soil Mechanics, Hemisphere Pr. 1997, pp. 315-317 or S. Aranson & L. S. Tsimring in The Physics of Granular Media, H. Hinrichsen & D. Wolf, eds, Wiley-VCH, (2004) pp. 146-147, incorporated herein by reference in their entireties. [0094] A force balance on the feature shown in Figure 8 leads to the equation:
I [Cs - cd + σzz (tanφs - tanφa) ] = L Δτ > tσxx (1)
for the feature to remain in place. The normal stress against the bottom surface of the feature is assumed the same as that against the top surface. The difference in shear strength between the static values (static yield locus 700) and dynamic values (dynamic yield locus 710) with normal stress σzz is denoted by Δτ . [0095] "Bredt flow parameter" (Br) is herein defined, expressing, in general, the propensity for printed features to shift in the build area of a three-dimensional printer during spreading of build material:
Δτ /σxx = Br > t / L * 0.1 (2)
[0096] The ratio t/L is slightly arbitrary. One may assume for practical purposes that features with a length at least several times the layer thickness ( L ~ 10 times t) are those that are preferably considered in this model. Layers with thickness of 100 μm are standard in three- dimensional printing machines that are currently available, and instability of isolated patches smaller than 1.0 mm may have a minimally discernable effect on the appearance of an article. [0097] For the flow conditions most useful for three dimensional printing, the build material is non-cohesive, i.e., the cohesion of the particulate material is much less than the dynamic pressure of material in flow. Using reasonable values for the bulk density of the build material and spreading speed in a standard ZPrinter®310 three-dimensional printer, one obtains an order of magnitude estimate :
Cs « cd « p(u+ωa)2 « 600 Pa (3)
[0098] A material having shear strength of this magnitude is a weak gel, such as yogurt. While it is not "strong" in any sense of the word, it is by no means "free-flowing." As an additional estimate of the lower bound of the cohesion, we may observe that the bead of free- flowing particulate build material may be in a state of yielding at the bottom of the pile when the counter-roller begins to move it across the build area. In a ZPrinter®310 three-dimensional printer, the bead is approximately 1 cm tall. Accordingly, we require the following inequality to hold:
cs « cd « pgh « 100 Pa (4)
[0099] This is typically a minimum acceptable range for cohesion in a particulate build material for it to be considered "free-flowing." While the compressive and shear stress imposed on the build material through the motion of the counter-roller may have a magnitude approximately 600 Pa, the cohesion is preferably accordingly less than 100 Pa in order for it not to adversely affect the layering of build material. [0100] With the assumption that the cohesion is negligibly small, the following simplification may be made: ( tanφs - tanφd ) > t σ∞ / L σ∑z (5)
and
σ XwX (l+sinφd) σzz (l-sinφd) (6)
This leads to the equation:
Equation 7 expresses a vitally important feature of free-flowing particulate build materials that are suitable for use in three-dimensional printing machines. The quantity on the left, Brnc, is termed the "Bredt flow parameter for noncohesive particulate materials," and it preferably has a value greater than about V10 for small printed features to remain stationary during spreading.
Measurement of static and dynamic friction coefficients
[0101] Methods exist for measuring the static yield properties of particulate materials in shear. See, for example, B.M. Das, Advanced Soil Mechanics, Hemisphere Pr. 1997, pp 313- 326. It is found, however, that the values for the yield parameters φ and c vary with experimental conditions, and it is preferable to measure the properties in a particular stress range of interest. [0102] An example of a piece of laboratory equipment that is capable of measuring the static friction characteristics of particulate materials is the "ShearScan TS 12" manufactured by Sci- Tec Inc. This device holds a sample of material in a cylindrical cell and applies a vertical load to the material to consolidate it to a specified level. The device then applies a gradually increasing transverse shearing force until it detects slip in the sample of material. It performs this measurement across a range of applied loads to develop a yield locus analogous to those pictured in Figure 8. Since the instrument measures the shear stress at the instant of rupture, this is the "static" friction in the particulate material.
[0103] An approximate laboratory procedure may provide estimates of the flow parameter for non-cohesive particulate build materials. This may be done by measuring the angle of repose of a pile of a particulate material under static and dynamic conditions. The procedure is executed as follows. On an unpolished type 304 stainless steel sheet with a 2B mill finish and a dimension of 12 inches square by 0.060 inches in thickness available from McMaster-Carr
based in Elmhurst , IL, a conical pile is formed from a particulate material sample by sprinkling particles very slowly at a bulk volumetric flow rate of 30 ± 15 mL per minute over one point using a 385 mL stainless steel funnel available from Lab Safety Supply in Janesville, WI from a height of about 1 cm above the growing top of the pile. The height of the pile is chosen such that gh « (u+ωa)2
This ensures that the stress at the bottom of the heap is in approximately the appropriate range. For ordinary three-dimensional printers manufactured by Z Corporation, this height is roughly 2 inches. [0104] The initial diameter, d, and height, h, of the pile are measured. The ratio 2h/d is an approximate measure of the static friction coefficient tan φs. Next, a small impact force delivered from an 18-8 stainless steel slotted spring pin, Vi inch in diameter and 2.25 inches long with a mass of 32.0 ± 0.5 grams available from McMaster-Carr dropped onto the edge of the stainless steel sheet from a height of 0.65 ± 0.02 inches so the pile collapses. It is typically preferable to deliver to the plate a relatively light impact so that the motion of the pile after the impact is primarily driven by gravity and not by kinetic energy. Two impacts may be sufficient. The final height and diameter of the collapsed pile are measured, and the ratio 2h/d is an approximate measure of the dynamic friction coefficient tan φa- [0105] Several particulate samples were measured in this manner, and the data are presented below in Table 9. The calculated flow parameter is the "noncohesive" form given in equation 7.
Table 9. Measurements of flow parameter for various candidate particulate build materials
• zplOO and zpl30 are products marketed by Z Corporation for building appearance models.
• 4F Lucite from Ineos Acrylics has a particle size between 55 μm and 70 μm.
• Tabular 50 μm Al2O3 acquired from KC Industries
• Glass Beads from Potter's Industries, 72 μm grain size, aminosilane surface treatment
• Neobee M20 was used to coat glass beads. Neobee M20 from Stepan Industries
[0106] As these data approximately show, build materials designed by Z Corporation for three dimensional printing all fall in the same range, a little bit higher than the required lower bound. Some scatter in the results is to be expected with this approximate technique. Although the static angle of repose of zplOO is higher than in zpl30, the flow parameter for the two build materials is nearly the same. In fact, qualitative experience shows that these two products perform about the same.
[0107] Of the other three materials tested, glass spheres alone had the poorest performance, with a flow parameter of only about 0.05. This, too, is supported by qualitative experience: glass beads alone are unsuitable for three dimensional printing from the standpoint of spreading. However, glass beads may be mixed with various processing aids and with other particulate materials that may be finer or equal to in particle size having a non-spherical and irregular particle shape to achieve a desirable Bredt parameter greater than 0.10, thereby being suitable for use in three dimensional printing.
[0108] To illustrate the extreme sensitivity of particulate behavior with even small additions of certain chemicals, generally referred to as "processing aids," a series of data were taken in which tiny (10 ppm) increments of a low- viscosity emulsifier are added to a sample of glass spheres. The flow parameter rises quickly, peaks, and falls away even more quickly even though both the static and dynamic friction angles increase through the series. The critical point occurs when the dynamic angle of repose transitions from a nearly constant value to a linearly increasing value. This shows that there can be rather sharp optima in composition to obtain useful spreading characteristics. [0109] This test is a fairly useful technique for identifying relative performance properties between different candidate materials. The preferred method for evaluating flow properties of candidate build materials during formal optimization after the initial selection period is to test samples of the material on a working three-dimensional printer. Certain pathological geometries are known to those experienced in the art, and they can be evaluated either qualitatively or quantitatively. One particularly useful geometry for observing stability during spreading is a flat plate studded with pegs that are oriented downward during the build. During printing, the earliest layers addressed are a series of disconnected patches that are relatively free to shift in the build material. After these have been formed, a plate is printed that joins all of the pegs together in a single object. One can easily examine whether the pegs are uniform and straight, and one can evaluate the quality of spreading on that basis.
Additional Flow Properties of Build Materials
[0110] Compositions have been disclosed that relate to control of the flow properties of the build material in three-dimensional printers. The three principal methods are the addition of liquid "processing aids," control of grain size distribution, and the addition of solid fillers that contribute to the frictional behavior of the build material. Many candidate materials have been disclosed previously, for example, in U.S. Patent Publication Number 2005/0003189. Some mechanical properties of dry particulate build materials are disclosed in the following discussion that are particularly suited for use in three dimensional printing, especially in contrast to other formulations of similar materials for other uses that do not require special flow characteristics of the raw materials.
[0111] A method that may be used to quantify a particulate material's suitability for three dimensional printing includes placing 1 liter in bulk volume of a particulate material in a metal cylinder with an inside dimension of 6.1 inches, and inside height of 6.2 inches so that the height of the powder is between 2.5 to 3.0 inches when the cylinder is capped with a translucent cover and laid on its side (i.e., the height of the cylinder is horizontal). The drum is then slowly rolled with a rotational velocity of 2.5 rotations/min ± 0.5 rotations/min until the powder reaches an angle where it avalanches upon itself. The distance that the drum rolled, s, is recorded and the angle, φ, can be determined from equation 8:
180
* - -' π (8) where r would equal the outside radius of the drum. The angle, φ, is the internal angle of friction that particulate material has under these particular test conditions at a room temperature between 65 to 75°F. Various particulate materials known to have good and bad spreading characteristics are compared using this test method, and desirable range of internal angles of friction were determined. Table 10 summarizes the particulate material compositions that were measured.
Table 10
Based on the results indicated in Table 10, one can conclude that powders that have an internal angle of friction greater than 40° and less than 70° are suitable for three dimensional printing in systems that use layers on the order of 125 μm.
[0112] Figure 9a is an exemplary CAD drawing of a test geometry that exhibits the distortion caused by the dragging of an article in a powder that is too flowable. Figures 9b and 9c are surface finish scans from a VIKING laser profilometer from Solarius. The figures show a 3D topographical representation of articles formed by three dimensional printing. In Figure 9b, a scan of an article made with zpl31 from Z Corporation exhibits smooth, even contours that closely follow the intended CAD data. Figure 9c is a scan of a typically "too flowable" powder with an internal friction angle <40°; the powder is too flowable and unable to resist the spreading forces causing previously printed layers to be displaced, resulting in an article that has a rough and uneven surface finish, or even has displaced artifacts missing from the surface of the article. The arrow in Figure 9c shows where geometry has shifted during printing.
[0113] Figure 10a is a CAD drawing of the formed article illustrated in Figures 10b and 10c. Referring to Figure 10b, as one may expect, a particulate material with an internal angle of friction that is between 40° and 70°, e.g., zpl31, provides a smoother finish than a particulate material with an internal angle of friction greater than 70° (Figure 10c) where the powder is too cohesive to spread an even layer of particulate material, resulting in an article that has a rough and uneven surface finish.
