US20040108081A1 - Filler-fiber composite - Google Patents
Filler-fiber composite Download PDFInfo
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- US20040108081A1 US20040108081A1 US10/314,584 US31458402A US2004108081A1 US 20040108081 A1 US20040108081 A1 US 20040108081A1 US 31458402 A US31458402 A US 31458402A US 2004108081 A1 US2004108081 A1 US 2004108081A1
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- Prior art keywords
- filler
- fiber composite
- percent
- calcium carbonate
- partially converted
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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
- D21H3/00—Paper or cardboard prepared by adding substances to the pulp or to the formed web on the paper-making machine and by applying substances to finished paper or cardboard (on the paper-making machine), also when the intention is to impregnate at least a part of the paper body
-
- 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
- D21H17/03—Non-macromolecular organic compounds
- D21H17/05—Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
- D21H17/14—Carboxylic acids; Derivatives thereof
- D21H17/15—Polycarboxylic acids, e.g. maleic acid
-
- 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
- D21H11/16—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only modified by a particular after-treatment
-
- 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
- D21H17/63—Inorganic compounds
- D21H17/67—Water-insoluble compounds, e.g. fillers, pigments
- D21H17/675—Oxides, hydroxides or carbonates
-
- 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
- D21H17/63—Inorganic compounds
- D21H17/70—Inorganic compounds forming new compounds in situ, e.g. within the pulp or paper, by chemical reaction with other substances added separately
-
- 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
- D21H23/00—Processes or apparatus for adding material to the pulp or to the paper
- D21H23/02—Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
- D21H23/04—Addition to the pulp; After-treatment of added substances in the pulp
Definitions
- the present invention relates to a filler-fiber composite, a process for its production, the use of such in the manufacture of paper or paperboard products and to paper produced therefrom. More particularly the invention relates to a filler-fiber composite in which the morphology and particle size of the mineral filler are established prior to the development of the bond to the fiber. Even more particularly, the present invention relates to a PCC filler-fiber composite, wherein the desired optical and physical properties of the paper produced therefrom are realized.
- an object of the present invention is to produce a filler-fiber composite. Another object of the present invention is to provide a method for producing a filler-fiber composite. While another object of the present invention is to produce a filler-fiber composite that maintains physical properties such as tensile strength, breaking length and internal bond strength. Still a further object of the present invention is to produce a filler-fiber composite that maintains optical properties such as ISO opacity and pigment scatter. While still a further object of the present invention is to provide a filler-fiber composite that is particularly useful in paper and paperboard products.
- U.S. Pat. No. 6,156,118 teaches mixing a calcium carbonate filler with noil fibers in a size of P50 or finer.
- U.S. Pat. No. 5,223,090 teaches a method for loading cellulosic fiber using high shear mixing of crumb pulp during carbon dioxide reaction.
- U.S. Pat. No. 5,665,205 teaches a method for combining a fiber pulp slurry and an alkaline salt slurry in the contact zone of a reactor and immediately contacting the slurry with carbon dioxide and mixing so as to precipitate filler onto secondary pulp fibers.
- U.S. Pat. No. 5,679,220 teaches a continuous process for in-situ deposition of fillers in papermaking fibers in a flow stream in which shear is applied to the gaseous phase to complete the conversion of calcium hydroxide to calcium carbonate immediately.
- U.S. Pat. No. 5,122,230 teaches process for modifying hydrophilic fibers with a substantially water insoluble inorganic substance in-situ precipitation.
- U.S. Pat. No. 5,733,461 teaches a method for recovery and use of fines present in a waste water stream produced in a paper manufacturing process.
- U.S. Pat. No. 5,731,080 teaches in-situ precipitation wherein the majority of a calcium carbonate trap the microfiber by reliable and non-reliable mechanical bonding without binders or retention aids.
- U.S. Pat. No. 5,928,470 teaches method of making metal oxide or metal hydroxide-modified cellulosic pulp.
- U.S. Pat. No. 6,235,150 teaches a method of producing a pulp fiber lumen loaded with calcium carbonate having a particle size of 0.4 microns to 1.5 microns.
