CA1214303A - Formable pulp compositions - Google Patents
Formable pulp compositionsInfo
- Publication number
- CA1214303A CA1214303A CA000437296A CA437296A CA1214303A CA 1214303 A CA1214303 A CA 1214303A CA 000437296 A CA000437296 A CA 000437296A CA 437296 A CA437296 A CA 437296A CA 1214303 A CA1214303 A CA 1214303A
- Authority
- CA
- Canada
- Prior art keywords
- hereof
- set forth
- parts
- binder
- slurry
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000000203 mixture Substances 0.000 title claims abstract description 35
- 239000011230 binding agent Substances 0.000 claims abstract description 107
- 239000002002 slurry Substances 0.000 claims abstract description 50
- 239000000463 material Substances 0.000 claims abstract description 44
- 235000013312 flour Nutrition 0.000 claims abstract description 25
- 235000013311 vegetables Nutrition 0.000 claims abstract description 25
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000000047 product Substances 0.000 claims description 48
- 239000004568 cement Substances 0.000 claims description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 16
- 239000004594 Masterbatch (MB) Substances 0.000 claims description 15
- 239000004816 latex Substances 0.000 claims description 14
- 229920000126 latex Polymers 0.000 claims description 14
- 239000007787 solid Substances 0.000 claims description 12
- 229920002472 Starch Polymers 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 10
- 239000008107 starch Substances 0.000 claims description 10
- 235000019698 starch Nutrition 0.000 claims description 10
- 238000005266 casting Methods 0.000 claims description 9
- 229920002451 polyvinyl alcohol Polymers 0.000 claims description 9
- 238000010298 pulverizing process Methods 0.000 claims description 9
- 239000002023 wood Substances 0.000 claims description 8
- 239000004372 Polyvinyl alcohol Substances 0.000 claims description 7
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims description 7
- 239000012783 reinforcing fiber Substances 0.000 claims description 7
- 238000001035 drying Methods 0.000 claims description 6
- 235000013339 cereals Nutrition 0.000 claims description 5
- 238000004132 cross linking Methods 0.000 claims description 5
- 239000012467 final product Substances 0.000 claims description 5
- 229920000877 Melamine resin Polymers 0.000 claims description 4
- 239000011398 Portland cement Substances 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 4
- JDSHMPZPIAZGSV-UHFFFAOYSA-N melamine Chemical group NC1=NC(N)=NC(N)=N1 JDSHMPZPIAZGSV-UHFFFAOYSA-N 0.000 claims description 4
- 238000000465 moulding Methods 0.000 claims description 4
- 229920000058 polyacrylate Polymers 0.000 claims description 4
- ODGAOXROABLFNM-UHFFFAOYSA-N polynoxylin Chemical compound O=C.NC(N)=O ODGAOXROABLFNM-UHFFFAOYSA-N 0.000 claims description 4
- 239000004800 polyvinyl chloride Substances 0.000 claims description 4
- 229920000915 polyvinyl chloride Polymers 0.000 claims description 4
- 238000001556 precipitation Methods 0.000 claims description 3
- 238000004049 embossing Methods 0.000 claims description 2
- 229920001807 Urea-formaldehyde Polymers 0.000 claims 3
- 239000011521 glass Substances 0.000 claims 3
- 238000007580 dry-mixing Methods 0.000 claims 1
- 238000009408 flooring Methods 0.000 abstract description 3
- 239000004615 ingredient Substances 0.000 description 13
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 7
- 239000000908 ammonium hydroxide Substances 0.000 description 7
- 239000002245 particle Substances 0.000 description 6
- 239000000843 powder Substances 0.000 description 6
- 229940037003 alum Drugs 0.000 description 5
- 229920002678 cellulose Polymers 0.000 description 5
- 239000001913 cellulose Substances 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- 229920005989 resin Polymers 0.000 description 5
- 239000011347 resin Substances 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- 239000003365 glass fiber Substances 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 3
- 229920013646 Hycar Polymers 0.000 description 3
- 239000000654 additive Substances 0.000 description 3
- 235000011089 carbon dioxide Nutrition 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 230000000717 retained effect Effects 0.000 description 3
- 244000068645 Carya illinoensis Species 0.000 description 2
- 235000009025 Carya illinoensis Nutrition 0.000 description 2
- IMROMDMJAWUWLK-UHFFFAOYSA-N Ethenol Chemical compound OC=C IMROMDMJAWUWLK-UHFFFAOYSA-N 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 239000001932 carya illinoensis shell powder Substances 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 238000009472 formulation Methods 0.000 description 2
- 238000003475 lamination Methods 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 239000011236 particulate material Substances 0.000 description 2
- 239000012779 reinforcing material Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 235000017060 Arachis glabrata Nutrition 0.000 description 1
- 244000105624 Arachis hypogaea Species 0.000 description 1
- 235000010777 Arachis hypogaea Nutrition 0.000 description 1
- 235000018262 Arachis monticola Nutrition 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- 240000000797 Hibiscus cannabinus Species 0.000 description 1
- 240000007049 Juglans regia Species 0.000 description 1
- 235000009496 Juglans regia Nutrition 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 241000282320 Panthera leo Species 0.000 description 1
- 229920001131 Pulp (paper) Polymers 0.000 description 1
- 241000533293 Sesbania emerus Species 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 239000012736 aqueous medium Substances 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 238000009950 felting Methods 0.000 description 1
- 239000011094 fiberboard Substances 0.000 description 1
- 239000010903 husk Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000012778 molding material Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 235000014571 nuts Nutrition 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 235000020232 peanut Nutrition 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 239000012763 reinforcing filler Substances 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 229920002379 silicone rubber Polymers 0.000 description 1
- 239000004945 silicone rubber Substances 0.000 description 1
- 238000000859 sublimation Methods 0.000 description 1
- 230000008022 sublimation Effects 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 229920005992 thermoplastic resin Polymers 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 235000020234 walnut Nutrition 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H13/00—Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
- D21H13/36—Inorganic fibres or flakes
- D21H13/38—Inorganic fibres or flakes siliceous
- D21H13/40—Inorganic fibres or flakes siliceous vitreous, e.g. mineral wool, glass fibres
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B28/00—Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements
- C04B28/02—Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements containing hydraulic cements other than calcium sulfates
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/001—Modification of pulp properties
- D21C9/002—Modification of pulp properties by chemical means; preparation of dewatered pulp, e.g. in sheet or bulk form, containing special additives
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H11/00—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
- D21H11/10—Mixtures of chemical and mechanical pulp
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/02—Material of vegetable origin
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/33—Synthetic macromolecular compounds
- D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21J—FIBREBOARD; MANUFACTURE OF ARTICLES FROM CELLULOSIC FIBROUS SUSPENSIONS OR FROM PAPIER-MACHE
- D21J1/00—Fibreboard
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21J—FIBREBOARD; MANUFACTURE OF ARTICLES FROM CELLULOSIC FIBROUS SUSPENSIONS OR FROM PAPIER-MACHE
- D21J3/00—Manufacture of articles by pressing wet fibre pulp, or papier-mâché, between moulds
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21J—FIBREBOARD; MANUFACTURE OF ARTICLES FROM CELLULOSIC FIBROUS SUSPENSIONS OR FROM PAPIER-MACHE
- D21J7/00—Manufacture of hollow articles from fibre suspensions or papier-mâché by deposition of fibres in or on a wire-net mould
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S524/00—Synthetic resins or natural rubbers -- part of the class 520 series
- Y10S524/907—Additive of specified shape other than fiber, particle, or powder
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31942—Of aldehyde or ketone condensation product
- Y10T428/31949—Next to cellulosic
- Y10T428/31957—Wood
- Y10T428/3196—Phenoplast
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Ceramic Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Materials Engineering (AREA)
- Paper (AREA)
Abstract
FORMABLE PULP COMPOSITIONS
Abstract The present invention concerns our discovery that aqueous cellulosic slurries comprising primary binder, newsprint, sulfite pulp, and vegetable shell flour can be prepared and formed as desired into various configurations. The materials thus formed are usable for a variety of purposes including furniture, paneling and flooring structures.
Abstract The present invention concerns our discovery that aqueous cellulosic slurries comprising primary binder, newsprint, sulfite pulp, and vegetable shell flour can be prepared and formed as desired into various configurations. The materials thus formed are usable for a variety of purposes including furniture, paneling and flooring structures.
Description
l~L43~D3 . FORMABLE P~LP ~OMPOSITIONS
The present invention relates to pulp compositions and more particularly to pulp compositions which may be formed into desired configurations.
Background of the Invention The preparation of molded cellulosic materials ..
has long been known in the art and substantial effort has been expended to develop moldable compositions which provide objects having good appearance and durability.
The present invention concerns novel compostions and processes which provide wood-like productsO
The Prior Art .
~ number of references describe aqueous compositions which may be molded into a desired configuration. For example, ~.S. Patent No. 3,825,471 discloses cardboard compositions prepared from kenaf fibers, cotton rags, gin waste and binder in an aqueous medium; U.S. Patent No. 3,988,270 describes extrudable aqueous compositions comprising up to 3% water, from 1 to 30~ of a vegetable shell flour and a thermoplastic resin; ~.S. Patent No. 4,012,561 discloses a process for forming decorative laminates comprising a substantial amount of waste newspaper whereby the newspaper is pulped and formed into sheets by conventional ,,~, ,.
fourdrinier technology and then laminated together in multiple layer sheets; and ~.S. Patent 4,248,743 discloses a composite comprising wood pulp and a polymeric matrix, sufficient poly~leric material being present to provide a continuous polymeric matrix phase.