[0114] This test, i.e., determination of an internal angle of friction, is a useful technique for identifying relative performance properties between different candidate materials. The preferred method for evaluating flow properties of candidate build materials during formal optimization after initial selection is to test samples of the material on a working three- dimensional printer. Certain pathological geometries are known to those experienced in the art, and they can be evaluated either qualitatively or quantitatively. One particularly useful article for observing stability during spreading is a flat plate studded with pegs that are oriented downward during the build. During printing, the earliest layers addressed are a series of disconnected patches that are relatively free to shift in the build material. After these have been formed, a plate is printed that joins all of the pegs together in a single object. One can easily examine whether the pegs are uniform and straight, and one can evaluate the quality of spreading on that basis. [0115] Those skilled in the art will readily appreciate that all parameters listed herein are meant to be exemplary and actual parameters depend upon the specific application for which the methods and materials of the present invention are used. It is, therefore, to be understood that the foregoing embodiments are presented by way of example only and that, within the scope of the appended claims and equivalents thereto, the invention may be practiced otherwise than as specifically described. [0116] What is claimed is:
Claims
1. A powder material system for three dimensional printing comprising: a substantially dry particulate material including: an aqueous-insoluble thermoplastic particulate material, plaster, and a water-soluble adhesive, wherein the dry particulate material is suitable for use in three dimensional printing to form an article comprising a plurality of layers, the layers including a reaction product of the particulate material and an aqueous fluid that contacts the particulate material during three dimensional printing.
2. The material system of claim 1, wherein a static and a dynamic friction coefficient of the particulate material possess a relationship defined by a Bredt parameter having a value in excess of 0.1.
3. The material system of claim 1 , wherein an internal angle of friction of the particulate material is selected from a range of 40° to 70°.
4. The material system of claim 1, wherein the particulate material comprises about 5% - 50% by weight of the aqueous-insoluble thermoplastic, about 25 - 90% by weight of the plaster, and about 5 - 30 % by weight of the water-soluble adhesive.
5. The material system of claim 1, wherein the aqueous-insoluble thermoplastic is selected from the group consisting of high molecular weight polyethylene, polyamide, poly-cyclic- olefins, and combinations thereof.
6. The material system of claim 1, wherein the particulate material further comprises a processing aid.
7. A kit comprising: a substantially dry particulate material including: an aqueous-insoluble thermoplastic particulate material, plaster, and a water-soluble adhesive; an aqueous fluid binder; and an infiltrant.
8. The kit of claim 7, wherein the infiltrant comprises 0-99.99% by weight hydroxylated hydrocarbon, 0-99.99% by weight a solid wax, 0-99.99% by weight a plasticizer, and 0.01-5% by weight a stabilizer.
9. The kit of claim 8, wherein the hydroxylated hydrocarbon comprises a hydrocarbon diol with a molecular weight greater than 1 18 g/mol, a melting point greater than 30°C, and a kinematic viscosity of less than or equal to 150 centiStokes at a temperature of at least 50°C.
10. The kit of claim 9, wherein the hydrocarbon diol comprises octane diol.
11. The kit of claim 9, wherein the hydrocarbon diol comprises decane diol.
12. The kit of claim 7, wherein the infiltrant comprises hydroxylated hydrocarbon including (i) a hydrocarbon diol with a molecular weight greater than 118 g/mol and a melting point greater than 30°C and (ii) a plasticizer.
13. The kit of claim 12, wherein the hydroxylated hydrocarbon comprises decane diol.
14. The kit of claim 12, wherein the plasticizer comprises benzene sulfonamide.
15. The kit of claim 12, wherein the plasticizer comprises propylene carbonate.
16. The kit of claim 8, wherein the hydroxylated hydrocarbon comprises an alcohol having a boiling point selected from a range of 25°C to 1000C, and the plasticizer has a boiling point selected from a range of 25°C to 1000C.
17. The kit of claim 16, wherein the alcohol comprises isopropanol.
18. The kit of claim 16, wherein the plasticizer comprises ethanol.
19. A method for forming an article by three dimensional printing, the method comprising the steps of: providing a particulate material comprising a plurality of adjacent particles, the particulate material comprising an aqueous-insoluble thermoplastic; applying to at least some of the plurality of particles an aqueous fluid binder in an amount sufficient to bond those particles together to define the article; and immersing the article in a liquid infiltrant medium.
20. The method of claim 19, wherein the liquid infiltrant medium comprises a hydroxylated hydrocarbon.
21. The method of claim 20, wherein the liquid infiltrant medium further comprises a plasticizer.
22. The method of claim 19, wherein the particulate material further comprises at least one of plaster, a water-soluble adhesive, a retarder, an accelerator, and a processing aid.
23. An essentially solid article manufactured by a three-dimensional printing process, the essentially solid article comprising a product of the reaction of a mixture comprising: a particulate material including an aqueous-insoluble thermoplastic particulate material, plaster, and a water-soluble adhesive; an aqueous fluid comprising water, a humectant, a rheology modifier, a surfactant, a preservative, and an optical brightening agent, and an infiltrant comprising a hydroxylated hydrocarbon, a wax, a plasticizer, and a stabilizer,
wherein the aqueous-insoluble thermoplastic particulate material is plasticized by the infiltrant.
24. An article comprising: a product of: a substantially dry particulate material including: an aqueous-insoluble thermoplastic particulate material, plaster, and a water-soluble adhesive; and
an infiltrant.
25. The article of claim 24, wherein the article has a strength of at least 5 MPa.
26. The article of claim 25, wherein the article has a strength of at least 15 MPa.
27. The article of claim 26, wherein the article has a strength of at least 20 MPa.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US90278207P | 2007-02-22 | 2007-02-22 | |
US60/902,782 | 2007-02-22 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2008103450A2 true WO2008103450A2 (en) | 2008-08-28 |
WO2008103450A3 WO2008103450A3 (en) | 2008-12-31 |
Family
ID=39710671
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2008/002362 WO2008103450A2 (en) | 2007-02-22 | 2008-02-22 | Three dimensional printing material system and method using plasticizer-assisted sintering |
Country Status (2)
Country | Link |
---|---|
US (2) | US7968626B2 (en) |
WO (1) | WO2008103450A2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103847104A (en) * | 2014-03-10 | 2014-06-11 | 天津大学 | Three-dimensional waxing printer and using method thereof |
US10265910B2 (en) | 2010-10-27 | 2019-04-23 | Rize Inc. | Process and apparatus for fabrication of three-dimensional objects |
Families Citing this family (48)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2001034371A2 (en) | 1999-11-05 | 2001-05-17 | Z Corporation | Material systems and methods of three-dimensional printing |
WO2008073297A2 (en) | 2006-12-08 | 2008-06-19 | Z Corporation | Three dimensional printing material system and method using peroxide cure |
JP5129267B2 (en) | 2007-01-10 | 2013-01-30 | スリーディー システムズ インコーポレーテッド | 3D printing material system with improved color, article performance and ease of use |
US7968626B2 (en) | 2007-02-22 | 2011-06-28 | Z Corporation | Three dimensional printing material system and method using plasticizer-assisted sintering |
US8406508B2 (en) * | 2008-01-11 | 2013-03-26 | Mark Pollack | Reproducible three dimensional vacuum forming technique |
DE102008058177A1 (en) * | 2008-11-20 | 2010-06-24 | Eos Gmbh Electro Optical Systems | Method for identifying laser sintering powders |
WO2012140658A2 (en) * | 2011-04-10 | 2012-10-18 | Objet Ltd. | System and method for layer by layer printing of an object with support |
WO2013043908A1 (en) * | 2011-09-20 | 2013-03-28 | The Regents Of The University Of California | 3d printing powder compositions and methods of use |
WO2013173733A1 (en) * | 2012-05-18 | 2013-11-21 | 3D Systems, Inc. | Support structures and deposition techniques for 3d printing |
IN2015DN01776A (en) | 2012-09-05 | 2015-05-29 | Aprecia Pharmaceuticals Co | |
US8888480B2 (en) | 2012-09-05 | 2014-11-18 | Aprecia Pharmaceuticals Company | Three-dimensional printing system and equipment assembly |
US9339489B2 (en) | 2013-03-15 | 2016-05-17 | Aprecia Pharmaceuticals Company | Rapid disperse dosage form containing levetiracetam |
CN109908355B (en) | 2013-03-15 | 2022-11-15 | 阿普雷奇亚制药有限责任公司 | Fast dispersing dosage form comprising levetiracetam |
JP6573903B2 (en) | 2014-03-25 | 2019-09-11 | ストラタシス リミテッド | Method and system for producing a layer crossing pattern |
WO2016032891A1 (en) | 2014-08-28 | 2016-03-03 | Incodema3D, LLC | Additive manufacturing device |
US10329428B2 (en) * | 2014-11-12 | 2019-06-25 | Nippon Electric Glass Co., Ltd. | Resin composition for three-dimensional modeling, method for manufacturing three-dimensional modeled object, and inorganic filler particles |
DE102014117519B4 (en) * | 2014-11-28 | 2016-06-09 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Method for producing and checking workpieces and workpiece |
CN107614265A (en) * | 2015-03-25 | 2018-01-19 | 斯特拉塔西斯公司 | The method and system of electrically conductive ink in-situ sintering |
US20180169698A1 (en) * | 2015-06-01 | 2018-06-21 | Zverse ,Inc. | Process for sealing, reinforcing and cosmetically coating cast or 3-d printed gypsum articles |
WO2016197099A1 (en) * | 2015-06-04 | 2016-12-08 | Massachusetts Institute Of Technology | Methods for fabricating low cost 3-d printed parts with expanded material properties |