- the present invention relates to a filler-fiber composite including feeding slake containing seed to a first stage reactor, reacting the slake containing seed in the first stage reactor in the presence of carbon dioxide to produce a first partially converted calcium hydroxide calcium carbonate slurry, reacting the first partially converted calcium hydroxide calcium carbonate slurry in a second stage reactor in the presence of carbon dioxide to produce a second partially converted calcium hydroxide calcium carbonate slurry and reacting the second partially converted calcium hydroxide calcium carbonate slurry in a third stage reactor in the presence of carbon dioxide and fibers to produce a filler-fiber composite.
- the present invention relates to a filler-fiber composite including feeding slake containing seed to a first stage reactor, reacting the slake containing seed in the first stage reactor in the presence of carbon dioxide to produce a first partially converted calcium hydroxide calcium carbonate slurry and reacting the first partially converted calcium carbonate slurry in a second stage reactor in the presence of carbon dioxide and fibers to produce a filler-fiber composite.
- the present invention relates to a filler-fiber composite including feeding slake containing citric acid to a first stage reactor, reacting the slake containing citric acid in the first stage reactor in the presence of carbon dioxide to produce a first partially converted calcium hydroxide calcium carbonate slurry, reacting the first partially converted calcium hydroxide calcium carbonate slurry in a second stage reactor in the presence of carbon dioxide to produce a second partially converted calcium hydroxide calcium carbonate slurry, and reacting the second partially converted calcium hydroxide calcium carbonate slurry in a third stage reactor in the presence of carbon dioxide and fibers to produce a filler-fiber composite.
- the present invention relates to a filler-fiber composite Including feeding slake containing citric acid to a first stage reactor, reacting the slake containing citric acid in the first stage reactor in the presence of carbon dioxide to produce a first partially converted calcium hydroxide calcium carbonate slurry, taking a first portion of the partially converted calcium hydroxide calcium carbonate slurry adding fibers and reacting such in a second stage reactor in the presence of carbon dioxide to produce a calcium carbonate ⁇ fiber composite to serve as a heel and taking a second portion of the partially converted calcium hydroxide calcium carbonate slurry adding fibers and surfactant and reacting in the presence of CO 2 to produce a second partially converted Ca(OH) 2 /CaCO 3 /fiber material and reacting the second partially converted Ca(OH) 2 /CaCO 3 /fiber material in the presence of CO 2 in a third stage reactor to produce a filler-fiber composite.
- the present invention relates to a filler-fiber composite including feeding slake containing citric acid to a first stage reactor, reacting the slake containing citric acid in the first stage reactor in the presence of carbon dioxide to produce a first partially converted calcium hydroxide calcium carbonate slurry, taking a first portion of the partially converted calcium hydroxide calcium carbonate slurry adding fibers and reacting such in a second stage reactor in the presence of carbon dioxide to produce a calcium carbonate/fiber composite to serve as a heel and taking a second portion of the partially converted calcium hydroxide calcium carbonate slurry adding fibers and polyacrylamide and reacting in the presence of CO 2 to produce a second partially converted Ca(OH) 2 /CaCO 3 /fiber material and reacting the second partially converted Ca(OH) 2 /CaCO 3 /fiber material in the presence of CO 2 in a third stage reactor to produce a filler-fiber composite.
- the present invention relates to a filler-fiber composite including feeding slake containing citric acid to a first stage reactor, reacting the slake containing citric acid in the first stage reactor in the presence of carbon dioxide to produce a CaCO 3 heel and adding slake containing sodium carbonate to the heel material of the first stage reactor in the presence of CO 2 to produce a partially converted calcium hydroxide calcium carbonate slurry and reacting the partially converted calcium hydroxide calcium carbonate slurry in a second stage reactor in the presence of carbon dioxide and fibers to produce a filler-fiber composite.
- Fiber as used in the present invention is defined as fiber produced by refining (any pulp refiner known in the pulp processing industry) cellulose and/or mechanical pulp fiber.
- the fibers are typically 0.1 to 2 microns in thickness and 10 to 400 microns in length and are additionally prepared according to U.S. Pat. No. 6,251,222, which is by this reference incorporated herein.
- the first step in this process involves making a high reactive Ca(OH) 2 milk-of-lime slake and screening it at ⁇ 325 mesh. This slake is then added to an agitated reactor, brought to a desired reaction temperature, 0.1 percent citric acid is added to the slake to inhibit aragonite formation, and reacted with CO 2 gas. The reaction proceeds 10 percent to 40 percent of the way through at which point the reaction is stopped. This produces a partially converted Ca(OH) 2 /CaCO 3 slurry (approximately 20 percent solids by weight) which is then fed into a reaction vessel at a rate that matches CO 2 gassing to maintain a given conductivity (ionic saturation) to produce a scalenohedral crystal.