Nevertheless, the compositions prepared according to -these references have not proved to be entirely satisfactory for forming moldable products.
Accordingly, one objective of the present 10 invention is to provide uni~ue aqueous-base~ moldable -compositions which may be formed in a variety of -~
configurations varying from flat sheets to distinctive ---shapes such as furniture. ---Another objective of the present invention is 15 to provide a process for utili~ing these materials to -:
provide materials having a desired configuration. ---Yet another objective of the present invention --~
is to provide molded products comprising sufficient -:-cellulosic materials to be accepted by consumers as ---20 "wood" products. -These and other advantages of the present -invention will become apparent from the detailed -~
description of the preferred embodiments which follow.
Summar~ of the Invention -The present invention concerns our discovery --:
that aqueous cellulosic slurries comprising primary binder, newsprint, sulfite pulp, and vegetable shell flour can be prepared and formed as desired into various configurations. The materials thus formed are usable --30 for a variety of purposes including furniture, paneling -and flooring structures. - -Detailed Description of Preferred Embodiments In one embodiment, the present invention comprises a cellulosic composition which is useful to prepare articles having desired configurations, said composition comprising by weiyht 100 parts of primary -binder, from about 25 to about 700 parts of newsprint, from about 25 to about 500 parts of sulfite pulp, from ;
.".,..~, : .
~2~3~
- 3 - LFM-73q4 about 2 5 to about 500 parts of vegetable shell flour and a suitable quantity of water.
In a second embodiment, the present invention comprises a cellulosic product having a desired configuration, said product comprising by weight 100 parts of primary binder, from about 2 5 to about 700 parts of newsprint, from about 25 to about 500 parts of --sulfite pulp and from about 25 to about 500 parts of :
vegetable shell flour. ~-In a third embodiment, the present invention comprises a process for preparing cellulosic articles having a desired configuration, said process comprising the steps of preparing an aqueous slurry comprising by weight from about 25 to about 700 parts of newsprint, from about 25 to about 500 parts of sulfite pulp, from -about 25 to about 500 parts of vegetable shell flour, ~-~
and optional components; adjusting the pH 25 necessary -to cause precipitation of a subse~3uently added primary ---binder onto the solid components of said slurry; -:
dispersing 100 parts of said primary binder in said slurry; disposing said slurry in a desired configuration; ~-removing excess water from said slurry to form a pre- -shaped article having the desired configuration; and drying said preshaped article. -In a fourth embodiment, the present invention -comprises a process for preparing cellulosic articles ~-having a desired configuration, said process comprising the steps of preparing a master batch slurry comprising from about 25 to about 700 parts of newsprint, from about 25 to about 500 parts of sulfite pulp and from about 25 to about 500 parts of vegetable shell flour; --forming said master batch slurry into a mat; intermixing -said mat with optional components and 100 parts of -primary binder; and forming the intermixed material into ~~-3 5 a desired configuration.
The molded cellulosic products presently known in 'he art typically comprise a maximum of about 40-45%
cellulosic materials. Although compositions containing --43~
- ~ - LPM-7344 higher levels of cellulose are known, these compositions have often proved to be unsatisfactory. For example, in .S. Patent No. ~,~48,743, which was referred to above, it is noted that Composition No. ~ (which comprises -:
about 56~ by weight of fiber) is crumbly and shows weak cleavage planes. -~
Surprisingly, we have discovered that moldable compositions may be prepared according to the present invention and used to produce products which contain -substantially higher quantities of cellulosic materials, perhaps on the order of 90% or more. These products are useful for a variety of purposes, such as floor and wall --~
. . .
coverings, decorative objects and furniture. Further, because of the high cellulose content, they are 15 acceptable 2S wood products. -Another advantage of the present invention is that products can be formed which have substantially -higher densities than products which are presently --formed according to the prior art. Thus, whereas the present invention can conveniently be used to prepare molded products having a density of as high as 55 or --more pounds per cubic foot (pcf), the prior art -processes based on beater saturation technology and the like have conventionally been used to produce products ---having much lowe.r densities.
The compositions of the present invention are based on 100 parts of primary binder. Examples of primary binders which will give suitable results are thermoset or thermoplastic binders such as urea-formal- -dehyde binders, melamine binders and latex binders, such as polyvinyl chloride binders, polyacrylate binders, polystyrene-butadiene (SBR) binders, chlorinated SBR
binder, and carboxylated SBR binders. It is understood, however, that the aforementioned listing of primary binders is provided by way of illustration and is not intended to limit the scope of the present invention.
The purpose of the primary binders is to impart wood-like properties to the resulting product. -~
Thus, the primary binders must be capable of providing acceptable tensile strengths, ~ransverse strength, nail-pull strength, and the like, such that the product is comparable to wood. In a preferred embodiment, the binder will be a self-crosslinking acrylic latex binder such as Rhoplex TR407 cr Hycar 2671.
In combination with the primary binder are included newsprint, sulfite pulp and vegetable shell flourl all of which comprise the cellulosic ingredients of the composition. While newsprint and sulfite pulp are well known components for beater saturation technology, the combination of all three components i5 unique. Although applicant does not desire to be bound by any theory of operability, it appears that the vegetable shell flour possesses the ability to fill the intersti~ial voids between the fibrous particles of pulp and newsprint, th~s leading to a highly preferred packing phenomenon. Thus, when the ~omposition is molded and compressed, products having high densities 20 and very smooth surfaces are obtained.
From about 25 to about 700 parts by weight of newsprint may be used to practice the present invention;
however, from about 50 to about 40Q parts of newsprint is preferred and from about 90 to about 310 parts of newsprint is especially preferred. The sulfite pulp may be present in from about 25 to about 500 parts by weight; however, from about 50 to about 350 parts of sulfite pulp is preferred and from about 90 to about 310 parts~is most preferred.
The vegetable shell flour may be derived from nut shells, such as pecan, walnut, or peanut shells, and also from other sources such as coffee bean shells and rice husks. From about 25 to about 500 parts by weight of vegetable shell flour may be used; however, from about 50 to about 350 parts of vegetable shell flour is preferred, and from about 90 to about 310 parts is most preferred.
.* Trademark ~D~ 3 In one preferred embodiment, the aforemen-tioned ingredients are formulated using standard beater saturation technology into an aqueous slurry which preferably comprises from about 2 to about 8~ solids by -weight. It must be kept in mind, however, that more or less water may be utilized depending on the desires of the artisan.
In addition to the aforementioned primary --binder and cellulosic ingredients, other materials may also be present in the slurry. For example, secondary binders may be used to promote better adhesion between -the primary binder and the cellulosic materials, provide better wet strength so that a we~ blanket of felted solids will hold together more readily during processing, provide improved impact resistance in the final product, and the like. Secondary binders are added for reasons other than to provide wood-like properties to the product because that is the function -of the primary binder. Examples of secondary binders are starch powder, polyvinyl alcohol, fondue cement, portland cement, medusa cement and the like. Fondue -cement is especially preferred because it has an ---affinity for water and tends not to be lost through the wires of the fourdrinier apparatus during felting. The 25 quantities of these materials may vary depending on -their nature. For example, from about 10 to about 350 parts by weiqht of starch powder may be used in relation to 100 parts of primary binder, although from about 20 to about 100 parts is preferred. Similarly, from about 30 to about 100 parts of cement may be used, although from about 50 to about 90 parts is preferred. In the usual situation, wet end additives such as alum and ammonium hydroxide will be required to adjust the p~ in -order to precipitate the binder. Optionally, the ---composition may also contain additional additivies such as wet-strength resins and glass fibers or other reinforcing fibers. Preferably, the re nforcing fibers will be unaffected by the temperature used during the molding operation. -3~;~
- 7 - L~M-7344 The cellulosic components of the presen~
invention will typically comprise by weight from about 43 to about 94~ of the final product. Preferably, however, they will comprise from about 60 to about 92%
5 OL the final product and, most preferably, from about 73~ to about 90%.
As a first step in preparing the slurry described above, a slurry of the cellulosic ingredients is prepared. For example, using standard beater 10 technology such as with an air impeller beater, a master ---batch slurry is prepared from shredded newsprint, a dispersable form of pulp and the vegetable shell flour. ---The master batch may be used to advantage in a variety of ways. ~or example, it may be felted onto fourdrinier 15 wires by means well known in the art. The felted --material may be retained in a wet state for later use or it may be dried using a drum or other appropriate means and similarly retained. Alternatively, it may be further mixed with the secondary binders, reinforcing materials, fillers, and the like and cast or molded into a final product. If the dried master batch is used, it can be pulverized, blended while in the dry state with other necessary ingredients and then compressed into a final configuration, or it can be repulped into a --25 slurry, blended with other components, and then placed -in a desired configuration.
The preferred method of forming final products :~
from a slurry will usually involve the addition of the secondary additives such as fondue cement, starch, reinforcing materials, wet strength resins and the like to the slurry, after which the p~ of the slurry is adjusted with alum and a base such as ammonium hydroxide, or by other means well-known in the art. The primary binder is then added and it precipitates onto 35 the solid particles, giving a slurry which may be placed --in a desired configuration.
The components and characteristics of a slurry - can be varied substantially depending on the desires of 3~33 8 - LFM-73~4 the artisan. Further, the utilities of the resulting slurries will usu211y be quite diverse because products varyin~ from furniture tc wall and floor coverings can be prepared wherein the cellulosic content is adjusted from relatively high (e.g. 90%) to relatively low (e.g.