US9840763B2 (en) | 2015-06-10 | 2017-12-12 | General Electric Company | Method for altering metal surfaces |
US10919217B2 (en) | 2015-07-23 | 2021-02-16 | Hewlett-Packard Development Company, L.P. | Three-dimensional (3D) printing build material composition |
BR112018001609A2 (en) | 2015-08-21 | 2018-09-18 | Aprecia Pharmaceuticals LLC | system and assembly of three-dimensional printing equipment |
JP6074490B1 (en) * | 2015-12-22 | 2017-02-01 | 株式会社ソディック | Laminate modeling apparatus and method for resuming program of additive manufacturing apparatus |
EP3231588A1 (en) * | 2016-04-12 | 2017-10-18 | Evonik Röhm GmbH | Spray-dried soft phase emulsion polymer for the filling of the spandrel in polymer bead layers in binder jetting method |
US9833839B2 (en) * | 2016-04-14 | 2017-12-05 | Desktop Metal, Inc. | Fabricating an interface layer for removable support |
EP3235867A1 (en) * | 2016-04-20 | 2017-10-25 | Evonik Röhm GmbH | Polymer beads from hard phase with domains of a soft phase |
CN108602267B (en) | 2016-05-12 | 2021-05-28 | 惠普发展公司,有限责任合伙企业 | Material group |
US10765658B2 (en) | 2016-06-22 | 2020-09-08 | Mastix LLC | Oral compositions delivering therapeutically effective amounts of cannabinoids |
JP2020506090A (en) * | 2017-02-02 | 2020-02-27 | アイメリーズ タルク アメリカ,インコーポレーテッド | Improving adhesion and coalescence between loads in 3D-printed plastic parts |
US11179904B2 (en) | 2017-04-12 | 2021-11-23 | Hewlett-Packard Development Company, L.P. | Three-dimensional (3D) part finishing system |
WO2019005044A1 (en) * | 2017-06-28 | 2019-01-03 | Hewlett-Packard Development Company, L.P. | Three-dimensional printed part |
US11919246B2 (en) | 2017-07-11 | 2024-03-05 | Daniel S. Clark | 5D part growing machine with volumetric display technology |
US10967578B2 (en) | 2017-07-11 | 2021-04-06 | Daniel S. Clark | 5D part growing machine with volumetric display technology |
CN107417299B (en) * | 2017-09-07 | 2019-10-22 | 南京工业大学 | A kind of aftertreatment technology of 3D printing plastering |
US11351724B2 (en) | 2017-10-03 | 2022-06-07 | General Electric Company | Selective sintering additive manufacturing method |
US11420384B2 (en) | 2017-10-03 | 2022-08-23 | General Electric Company | Selective curing additive manufacturing method |
US11590691B2 (en) | 2017-11-02 | 2023-02-28 | General Electric Company | Plate-based additive manufacturing apparatus and method |
US11254052B2 (en) | 2017-11-02 | 2022-02-22 | General Electric Company | Vatless additive manufacturing apparatus and method |
US10821668B2 (en) | 2018-01-26 | 2020-11-03 | General Electric Company | Method for producing a component layer-by- layer |
US10821669B2 (en) | 2018-01-26 | 2020-11-03 | General Electric Company | Method for producing a component layer-by-layer |
WO2020086074A1 (en) * | 2018-10-24 | 2020-04-30 | Hewlett-Packard Development Company, L.P. | Three-dimensional printing |
US11794412B2 (en) | 2019-02-20 | 2023-10-24 | General Electric Company | Method and apparatus for layer thickness control in additive manufacturing |
US11498283B2 (en) | 2019-02-20 | 2022-11-15 | General Electric Company | Method and apparatus for build thickness control in additive manufacturing |
US11179891B2 (en) | 2019-03-15 | 2021-11-23 | General Electric Company | Method and apparatus for additive manufacturing with shared components |
US11731367B2 (en) | 2021-06-23 | 2023-08-22 | General Electric Company | Drive system for additive manufacturing |
US11826950B2 (en) | 2021-07-09 | 2023-11-28 | General Electric Company | Resin management system for additive manufacturing |
US11813799B2 (en) | 2021-09-01 | 2023-11-14 | General Electric Company | Control systems and methods for additive manufacturing |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6403002B1 (en) * | 1997-05-14 | 2002-06-11 | Buss Muller Technology Gmbh | Method and device for producing a shaped body |
US6416850B1 (en) * | 1996-09-04 | 2002-07-09 | Z Corporation | Three dimensional printing materials system |
US20040038009A1 (en) * | 2002-08-21 | 2004-02-26 | Leyden Richard Noel | Water-based material systems and methods for 3D printing |
US20040056378A1 (en) * | 2002-09-25 | 2004-03-25 | Bredt James F. | Three dimensional printing material system and method |
US20040138336A1 (en) * | 1996-09-04 | 2004-07-15 | Z Corporation | Three dimensional printing material system and method |
WO2005023524A2 (en) * | 2003-08-29 | 2005-03-17 | Z Corporation | Absorbent fillers for three-dimensional printing |
Family Cites Families (388)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US555336A (en) * | 1896-02-25 | James roche | ||
US2156242A (en) | 1935-05-09 | 1939-04-25 | Lilly Co Eli | Ergot derivative and process of obtaining it |
US2296636A (en) | 1938-12-08 | 1942-09-22 | Du Pont | High surface hiding pigment material and process of making the same |
US2522548A (en) | 1946-10-03 | 1950-09-19 | Thoger G Jungersen | Method of making a phosphate gel and mold with phosphate gel binder |
US2662024A (en) | 1951-03-01 | 1953-12-08 | Kaiser Gypsum Company Inc | Cementitious compositions |
US3303147A (en) | 1963-01-15 | 1967-02-07 | Nat Gypsum Co | Dry powder for wallboard joint treatment |
US3297601A (en) | 1963-08-13 | 1967-01-10 | United States Gypsum Co | Substantially dry joint compound comprising calcium sulfate, polyvinyl acetate and starch |
US3309328A (en) | 1964-06-03 | 1967-03-14 | Allied Chem | High strength adhesive for building materials |
CH423346A (en) | 1964-08-27 | 1966-10-31 | Jacques Dr Jenny | Process for the production of a hoof covering, and the covering produced according to this |
US4041476A (en) | 1971-07-23 | 1977-08-09 | Wyn Kelly Swainson | Method, medium and apparatus for producing three-dimensional figure product |
US3525632A (en) | 1967-11-08 | 1970-08-25 | Resco Products Inc | Method for forming a concrete cement composition |
GB1250631A (en) | 1968-01-25 | 1971-10-20 | ||
US3821006A (en) | 1971-04-16 | 1974-06-28 | Dentsply Int Inc | Patching method |
CH1917171A4 (en) | 1971-12-30 | 1975-04-30 | ||
US3852083A (en) | 1972-03-30 | 1974-12-03 | J Yang | Manufacture of plaster of paris products containing latex |
US3930872A (en) | 1973-04-17 | 1976-01-06 | Ashland Oil, Inc. | Binder compositions |
US3835074A (en) | 1973-04-26 | 1974-09-10 | Hercules Inc | Joint cement compositions |
US3870538A (en) | 1973-05-07 | 1975-03-11 | Nat Gypsum Co | Gypsum set accelerator |
US3926870A (en) | 1973-10-15 | 1975-12-16 | Warner Lambert Co | Denture adhesive preparation containing an anionic protein material |
US3932923A (en) | 1974-10-21 | 1976-01-20 | Dynell Electronics Corporation | Method of generating and constructing three-dimensional bodies |
US4078229A (en) | 1975-01-27 | 1978-03-07 | Swanson Wyn K | Three dimensional systems |
GB1498057A (en) | 1975-04-17 | 1978-01-18 | Ass Portland Cement | Hydraulic cements |
US4303556A (en) | 1977-11-02 | 1981-12-01 | The Procter & Gamble Company | Spray-dried detergent compositions |
US4288861A (en) | 1977-12-01 | 1981-09-08 | Formigraphic Engine Corporation | Three-dimensional systems |
CH621597A5 (en) | 1978-02-13 | 1981-02-13 | Epsi Brevets & Participations | |
GB2048235A (en) | 1979-04-25 | 1980-12-10 | Bpb Industries Ltd | Improved Joint Cement |
US4247508B1 (en) | 1979-12-03 | 1996-10-01 | Dtm Corp | Molding process |
US4310996A (en) | 1980-04-23 | 1982-01-19 | General Electric Co. | Cement reinforced gypsum foam with mineral wool |
US4327156A (en) | 1980-05-12 | 1982-04-27 | Minnesota Mining And Manufacturing Company | Infiltrated powdered metal composite article |
DE3041794A1 (en) | 1980-11-06 | 1982-05-13 | Dynamit Nobel Ag, 5210 Troisdorf | METHOD FOR PRODUCING DESSINED MOLDED BODIES FROM A CURABLE DIMENSION BASED ON DUROPLASTIC PLASTICS |
DE3048506C2 (en) | 1980-12-22 | 1986-09-11 | Rigips GmbH, 3452 Bodenwerder | Dry powder plaster mixture and process for its preparation |
EP0077618B1 (en) | 1981-10-15 | 1986-12-17 | Ciba Specialty Chemicals Water Treatments Limited | Adhesives for prepasted wallcoverings |
EP0091262B1 (en) | 1982-04-07 | 1986-03-05 | Adnovum Ag | Heat-activatable multi-component sheet material and process for making same |
US4444594A (en) | 1982-12-09 | 1984-04-24 | Armstrong World Industries, Inc. | Acid cured inorganic binder compositions which are compatible with mineral wool |
US4613627A (en) | 1982-12-13 | 1986-09-23 | Usg Acoustical Products Company | Process for the manufacture of shaped fibrous products and the resultant product |
US4618390A (en) | 1983-06-13 | 1986-10-21 | Ashland Oil, Inc. | Method for preparing laminated articles |
US4755227A (en) | 1983-08-11 | 1988-07-05 | Stauffer Chemical Company | Production of solid phosphorus pentioxide containing materials for fast-setting cements |
DE3439493A1 (en) | 1984-10-27 | 1986-05-07 | Wuertex Maschinenbau Hofmann G | Process for the continuous production of mouldings, in particular slabs, from a mixture of gypsum and fibre material and device for carrying out the process |
GB2155944B (en) | 1984-03-16 | 1988-04-27 | Building Adhesives Ltd | Powder compositions for producing tile adhesives and grouts |
US4665492A (en) | 1984-07-02 | 1987-05-12 | Masters William E | Computer automated manufacturing process and system |
US4575330A (en) | 1984-08-08 | 1986-03-11 | Uvp, Inc. | Apparatus for production of three-dimensional objects by stereolithography |
US5344298A (en) | 1984-08-08 | 1994-09-06 | 3D Systems, Inc. | Apparatus for making three-dimensional objects by stereolithography |
US5571471A (en) | 1984-08-08 | 1996-11-05 | 3D Systems, Inc. | Method of production of three-dimensional objects by stereolithography |
US5236637A (en) | 1984-08-08 | 1993-08-17 | 3D Systems, Inc. | Method of and apparatus for production of three dimensional objects by stereolithography |
US4929402A (en) | 1984-08-08 | 1990-05-29 | 3D Systems, Inc. | Method for production of three-dimensional objects by stereolithography |
US5174943A (en) | 1984-08-08 | 1992-12-29 | 3D Systems, Inc. | Method for production of three-dimensional objects by stereolithography |
JPS62260754A (en) | 1986-05-07 | 1987-11-13 | 三井東圧化学株式会社 | Manufacture of gypsum board |
IL84936A (en) | 1987-12-23 | 1997-02-18 | Cubital Ltd | Three-dimensional modelling apparatus |
ATE113746T1 (en) | 1986-06-03 | 1994-11-15 | Cubital Ltd | DEVICE FOR DEVELOPING THREE-DIMENSIONAL MODELS. |