- the product made once stabilization is achieved (approximately 95 percent converted) is then mixed with diluted fibers (approximately 1.5 percent concentration) and water. This mixture is then reacted with CO 2 gas to endpoint pH 7.0.
- the product manufactured using this method can contain from about 0.2 percent to about 99.8 percent scalenohedral PCC with respect to fibers at 3 percent to 5 percent total solids.
- the product has a specific surface area from about 5 meters squared per gram to about 11 meters squared per gram; product solids from about 3 percent to about 5 percent and a PCC content from about 0.2 percent to about 99.8 percent, and is predominantly scalenohedral in morphology.
- the first step in this process involves making a high reactive Ca (OH) 2 milk-of-lime slake and screened at ⁇ 325 mesh.
- the concentration of this slake is approximately 15 percent by weight.
- This slake is then added to an agitated reactor, brought to a desired reaction temperature, from about 0.05 percent to about 0.04 percent additive is added to direct morphology and size, and reacted with CO 2 gas.
- the reaction proceeds 10 percent to 40 percent of the way through at which point the reaction is stopped.
- This produces a partially converted Ca (OH) 2 /CaCO 3 slurry which is then fed into a reaction vessel at a rate that matches CO 2 gassing to maintain a given conductivity (ionic saturation) to produce an acicular, aragonitic crystal.
- the reaction continues until process stabilization is achieved.
- the product made once stabilization is achieved (approximately 95 percent calcium carbonate) is mixed with diluted fibers (approximately 1.5 percent concentration) and water.
- the calcium carbonate and fibers are then reacted with CO 2 gas to an endpoint of pH 7.0.
- the product manufactured using this method contains from about 0.2 percent to about 99.8 percent aragonitic PCC with respect to the fibers at about 3 percent to about 5 percent total solids.
- the product has a specific surface area of about 5 meters squared per gram to about 8 meters squared per gram; product solids from about 3 percent to about 5 percent by weight and a PCC content from about 0.2 percent to about 99.8 percent with respect to fibers and has a predominantly aragonitic morphology.
- the first step in this process involves making a high reactive Ca (OH) 2 milk-of-lime slake which is screened at ⁇ 325 mesh and has a concentration of approximately 20 percent by weight. 0.1 percent citric acid is added to inhibit aragonite formation. A portion of this slake is added to an agitated reactor, brought to a desired reaction temperature and carbonated with CO 2 gas. The reaction proceeds to conductivity minimum producing a “heel”.
- a “heel” is defined as a fully converted calcium carbonate crystal with average particle size typically in the range of about 1 micron to about 2.5 micron with any crystal morphology. Sodium carbonate is added to the remainder of the slake not used in the manufacture of the “heel” material.
- This slake and CO 2 is added to the “heel” material at a CO 2 gassing rate to maintain a given conductivity (ionic saturation) to produce a rhombohedral crystal.
- the reaction is continued until process stabilization is achieved.
- this product (approximately 90 percent to 95 percent converted) is mixed with diluted fibers (approximately 1.5 percent concentration) and water. Additional CO 2 is added to an endpoint of pH 7.0.
- the product manufactured using this method contains from about 0.2 percent to about 99.8 percent rhombohedral PCC with respect to fibers and is about 3 percent to about 5 percent total solids.
- the product has a specific surface area from about 5 meters squared per gram to about 8 meters squared per gram; product solids from about 3 percent to about 5 percent; and PCC content from about 0.2 percent to about 99.8 percent and has a predominantly rhombohedral morphology:
- a “seed” is defined as a fully converted aragonitic crystal that has been endpointed and milled to a high specific surface area (i.e. greater than 30 meters squared per gram and typically a particle size of 0.1 to 0.4 microns).
- the 2.3:1 Ca(OH) 2 /CaCO 3 slurry was transferred to an agitated 20-liter storage vessel. Transferred 2 liters of the 2.3:1 Ca(OH) 2 /CaCO 3 slurry to a first 4-liter agitated, double jacketed stainless steel reaction vessel with agitation set at 1250rpm and the temperature was brought to 52 degrees Celsius. Began addition of 20 percent CO 2 gas in air (1.00 standard liter minute CO 2 /3.99 standard liter minute air) to the first 4-liter reaction vessel and the reaction was continued until a pH of 7.0 was achieved producing a 100 percent CaCO 3 slurry. The temperature of the 100 percent CaCO 3 slurry of the first 4-liter reaction vessel was brought to 63 degrees Celsius.