45%) levels. Certain preferences will become apparent, however. For example, if the materials are intended for use as functional items such as furniture, a higher --primary binder level of perhaps 35-40~ will often be --10 preferred in combination with a cellulosic content of ::
perhaps as low as 45%. On the other hand, if a sheet material such as a wall or floor covering is intended, a --higher cellulose content on the order of perhaps 85% may -be desired, in combination with a correspondingly lower ---15 binder content. :-If the desired configuration is a sheet product, the sheet may be prepared as described above, laminated together in layers, and pressed or embossed to --give composite structures which are usable as wood-type 20 sheet materials for flooring or tile products. -Alternatively, the sheets can be pulverized to yield ~
ground stock which can be used as disclosed herein.
Decoratively molded objects such as furniture may be prepared either directly from a slurry or from :-ground stock. When a slurry is used, a casting having the desired configuration may be prepared using metal or, preferably, silicone rubber, molding materials. The --casting may be equipped with a vacuum apparatus to -assist in the removal of excess water, or it may be a conventional non-vacuum casting. In either event the binder-coated slurry is pumped into the casting and --preferably pre~shaped by covering the casting with gauze and roughly shaping the solid using a contoured backing plate. The gauze permits excess water to escape 35 and also permits the backing plate to be separated -without damaging the wet pulp. When preshaping is complete, the backing plate is separated, the gauze is - removed and the backing plate is reinserted. Then, as a ~1~2~
~ 9 ~ L~M-734 last step, the molded material is dried under heat and pressure, cooled, and removed from the press to give a high-density product.
When ground stock is used, a sheet material comprising all of the desired ingredients is prepared and dried. The sheet is then pulverized into stock which preferably has a uniform particle size. It has been found that this may be conveniently accomplished by chilling the sheet prior to pulverizing it. If the 10 sheet is pulverized without chilling, however, lumps and -non-uniform particles are often obtained. The ~se of -substantially non-uniorm particles will often lead to undesirable appearance and strength characteristics and should be avoided. The pulverized stock is next placed in a mold where it is heated under pressure, essentially as describe~ above, to provide a high-density product.
Either of the above methods can be used to --prepare products having a wide range of densities, such :-as from about one to about 55 pcf. However, they are 20 especially useful to prepare products having densities :
of from about 20 to about 55 pcf and, in particular, from about 30 to about 55 pcf, depending on the desires -of the artisan.
The advantages and attributes of the present invention may be more clearly understood by reference to the following examples which are intended to illustrate, --but not to limit, the scope of the present invention. --Example 1 :
This example will illustrate the preparation 30 of a Master Batch. A mixture comprising 2~ solids by --weight was pulped in a hydropulper for 10 minutes. The mixture comprised water, 16.6 pounds of sulfite pulp, -16.6 pounds of newsprint and 16.6 pounds of pecan shell -~
flour. After refining in a Jordan refiner, the stock was diluted to a consistency of 1~ solids and felted onto fourdrinier wires at a wet gauge of 3/32 inch. The resulting material, which had good wet strength, was - rolled up and stored in a closed container for later use.
~L4~3 LFM-7344 Example 2 A slurry was prepared with an air impeller beater from 7 liters of water and 99.9 grams (dry weight) of Master Batch (Example 1). To the slurry was then added 2.5 grams ~dry basis) of wet strength resin ~Kymene 2064 from Hercules as a 3O5~ aqueo~s solution) and 6.7 grams of starch powder. Twelve grams of al~m and sufficient ammonium hydroxide solution to bring the pH to 7 were added, after which 25 grams of a self-crosslinking acrylic latex primary binder (Hycar
The present invention relates to pulp compositions and more particularly to pulp compositions which may be formed into desired configurations.
Background of the Invention The preparation of molded cellulosic materials ..
has long been known in the art and substantial effort has been expended to develop moldable compositions which provide objects having good appearance and durability.
The present invention concerns novel compostions and processes which provide wood-like productsO
The Prior Art .
~ number of references describe aqueous compositions which may be molded into a desired configuration. For example, ~.S. Patent No. 3,825,471 discloses cardboard compositions prepared from kenaf fibers, cotton rags, gin waste and binder in an aqueous medium; U.S. Patent No. 3,988,270 describes extrudable aqueous compositions comprising up to 3% water, from 1 to 30~ of a vegetable shell flour and a thermoplastic resin; ~.S. Patent No. 4,012,561 discloses a process for forming decorative laminates comprising a substantial amount of waste newspaper whereby the newspaper is pulped and formed into sheets by conventional ,,~, ,.
fourdrinier technology and then laminated together in multiple layer sheets; and ~.S. Patent 4,248,743 discloses a composite comprising wood pulp and a polymeric matrix, sufficient poly~leric material being present to provide a continuous polymeric matrix phase.
Nevertheless, the compositions prepared according to -these references have not proved to be entirely satisfactory for forming moldable products.
Accordingly, one objective of the present 10 invention is to provide uni~ue aqueous-base~ moldable -compositions which may be formed in a variety of -~
configurations varying from flat sheets to distinctive ---shapes such as furniture. ---Another objective of the present invention is 15 to provide a process for utili~ing these materials to -:
provide materials having a desired configuration. ---Yet another objective of the present invention --~
is to provide molded products comprising sufficient -:-cellulosic materials to be accepted by consumers as ---20 "wood" products. -These and other advantages of the present -invention will become apparent from the detailed -~
description of the preferred embodiments which follow.
Summar~ of the Invention -The present invention concerns our discovery --:
that aqueous cellulosic slurries comprising primary binder, newsprint, sulfite pulp, and vegetable shell flour can be prepared and formed as desired into various configurations. The materials thus formed are usable --30 for a variety of purposes including furniture, paneling -and flooring structures. - -Detailed Description of Preferred Embodiments In one embodiment, the present invention comprises a cellulosic composition which is useful to prepare articles having desired configurations, said composition comprising by weiyht 100 parts of primary -binder, from about 25 to about 700 parts of newsprint, from about 25 to about 500 parts of sulfite pulp, from ;
.".,..~, : .
~2~3~
- 3 - LFM-73q4 about 2 5 to about 500 parts of vegetable shell flour and a suitable quantity of water.
In a second embodiment, the present invention comprises a cellulosic product having a desired configuration, said product comprising by weight 100 parts of primary binder, from about 2 5 to about 700 parts of newsprint, from about 25 to about 500 parts of --sulfite pulp and from about 25 to about 500 parts of :
vegetable shell flour. ~-In a third embodiment, the present invention comprises a process for preparing cellulosic articles having a desired configuration, said process comprising the steps of preparing an aqueous slurry comprising by weight from about 25 to about 700 parts of newsprint, from about 25 to about 500 parts of sulfite pulp, from -about 25 to about 500 parts of vegetable shell flour, ~-~
and optional components; adjusting the pH 25 necessary -to cause precipitation of a subse~3uently added primary ---binder onto the solid components of said slurry; -:
dispersing 100 parts of said primary binder in said slurry; disposing said slurry in a desired configuration; ~-removing excess water from said slurry to form a pre- -shaped article having the desired configuration; and drying said preshaped article. -In a fourth embodiment, the present invention -comprises a process for preparing cellulosic articles ~-having a desired configuration, said process comprising the steps of preparing a master batch slurry comprising from about 25 to about 700 parts of newsprint, from about 25 to about 500 parts of sulfite pulp and from about 25 to about 500 parts of vegetable shell flour; --forming said master batch slurry into a mat; intermixing -said mat with optional components and 100 parts of -primary binder; and forming the intermixed material into ~~-3 5 a desired configuration.
The molded cellulosic products presently known in 'he art typically comprise a maximum of about 40-45%
cellulosic materials. Although compositions containing --43~
- ~ - LPM-7344 higher levels of cellulose are known, these compositions have often proved to be unsatisfactory. For example, in .S. Patent No. ~,~48,743, which was referred to above, it is noted that Composition No. ~ (which comprises -:
about 56~ by weight of fiber) is crumbly and shows weak cleavage planes. -~
Surprisingly, we have discovered that moldable compositions may be prepared according to the present invention and used to produce products which contain -substantially higher quantities of cellulosic materials, perhaps on the order of 90% or more. These products are useful for a variety of purposes, such as floor and wall --~
. . .
coverings, decorative objects and furniture. Further, because of the high cellulose content, they are 15 acceptable 2S wood products. -Another advantage of the present invention is that products can be formed which have substantially -higher densities than products which are presently --formed according to the prior art. Thus, whereas the present invention can conveniently be used to prepare molded products having a density of as high as 55 or --more pounds per cubic foot (pcf), the prior art -processes based on beater saturation technology and the like have conventionally been used to produce products ---having much lowe.r densities.
The compositions of the present invention are based on 100 parts of primary binder. Examples of primary binders which will give suitable results are thermoset or thermoplastic binders such as urea-formal- -dehyde binders, melamine binders and latex binders, such as polyvinyl chloride binders, polyacrylate binders, polystyrene-butadiene (SBR) binders, chlorinated SBR
binder, and carboxylated SBR binders. It is understood, however, that the aforementioned listing of primary binders is provided by way of illustration and is not intended to limit the scope of the present invention.