US5263130A (en) | 1986-06-03 | 1993-11-16 | Cubital Ltd. | Three dimensional modelling apparatus |
US4752352A (en) | 1986-06-06 | 1988-06-21 | Michael Feygin | Apparatus and method for forming an integral object from laminations |
US5017753A (en) | 1986-10-17 | 1991-05-21 | Board Of Regents, The University Of Texas System | Method and apparatus for producing parts by selective sintering |
US5155324A (en) | 1986-10-17 | 1992-10-13 | Deckard Carl R | Method for selective laser sintering with layerwise cross-scanning |
US4863538A (en) | 1986-10-17 | 1989-09-05 | Board Of Regents, The University Of Texas System | Method and apparatus for producing parts by selective sintering |
US5076869A (en) | 1986-10-17 | 1991-12-31 | Board Of Regents, The University Of Texas System | Multiple material systems for selective beam sintering |
US5296062A (en) | 1986-10-17 | 1994-03-22 | The Board Of Regents, The University Of Texas System | Multiple material systems for selective beam sintering |
EP0538244B1 (en) | 1986-10-17 | 1996-05-22 | Board Of Regents, The University Of Texas System | Method and apparatus for producing parts by selective sintering |
US4944817A (en) | 1986-10-17 | 1990-07-31 | Board Of Regents, The University Of Texas System | Multiple material systems for selective beam sintering |
US5147587A (en) | 1986-10-17 | 1992-09-15 | Board Of Regents, The University Of Texas System | Method of producing parts and molds using composite ceramic powders |
US4758278A (en) | 1986-11-28 | 1988-07-19 | E. I. Du Pont De Nemours And Company | Magnesium oxide powder for workable, rapid-setting phosphate-containing cement compositions |
US4801477A (en) | 1987-09-29 | 1989-01-31 | Fudim Efrem V | Method and apparatus for production of three-dimensional objects by photosolidification |
US4752498A (en) | 1987-03-02 | 1988-06-21 | Fudim Efrem V | Method and apparatus for production of three-dimensional objects by photosolidification |
US5287435A (en) | 1987-06-02 | 1994-02-15 | Cubital Ltd. | Three dimensional modeling |
US5386500A (en) | 1987-06-02 | 1995-01-31 | Cubital Ltd. | Three dimensional modeling apparatus |
US5015312A (en) | 1987-09-29 | 1991-05-14 | Kinzie Norman F | Method and apparatus for constructing a three-dimensional surface of predetermined shape and color |
IL84752A (en) | 1987-12-08 | 1991-11-21 | Elscint Ltd | Anatomical models and methods for manufacturing such models |
US4942001A (en) | 1988-03-02 | 1990-07-17 | Inc. DeSoto | Method of forming a three-dimensional object by stereolithography and composition therefore |
US4996282A (en) | 1988-03-24 | 1991-02-26 | Desoto, Inc. | Cationically curable polyurethane compositions having vinyl ether functionality |
US4945032A (en) | 1988-03-31 | 1990-07-31 | Desoto, Inc. | Stereolithography using repeated exposures to increase strength and reduce distortion |
EP0366748A4 (en) | 1988-04-11 | 1991-09-25 | Australasian Lasers Pty. Ltd. | Laser based plastic model making workstation |
US5711911A (en) | 1988-04-18 | 1998-01-27 | 3D Systems, Inc. | Method of and apparatus for making a three-dimensional object by stereolithography |
US5182055A (en) | 1988-04-18 | 1993-01-26 | 3D Systems, Inc. | Method of making a three-dimensional object by stereolithography |
US4999143A (en) | 1988-04-18 | 1991-03-12 | 3D Systems, Inc. | Methods and apparatus for production of three-dimensional objects by stereolithography |
ATE150693T1 (en) | 1988-04-18 | 1997-04-15 | 3D Systems Inc | REDUCING STEREOLITHOGRAPHIC BENDING |
US5015424A (en) | 1988-04-18 | 1991-05-14 | 3D Systems, Inc. | Methods and apparatus for production of three-dimensional objects by stereolithography |
US5184307A (en) | 1988-04-18 | 1993-02-02 | 3D Systems, Inc. | Method and apparatus for production of high resolution three-dimensional objects by stereolithography |
US5059359A (en) | 1988-04-18 | 1991-10-22 | 3 D Systems, Inc. | Methods and apparatus for production of three-dimensional objects by stereolithography |
US4996010A (en) | 1988-04-18 | 1991-02-26 | 3D Systems, Inc. | Methods and apparatus for production of three-dimensional objects by stereolithography |
US5141680A (en) | 1988-04-18 | 1992-08-25 | 3D Systems, Inc. | Thermal stereolighography |
US5495328A (en) | 1988-04-18 | 1996-02-27 | 3D Systems, Inc. | Apparatus and method for calibrating and normalizing a stereolithographic apparatus |
US5076974A (en) | 1988-04-18 | 1991-12-31 | 3 D Systems, Inc. | Methods of curing partially polymerized parts |
US5182056A (en) | 1988-04-18 | 1993-01-26 | 3D Systems, Inc. | Stereolithography method and apparatus employing various penetration depths |
US5137662A (en) | 1988-11-08 | 1992-08-11 | 3-D Systems, Inc. | Method and apparatus for production of three-dimensional objects by stereolithography |
DE354637T1 (en) | 1988-04-18 | 1996-06-27 | 3D Systems Inc | Stereolithographic CAD / CAM data conversion. |
US5267013A (en) | 1988-04-18 | 1993-11-30 | 3D Systems, Inc. | Apparatus and method for profiling a beam |
US5772947A (en) | 1988-04-18 | 1998-06-30 | 3D Systems Inc | Stereolithographic curl reduction |
US5130064A (en) | 1988-04-18 | 1992-07-14 | 3D Systems, Inc. | Method of making a three dimensional object by stereolithography |
US5256340A (en) | 1988-04-18 | 1993-10-26 | 3D Systems, Inc. | Method of making a three-dimensional object by stereolithography |
JP2963478B2 (en) | 1988-04-18 | 1999-10-18 | スリーディー、システムズ、インコーポレーテッド | Method and apparatus for forming a three-dimensional object |
ES2043958T3 (en) * | 1988-06-24 | 1994-01-01 | Pro Mineral Ges | PROCEDURE FOR THE PREPARATION OF A HYDRAULIC BINDING AGENT THAT SOLVES RAPIDLY AFTER Kneading WITH WATER. |
US4844144A (en) | 1988-08-08 | 1989-07-04 | Desoto, Inc. | Investment casting utilizing patterns produced by stereolithography |
US4943928A (en) | 1988-09-19 | 1990-07-24 | Campbell Albert E | Elongated carrier with a plurality of spot-sources of heat for use with stereolithographic system |
US5385772A (en) | 1988-09-19 | 1995-01-31 | Adco Products, Inc. | Pressure-sensitive adhesive systems with filler |
US5174931A (en) | 1988-09-26 | 1992-12-29 | 3D Systems, Inc. | Method of and apparatus for making a three-dimensional product by stereolithography |
US5258146A (en) | 1988-09-26 | 1993-11-02 | 3D Systems, Inc. | Method of and apparatus for measuring and controlling fluid level in stereolithography |
US5637175A (en) | 1988-10-05 | 1997-06-10 | Helisys Corporation | Apparatus for forming an integral object from laminations |
IL88359A (en) | 1988-11-10 | 1993-06-10 | Cubital Ltd | Method and apparatus for volumetric digitization of 3-dimensional objects |
US5171490A (en) | 1988-11-29 | 1992-12-15 | Fudim Efrem V | Method and apparatus for production of three-dimensional objects by irradiation of photopolymers |
US5135379A (en) | 1988-11-29 | 1992-08-04 | Fudim Efrem V | Apparatus for production of three-dimensional objects by photosolidification |
GB8827952D0 (en) | 1988-11-30 | 1989-01-05 | Screen Form Inc | Display device |
IL88626A0 (en) | 1988-12-07 | 1989-07-31 | N C T Limited | Method and apparatus for making three-dimensional objects |
US5089184A (en) | 1989-01-18 | 1992-02-18 | Mitsui Engineering And Shipbuilding Co., Ltd. | Optical molding method |
US5038014A (en) | 1989-02-08 | 1991-08-06 | General Electric Company | Fabrication of components by layered deposition |
US5352310A (en) | 1989-02-17 | 1994-10-04 | Natter Marc D | Actinic activation shaping system and method |
JP2794444B2 (en) * | 1989-03-07 | 1998-09-03 | 日本石油化学株式会社 | Method for producing dibenzylbenzenes |
JP2715527B2 (en) | 1989-03-14 | 1998-02-18 | ソニー株式会社 | 3D shape forming method |
US4942060A (en) | 1989-04-21 | 1990-07-17 | E. I. Du Pont De Nemours And Company | Solid imaging method utilizing photohardenable compositions of self limiting thickness by phase separation |
US5051334A (en) | 1989-04-21 | 1991-09-24 | E. I. Du Pont De Nemours And Company | Solid imaging method using photohardenable compositions containing hollow spheres |
US5128235A (en) | 1989-04-21 | 1992-07-07 | E. I. Du Pont De Nemours And Company | Method of forming a three-dimensional object comprising additives imparting reduction of shrinkage to photohardenable compositions |
US5011635A (en) | 1989-05-18 | 1991-04-30 | Desoto, Inc. | Stereolithographic method and apparatus in which a membrane separates phases |
GB2233928B (en) | 1989-05-23 | 1992-12-23 | Brother Ind Ltd | Apparatus and method for forming three-dimensional article |
US5143663A (en) | 1989-06-12 | 1992-09-01 | 3D Systems, Inc. | Stereolithography method and apparatus |
US5248456A (en) | 1989-06-12 | 1993-09-28 | 3D Systems, Inc. | Method and apparatus for cleaning stereolithographically produced objects |
US5216616A (en) | 1989-06-26 | 1993-06-01 | Masters William E | System and method for computer automated manufacture with reduced object shape distortion |
US5134569A (en) | 1989-06-26 | 1992-07-28 | Masters William E | System and method for computer automated manufacturing using fluent material |
JPH0336019A (en) | 1989-07-03 | 1991-02-15 | Brother Ind Ltd | Three-dimensional molding method and device thereof |
JPH0624773B2 (en) | 1989-07-07 | 1994-04-06 | 三井造船株式会社 | Optical modeling method |
US5096491A (en) | 1989-07-19 | 1992-03-17 | Honshu Paper Co., Ltd. | Aqueous starch slurry adhesive |
US5053090A (en) | 1989-09-05 | 1991-10-01 | Board Of Regents, The University Of Texas System | Selective laser sintering with assisted powder handling |
JPH03244528A (en) | 1989-09-28 | 1991-10-31 | Three D Syst Inc | Device and method forming substantially flat and solid face for processing planograph |
US5234636A (en) | 1989-09-29 | 1993-08-10 | 3D Systems, Inc. | Methods of coating stereolithographic parts |
US5632848A (en) | 1989-10-12 | 1997-05-27 | Georgia-Pacific Corporation | Continuous processing equipment for making fiberboard |
US5088047A (en) | 1989-10-16 | 1992-02-11 | Bynum David K | Automated manufacturing system using thin sections |
US5182715A (en) | 1989-10-27 | 1993-01-26 | 3D Systems, Inc. | Rapid and accurate production of stereolighographic parts |
DE59007720D1 (en) | 1989-10-27 | 1994-12-22 | Ciba Geigy Ag | Method for tuning the radiation sensitivity of photopolymerizable compositions. |