- control fiber of the present invention was refined at the Empire State Paper Research Institute (ESPRI) using an Escher-Wyss (conical) refiner to an 80° SR (freeness). Measured by a fiber quality analyzer (using arithmatic means) the control fiber measured 200-400 microns
- the morphology controlled filler-fiber composite showed equivalent or greater physical properties (i.e. tensil strength, breaking length, and internal bond strength) as compared with the control filler-fiber.
- TABLE 4 ISO Opacity Optical Properties Filler Loading Scalenohedral Aragonitic Rhombohedral Control Levels Filler-fiber Filler-fiber Filler-fiber Filler-fiber 20 89.20 88.20 87.38 88.18 25 89.93 89.15 88.78 89.55 30 90.95 90.40 89.68 90.83
- the morphology controlled filler-fiber composite showed equivalent optical properties (i.e. ISO Opacity and Pigment Scatter) as compared with the control filler-fiber.
Abstract
The present invention relates to a filler-fiber composite, a process for its production, the use of such in the manufacture of paper or paperboard products and to paper produced therefrom. More particularly the invention relates to a filler-fiber composite in which the morphology and particle size of the mineral filler are established prior to the development of the bond to the fiber. Even more particularly, the present invention relates to a PCC filler-fiber composite, wherein the desired optical and physical properties of the paper produced therefrom are realized.
Description
- The present invention relates to a filler-fiber composite, a process for its production, the use of such in the manufacture of paper or paperboard products and to paper produced therefrom. More particularly the invention relates to a filler-fiber composite in which the morphology and particle size of the mineral filler are established prior to the development of the bond to the fiber. Even more particularly, the present invention relates to a PCC filler-fiber composite, wherein the desired optical and physical properties of the paper produced therefrom are realized.
- Loading particulate fillers such as calcium carbonate, talc and clay on fibers for the subsequent manufacture of paper and paper products continues to be a challenge. A number of methods, having some degree of success, have been used to address this issue. To insure that fillers remain with or within the fiber web, retention aids have been used, direct precipitation onto the fibers have been used, a method to attach the filler directly to the surface of the fiber have been used, mixing the fiber and the filler have been used, precipitation within never dried pulp have been used, a method for filling the cellulosic fiber have been used, high shear mixing have been used, fiberous material and calcium carbonate have been reacted with carbon dioxide in a closed pressurized container, fillers have been trapped by mechanical bonding, cationically charged polymers have been used and pulp fiber lumen loaded with calcium carbonate have all been used to retain filler in fiber for subsequent use in paper. Most of the methods for fiber retention are both expensive and ineffective.
- Therefore, what is needed is a filler fiber composite and a method for producing the same that is both effective in retaining the filler and inexpensive for the paper maker to utilize.
- Therefore, an object of the present invention is to produce a filler-fiber composite. Another object of the present invention is to provide a method for producing a filler-fiber composite. While another object of the present invention is to produce a filler-fiber composite that maintains physical properties such as tensile strength, breaking length and internal bond strength. Still a further object of the present invention is to produce a filler-fiber composite that maintains optical properties such as ISO opacity and pigment scatter. While still a further object of the present invention is to provide a filler-fiber composite that is particularly useful in paper and paperboard products.
- U.S. Pat. No. 6,156,118 teaches mixing a calcium carbonate filler with noil fibers in a size of P50 or finer.
- U.S. Pat. No. 5,096,539 teaches in-situ precipitation of an inorganic filler with never dried pulp.
- U.S. Pat. No. 5,223,090 teaches a method for loading cellulosic fiber using high shear mixing of crumb pulp during carbon dioxide reaction.
- U.S. Pat. No. 5,665,205 teaches a method for combining a fiber pulp slurry and an alkaline salt slurry in the contact zone of a reactor and immediately contacting the slurry with carbon dioxide and mixing so as to precipitate filler onto secondary pulp fibers.
- U.S. Pat. No. 5,679,220 teaches a continuous process for in-situ deposition of fillers in papermaking fibers in a flow stream in which shear is applied to the gaseous phase to complete the conversion of calcium hydroxide to calcium carbonate immediately.