The purpose of the primary binders is to impart wood-like properties to the resulting product. -~
Thus, the primary binders must be capable of providing acceptable tensile strengths, ~ransverse strength, nail-pull strength, and the like, such that the product is comparable to wood. In a preferred embodiment, the binder will be a self-crosslinking acrylic latex binder such as Rhoplex TR407 cr Hycar 2671.
In combination with the primary binder are included newsprint, sulfite pulp and vegetable shell flourl all of which comprise the cellulosic ingredients of the composition. While newsprint and sulfite pulp are well known components for beater saturation technology, the combination of all three components i5 unique. Although applicant does not desire to be bound by any theory of operability, it appears that the vegetable shell flour possesses the ability to fill the intersti~ial voids between the fibrous particles of pulp and newsprint, th~s leading to a highly preferred packing phenomenon. Thus, when the ~omposition is molded and compressed, products having high densities 20 and very smooth surfaces are obtained.
From about 25 to about 700 parts by weight of newsprint may be used to practice the present invention;
however, from about 50 to about 40Q parts of newsprint is preferred and from about 90 to about 310 parts of newsprint is especially preferred. The sulfite pulp may be present in from about 25 to about 500 parts by weight; however, from about 50 to about 350 parts of sulfite pulp is preferred and from about 90 to about 310 parts~is most preferred.
The vegetable shell flour may be derived from nut shells, such as pecan, walnut, or peanut shells, and also from other sources such as coffee bean shells and rice husks. From about 25 to about 500 parts by weight of vegetable shell flour may be used; however, from about 50 to about 350 parts of vegetable shell flour is preferred, and from about 90 to about 310 parts is most preferred.
.* Trademark ~D~ 3 In one preferred embodiment, the aforemen-tioned ingredients are formulated using standard beater saturation technology into an aqueous slurry which preferably comprises from about 2 to about 8~ solids by -weight. It must be kept in mind, however, that more or less water may be utilized depending on the desires of the artisan.
In addition to the aforementioned primary --binder and cellulosic ingredients, other materials may also be present in the slurry. For example, secondary binders may be used to promote better adhesion between -the primary binder and the cellulosic materials, provide better wet strength so that a we~ blanket of felted solids will hold together more readily during processing, provide improved impact resistance in the final product, and the like. Secondary binders are added for reasons other than to provide wood-like properties to the product because that is the function -of the primary binder. Examples of secondary binders are starch powder, polyvinyl alcohol, fondue cement, portland cement, medusa cement and the like. Fondue -cement is especially preferred because it has an ---affinity for water and tends not to be lost through the wires of the fourdrinier apparatus during felting. The 25 quantities of these materials may vary depending on -their nature. For example, from about 10 to about 350 parts by weiqht of starch powder may be used in relation to 100 parts of primary binder, although from about 20 to about 100 parts is preferred. Similarly, from about 30 to about 100 parts of cement may be used, although from about 50 to about 90 parts is preferred. In the usual situation, wet end additives such as alum and ammonium hydroxide will be required to adjust the p~ in -order to precipitate the binder. Optionally, the ---composition may also contain additional additivies such as wet-strength resins and glass fibers or other reinforcing fibers. Preferably, the re nforcing fibers will be unaffected by the temperature used during the molding operation. -3~;~
- 7 - L~M-7344 The cellulosic components of the presen~
invention will typically comprise by weight from about 43 to about 94~ of the final product. Preferably, however, they will comprise from about 60 to about 92%
5 OL the final product and, most preferably, from about 73~ to about 90%.
As a first step in preparing the slurry described above, a slurry of the cellulosic ingredients is prepared. For example, using standard beater 10 technology such as with an air impeller beater, a master ---batch slurry is prepared from shredded newsprint, a dispersable form of pulp and the vegetable shell flour. ---The master batch may be used to advantage in a variety of ways. ~or example, it may be felted onto fourdrinier 15 wires by means well known in the art. The felted --material may be retained in a wet state for later use or it may be dried using a drum or other appropriate means and similarly retained. Alternatively, it may be further mixed with the secondary binders, reinforcing materials, fillers, and the like and cast or molded into a final product. If the dried master batch is used, it can be pulverized, blended while in the dry state with other necessary ingredients and then compressed into a final configuration, or it can be repulped into a --25 slurry, blended with other components, and then placed -in a desired configuration.
The preferred method of forming final products :~
from a slurry will usually involve the addition of the secondary additives such as fondue cement, starch, reinforcing materials, wet strength resins and the like to the slurry, after which the p~ of the slurry is adjusted with alum and a base such as ammonium hydroxide, or by other means well-known in the art. The primary binder is then added and it precipitates onto 35 the solid particles, giving a slurry which may be placed --in a desired configuration.
The components and characteristics of a slurry - can be varied substantially depending on the desires of 3~33 8 - LFM-73~4 the artisan. Further, the utilities of the resulting slurries will usu211y be quite diverse because products varyin~ from furniture tc wall and floor coverings can be prepared wherein the cellulosic content is adjusted from relatively high (e.g. 90%) to relatively low (e.g.
45%) levels. Certain preferences will become apparent, however. For example, if the materials are intended for use as functional items such as furniture, a higher --primary binder level of perhaps 35-40~ will often be --10 preferred in combination with a cellulosic content of ::
perhaps as low as 45%. On the other hand, if a sheet material such as a wall or floor covering is intended, a --higher cellulose content on the order of perhaps 85% may -be desired, in combination with a correspondingly lower ---15 binder content. :-If the desired configuration is a sheet product, the sheet may be prepared as described above, laminated together in layers, and pressed or embossed to --give composite structures which are usable as wood-type 20 sheet materials for flooring or tile products. -Alternatively, the sheets can be pulverized to yield ~
ground stock which can be used as disclosed herein.
Decoratively molded objects such as furniture may be prepared either directly from a slurry or from :-ground stock. When a slurry is used, a casting having the desired configuration may be prepared using metal or, preferably, silicone rubber, molding materials. The --casting may be equipped with a vacuum apparatus to -assist in the removal of excess water, or it may be a conventional non-vacuum casting. In either event the binder-coated slurry is pumped into the casting and --preferably pre~shaped by covering the casting with gauze and roughly shaping the solid using a contoured backing plate. The gauze permits excess water to escape 35 and also permits the backing plate to be separated -without damaging the wet pulp. When preshaping is complete, the backing plate is separated, the gauze is - removed and the backing plate is reinserted. Then, as a ~1~2~
~ 9 ~ L~M-734 last step, the molded material is dried under heat and pressure, cooled, and removed from the press to give a high-density product.
When ground stock is used, a sheet material comprising all of the desired ingredients is prepared and dried. The sheet is then pulverized into stock which preferably has a uniform particle size. It has been found that this may be conveniently accomplished by chilling the sheet prior to pulverizing it. If the 10 sheet is pulverized without chilling, however, lumps and -non-uniform particles are often obtained. The ~se of -substantially non-uniorm particles will often lead to undesirable appearance and strength characteristics and should be avoided. The pulverized stock is next placed in a mold where it is heated under pressure, essentially as describe~ above, to provide a high-density product.
Either of the above methods can be used to --prepare products having a wide range of densities, such :-as from about one to about 55 pcf. However, they are 20 especially useful to prepare products having densities :
of from about 20 to about 55 pcf and, in particular, from about 30 to about 55 pcf, depending on the desires -of the artisan.
The advantages and attributes of the present invention may be more clearly understood by reference to the following examples which are intended to illustrate, --but not to limit, the scope of the present invention. --Example 1 :
This example will illustrate the preparation 30 of a Master Batch. A mixture comprising 2~ solids by --weight was pulped in a hydropulper for 10 minutes. The mixture comprised water, 16.6 pounds of sulfite pulp, -16.6 pounds of newsprint and 16.6 pounds of pecan shell -~
flour. After refining in a Jordan refiner, the stock was diluted to a consistency of 1~ solids and felted onto fourdrinier wires at a wet gauge of 3/32 inch. The resulting material, which had good wet strength, was - rolled up and stored in a closed container for later use.
~L4~3 LFM-7344 Example 2 A slurry was prepared with an air impeller beater from 7 liters of water and 99.9 grams (dry weight) of Master Batch (Example 1). To the slurry was then added 2.5 grams ~dry basis) of wet strength resin ~Kymene 2064 from Hercules as a 3O5~ aqueo~s solution) and 6.7 grams of starch powder. Twelve grams of al~m and sufficient ammonium hydroxide solution to bring the pH to 7 were added, after which 25 grams of a self-crosslinking acrylic latex primary binder (Hycar
2~71 from B~ F. Goodrich) was added. The binder immediately precipitated onto the particulate materials.
The particulate matter was felted onto fourdrinier-type wires to give a product having a thickness of approximately 1/16 inch. This product could be held, handled and transported in a wet state without losing its integrity. When dried on a drum at approximately 300~, the dried product similarly maintainea its integrity and could be held, handled, and transported.
This material was amenable to (1) pulverization and recastihg and (2) lamination, as hereinafter described.
Exam~le 3 A quantity of Master Batch W2S drum-dried at 300 F and retained for later ~se. Subsequently, the sheet material, which had a thickness of 3/32 inch, was pulveri~ed using a Fitzmill, and two formulations were prepared as follows:
Example Example Ingredient 3A 3B
30 Water 14 Liters 14 Liters Master batch (dry weight) 9009 9009 Pecan shell flour 36.2g --Fondue cement -- 72.49 Starch powder 30g 309 35 Glass fibers ~.69 9.6g Polyvinyl alcohol (Elvanol BT
from duPont) lOg 109 * Trademark ~l29L~3~
L~M-734 Example Example Ingredient 3A 3B
Wet strength resin (Kymene 2064 from Hercules;
The particulate matter was felted onto fourdrinier-type wires to give a product having a thickness of approximately 1/16 inch. This product could be held, handled and transported in a wet state without losing its integrity. When dried on a drum at approximately 300~, the dried product similarly maintainea its integrity and could be held, handled, and transported.