US5133987A (en) | 1989-10-27 | 1992-07-28 | 3D Systems, Inc. | Stereolithographic apparatus and method |
US5121329A (en) | 1989-10-30 | 1992-06-09 | Stratasys, Inc. | Apparatus and method for creating three-dimensional objects |
US5135695A (en) | 1989-12-04 | 1992-08-04 | Board Of Regents The University Of Texas System | Positioning, focusing and monitoring of gas phase selective beam deposition |
US5017317A (en) | 1989-12-04 | 1991-05-21 | Board Of Regents, The Uni. Of Texas System | Gas phase selective beam deposition |
US5169579A (en) | 1989-12-04 | 1992-12-08 | Board Of Regents, The University Of Texas System | Catalyst and plasma assisted nucleation and renucleation of gas phase selective laser deposition |
US5387380A (en) | 1989-12-08 | 1995-02-07 | Massachusetts Institute Of Technology | Three-dimensional printing techniques |
US5204055A (en) | 1989-12-08 | 1993-04-20 | Massachusetts Institute Of Technology | Three-dimensional printing techniques |
US5009585A (en) | 1989-12-18 | 1991-04-23 | Mitsui Engineering & Shipbuilding Co., Ltd. | Optical molding apparatus and movable base device therefor |
US5143817A (en) | 1989-12-22 | 1992-09-01 | E. I. Du Pont De Nemours And Company | Solid imaging system |
US5139711A (en) | 1989-12-25 | 1992-08-18 | Matsushita Electric Works, Ltd. | Process of and apparatus for making three dimensional objects |
US5236812A (en) | 1989-12-29 | 1993-08-17 | E. I. Du Pont De Nemours And Company | Solid imaging method and apparatus |
CA2075384C (en) | 1990-02-06 | 2004-04-20 | Karl Tiefenbacher | Process of producing rottable thin-walled shaped bodies made of starch |
US5071337A (en) | 1990-02-15 | 1991-12-10 | Quadrax Corporation | Apparatus for forming a solid three-dimensional article from a liquid medium |
US5358673A (en) | 1990-02-15 | 1994-10-25 | 3D Systems, Inc. | Applicator device and method for dispensing a liquid medium in a laser modeling machine |
US5338611A (en) | 1990-02-20 | 1994-08-16 | Aluminum Company Of America | Method of welding thermoplastic substrates with microwave frequencies |
US5626919A (en) | 1990-03-01 | 1997-05-06 | E. I. Du Pont De Nemours And Company | Solid imaging apparatus and method with coating station |
US5693144A (en) | 1990-03-19 | 1997-12-02 | 3D Systems, Inc. | Vibrationally enhanced stereolithographic recoating |
FR2659971B1 (en) | 1990-03-20 | 1992-07-10 | Dassault Avions | PROCESS FOR PRODUCING THREE-DIMENSIONAL OBJECTS BY PHOTO-TRANSFORMATION AND APPARATUS FOR CARRYING OUT SUCH A PROCESS. |
DE4012044A1 (en) | 1990-04-13 | 1991-10-17 | Heidelberger Zement Ag | Prodn. of moulds-models etc., for ceramic industry - made of absorbent core material coated with wear-resistant material |
US5094935A (en) | 1990-06-26 | 1992-03-10 | E. I. Dupont De Nemours And Company | Method and apparatus for fabricating three dimensional objects from photoformed precursor sheets |
GB9123070D0 (en) | 1991-10-30 | 1991-12-18 | Domino Printing Sciences Plc | Ink |
US5096530A (en) | 1990-06-28 | 1992-03-17 | 3D Systems, Inc. | Resin film recoating method and apparatus |
US5175077A (en) | 1990-07-05 | 1992-12-29 | E. I. Du Pont De Nemours And Company | Solid imaging system using photohardening inhibition |
US5158858A (en) | 1990-07-05 | 1992-10-27 | E. I. Du Pont De Nemours And Company | Solid imaging system using differential tension elastomeric film |
US5248249A (en) | 1990-07-27 | 1993-09-28 | Sony Corporation | Three-dimensional structure forming apparatus provided with a liquid-level control system for a main resin tank |
US5127037A (en) | 1990-08-15 | 1992-06-30 | Bynum David K | Apparatus for forming a three-dimensional reproduction of an object from laminations |
US5342566A (en) | 1990-08-23 | 1994-08-30 | Carl Schenck Ag | Method of manufacturing fiber gypsum board |
US5192559A (en) | 1990-09-27 | 1993-03-09 | 3D Systems, Inc. | Apparatus for building three-dimensional objects with sheets |
US5569349A (en) | 1990-10-04 | 1996-10-29 | 3D Systems, Inc. | Thermal stereolithography |
US5198159A (en) | 1990-10-09 | 1993-03-30 | Matsushita Electric Works, Ltd. | Process of fabricating three-dimensional objects from a light curable resin liquid |
US5204124A (en) | 1990-10-09 | 1993-04-20 | Stanley Secretan | Continuous extruded bead object fabrication apparatus |
US5122441A (en) | 1990-10-29 | 1992-06-16 | E. I. Du Pont De Nemours And Company | Method for fabricating an integral three-dimensional object from layers of a photoformable composition |
US5597520A (en) | 1990-10-30 | 1997-01-28 | Smalley; Dennis R. | Simultaneous multiple layer curing in stereolithography |
US5192469A (en) | 1990-10-30 | 1993-03-09 | 3D Systems, Inc. | Simultaneous multiple layer curing in stereolithography |
US5209878A (en) | 1990-10-30 | 1993-05-11 | 3D Systems, Inc. | Surface resolution in three-dimensional objects by inclusion of thin fill layers |
US5238639A (en) | 1990-10-31 | 1993-08-24 | 3D Systems, Inc. | Method and apparatus for stereolithographic curl balancing |
US5155321A (en) | 1990-11-09 | 1992-10-13 | Dtm Corporation | Radiant heating apparatus for providing uniform surface temperature useful in selective laser sintering |
US5328539A (en) | 1990-11-28 | 1994-07-12 | H. B. Fuller Licensing & Financing Inc. | Radio frequency heating of thermoplastic receptor compositions |
US5182134A (en) | 1990-11-28 | 1993-01-26 | H. B. Fuller Licensing & Financing Inc. | Radio frequency cure of thermoset-receptor compositions |
US5167882A (en) | 1990-12-21 | 1992-12-01 | Loctite Corporation | Stereolithography method |
US5286573A (en) | 1990-12-03 | 1994-02-15 | Fritz Prinz | Method and support structures for creation of objects by layer deposition |
JP3046436B2 (en) | 1990-12-17 | 2000-05-29 | 株式会社東芝 | Ceramic capacitors |
US5460758A (en) | 1990-12-21 | 1995-10-24 | Eos Gmbh Electro Optical Systems | Method and apparatus for production of a three-dimensional object |
JP2597778B2 (en) | 1991-01-03 | 1997-04-09 | ストラタシイス,インコーポレイテッド | Three-dimensional object assembling system and assembling method |
US5740051A (en) | 1991-01-25 | 1998-04-14 | Sanders Prototypes, Inc. | 3-D model making |
US5506607A (en) | 1991-01-25 | 1996-04-09 | Sanders Prototypes Inc. | 3-D model maker |
EP0500225B1 (en) | 1991-01-31 | 1995-12-06 | Texas Instruments Incorporated | Method and system for computer-controlled manufacture of three dimensional objects from computer data |
US5594652A (en) | 1991-01-31 | 1997-01-14 | Texas Instruments Incorporated | Method and apparatus for the computer-controlled manufacture of three-dimensional objects from computer data |
US5474719A (en) | 1991-02-14 | 1995-12-12 | E. I. Du Pont De Nemours And Company | Method for forming solid objects utilizing viscosity reducible compositions |
US5176188A (en) | 1991-02-14 | 1993-01-05 | E. I. Du Pont De Nemours And Company | Investment casting method and pattern material comprising thermally-collapsible expanded microspheres |
US5217653A (en) | 1991-02-18 | 1993-06-08 | Leonid Mashinsky | Method and apparatus for producing a stepless 3-dimensional object by stereolithography |
WO1992015620A1 (en) | 1991-02-27 | 1992-09-17 | Allied-Signal Inc. | Stereolithography using vinyl ether based polymers |
US5204823A (en) | 1991-03-20 | 1993-04-20 | Calcomp Inc. | Method and apparatus for high-speed layer thickness curing in 3-D model making |
EP0509523B1 (en) | 1991-04-19 | 1996-03-06 | Fuji Photo Film Co., Ltd. | Direct-image type lithographic printing plate precursor |
US5173220A (en) | 1991-04-26 | 1992-12-22 | Motorola, Inc. | Method of manufacturing a three-dimensional plastic article |
US5510226A (en) | 1991-05-01 | 1996-04-23 | Alliedsignal Inc. | Stereolithography using vinyl ether-epoxide polymers |
NL193122C (en) | 1991-05-01 | 1998-11-03 | Allied Signal Inc | Stereolithography using vinyl ether epoxide polymers. |
US5157423A (en) | 1991-05-08 | 1992-10-20 | Cubital Ltd. | Apparatus for pattern generation on a dielectric substrate |
US5238614A (en) | 1991-05-28 | 1993-08-24 | Matsushita Electric Words, Ltd., Japan | Process of fabricating three-dimensional objects from a light curable resin liquid |
US5154762A (en) | 1991-05-31 | 1992-10-13 | Minnesota Mining And Manufacturing Company | Universal water-based medical and dental cement |
US5278442A (en) | 1991-07-15 | 1994-01-11 | Prinz Fritz B | Electronic packages and smart structures formed by thermal spray deposition |
JPH0525898A (en) | 1991-07-23 | 1993-02-02 | Yayoi Kagaku Kogyo Kk | Surface preparation agent and execution of work therewith |
US5207371A (en) | 1991-07-29 | 1993-05-04 | Prinz Fritz B | Method and apparatus for fabrication of three-dimensional metal articles by weld deposition |
US5677107A (en) | 1991-10-02 | 1997-10-14 | Spectra Group Limited, Inc. | Production of three-dimensional objects |
US5203944A (en) | 1991-10-10 | 1993-04-20 | Prinz Fritz B | Method for fabrication of three-dimensional articles by thermal spray deposition using masks as support structures |
DE4134265C2 (en) | 1991-10-16 | 1993-11-25 | Eos Electro Optical Syst | Device and method for producing a three-dimensional object by means of stereography |
US5279665A (en) | 1991-10-30 | 1994-01-18 | Ashland Oil, Inc. | Inorganic foundry binder systems and their uses |
US5252264A (en) | 1991-11-08 | 1993-10-12 | Dtm Corporation | Apparatus and method for producing parts with multi-directional powder delivery |
US5348693A (en) | 1991-11-12 | 1994-09-20 | Advanced Cardiovascular Systems, Inc. | Formation of three dimensional objects and assemblies |
US5314003A (en) | 1991-12-24 | 1994-05-24 | Microelectronics And Computer Technology Corporation | Three-dimensional metal fabrication using a laser |
US5247180A (en) | 1991-12-30 | 1993-09-21 | Texas Instruments Incorporated | Stereolithographic apparatus and method of use |
US5345414A (en) | 1992-01-27 | 1994-09-06 | Rohm Co., Ltd. | Semiconductor memory device having ferroelectric film |
US5545367A (en) | 1992-04-15 | 1996-08-13 | Soane Technologies, Inc. | Rapid prototype three dimensional stereolithography |
US5432045A (en) | 1992-05-28 | 1995-07-11 | Cmet, Inc. | Photo-solidification modeling apparatus and photo-solidification modeling method having an improved recoating process |
FR2691818B1 (en) | 1992-06-02 | 1997-01-03 | Alsthom Cge Alcatel | METHOD FOR MANUFACTURING A FRACTAL OBJECT BY STEREOLITHOGRAPHY AND FRACTAL OBJECT OBTAINED BY SUCH A PROCESS. |