- U.S. Pat. No. 5,122,230 teaches process for modifying hydrophilic fibers with a substantially water insoluble inorganic substance in-situ precipitation.
- U.S. Pat. No. 5,733,461 teaches a method for recovery and use of fines present in a waste water stream produced in a paper manufacturing process.
- U.S. Pat. No. 5,731,080 teaches in-situ precipitation wherein the majority of a calcium carbonate trap the microfiber by reliable and non-reliable mechanical bonding without binders or retention aids.
- U.S. Pat. No. 5,928,470 teaches method of making metal oxide or metal hydroxide-modified cellulosic pulp.
- U.S. Pat. No. 6,235,150 teaches a method of producing a pulp fiber lumen loaded with calcium carbonate having a particle size of 0.4 microns to 1.5 microns.
- The problem of insuring that filler materials, such as calcium carbonate, ground calcium carbonate, clay and talc, remain within fibers that are ultimately to be used in paper has been subjected to a number of proofs. However, none of the prior related art discloses a filler fiber composite where the morphology of the filler is predetermined prior to introducing fibers, a method for its production nor its use in paper or paper products.
- The present invention relates to a filler-fiber composite including feeding slake containing seed to a first stage reactor, reacting the slake containing seed in the first stage reactor in the presence of carbon dioxide to produce a first partially converted calcium hydroxide calcium carbonate slurry, reacting the first partially converted calcium hydroxide calcium carbonate slurry in a second stage reactor in the presence of carbon dioxide to produce a second partially converted calcium hydroxide calcium carbonate slurry and reacting the second partially converted calcium hydroxide calcium carbonate slurry in a third stage reactor in the presence of carbon dioxide and fibers to produce a filler-fiber composite.
- In another aspect, the present invention relates to a filler-fiber composite including feeding slake containing seed to a first stage reactor, reacting the slake containing seed in the first stage reactor in the presence of carbon dioxide to produce a first partially converted calcium hydroxide calcium carbonate slurry and reacting the first partially converted calcium carbonate slurry in a second stage reactor in the presence of carbon dioxide and fibers to produce a filler-fiber composite.
- In a further aspect, the present invention relates to a filler-fiber composite including feeding slake containing citric acid to a first stage reactor, reacting the slake containing citric acid in the first stage reactor in the presence of carbon dioxide to produce a first partially converted calcium hydroxide calcium carbonate slurry, reacting the first partially converted calcium hydroxide calcium carbonate slurry in a second stage reactor in the presence of carbon dioxide to produce a second partially converted calcium hydroxide calcium carbonate slurry, and reacting the second partially converted calcium hydroxide calcium carbonate slurry in a third stage reactor in the presence of carbon dioxide and fibers to produce a filler-fiber composite.
- In yet a further aspect, the present invention relates to a filler-fiber composite Including feeding slake containing citric acid to a first stage reactor, reacting the slake containing citric acid in the first stage reactor in the presence of carbon dioxide to produce a first partially converted calcium hydroxide calcium carbonate slurry, taking a first portion of the partially converted calcium hydroxide calcium carbonate slurry adding fibers and reacting such in a second stage reactor in the presence of carbon dioxide to produce a calcium carbonate\fiber composite to serve as a heel and taking a second portion of the partially converted calcium hydroxide calcium carbonate slurry adding fibers and surfactant and reacting in the presence of CO2 to produce a second partially converted Ca(OH)2/CaCO3/fiber material and reacting the second partially converted Ca(OH)2/CaCO3/fiber material in the presence of CO2 in a third stage reactor to produce a filler-fiber composite.
- In still a further aspect, the present invention relates to a filler-fiber composite including feeding slake containing citric acid to a first stage reactor, reacting the slake containing citric acid in the first stage reactor in the presence of carbon dioxide to produce a first partially converted calcium hydroxide calcium carbonate slurry, taking a first portion of the partially converted calcium hydroxide calcium carbonate slurry adding fibers and reacting such in a second stage reactor in the presence of carbon dioxide to produce a calcium carbonate/fiber composite to serve as a heel and taking a second portion of the partially converted calcium hydroxide calcium carbonate slurry adding fibers and polyacrylamide and reacting in the presence of CO2 to produce a second partially converted Ca(OH)2/CaCO3/fiber material and reacting the second partially converted Ca(OH)2/CaCO3/fiber material in the presence of CO2 in a third stage reactor to produce a filler-fiber composite.