This material was amenable to (1) pulverization and recastihg and (2) lamination, as hereinafter described.
Exam~le 3 A quantity of Master Batch W2S drum-dried at 300 F and retained for later ~se. Subsequently, the sheet material, which had a thickness of 3/32 inch, was pulveri~ed using a Fitzmill, and two formulations were prepared as follows:
Example Example Ingredient 3A 3B
30 Water 14 Liters 14 Liters Master batch (dry weight) 9009 9009 Pecan shell flour 36.2g --Fondue cement -- 72.49 Starch powder 30g 309 35 Glass fibers ~.69 9.6g Polyvinyl alcohol (Elvanol BT
from duPont) lOg 109 * Trademark ~l29L~3~
L~M-734 Example Example Ingredient 3A 3B
Wet strength resin (Kymene 2064 from Hercules;
3.5% aqueous solution) 251 ml 251 ml Alum 36g 36g Ammonium hydroxide * *
Acrylic latex binder (dry basis) ::
(Rhoplex TR407 from Rohm & Haas) 165g 165g *Volume not measured; sufficient quantity added to adjust pH to 7 .
.
In preparing these formulations, the master batch and the excess pecan shell flour (as required) were slurried in water and the remaining ingredients were added in order, as applicable. The mixture was made neutral with ammonium hydroxide and, as a last step, the primary binder was added, immediately precipitating onto the particulate materials.
Each slurry was pumped into appropriate molds.
As one example, an aluminum mold 9" x 9" x 1/2 " was filled with slurry, covered with gauze, and a backing plate was inserted. Cold pressure was applied to squeeze out the excess water. The backing plate was 2 5 then removed, the gauze was removed, and the backing plate was reinserted. The wet, molded material was finally dried at 350-400~ for 7-15 minutes to give dried 9-inch sguare tiles. The cellulose content of Example 3A was about 7 9% whereas that of Example 3B was 3 0 about 73 . 5~6 .
These tiles were tested for Tensile Strength Perpendicular to Surface and were subjected to a `,~ail Withdrawal Test, both essentially as described in ASTM D 1037-78. They were also subjected to a .3 5 Transverse Strength test essentially as described in ANSI/ASTM C 209-72. The results cbtained were as rollows: -. . .
3~3 - 12 - L~M-7344 Test Result (average Test of three measurements) Example Example 3A _ 3B __ Perp. Tensile Strength (lb./in2 at failure) 33.2 88.5 :.
Nail Withdrawal (lbs.) 11.25 15.33 at ave. thickness tin.) of 0.434 0.438 :....
Transverse Strength (load at failure, lbs.) 48.9 90.7 (modulus of rupture, psi) 835 1509 .....
Apparent Density (pcf) 32.52 43.09 Example 4 ~sing the dry master batch descrlbed in Example 3, an aqueous slurry having a solids content of 2% was prepared comprising the following components: :
......
Ingredient Quantity Master batch (dry weight) 1150g Fondue cement 72.4g -20 Starch powder 30g Polyvinyl alcohol (Elvanol BT
from duPont) 109 The slurry was refined using a Jordan refiner, the solids content was adjusted to 1.5%, and the following 25 ingredients were added, in order '.'~
Ingredient Quantity .....
Glass fibers 14.4g ~et strength resin (Kymene 2064 from Hercules; 3.5% aqueous - -solution) 251 ml Alum 36g Ammonium hydroxide *
.. ...
: .
~d~ 0/3 Insredient Quantity Acrylic latex binder (dry basis) (1:1 blend of Rhoplex TR407 from ---Rohm & Haas and Hycar 2671 from --5B. F. Goodrich) 3309 *Volume not measured; sufficient quantity added to adjust pH to 7 -':::
, . . .
The solids content was adjusted to 1~ and the slurry was ---felted onto fourdrinier wires to give a wet mat of material. The mat was drum dried at 300F to give a layer of material 1/16 inch thick having a cellulose content of about 49%. This sheet was handled in a -variety of ways, as follows: -Example 4A
lS This example will illustrate the preparation -~
of sheet product by pulverizing the sheets of Example 4 --and forming the powder in a mold. A quantity of the ---1/16-inch thick sheeting prepared according to Example 4 -was cut into approximately 1 to 2-inch strips, covered --.
with pulverized dry ice for 30 seconds and the sheet (including dry ice) was fed into a Fitzmill. The resulting particles were of substantially uniform size, were free of lumps and had a consistency comparable to freeze-dri~d coffee.
A quantity of this material (at room temperature after sublimation of the dry ice) was placed in a 1/2-inch mold and compressed at about 425F for 20 minutes under about 1,100 psi pressure.
The resulting board, which had a nominal --30 thickness of 1/2 inch was tested for perpendicular --tensile strength and perpendicular screw withdrawal ~-essentially according to ASTM D 1037-78, giving the --following results: --.....
-. .
- 14 - LPM-734~
Particleboard Fiberboard Exarnple Test Control Control 4A
E~oard thickness (inch) 0.501 0.505 0.460 Perp. tensile strength (lb./in2 at failure) 145.5 161.5 251.7 Perp. screw withdrawal (lbs. at failure)235.8328.8 276.3 --Apparent Density (pcf) 50.76 46.32 69.12 Modulus of Rupture (psi) 3546 5394 2447 --Example 4B
This example will illustrate the lamination of ---a plurality of layers as obtained from Example 4 to -provide a laminated vinyl structure. Seven layers of sheets prepared according to Example 4 were placed in a -press at 425F for 20 minutes under 1,160 psi pressure.
One face of the press was provided with a wood grain ---embossing plate which imparted a wood grain finish to the face of the material. The resulting product had a --definite wood grain appearance as would be found with a decorative wall panel or as inside backing for a piece of furniture, the latter typically being provided in the prior art by hardboard. -Example 5 This example will illustrate the dry forming 25 of a molded product. The proportions of ingredients, --excluding the wet end additives (water, Kymene, alum and ammonium hydroxide), are set forth in Example 3B. :
The pulverized Master Batch was dry mixed with the cement, starch, glass fibers, polyvinyl alcohol and 30 binder, and the mixture was placed in a mold. The mold -was heated to about 400F for about 20 minutes under -about 1100 psi pressure 'o produce a product which was somewhat less satisfactory than the products produced according to Examples 3 and 4.
This invention is not restricted solely to the descrip~ions and illustrations provided above, but encompasses all modifications envisaged by the following ---claims. :~
Acrylic latex binder (dry basis) ::
(Rhoplex TR407 from Rohm & Haas) 165g 165g *Volume not measured; sufficient quantity added to adjust pH to 7 .
.
In preparing these formulations, the master batch and the excess pecan shell flour (as required) were slurried in water and the remaining ingredients were added in order, as applicable. The mixture was made neutral with ammonium hydroxide and, as a last step, the primary binder was added, immediately precipitating onto the particulate materials.
Each slurry was pumped into appropriate molds.
As one example, an aluminum mold 9" x 9" x 1/2 " was filled with slurry, covered with gauze, and a backing plate was inserted. Cold pressure was applied to squeeze out the excess water. The backing plate was 2 5 then removed, the gauze was removed, and the backing plate was reinserted. The wet, molded material was finally dried at 350-400~ for 7-15 minutes to give dried 9-inch sguare tiles. The cellulose content of Example 3A was about 7 9% whereas that of Example 3B was 3 0 about 73 . 5~6 .
These tiles were tested for Tensile Strength Perpendicular to Surface and were subjected to a `,~ail Withdrawal Test, both essentially as described in ASTM D 1037-78. They were also subjected to a .3 5 Transverse Strength test essentially as described in ANSI/ASTM C 209-72. The results cbtained were as rollows: -. . .
3~3 - 12 - L~M-7344 Test Result (average Test of three measurements) Example Example 3A _ 3B __ Perp. Tensile Strength (lb./in2 at failure) 33.2 88.5 :.
Nail Withdrawal (lbs.) 11.25 15.33 at ave. thickness tin.) of 0.434 0.438 :....
Transverse Strength (load at failure, lbs.) 48.9 90.7 (modulus of rupture, psi) 835 1509 .....
Apparent Density (pcf) 32.52 43.09 Example 4 ~sing the dry master batch descrlbed in Example 3, an aqueous slurry having a solids content of 2% was prepared comprising the following components: :
......
Ingredient Quantity Master batch (dry weight) 1150g Fondue cement 72.4g -20 Starch powder 30g Polyvinyl alcohol (Elvanol BT
from duPont) 109 The slurry was refined using a Jordan refiner, the solids content was adjusted to 1.5%, and the following 25 ingredients were added, in order '.'~
Ingredient Quantity .....
Glass fibers 14.4g ~et strength resin (Kymene 2064 from Hercules; 3.5% aqueous - -solution) 251 ml Alum 36g Ammonium hydroxide *
.. ...
: .
~d~ 0/3 Insredient Quantity Acrylic latex binder (dry basis) (1:1 blend of Rhoplex TR407 from ---Rohm & Haas and Hycar 2671 from --5B. F. Goodrich) 3309 *Volume not measured; sufficient quantity added to adjust pH to 7 -':::
, . . .