FR2692065A1 (en) | 1992-06-05 | 1993-12-10 | Laser Int Sa | Process for the production of industrial parts by the action of light on a liquid polymerizable or crosslinkable material without the need for supports. |
US5365996A (en) | 1992-06-10 | 1994-11-22 | Amei Technologies Inc. | Method and apparatus for making customized fixation devices |
US5306446A (en) | 1992-07-10 | 1994-04-26 | Howe Robert J | Apparatus with roller and for irradiation of photopolymers |
DE69315003T2 (en) | 1992-07-17 | 1998-03-12 | Ethicon Inc | Radiation-curable urethane-acrylate prepolymers and cross-linked polymers |
US5281789A (en) | 1992-07-24 | 1994-01-25 | Robert Merz | Method and apparatus for depositing molten metal |
US5506046A (en) | 1992-08-11 | 1996-04-09 | E. Khashoggi Industries | Articles of manufacture fashioned from sheets having a highly inorganically filled organic polymer matrix |
NZ255666A (en) | 1992-08-11 | 1997-04-24 | Khashoggi E Ind | Food/drink containers formed from a hydraulically settable binder, water and a rheology-modifying agent |
US5660900A (en) | 1992-08-11 | 1997-08-26 | E. Khashoggi Industries | Inorganically filled, starch-bound compositions for manufacturing containers and other articles having a thermodynamically controlled cellular matrix |
US5512162A (en) | 1992-08-13 | 1996-04-30 | Massachusetts Institute Of Technology | Method for photo-forming small shaped metal containing articles from porous precursors |
US5370692A (en) | 1992-08-14 | 1994-12-06 | Guild Associates, Inc. | Rapid, customized bone prosthesis |
JPH06114948A (en) | 1992-10-01 | 1994-04-26 | Shiimetsuto Kk | Optically curable molded form with uncured liquid outlet and molding method therefor |
DE4233812C1 (en) | 1992-10-07 | 1993-11-04 | Eos Electro Optical Syst | METHOD AND DEVICE FOR PRODUCING THREE-DIMENSIONAL OBJECTS |
US5264061A (en) | 1992-10-22 | 1993-11-23 | Motorola, Inc. | Method of forming a three-dimensional printed circuit assembly |
US5603797A (en) | 1992-11-16 | 1997-02-18 | E-Systems, Inc. | Flexible reinforced rubber part manufacturing process utilizing stereolithography tooling |
US5527877A (en) | 1992-11-23 | 1996-06-18 | Dtm Corporation | Sinterable semi-crystalline powder and near-fully dense article formed therewith |
US5342919A (en) | 1992-11-23 | 1994-08-30 | Dtm Corporation | Sinterable semi-crystalline powder and near-fully dense article formed therewith |
US5648450A (en) | 1992-11-23 | 1997-07-15 | Dtm Corporation | Sinterable semi-crystalline powder and near-fully dense article formed therein |
US5490882A (en) | 1992-11-30 | 1996-02-13 | Massachusetts Institute Of Technology | Process for removing loose powder particles from interior passages of a body |
US5352405A (en) | 1992-12-18 | 1994-10-04 | Dtm Corporation | Thermal control of selective laser sintering via control of the laser scan |
US5430666A (en) | 1992-12-18 | 1995-07-04 | Dtm Corporation | Automated method and apparatus for calibration of laser scanning in a selective laser sintering apparatus |
TW259797B (en) | 1992-12-23 | 1995-10-11 | Ciba Geigy | |
DE4300478C2 (en) | 1993-01-11 | 1998-05-20 | Eos Electro Optical Syst | Method and device for producing a three-dimensional object |
JP2558431B2 (en) | 1993-01-15 | 1996-11-27 | ストラタシイス,インコーポレイテッド | Method for operating system for manufacturing three-dimensional structure and apparatus for manufacturing three-dimensional structure |
DE4302418A1 (en) | 1993-01-28 | 1994-08-11 | Eos Electro Optical Syst | Method and device for producing a three-dimensional object |
US5514378A (en) | 1993-02-01 | 1996-05-07 | Massachusetts Institute Of Technology | Biocompatible polymer membranes and methods of preparation of three dimensional membrane structures |
US5296335A (en) | 1993-02-22 | 1994-03-22 | E-Systems, Inc. | Method for manufacturing fiber-reinforced parts utilizing stereolithography tooling |
TW418346B (en) | 1993-03-05 | 2001-01-11 | Ciba Sc Holding Ag | Photopolymerisable compositions containing tetraacrylates |
JP2805674B2 (en) | 1993-03-22 | 1998-09-30 | ソニー株式会社 | Optical shaping method and optical shaping apparatus |
US5429908A (en) | 1993-04-12 | 1995-07-04 | E. I. Du Pont De Nemours And Company | Exposure method for reducing distortion in models produced through solid imaging by forming a non-continuous image of a pattern which is then imaged to form a continuous hardened image of the pattern |
KR970011573B1 (en) | 1993-04-14 | 1997-07-12 | 마쯔시다덴기산교 가부시기가이샤 | Three dimensional object-forming method |
DE4316184A1 (en) | 1993-05-14 | 1994-11-17 | Hoechst Ag | Process for producing ceramic microstructures from polymeric precursors |
US5450205A (en) | 1993-05-28 | 1995-09-12 | Massachusetts Institute Of Technology | Apparatus and method for real-time measurement of thin film layer thickness and changes thereof |
DE4319128C1 (en) | 1993-06-09 | 1995-02-23 | Fraunhofer Ges Forschung | Method and device for the free-forming production of three-dimensional components of a predetermined shape |
US5684713A (en) | 1993-06-30 | 1997-11-04 | Massachusetts Institute Of Technology | Method and apparatus for the recursive design of physical structures |
US5391460A (en) | 1993-07-12 | 1995-02-21 | Hughes Aircraft Company | Resin composition and process for investment casting using stereolithography |
ES2150977T3 (en) | 1993-08-09 | 2000-12-16 | Vantico Ag | NEW (MET) ACRYLATES CONTAINING URETANIAN GROUPS. |
US5738921A (en) | 1993-08-10 | 1998-04-14 | E. Khashoggi Industries, Llc | Compositions and methods for manufacturing sealable, liquid-tight containers comprising an inorganically filled matrix |
US5458825A (en) | 1993-08-12 | 1995-10-17 | Hoover Universal, Inc. | Utilization of blow molding tooling manufactured by sterolithography for rapid container prototyping |
ES2127365T5 (en) | 1993-08-26 | 2002-08-16 | Vantico Ag | COMPOSITION LIQUID RETICULABLE BY RADIATION, INTENDED SPECIFICALLY TO STEREOLITOGRAPHY. |
US5608814A (en) | 1993-08-26 | 1997-03-04 | General Electric Company | Method of dynamic thresholding for flaw detection in ultrasonic C-scan images |
US5439622A (en) | 1993-09-07 | 1995-08-08 | Motorola, Inc. | Method and apparatus for producing molded parts |
US5498782A (en) | 1993-09-08 | 1996-03-12 | Union Carbide Chemicals & Plastics Technology Corporation | Distortion control additives for ultraviolet-curable compositions |
US5426722A (en) | 1993-09-09 | 1995-06-20 | Stratasys, Inc. | Method for optimizing the motion of a multi-axis robot |
US5741215A (en) | 1993-09-10 | 1998-04-21 | The University Of Queensland | Stereolithographic anatomical modelling process |
EP0646580B1 (en) | 1993-09-16 | 2000-05-31 | Ciba SC Holding AG | Vinylether compounds with additional functional groups differing from vinylether and their use in the formulation of curable compositions |
US5382289A (en) | 1993-09-17 | 1995-01-17 | Ashland Oil, Inc. | Inorganic foundry binder systems and their uses |
JPH0788966A (en) | 1993-09-22 | 1995-04-04 | Matsushita Electric Works Ltd | Method for forming three-dimensional shape |
US5435902A (en) | 1993-10-01 | 1995-07-25 | Andre, Sr.; Larry E. | Method of incremental object fabrication |
US5976339A (en) | 1993-10-01 | 1999-11-02 | Andre, Sr.; Larry Edward | Method of incremental layered object fabrication |
JP2706611B2 (en) | 1993-10-14 | 1998-01-28 | 帝人製機株式会社 | Stereolithography method and stereolithography device |
US5518680A (en) | 1993-10-18 | 1996-05-21 | Massachusetts Institute Of Technology | Tissue regeneration matrices by solid free form fabrication techniques |
US5490962A (en) | 1993-10-18 | 1996-02-13 | Massachusetts Institute Of Technology | Preparation of medical devices by solid free-form fabrication methods |
US5418112A (en) | 1993-11-10 | 1995-05-23 | W. R. Grace & Co.-Conn. | Photosensitive compositions useful in three-dimensional part-building and having improved photospeed |
US5555481A (en) | 1993-11-15 | 1996-09-10 | Rensselaer Polytechnic Institute | Method of producing solid parts using two distinct classes of materials |
US5514232A (en) | 1993-11-24 | 1996-05-07 | Burns; Marshall | Method and apparatus for automatic fabrication of three-dimensional objects |
JP3287683B2 (en) | 1993-12-28 | 2002-06-04 | 日本たばこ産業株式会社 | Leaf tobacco automatic feeding device |
FR2714668B1 (en) | 1993-12-31 | 1996-01-26 | Rhone Poulenc Chimie | Preparation of phosphomagnesium cements. |
US5703138A (en) | 1994-01-12 | 1997-12-30 | Dymax Corporation | Oxygen-curable coating composition |
US5491643A (en) | 1994-02-04 | 1996-02-13 | Stratasys, Inc. | Method for optimizing parameters characteristic of an object developed in a rapid prototyping system |
JPH07214675A (en) | 1994-02-07 | 1995-08-15 | Matsushita Electric Ind Co Ltd | Method and apparatus for forming resin shaped object |
US5665118A (en) | 1994-02-18 | 1997-09-09 | Johnson & Johnson Professional, Inc. | Bone prostheses with direct cast macrotextured surface regions and method for manufacturing the same |
BE1008128A3 (en) | 1994-03-10 | 1996-01-23 | Materialise Nv | Method for supporting an object manufactured by stereo lithography or any rapid prototype manufacturing and method for manufacturing the taking used steunkonstruktie. |
US5433280A (en) | 1994-03-16 | 1995-07-18 | Baker Hughes Incorporated | Fabrication method for rotary bits and bit components and bits and components produced thereby |
US5429788A (en) | 1994-03-28 | 1995-07-04 | Kimberly-Clark Corporation | Apparatus and method for depositing particulate material in a composite substrate |
DE59501852D1 (en) | 1994-05-13 | 1998-05-14 | Eos Electro Optical Syst | METHOD AND DEVICE FOR PRODUCING THREE-DIMENSIONAL OBJECTS |
US5503785A (en) | 1994-06-02 | 1996-04-02 | Stratasys, Inc. | Process of support removal for fused deposition modeling |
JP3024695B2 (en) | 1994-06-08 | 2000-03-21 | 東京応化工業株式会社 | Positive photoresist composition |
US5494618A (en) | 1994-06-27 | 1996-02-27 | Alliedsignal Inc. | Increasing the useful range of cationic photoinitiators in stereolithography |
US5705116A (en) | 1994-06-27 | 1998-01-06 | Sitzmann; Eugene Valentine | Increasing the useful range of cationic photoinitiators in stereolithography |
US5639402A (en) | 1994-08-08 | 1997-06-17 | Barlow; Joel W. | Method for fabricating artificial bone implant green parts |