- In a final aspect, the present invention relates to a filler-fiber composite including feeding slake containing citric acid to a first stage reactor, reacting the slake containing citric acid in the first stage reactor in the presence of carbon dioxide to produce a CaCO3 heel and adding slake containing sodium carbonate to the heel material of the first stage reactor in the presence of CO2 to produce a partially converted calcium hydroxide calcium carbonate slurry and reacting the partially converted calcium hydroxide calcium carbonate slurry in a second stage reactor in the presence of carbon dioxide and fibers to produce a filler-fiber composite.
- Fiber as used in the present invention is defined as fiber produced by refining (any pulp refiner known in the pulp processing industry) cellulose and/or mechanical pulp fiber. The fibers are typically 0.1 to 2 microns in thickness and 10 to 400 microns in length and are additionally prepared according to U.S. Pat. No. 6,251,222, which is by this reference incorporated herein.
- Precipitation of PCC with Varying Morphologies
- Continuous Flow Stir Tank Reactor (CFSTR)
- Scalenohedral Morphology
- The first step in this process involves making a high reactive Ca(OH)2 milk-of-lime slake and screening it at −325 mesh. This slake is then added to an agitated reactor, brought to a desired reaction temperature, 0.1 percent citric acid is added to the slake to inhibit aragonite formation, and reacted with CO2 gas. The reaction proceeds 10 percent to 40 percent of the way through at which point the reaction is stopped. This produces a partially converted Ca(OH)2/CaCO3 slurry (approximately 20 percent solids by weight) which is then fed into a reaction vessel at a rate that matches CO2 gassing to maintain a given conductivity (ionic saturation) to produce a scalenohedral crystal. This reaction proceeds until stabilization of the process is achieved. The product made once stabilization is achieved (approximately 95 percent converted) is then mixed with diluted fibers (approximately 1.5 percent concentration) and water. This mixture is then reacted with CO2 gas to endpoint pH 7.0. The product manufactured using this method can contain from about 0.2 percent to about 99.8 percent scalenohedral PCC with respect to fibers at 3 percent to 5 percent total solids.
- The product has a specific surface area from about 5 meters squared per gram to about 11 meters squared per gram; product solids from about 3 percent to about 5 percent and a PCC content from about 0.2 percent to about 99.8 percent, and is predominantly scalenohedral in morphology.
- Aragonitic Morphology
- The first step in this process involves making a high reactive Ca (OH)2 milk-of-lime slake and screened at −325 mesh. The concentration of this slake is approximately 15 percent by weight. This slake is then added to an agitated reactor, brought to a desired reaction temperature, from about 0.05 percent to about 0.04 percent additive is added to direct morphology and size, and reacted with CO2 gas. The reaction proceeds 10 percent to 40 percent of the way through at which point the reaction is stopped. This produces a partially converted Ca (OH)2/CaCO3 slurry which is then fed into a reaction vessel at a rate that matches CO2 gassing to maintain a given conductivity (ionic saturation) to produce an acicular, aragonitic crystal. The reaction continues until process stabilization is achieved. The product made once stabilization is achieved, (approximately 95 percent calcium carbonate) is mixed with diluted fibers (approximately 1.5 percent concentration) and water. The calcium carbonate and fibers are then reacted with CO2 gas to an endpoint of pH 7.0. The product manufactured using this method contains from about 0.2 percent to about 99.8 percent aragonitic PCC with respect to the fibers at about 3 percent to about 5 percent total solids.
- The product has a specific surface area of about 5 meters squared per gram to about 8 meters squared per gram; product solids from about 3 percent to about 5 percent by weight and a PCC content from about 0.2 percent to about 99.8 percent with respect to fibers and has a predominantly aragonitic morphology.