The solids content was adjusted to 1~ and the slurry was ---felted onto fourdrinier wires to give a wet mat of material. The mat was drum dried at 300F to give a layer of material 1/16 inch thick having a cellulose content of about 49%. This sheet was handled in a -variety of ways, as follows: -Example 4A
lS This example will illustrate the preparation -~
of sheet product by pulverizing the sheets of Example 4 --and forming the powder in a mold. A quantity of the ---1/16-inch thick sheeting prepared according to Example 4 -was cut into approximately 1 to 2-inch strips, covered --.
with pulverized dry ice for 30 seconds and the sheet (including dry ice) was fed into a Fitzmill. The resulting particles were of substantially uniform size, were free of lumps and had a consistency comparable to freeze-dri~d coffee.
A quantity of this material (at room temperature after sublimation of the dry ice) was placed in a 1/2-inch mold and compressed at about 425F for 20 minutes under about 1,100 psi pressure.
The resulting board, which had a nominal --30 thickness of 1/2 inch was tested for perpendicular --tensile strength and perpendicular screw withdrawal ~-essentially according to ASTM D 1037-78, giving the --following results: --.....
-. .
- 14 - LPM-734~
Particleboard Fiberboard Exarnple Test Control Control 4A
E~oard thickness (inch) 0.501 0.505 0.460 Perp. tensile strength (lb./in2 at failure) 145.5 161.5 251.7 Perp. screw withdrawal (lbs. at failure)235.8328.8 276.3 --Apparent Density (pcf) 50.76 46.32 69.12 Modulus of Rupture (psi) 3546 5394 2447 --Example 4B
This example will illustrate the lamination of ---a plurality of layers as obtained from Example 4 to -provide a laminated vinyl structure. Seven layers of sheets prepared according to Example 4 were placed in a -press at 425F for 20 minutes under 1,160 psi pressure.
One face of the press was provided with a wood grain ---embossing plate which imparted a wood grain finish to the face of the material. The resulting product had a --definite wood grain appearance as would be found with a decorative wall panel or as inside backing for a piece of furniture, the latter typically being provided in the prior art by hardboard. -Example 5 This example will illustrate the dry forming 25 of a molded product. The proportions of ingredients, --excluding the wet end additives (water, Kymene, alum and ammonium hydroxide), are set forth in Example 3B. :
The pulverized Master Batch was dry mixed with the cement, starch, glass fibers, polyvinyl alcohol and 30 binder, and the mixture was placed in a mold. The mold -was heated to about 400F for about 20 minutes under -about 1100 psi pressure 'o produce a product which was somewhat less satisfactory than the products produced according to Examples 3 and 4.
This invention is not restricted solely to the descrip~ions and illustrations provided above, but encompasses all modifications envisaged by the following ---claims. :~
Claims (54)
1. A cellulosic composition useful to prepare shaped cellulosic articles, said composition comprising by weight 100 parts of primary binder, from about 25 to about 700 parts of newsprint, from about 25 to about 500 parts of sulfite pulp, from about 25 to about 500 parts of vegetable shell flour, and a suitable quantity of water.
2. The invention as set forth in claim 1 hereof wherein said composition comprises from about 50 to about 400 parts of newsprint, from about 50 to about 350 parts of sulfite pulp, and from about 50 to about 350 parts of vegetable shell flour for every 100 parts of primary binder.
3. The invention as set forth in claim 2 hereof wherein said composition comprises from about 90 to about 310 parts each of the newsprint, the sulfite pulp and the vegetable shell flour.
4. The invention as set forth in claims 1, 2 or 3 hereof wherein said composition comprises at least one secondary binder.
5. The invention as set forth in claims 1, 2 or 3 hereof wherein said composition comprises at least one secondary binder selected from the group consisting of powdered starch, cement, and polyvinyl alcohol.
6. The invention as set forth in claims 1, 2 or 3 hereof wherein said composition comprises at least one secondary binder which is a cement selected from the group consisting of portland cement, fondue cement and medusa cement.
7. The invention as set forth in claims 1, 2 or 3 hereof wherein said composition comprises reinforcing fibers.
8. The invention as set forth in claims 1, 2 or 3 hereof wherein said composition comprises glass reinforcing fibers.
9. The invention as set forth in claims 1, 2 or 3 hereof wherein said primary binder is a melamine binder, a urea-formaldehyde binder or a latex binder.
10. The invention as set forth in claims 1, 2 or 3 hereof wherein said primary binder is a latex binder selected from the group consisting of polyvinyl chloride binders, polyacrylate binders, SBR binders, chlorinated SBR binders and carboxylated SBR binders.
11. The invention as set forth in claims 1, 2 or 3 hereof wherein said primary binder is a self cross-linking acrylic latex binder.
12. A cellulosic product in the form of shaped cellu-losic articles,said product comprising by weight 100 parts of primary binder, from about 25 to about 700 parts of newsprint, from about 25 to about 500 parts of sulfite pulp and from about 25 to about 500 parts of vegetable shell flour.
13. The invention as set forth in claim 12 hereof wherein said product comprises from about 50 to about 400 parts of newsprint, from about 50 to about 350 parts of sulfite pulp, and from about 50 to about 350 parts of vegetable shell flour for every 100 parts of primary binder.
14. The invention as set forth in claim 13 hereof wherein said product comprises from about 90 to about 310 parts each of the newsprint, the sulfite pulp and the vegetable shell flour.
15. The invention as set forth in claims 12, 13 or 14 hereof wherein said product comprises at least one secondary binder.
16. The invention as set forth in claims 12, 13 or 14 hereof wherein said product comprises at least one secondary binder selected from the group consisting of powdered starch, cement, and polyvinyl alcohol.
17. The invention as set forth in claims 12, 13 or 14 hereof wherein said product comprises at least one secondary binder which is a cement selected from the group consisting of portland cement, fondue cement and medusa cement.
18. The invention as set forth in claims 12, 13 or 14 hereof wherein said product comprises reinforcing fibers.
19. The invention as set forth in claims 12, 13 or 14 hereof wherein said product comprises glass reinforcing fibers.
20. The invention as set forth in claims 12, 13 or 14 hereof wherein said primary binder is a melamine binder, a urea-formaldehyde binder or a latex binder.
21. The invention as set forth in claims 12, 13 or 14 hereof wherein said primary binder is a latex binder selected from the group consisting of polyvinyl chloride binders, polyacrylate binders, SBR binders, chlorinated SBR binders and carboxylated SBR binders.
22. The invention as set forth in claims 12, 13 or 14 hereof wherein said primary binder is a self cross-linking acrylic latex binder.
23. The invention as set forth in claims 12, 13 or 14 hereof wherein said product comprises not less than about 45% cellulosic material.
24. The invention as set forth in claims 12, 13 or 14 hereof wherein said product comprises not less than about 60% cellulosic material.
25. The invention as set forth in claim 12, 13 or 14 hereof wherein said product comprises from about 73 to about 90% cellulosic material.
26. The invention as set forth in claims 12, 13 or 14 hereof wherein the density of said product is not less than about 10 lbs. per cubic foot.
27. The invention as set forth in claims 12, 13 or 14 hereof wherein the density of said product is not less than about 20 lbs. per cubic foot.
28. The invention as set forth in claims 12, 13 or 14 hereof wherein the density of said product is not less than about 30 lbs. per cubic foot.
29. A process for preparing shaped cellulosic articles, said process comprising the steps of preparing an aqueous slurry comprising by weight from about 25 to about 700 parts of newsprint, from about 25 to about 500 parts of sulfite pulp, from about 25 to about 500 parts of vegetable shell flour, and optional components;
adjusting the pH as necessary to cause precipitation of a subsequently added primary binder onto the solid components of said slurry;
dispersing 100 parts of said primary binder in said slurry;
disposing said slurry in a desired configuration;
removing excess water to form a preshaped article; and drying said preshaped article.
adjusting the pH as necessary to cause precipitation of a subsequently added primary binder onto the solid components of said slurry;
dispersing 100 parts of said primary binder in said slurry;
disposing said slurry in a desired configuration;
removing excess water to form a preshaped article; and drying said preshaped article.
30. The invention as set forth in claim 29 hereof wherein said slurry comprises from about 50 to about 400 parts of newsprint, from about 50 to about 350 parts of sulfite pulp, and from about 50 to about 350 parts of vegetable shell flour for every 100 parts of primary binder.
31. The invention as set forth in claim 30 hereof wherein said slurry comprises from about 90 to about 310 parts each of the newsprint, the sulfite pulp and the vegetable shell flour.
32. The invention as set forth in claims 29, 30 or 31 hereof wherein said slurry comprises at least one secondary binder.
33. The invention as set forth in claims 29, 30 or 31 hereof wherein said slurry comprises at least one secondary binder selected from the group consisting of powdered starch, cement and polyvinyl alcohol.
34. The invention as set forth in claims 29, 30 or 31 hereof wherein said slurry comprises at least one secondary binder which is a cement selected from the group consisting of portland cement, fondue cement and medusa cement.
35. The invention as set forth in claims 29, 30 or 31 hereof wherein said slurry comprises reinforcing fibers.
36. The invention as set forth in claims 29, 30 or 31 hereof wherein said slurry comprises glass reinforcing fibers.
37. The invention as set forth in claims 29, 30 or 31 hereof wherein said primary binder is a melamine binder, a urea-formaldehyde binder or a latex binder.