TW381106B (en) | 1994-09-02 | 2000-02-01 | Ciba Sc Holding Ag | Alkoxyphenyl-substituted bisacylphosphine oxides |
JP2615429B2 (en) | 1994-09-13 | 1997-05-28 | 工業技術院長 | Creating 3D solid shapes |
JP3523338B2 (en) | 1994-09-14 | 2004-04-26 | 富士通株式会社 | 3D model creation method and apparatus |
US5572431A (en) | 1994-10-19 | 1996-11-05 | Bpm Technology, Inc. | Apparatus and method for thermal normalization in three-dimensional article manufacturing |
US5717599A (en) | 1994-10-19 | 1998-02-10 | Bpm Technology, Inc. | Apparatus and method for dispensing build material to make a three-dimensional article |
US5633021A (en) | 1994-10-19 | 1997-05-27 | Bpm Technology, Inc. | Apparatus for making a three-dimensional article |
US5555176A (en) | 1994-10-19 | 1996-09-10 | Bpm Technology, Inc. | Apparatus and method for making three-dimensional articles using bursts of droplets |
US5593531A (en) | 1994-11-09 | 1997-01-14 | Texas Instruments Incorporated | System, method and process for fabrication of 3-dimensional objects by a static electrostatic imaging and lamination device |
US5482659A (en) | 1994-12-22 | 1996-01-09 | United Technologies Corporation | Method of post processing stereolithographically produced objects |
JPH08183820A (en) | 1994-12-28 | 1996-07-16 | Takemoto Oil & Fat Co Ltd | Stereolithographic resin and stereolithographic resin composition |
JP2871500B2 (en) | 1994-12-28 | 1999-03-17 | 竹本油脂株式会社 | Optical three-dimensional modeling resin and optical three-dimensional modeling resin composition |
US5611883A (en) | 1995-01-09 | 1997-03-18 | Board Of Regents, The University Of Texas System | Joining ceramics and attaching fasteners to ceramics by gas phase selective beam deposition |
US5507336A (en) | 1995-01-17 | 1996-04-16 | The Procter & Gamble Company | Method of constructing fully dense metal molds and parts |
MX9705844A (en) | 1995-02-01 | 1997-11-29 | 3D Systems Inc | Rapid recoating of three-dimensional objects formed on a cross-sectional basis. |
US5529471A (en) | 1995-02-03 | 1996-06-25 | University Of Southern California | Additive fabrication apparatus and method |
US5573721A (en) | 1995-02-16 | 1996-11-12 | Hercules Incorporated | Use of a support liquid to manufacture three-dimensional objects |
US5659478A (en) | 1995-02-21 | 1997-08-19 | Motorola, Inc. | Rapid product realization process |
US5728345A (en) | 1995-03-03 | 1998-03-17 | General Motors Corporation | Method for making an electrode for electrical discharge machining by use of a stereolithography model |
US5616293A (en) | 1995-03-03 | 1997-04-01 | General Motors Corporation | Rapid making of a prototype part or mold using stereolithography model |
TW418215B (en) | 1995-03-13 | 2001-01-11 | Ciba Sc Holding Ag | A process for the production of three-dimensional articles in a stereolithography bath comprising the step of sequentially irradiating a plurality of layers of a liquid radiation-curable composition |
US5534059A (en) | 1995-03-20 | 1996-07-09 | United States Gypsum Co. | Machinable plaster |
US5639413A (en) | 1995-03-30 | 1997-06-17 | Crivello; James Vincent | Methods and compositions related to stereolithography |
DE19511772C2 (en) | 1995-03-30 | 1997-09-04 | Eos Electro Optical Syst | Device and method for producing a three-dimensional object |
US5733497A (en) | 1995-03-31 | 1998-03-31 | Dtm Corporation | Selective laser sintering with composite plastic material |
US5596504A (en) | 1995-04-10 | 1997-01-21 | Clemson University | Apparatus and method for layered modeling of intended objects represented in STL format and adaptive slicing thereof |
DE19514740C1 (en) | 1995-04-21 | 1996-04-11 | Eos Electro Optical Syst | Appts. for producing three-dimensional objects by laser sintering |
DE19515165C2 (en) | 1995-04-25 | 1997-03-06 | Eos Electro Optical Syst | Device for producing an object using stereolithography |
US5707780A (en) | 1995-06-07 | 1998-01-13 | E. I. Du Pont De Nemours And Company | Photohardenable epoxy composition |
US5746967A (en) | 1995-06-26 | 1998-05-05 | Fox Lite, Inc. | Method of curing thermoset resin with visible light |
US5663883A (en) | 1995-08-21 | 1997-09-02 | University Of Utah Research Foundation | Rapid prototyping method |
US5622577A (en) | 1995-08-28 | 1997-04-22 | Delco Electronics Corp. | Rapid prototyping process and cooling chamber therefor |
US5746844A (en) | 1995-09-08 | 1998-05-05 | Aeroquip Corporation | Method and apparatus for creating a free-form three-dimensional article using a layer-by-layer deposition of molten metal and using a stress-reducing annealing process on the deposited metal |
US5653925A (en) | 1995-09-26 | 1997-08-05 | Stratasys, Inc. | Method for controlled porosity three-dimensional modeling |
US5943235A (en) | 1995-09-27 | 1999-08-24 | 3D Systems, Inc. | Rapid prototyping system and method with support region data processing |
US5749041A (en) | 1995-10-13 | 1998-05-05 | Dtm Corporation | Method of forming three-dimensional articles using thermosetting materials |
EP0776713B1 (en) | 1995-11-09 | 1999-09-01 | Toyota Jidosha Kabushiki Kaisha | A method for laminate forming a sand mould and a method for producing a casting using the same |
US5640667A (en) | 1995-11-27 | 1997-06-17 | Board Of Regents, The University Of Texas System | Laser-directed fabrication of full-density metal articles using hot isostatic processing |
US6077887A (en) | 1995-11-29 | 2000-06-20 | Akzo Nobel Surface Chemistry Ab | Polyelectrolyte composition |
FR2742142B1 (en) | 1995-12-08 | 1998-01-16 | Rhone Poulenc Chimie | NOVEL BINDING PHASE FOR PHOSPHOMAGNETIC CEMENTS AND THEIR USE FOR THE PREPARATION OF MORTARS |
US5660621A (en) | 1995-12-29 | 1997-08-26 | Massachusetts Institute Of Technology | Binder composition for use in three dimensional printing |
US5738817A (en) | 1996-02-08 | 1998-04-14 | Rutgers, The State University | Solid freeform fabrication methods |
US5705117A (en) | 1996-03-01 | 1998-01-06 | Delco Electronics Corporaiton | Method of combining metal and ceramic inserts into stereolithography components |
US5641448A (en) | 1996-03-11 | 1997-06-24 | National Research Council Of Canada | Method of producing plastic injection molds for prototype parts |
US5730817A (en) | 1996-04-22 | 1998-03-24 | Helisys, Inc. | Laminated object manufacturing system |
US5700406A (en) | 1996-04-26 | 1997-12-23 | Bpm Technology, Inc. | Process of and apparatus for making a three-dimensional article |
US5697043A (en) | 1996-05-23 | 1997-12-09 | Battelle Memorial Institute | Method of freeform fabrication by selective gelation of powder suspensions |
US5707578A (en) | 1996-06-14 | 1998-01-13 | Hach Company | Method for making mold inserts |
ES2251024T3 (en) | 1996-06-25 | 2006-04-16 | Hexion Specialty Chemicals, Inc. | BINDERS FOR MALE AND MOLDS. |
US6007318A (en) | 1996-12-20 | 1999-12-28 | Z Corporation | Method and apparatus for prototyping a three-dimensional object |
US6989115B2 (en) | 1996-12-20 | 2006-01-24 | Z Corporation | Method and apparatus for prototyping a three-dimensional object |
US7037382B2 (en) | 1996-12-20 | 2006-05-02 | Z Corporation | Three-dimensional printer |
US5940674A (en) | 1997-04-09 | 1999-08-17 | Massachusetts Institute Of Technology | Three-dimensional product manufacture using masks |
DE19715582B4 (en) | 1997-04-15 | 2009-02-12 | Ederer, Ingo, Dr. | Method and system for generating three-dimensional bodies from computer data |
SE509088C2 (en) | 1997-04-30 | 1998-12-07 | Ralf Larsson | Methods and apparatus for the production of volume bodies |
DE19723892C1 (en) | 1997-06-06 | 1998-09-03 | Rainer Hoechsmann | Method for producing components by build-up technology |
EP0990004B1 (en) | 1997-06-26 | 2002-08-07 | The Dow Chemical Company | Improved acid catalyzed polymerization |
DE19727677A1 (en) * | 1997-06-30 | 1999-01-07 | Huels Chemische Werke Ag | Method and device for producing three-dimensional objects |
US6136088A (en) | 1997-10-09 | 2000-10-24 | Mbt Holding Ag | Rapid setting, high early strength binders |
US6753108B1 (en) | 1998-02-24 | 2004-06-22 | Superior Micropowders, Llc | Energy devices and methods for the fabrication of energy devices |
US6348679B1 (en) | 1998-03-17 | 2002-02-19 | Ameritherm, Inc. | RF active compositions for use in adhesion, bonding and coating |
US6821462B2 (en) | 1998-07-10 | 2004-11-23 | Jeneric/Pentron, Inc. | Mass production of shells and models for dental restorations produced by solid free-form fabrication methods |
US6378974B1 (en) * | 1998-09-14 | 2002-04-30 | Agfa-Gevaert | Ink jet method with improved tonal range |
US6363606B1 (en) | 1998-10-16 | 2002-04-02 | Agere Systems Guardian Corp. | Process for forming integrated structures using three dimensional printing techniques |
DE69928973T2 (en) | 1998-10-29 | 2006-09-07 | Z Corp., Burlington | Composition for three-dimensional printing |
DE19853834A1 (en) | 1998-11-21 | 2000-05-31 | Ingo Ederer | Production of casting molds comprises depositing particulate material on support, applying binder and hardener to form solidified structure in selected region, and removing solidified structure |
US6433038B1 (en) | 1999-03-16 | 2002-08-13 | Seiko Epson Corporation | Photocurable ink composition for ink jet recording and ink jet recording method using the same |
US6071675A (en) | 1999-06-05 | 2000-06-06 | Teng; Gary Ganghui | On-press development of a lithographic plate comprising dispersed solid particles |
JP2001015613A (en) | 1999-06-29 | 2001-01-19 | Sony Corp | Nonvolatile semiconductor storage device and manufacture thereof |
US6401001B1 (en) | 1999-07-22 | 2002-06-04 | Nanotek Instruments, Inc. | Layer manufacturing using deposition of fused droplets |
US6884311B1 (en) * | 1999-09-09 | 2005-04-26 | Jodi A. Dalvey | Method of image transfer on a colored base |
JP2001150556A (en) | 1999-09-14 | 2001-06-05 | Minolta Co Ltd | Three-dimensional shaping device and three-dimensional shaping method |
WO2001034371A2 (en) | 1999-11-05 | 2001-05-17 | Z Corporation | Material systems and methods of three-dimensional printing |
US20030173695A1 (en) | 1999-11-12 | 2003-09-18 | Therics, Inc. | Rapid prototyping and manufacturing process |
JP3212581B2 (en) | 1999-12-08 | 2001-09-25 | 株式会社筒井プラスチック | Method of manufacturing powder shaped article reinforced by chemical bonding of impregnating liquid |
US20050104241A1 (en) | 2000-01-18 | 2005-05-19 | Objet Geometried Ltd. | Apparatus and method for three dimensional model printing |