- Rhombohedral Morphology
- The first step in this process involves making a high reactive Ca (OH)2 milk-of-lime slake which is screened at −325 mesh and has a concentration of approximately 20 percent by weight. 0.1 percent citric acid is added to inhibit aragonite formation. A portion of this slake is added to an agitated reactor, brought to a desired reaction temperature and carbonated with CO2 gas. The reaction proceeds to conductivity minimum producing a “heel”. A “heel” is defined as a fully converted calcium carbonate crystal with average particle size typically in the range of about 1 micron to about 2.5 micron with any crystal morphology. Sodium carbonate is added to the remainder of the slake not used in the manufacture of the “heel” material. This slake and CO2 is added to the “heel” material at a CO2 gassing rate to maintain a given conductivity (ionic saturation) to produce a rhombohedral crystal. The reaction is continued until process stabilization is achieved. Once stabilization is achieved, this product (approximately 90 percent to 95 percent converted) is mixed with diluted fibers (approximately 1.5 percent concentration) and water. Additional CO2 is added to an endpoint of pH 7.0. The product manufactured using this method contains from about 0.2 percent to about 99.8 percent rhombohedral PCC with respect to fibers and is about 3 percent to about 5 percent total solids.
- The product has a specific surface area from about 5 meters squared per gram to about 8 meters squared per gram; product solids from about 3 percent to about 5 percent; and PCC content from about 0.2 percent to about 99.8 percent and has a predominantly rhombohedral morphology:
- The following examples are intended to exemplify the invention and are not intended to limit the scope of the invention.
- Scalenohedral PCC
- Reacted 15 liters of water with 3 kilogram CaO at 50 degrees Celsius producing a 20 percent by weight Ca(OH)2 slake. The Ca(OH)2 slake was then screened at −325 mesh producing a screened slake that was transferred to a first 30-liter double jacketed stainless steel reaction vessel with an agitation of 615 revolutions per minute (rpm). 0.1 percent citric acid, by weight of total theoretical CaCO3 to be produced, was added to the screened slake in a 30-liter reaction vessel and the temperature of the contents brought to 40 degrees Celsius. Began addition of 20 percent CO2 gas in air (14.83 standard liter minute CO2/59.30 standard liter minute air) to the 30-liter reaction vessel to produce a 2:1 Ca (OH)2/CaCO3 slurry. At this point, CO2 gassing was stopped and the slurry was transferred to an agitated 20-liter storage vessel.
- 2 liters of the 2:1 Ca(OH)2/CaCO3 slurry was transferred to a first 4-liter agitated (1250 rpm) stainless steel, double jacketed reaction vessel. The temperature was brought to 51 degrees Celsius and 20 percent CO2 gas in air (1.41 standard liter minute CO2/5.64 standard liter minute air) was added to the first 4-liter reaction vessel until a pH of 7.0 was achieved producing a CaCO3 slurry. Once a pH 7.0 was achieved began addition of the 2:1 Ca(OH)2/CaCO3 slurry of the 20-liter storage vessel to the first 4-liter reaction vessel while continuing to add 20 percent CO2 gas in air (1.41 standard liter minute CO2/5.64 standard liter minute air) to the first 4-liter reaction vessel to maintain a conductivity of approximately 90 percent ionic saturation. The addition of Ca(OH)2/CaCO3 slurry and CO2 to the first 4-liter reaction vessel was continued for approximately 12 hours until product physical properties remained essentially unchanged, producing a CaCO3 slurry that was approximately 98 percent converted. Transferred 0.18 liters of the 98 percent CaCO3 slurry to a second 4-liter agitated (1250 rpm), stainless steel, double jacketed reaction vessel, added 0.66 liters of 3.8 percent by dry weight cellulosic fibers and diluted to 1.5 percent consistency. This mixture of CaCO3 slurry and fiber was reacted with 20 percent CO2 in air (1.41 standard liter minute CO2/5.64 standard liter minute air) to produce a CaCO3 filler-fiber composite. The calcium carbonate filler had a predominantly scalenohedral morphology.