38. The invention as set forth in claims 29, 30 or 31 hereof wherein said primary binder is a latex binder selected from the group consisting of polyvinyl chloride binders, polyacrylate binders, SBR binders, chlorinated SBR binders and carboxylated SBR binders.
39. The invention as set forth in claims 29, 30 or 31 hereof wherein said primary binder is a self cross-linking acrylic latex binder.
40. The invention as set forth in claims 29, 30 or 31 hereof wherein said dried preshaped article comprises not less than about 45% cellulosic material.
41. The invention as set forth in claims 29, 30 or 31 hereof wherein said dried preshaped article comprises not less than about 60% cellulosic material.
42. The invention as set forth in claims 29, 30 or 31 hereof wherein said dried preshaped article comprises from about 73 to about 90% cellulosic material.
43. The invention as set forth in claims 29, 30 or 31 hereof wherein the density of said dried preshaped article is not less than about 10 lbs. per cubic foot.
44. The invention as set forth in claims 29, 30 or 31 hereof wherein the density of said dried preshaped article is not less than about 20 lbs. per cubic foot.
45. The invention as set forth in claims 29, 30 or 31 hereof wherein the density of said dried preshaped article is not less than about 30 lbs. per cubic foot.
46. The invention as set forth in claims 29, 30 or 31 hereof comprising the additional steps of pulverizing said preshaped article, placing the pulverized material in a casting having a desired configuration, and molding said pulverized material.
47. The invention as set forth in claims 29, 30 or 31 hereof comprising the additional steps of chilling and pulverizing said preshaped article, placing the pulverized material in a casting having a desired configuration, and molding said pulverized material.
48. The invention as set forth in claims 29, 30 or 31 hereof comprising the additional steps of pulverizing said preshaped article, placing the pulverized material in a casting having a desired configuration, said casting being provided with a wood grain embossing plate which will impart a wood grain appearance to said final product, and molding said pulverized material.
49. A process for preparing shaped cellulosic articles, said process comprising the steps of preparing a master batch slurry comprising from about 25 to about 700 parts of newsprint, from about 25 to about 500 parts of sulfite pulp and from about 25 to about 500 parts of vegetable shell flour;
forming said master batch slurry into a mat;
intermixing said mat with optional components and 100 parts of primary binder; and forming the intermixed material into a desired configuration.
forming said master batch slurry into a mat;
intermixing said mat with optional components and 100 parts of primary binder; and forming the intermixed material into a desired configuration.
50. The invention as set forth in claim 49 hereof wherein said slurry comprises from about 50 to about 400 parts of newsprint, from about 50 to about 350 parts of sulfite pulp and from about 50 to about 350 parts of vegetable shell flour for every 100 parts of primary binder.
51. The invention as set forth in claim 50 hereof wherein said slurry comprises from about 90 to about 310 parts each of the newsprint, the sulfite pulp and the vegetable shell flour.
52. The invention as set forth in claims 49, 50 or 51 hereof wherein said articles are prepared by drying and pulverizing said mat, and intermixing the pulverized material with said optional components and said binder.
53. The invention as set forth in claims 49, 50 or 51 hereof wherein said articles are prepared by drying and pulverizing said mat, and intermixing the pulverized material with said optional components and said binder by preparing a slurry comprising said pulverized material and said optional components;
adjusting the pH as necessary to cause precipitation of said primary binder onto the solid components of said slurry when said primary binder is subsequently added;
dispersing said primary binder in said slurry; disposing said slurry in a desired configuration; removing excess water to form a preshaped article; and drying said preshaped article.
adjusting the pH as necessary to cause precipitation of said primary binder onto the solid components of said slurry when said primary binder is subsequently added;
dispersing said primary binder in said slurry; disposing said slurry in a desired configuration; removing excess water to form a preshaped article; and drying said preshaped article.
54. The invention as set forth in claim 49, 50 or 51 hereof wherein said articles are prepared by drying and pulverizing said mat, and dry mixing the pulverized material with said optional components and said binders.
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US42924382A | 1982-09-30 | 1982-09-30 | |
US429,243 | 1982-09-30 | ||
US06/532,351 US4562218A (en) | 1982-09-30 | 1983-09-16 | Formable pulp compositions |
US532,351 | 1983-09-16 |
Publications (1)
Publication Number | Publication Date |
---|---|
CA1214303A true CA1214303A (en) | 1986-11-25 |
Family
ID=27028110
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA000437296A Expired CA1214303A (en) | 1982-09-30 | 1983-09-22 | Formable pulp compositions |
Country Status (3)
Country | Link |
---|---|
US (1) | US4562218A (en) |
AU (1) | AU554826B2 (en) |
CA (1) | CA1214303A (en) |
Families Citing this family (85)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2163784B (en) * | 1984-08-30 | 1987-06-10 | Ferodo Ltd | Wet laid friction facing material |
US4638907A (en) * | 1984-11-28 | 1987-01-27 | The Procter & Gamble Company | Laminated laundry product |
US4652390A (en) * | 1985-06-25 | 1987-03-24 | The Procter & Gamble Company | Oxidation resistant tissue for dry laundry actives and bleach compatible products |
US4839076A (en) * | 1988-04-07 | 1989-06-13 | The Procter & Gamble Company | Pouched through the washer and dryer laundry additive product having at least one wall comprised of finely apertured polymeric film |
US4942191A (en) * | 1988-04-25 | 1990-07-17 | Borden, Inc. | Aldehyde condensation resin glue compositions having pea and other leguminous flour extenders |
US5200899A (en) * | 1990-04-20 | 1993-04-06 | Regents Of The University Of Michigan | Method and system for detecting the misfire of an internal combustion engine utilizing angular velocity fluctuations |
DE4135330C1 (en) * | 1991-10-26 | 1992-12-03 | Christian 8359 Ortenburg De Ellwein | Building material used as replacement for wood - comprises mixt. of old paper, water, and starch which is worked to the wood type prod. using heat and pressure |
WO1994004330A1 (en) | 1992-08-11 | 1994-03-03 | E. Khashoggi Industries | Hydraulically settable containers |
US5683772A (en) * | 1992-08-11 | 1997-11-04 | E. Khashoggi Industries | Articles having a starch-bound cellular matrix reinforced with uniformly dispersed fibers |
US5658603A (en) | 1992-08-11 | 1997-08-19 | E. Khashoggi Industries | Systems for molding articles having an inorganically filled organic polymer matrix |
US5631097A (en) | 1992-08-11 | 1997-05-20 | E. Khashoggi Industries | Laminate insulation barriers having a cementitious structural matrix and methods for their manufacture |
US5453310A (en) | 1992-08-11 | 1995-09-26 | E. Khashoggi Industries | Cementitious materials for use in packaging containers and their methods of manufacture |
US5800647A (en) | 1992-08-11 | 1998-09-01 | E. Khashoggi Industries, Llc | Methods for manufacturing articles from sheets having a highly inorganically filled organic polymer matrix |
US5665439A (en) | 1992-08-11 | 1997-09-09 | E. Khashoggi Industries | Articles of manufacture fashioned from hydraulically settable sheets |
US5662731A (en) | 1992-08-11 | 1997-09-02 | E. Khashoggi Industries | Compositions for manufacturing fiber-reinforced, starch-bound articles having a foamed cellular matrix |
US5580409A (en) | 1992-08-11 | 1996-12-03 | E. Khashoggi Industries | Methods for manufacturing articles of manufacture from hydraulically settable sheets |
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 |
US5830305A (en) | 1992-08-11 | 1998-11-03 | E. Khashoggi Industries, Llc | Methods of molding articles having an inorganically filled organic polymer matrix |
US5641584A (en) | 1992-08-11 | 1997-06-24 | E. Khashoggi Industries | Highly insulative cementitious matrices and methods for their manufacture |
US5582670A (en) | 1992-08-11 | 1996-12-10 | E. Khashoggi Industries | Methods for the manufacture of sheets having a highly inorganically filled organic polymer matrix |
US5928741A (en) | 1992-08-11 | 1999-07-27 | E. Khashoggi Industries, Llc | Laminated articles of manufacture fashioned from sheets having a highly inorganically filled organic polymer matrix |
US5580624A (en) | 1992-08-11 | 1996-12-03 | E. Khashoggi Industries | Food and beverage containers made from inorganic aggregates and polysaccharide, protein, or synthetic organic binders, and the methods of manufacturing such containers |
US5851634A (en) | 1992-08-11 | 1998-12-22 | E. Khashoggi Industries | Hinges for highly inorganically filled composite materials |