JP2001207584A (en) | 2000-01-31 | 2001-08-03 | Nichiha Corp | Colored building board and method for manufacturing |
US6423255B1 (en) | 2000-03-24 | 2002-07-23 | Rainer Hoechsmann | Method for manufacturing a structural part by deposition technique |
US20010050031A1 (en) | 2000-04-14 | 2001-12-13 | Z Corporation | Compositions for three-dimensional printing of solid objects |
DE10018987A1 (en) | 2000-04-17 | 2001-10-31 | Envision Technologies Gmbh | Device and method for producing three-dimensional objects |
US6397922B1 (en) | 2000-05-24 | 2002-06-04 | Massachusetts Institute Of Technology | Molds for casting with customized internal structure to collapse upon cooling and to facilitate control of heat transfer |
DE10026955A1 (en) | 2000-05-30 | 2001-12-13 | Daimler Chrysler Ag | Material system for use in 3D printing |
WO2002003966A2 (en) | 2000-07-10 | 2002-01-17 | Therics, Inc. | Method and materials for controlling migration of binder liquid in a powder |
US6780368B2 (en) | 2001-04-10 | 2004-08-24 | Nanotek Instruments, Inc. | Layer manufacturing of a multi-material or multi-color 3-D object using electrostatic imaging and lamination |
DE10158233A1 (en) | 2001-08-23 | 2003-03-13 | Rolf Muelhaupt | Reactive system for three-dimensional printing comprises two or more components that react chemically with one another to form a solid after adding a liquid medium |
US7011783B2 (en) | 2001-10-24 | 2006-03-14 | 3D Systems, Inc. | Cooling techniques in solid freeform fabrication |
WO2003037607A1 (en) | 2001-10-29 | 2003-05-08 | Therics, Inc. | A system and method for uniaxial compression of an article, such as a three-dimensionally printed dosage form |
US6713125B1 (en) | 2002-03-13 | 2004-03-30 | 3D Systems, Inc. | Infiltration of three-dimensional objects formed by solid freeform fabrication |
US6742456B1 (en) | 2002-11-14 | 2004-06-01 | Hewlett-Packard Development Company, L.P. | Rapid prototyping material systems |
ITGE20020104A1 (en) | 2002-11-22 | 2004-05-23 | Fabrizio Parodi | QUICKLY HEATING POLYMERIC COMPOSITIONS |
AU2003900180A0 (en) | 2003-01-16 | 2003-01-30 | Silverbrook Research Pty Ltd | Method and apparatus (dam001) |
DE10306886A1 (en) | 2003-02-18 | 2004-09-02 | Daimlerchrysler Ag | Three dimensional object manufacture comprises forming adhesive coated particle layers on top of one another, subjecting each layer to ionizing particles before activating adhesive and smoothing with a blade |
DE10310385B4 (en) | 2003-03-07 | 2006-09-21 | Daimlerchrysler Ag | Method for the production of three-dimensional bodies by means of powder-based layer-building methods |
EP1459871B1 (en) | 2003-03-15 | 2011-04-06 | Evonik Degussa GmbH | Method and apparatus for manufacturing three dimensional objects using microwave radiation and shaped body produced according to this method |
EP1475220A3 (en) | 2003-05-09 | 2009-07-08 | FUJIFILM Corporation | Process for producing three-dimensional model, and three-dimensional model |
EP1475221A3 (en) | 2003-05-09 | 2008-12-03 | FUJIFILM Corporation | Process for producing three-dimensional model |
KR101120156B1 (en) | 2003-05-21 | 2012-02-22 | 제트 코포레이션 | Thermoplastic Powder Material System for Appearance Models from 3D Printing Systems |
US7807077B2 (en) | 2003-06-16 | 2010-10-05 | Voxeljet Technology Gmbh | Methods and systems for the manufacture of layered three-dimensional forms |
US6930144B2 (en) | 2003-06-24 | 2005-08-16 | Hewlett-Packard Development Company, L.P. | Cement system including a binder for use in freeform fabrication |
US20050014005A1 (en) | 2003-07-18 | 2005-01-20 | Laura Kramer | Ink-jettable reactive polymer systems for free-form fabrication of solid three-dimensional objects |
GB0317387D0 (en) | 2003-07-25 | 2003-08-27 | Univ Loughborough | Method and apparatus for combining particulate material |
US7120512B2 (en) | 2003-08-25 | 2006-10-10 | Hewlett-Packard Development Company, L.P. | Method and a system for solid freeform fabricating using non-reactive powder |
EP1661690A4 (en) | 2003-08-27 | 2009-08-12 | Fujifilm Corp | Method of producing three-dimensional model |
US20070029698A1 (en) | 2003-09-11 | 2007-02-08 | Rynerson Michael L | Layered manufactured articles having small-diameter fluid conduction vents and method of making same |
US7365129B2 (en) | 2003-10-14 | 2008-04-29 | Hewlett-Packard Development Company, L.P. | Polymer systems with reactive and fusible properties for solid freeform fabrication |
ITVA20030040A1 (en) | 2003-10-27 | 2005-04-28 | Lamberti Spa | WHITE SOLID PHOTOINIZER FOR POWDER AND PROCEDURE FOR ITS PREPARATION. |
US7381360B2 (en) | 2003-11-03 | 2008-06-03 | Hewlett-Packard Development Company, L.P. | Solid free-form fabrication of three-dimensional objects |
US7608672B2 (en) | 2004-02-12 | 2009-10-27 | Illinois Tool Works Inc. | Infiltrant system for rapid prototyping process |
DE102004012682A1 (en) | 2004-03-16 | 2005-10-06 | Degussa Ag | Process for the production of three-dimensional objects by means of laser technology and application of an absorber by inkjet method |
DE102004014806B4 (en) | 2004-03-24 | 2006-09-14 | Daimlerchrysler Ag | Rapid technology component |
DE102004020452A1 (en) | 2004-04-27 | 2005-12-01 | Degussa Ag | Method for producing three-dimensional objects by means of electromagnetic radiation and applying an absorber by inkjet method |
US7389154B2 (en) | 2004-09-29 | 2008-06-17 | Hewlett-Packard Development Company, L.P. | Fabricating a three-dimensional object |
CN101326046A (en) | 2005-09-20 | 2008-12-17 | Pts软件公司 | An apparatus for building a three-dimensional article and a method for building a three-dimensional article |
CN100344440C (en) | 2005-12-19 | 2007-10-24 | 南京师范大学 | Making process of 3D color object |
WO2007114895A2 (en) * | 2006-04-06 | 2007-10-11 | Z Corporation | Production of three-dimensional objects by use of electromagnetic radiation |
CN1857930A (en) | 2006-05-22 | 2006-11-08 | 西安交通大学 | Three dimension color printing quick forming device and method |
WO2008073297A2 (en) | 2006-12-08 | 2008-06-19 | Z Corporation | Three dimensional printing material system and method using peroxide cure |
JP5129267B2 (en) | 2007-01-10 | 2013-01-30 | スリーディー システムズ インコーポレーテッド | 3D printing material system with improved color, article performance and ease of use |
US7968626B2 (en) | 2007-02-22 | 2011-06-28 | Z Corporation | Three dimensional printing material system and method using plasticizer-assisted sintering |
-
2008
- 2008-02-22 US US12/035,743 patent/US7968626B2/en active Active
- 2008-02-22 WO PCT/US2008/002362 patent/WO2008103450A2/en active Application Filing
-
2011
- 2011-02-02 US US13/019,729 patent/US8506862B2/en active Active
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6416850B1 (en) * | 1996-09-04 | 2002-07-09 | Z Corporation | Three dimensional printing materials system |
US20040138336A1 (en) * | 1996-09-04 | 2004-07-15 | Z Corporation | Three dimensional printing material system and method |
US6403002B1 (en) * | 1997-05-14 | 2002-06-11 | Buss Muller Technology Gmbh | Method and device for producing a shaped body |
US20040038009A1 (en) * | 2002-08-21 | 2004-02-26 | Leyden Richard Noel | Water-based material systems and methods for 3D printing |
US20040056378A1 (en) * | 2002-09-25 | 2004-03-25 | Bredt James F. | Three dimensional printing material system and method |
WO2005023524A2 (en) * | 2003-08-29 | 2005-03-17 | Z Corporation | Absorbent fillers for three-dimensional printing |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10265910B2 (en) | 2010-10-27 | 2019-04-23 | Rize Inc. | Process and apparatus for fabrication of three-dimensional objects |
US10357918B2 (en) | 2010-10-27 | 2019-07-23 | Rize Inc. | Process and apparatus for fabrication of three dimensional objects |
EP2632696B1 (en) * | 2010-10-27 | 2020-07-29 | Rize Inc. | Process and apparatus for fabrication of three-dimensional objects |
US11148354B2 (en) | 2010-10-27 | 2021-10-19 | Rize, Inc. | Process and apparatus for fabrication of three dimensional objects |
CN103847104A (en) * | 2014-03-10 | 2014-06-11 | 天津大学 | Three-dimensional waxing printer and using method thereof |
Also Published As
Publication number | Publication date |
---|---|
US20110156301A1 (en) | 2011-06-30 |
WO2008103450A3 (en) | 2008-12-31 |
US20080281019A1 (en) | 2008-11-13 |
US8506862B2 (en) | 2013-08-13 |
US7968626B2 (en) | 2011-06-28 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US8506862B2 (en) | Three dimensional printing material system and method using plasticizer-assisted sintering | |
EP2109528B1 (en) | Three-dimensional printing material system with improved color, article performance, and ease of use and method using it | |
US7550518B2 (en) | Methods and compositions for three-dimensional printing of solid objects | |
JP5160711B2 (en) | Fluid composition for three-dimensional printing of solid objects | |
KR101407801B1 (en) | Three dimensional printing material system and method using peroxide cure | |
JP6921207B2 (en) | Manufacture and use of porous bead polymers in 3D printing by binder jetting | |
Utela et al. | A review of process development steps for new material systems in three dimensional printing (3DP) | |
TWI659940B (en) | Sintering and shaping method and sintered shaped article | |
US9353284B2 (en) | Three dimensional printing material system and method | |
US11897193B2 (en) | Build material slurry | |
JP2018080359A (en) | Powder material for stereoscopic molding, material set for stereoscopic molding, and apparatus and method for manufacturing a stereoscopic molded object | |
EP3311984A1 (en) | Powder material for solid freeform fabrication, material set of solid freeform fabrication, device for manufacturing solid freeform fabrication object, and method of manufacturing solid freeform fabrication object | |
WO2021076109A1 (en) | Three-dimensional printing with cellulose-based additives | |
WO2022240384A1 (en) | Three-dimensional printing kits | |
WO2022268546A1 (en) | Material system for 3d printing | |
EP4108361A1 (en) | Material system for 3d printing | |
WO2021183092A1 (en) | Hydrogel three-dimensional printing with amine sensing agents |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
122 | Ep: pct application non-entry in european phase |
Ref document number: 08725951 Country of ref document: EP Kind code of ref document: A2 |