US5720913A (en) | 1992-08-11 | 1998-02-24 | E. Khashoggi Industries | Methods for manufacturing sheets from hydraulically settable compositions |
US5830548A (en) | 1992-08-11 | 1998-11-03 | E. Khashoggi Industries, Llc | Articles of manufacture and methods for manufacturing laminate structures including inorganically filled sheets |
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 |
US5709827A (en) * | 1992-08-11 | 1998-01-20 | E. Khashoggi Industries | Methods for manufacturing articles having a starch-bound cellular matrix |
US5545450A (en) | 1992-08-11 | 1996-08-13 | E. Khashoggi Industries | Molded articles having an inorganically filled organic polymer matrix |
US5810961A (en) * | 1993-11-19 | 1998-09-22 | E. Khashoggi Industries, Llc | Methods for manufacturing molded sheets having a high starch content |
CA2100320C (en) * | 1992-08-31 | 2011-02-08 | Michael J. Deaner | Advanced polymer wood composite |
CA2100319C (en) * | 1992-08-31 | 2003-10-07 | Michael J. Deaner | Advanced polymer/wood composite structural member |
US6004668A (en) * | 1992-08-31 | 1999-12-21 | Andersen Corporation | Advanced polymer wood composite |
US5406768A (en) * | 1992-09-01 | 1995-04-18 | Andersen Corporation | Advanced polymer and wood fiber composite structural component |
US5733671A (en) * | 1992-11-12 | 1998-03-31 | San Diego State University Foundation | Cellulose fiber reinforced cementitious materials and method of producing same |
US5716675A (en) * | 1992-11-25 | 1998-02-10 | E. Khashoggi Industries | Methods for treating the surface of starch-based articles with glycerin |
DK169728B1 (en) | 1993-02-02 | 1995-01-23 | Stein Gaasland | Process for releasing cellulose-based fibers from each other in water and molding for plastic molding of cellulosic fiber products |
US5441801A (en) * | 1993-02-12 | 1995-08-15 | Andersen Corporation | Advanced polymer/wood composite pellet process |
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 |
US5736209A (en) * | 1993-11-19 | 1998-04-07 | E. Kashoggi, Industries, Llc | Compositions having a high ungelatinized starch content and sheets molded therefrom |
US6083586A (en) * | 1993-11-19 | 2000-07-04 | E. Khashoggi Industries, Llc | Sheets having a starch-based binding matrix |
US5776388A (en) * | 1994-02-07 | 1998-07-07 | E. Khashoggi Industries, Llc | Methods for molding articles which include a hinged starch-bound cellular matrix |
US5843544A (en) * | 1994-02-07 | 1998-12-01 | E. Khashoggi Industries | Articles which include a hinged starch-bound cellular matrix |
US5705203A (en) * | 1994-02-07 | 1998-01-06 | E. Khashoggi Industries | Systems for molding articles which include a hinged starch-bound cellular matrix |
US5948524A (en) * | 1996-01-08 | 1999-09-07 | Andersen Corporation | Advanced engineering resin and wood fiber composite |
US6011091A (en) | 1996-02-01 | 2000-01-04 | Crane Plastics Company Limited Partnership | Vinyl based cellulose reinforced composite |
DE19607963C1 (en) * | 1996-03-01 | 1997-05-22 | Carsten Klatt | Thermal insulation |
US6168857B1 (en) | 1996-04-09 | 2001-01-02 | E. Khashoggi Industries, Llc | Compositions and methods for manufacturing starch-based compositions |
US5847016A (en) * | 1996-05-16 | 1998-12-08 | Marley Mouldings Inc. | Polymer and wood flour composite extrusion |
US5866264A (en) * | 1996-10-22 | 1999-02-02 | Crane Plastics Company Limited Partnership | Renewable surface for extruded synthetic wood material |
US6117924A (en) * | 1996-10-22 | 2000-09-12 | Crane Plastics Company Limited Partnership | Extrusion of synthetic wood material |
US5827462A (en) * | 1996-10-22 | 1998-10-27 | Crane Plastics Company Limited Partnership | Balanced cooling of extruded synthetic wood material |
US6180257B1 (en) | 1996-10-29 | 2001-01-30 | Crane Plastics Company Limited Partnership | Compression molding of synthetic wood material |
US6344504B1 (en) | 1996-10-31 | 2002-02-05 | Crane Plastics Company Limited Partnership | Extrusion of synthetic wood material |
US20020010229A1 (en) | 1997-09-02 | 2002-01-24 | Marshall Medoff | Cellulosic and lignocellulosic materials and compositions and composites made therefrom |
US20030187102A1 (en) | 1997-09-02 | 2003-10-02 | Marshall Medoff | Compositions and composites of cellulosic and lignocellulosic materials and resins, and methods of making the same |
US6464913B1 (en) | 1997-09-05 | 2002-10-15 | Crane Plastics Company Limited Partnership | In-line compounding and extrusion system |
US6344268B1 (en) | 1998-04-03 | 2002-02-05 | Certainteed Corporation | Foamed polymer-fiber composite |
US6337138B1 (en) | 1998-12-28 | 2002-01-08 | Crane Plastics Company Limited Partnership | Cellulosic, inorganic-filled plastic composite |
US6280667B1 (en) | 1999-04-19 | 2001-08-28 | Andersen Corporation | Process for making thermoplastic-biofiber composite materials and articles including a poly(vinylchloride) component |
US6971211B1 (en) | 1999-05-22 | 2005-12-06 | Crane Plastics Company Llc | Cellulosic/polymer composite material |
US7537826B2 (en) | 1999-06-22 | 2009-05-26 | Xyleco, Inc. | Cellulosic and lignocellulosic materials and compositions and composites made therefrom |
US6662515B2 (en) | 2000-03-31 | 2003-12-16 | Crane Plastics Company Llc | Synthetic wood post cap |
US6579605B2 (en) | 2000-07-31 | 2003-06-17 | Crane Plastics Company Llc | Multilayer synthetic wood component |
US6637213B2 (en) | 2001-01-19 | 2003-10-28 | Crane Plastics Company Llc | Cooling of extruded and compression molded materials |
US6578368B1 (en) | 2001-01-19 | 2003-06-17 | Crane Plastics Company Llc | Cryogenic cooling of extruded and compression molded materials |
ITTV20010097A1 (en) * | 2001-07-16 | 2003-01-16 | Cofav Spa | PROCESS FOR THE PRODUCTION OF A VEGETABLE FLOUR WITH THE USE OF RESIDUES FROM AGRICULTURAL PROCESSING AND PROCEDURE FOR THE PRODUCTION |
US6632863B2 (en) | 2001-10-25 | 2003-10-14 | Crane Plastics Company Llc | Cellulose/polyolefin composite pellet |
US6780359B1 (en) | 2002-01-29 | 2004-08-24 | Crane Plastics Company Llc | Synthetic wood composite material and method for molding |
US20030168768A1 (en) * | 2002-03-06 | 2003-09-11 | Weng Hung-Chang | Method for producing environment-protective paper based plastic material |
US20050275138A1 (en) * | 2004-05-27 | 2005-12-15 | Eric Rosen | Building material for forming an architectural surface covering and method for producing the same |
US8074339B1 (en) | 2004-11-22 | 2011-12-13 | The Crane Group Companies Limited | Methods of manufacturing a lattice having a distressed appearance |
US20150328347A1 (en) | 2005-03-24 | 2015-11-19 | Xyleco, Inc. | Fibrous materials and composites |
US7708214B2 (en) | 2005-08-24 | 2010-05-04 | Xyleco, Inc. | Fibrous materials and composites |
BR122017001970B1 (en) | 2005-03-24 | 2020-05-19 | Xyleco Inc | method of densifying a fibrous material |
WO2006134503A1 (en) * | 2005-06-14 | 2006-12-21 | Brødrene Hartmann A/S | Three-dimensional packaging product |
US8167275B1 (en) | 2005-11-30 | 2012-05-01 | The Crane Group Companies Limited | Rail system and method for assembly |
NZ544493A (en) * | 2005-12-22 | 2008-07-31 | Nz Forest Research Inst Ltd | Method for producing wood fibre composite products |
US7743567B1 (en) | 2006-01-20 | 2010-06-29 | The Crane Group Companies Limited | Fiberglass/cellulosic composite and method for molding |
US8460797B1 (en) | 2006-12-29 | 2013-06-11 | Timbertech Limited | Capped component and method for forming |
JP4753908B2 (en) * | 2007-04-04 | 2011-08-24 | 株式会社 伊藤園 | Silver skin compounded paper and method for producing the same |
WO2011099837A1 (en) * | 2010-02-09 | 2011-08-18 | Narayanasamy R Mohanthas | Biodegradable molded products |
US9169385B2 (en) * | 2011-09-30 | 2015-10-27 | Georgia-Pacific Chemicals Llc | Powdered resins with fillers |
US11078630B2 (en) * | 2016-11-03 | 2021-08-03 | Oregon State University | Molded pomace pulp products and methods |
ES2799248B2 (en) * | 2019-06-11 | 2021-07-06 | Iberboard Mill S L | PAPER AND / OR CARDBOARD MANUFACTURING PROCESS FROM DRIED FRUIT HELL FLOUR |
CN110387773A (en) * | 2019-06-24 | 2019-10-29 | 东莞职业技术学院 | A kind of novel environment friendly paper and its preparation process |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1405587A (en) * | 1971-07-21 | 1975-09-10 | Nat Res Dev | Production of shaped articles |
SU395538A1 (en) * | 1971-11-17 | 1973-08-28 | METHOD OF MANUFACTURING CARDBOARD FOR DRY-DRIVE VARIOUS GINA DRIVES | |
US4111730A (en) * | 1972-03-21 | 1978-09-05 | Balatinecz John J | Producing recycle composition paper flake board |
US3907728A (en) * | 1973-10-12 | 1975-09-23 | Boise Cascade Corp | Thermosetting adhesive compositions extended with cellulosic paper mill sludges |
-
1983
- 1983-09-16 US US06/532,351 patent/US4562218A/en not_active Expired - Fee Related
- 1983-09-22 AU AU19374/83A patent/AU554826B2/en not_active Ceased
- 1983-09-22 CA CA000437296A patent/CA1214303A/en not_active Expired
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AU554826B2 (en) | 1986-09-04 |
US4562218A (en) | 1985-12-31 |
AU1937483A (en) | 1984-04-05 |
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