- Aragonitic PCC
- Reacted 10.5 liters of water with 2.1 kilograms CaO at 50 degrees Celsius producing a 15 percent by weight Ca(OH)2 slake. The Ca(OH)2 slake was then screened at −325 mesh producing a screened slake that was transferred to a 30-liter double jacketed stainless steel reaction vessel with an agitation of 615rpm. Added 0.1 percent by weight of a high surface area (HSSA) aragonitic seed (surface area ˜40 meters squared per gram, approximately 25 percent solids) to the 30-liter reaction vessel and brought the temperature of the contents to 51 degrees Celsius. A “seed” is defined as a fully converted aragonitic crystal that has been endpointed and milled to a high specific surface area (i.e. greater than 30 meters squared per gram and typically a particle size of 0.1 to 0.4 microns). Began addition of 10 percent CO2 gas in air (5.24 standard liter minute CO2/47.12 standard liter minute air) to the 30-liter stainless steel, double jacketed reaction vessel for a 15-minute period after which the CO2 concentration was increased to 20 percent in air (10.47 standard liter minute CO2/41.89 standard liter minute air) for an additional 15 minutes producing a 2.3:1 Ca (OH)2/CaCO3 slurry. At which time CO2 gassing was stopped. The 2.3:1 Ca(OH)2/CaCO3 slurry was transferred to an agitated 20-liter storage vessel. Transferred 2 liters of the 2.3:1 Ca(OH)2/CaCO3 slurry to a first 4-liter agitated, double jacketed stainless steel reaction vessel with agitation set at 1250rpm and the temperature was brought to 52 degrees Celsius. Began addition of 20 percent CO2 gas in air (1.00 standard liter minute CO2/3.99 standard liter minute air) to the first 4-liter reaction vessel and the reaction was continued until a pH of 7.0 was achieved producing a 100 percent CaCO3 slurry. The temperature of the 100 percent CaCO3 slurry of the first 4-liter reaction vessel was brought to 63 degrees Celsius. Began addition of the 2.3:1 Ca(OH)2/CaCO3 slurry of the 20-liter storage vessel to the first 4-liter reaction vessel while continuing to add 20 percent CO2 in air (1.00 standard liter minute CO2/3.99 standard liter minute air) to the first 4-liter reaction vessel maintaining a conductivity of approximately 90 percent ionic saturation. Continued the reaction for approximately 9 hours until the physical properties of the resultant product remained essentially unchanged, producing a 98 percent by wt. CaCO3 slurry.
- Transferred 0.35 liters of the 98 percent CaCO3 slurry to a second 4-liter agitated (1250 rpm), stainless steel, double jacketed reaction vessel, added 0.66 liters of 3.8 percent by wt. cellulosic fiber and 1.0 liters water to the second 4-liter reactor producing a 1.5 percent by wt. CaCO3/fiber mixture. Added an additional 20 percent CO2 in air (1.00 standard liter minute CO2/3.99 standard liter minute air) to the second 4-liter reaction vessel until a pH of 7.0 was reached at which time the reaction was completed producing a CaCO3/fiber composite. The composite consisted of approximately 75 percent aragonitic PCC to fiber.
- Rhombohedral PCC
- Reacted 15 liters of water with 3 kilograms CaO at 50 degrees Celsius producing a 20 percent by weight Ca(OH)2 slake. The Ca(OH)2 slake was screened at −325 mesh producing a screened slake that was transferred to an agitated 20-liter storage vessel. Transferred 2-liters of the screened slake from the 20-liter storage vessel to a first 4-liter agitated, stainless steel, double jacketed reaction vessel and began agitation at 1250 rpm. Added 0.03 percent citric acid by weight of theoretical CaCO3 to the first 4-liter reaction vessel and raised the temperature of the contents to 50 degrees Celsius. Added 20 percent CO2 gas in air (1.44 standard liter minute CO2/5.77 standard liter minute air) to the first 4-liter reaction vessel until a pH of 7.0 was achieved producing a 100 percent CaCO3 slurry. To the screened slake in the 20-liter storage vessel, added a solution of 1.3 percent by weight of Na2CO3, based on theoretical yield of CaCO3, producing a Ca(OH)2/Na2CO3 slake. Increased the temperature of the contents of the first 4-liter reaction vessel to approximately 68 degrees Celsius and began addition of the Ca(OH)2/Na2CO3 slake of the 20-liter storage vessel to the first 4-liter reaction vessel while continuing to add 20 percent CO2 in air (1.44 standard liter minute CO2/5.77 standard liter minute air) to the first 4-liter reaction vessel maintaining a conductivity of approximately 50 percent ionic saturation. Addition of the Ca(OH)2/Na2CO3 slake and CO2 was continued for approximately 12 hours until physical properties of the resultant product remained essentially unchanged producing an approximate 98 percent by wt. CaCO3 slurry.
- Transferred 0.22 liters of the 98 percent CaCO3 slurry to a second 4-liter agitated (1250 rpm) dual jacketed, stainless steel reaction vessel and added 0.66 liters of 3.8 percent by weight cellulosic fiber and 1.0 liters water to the second 4-liter reactor producing a 1.5 percent by weight CaCO3/fiber mixture. Added an additional 20 percent CO2 in air (1.44 standard liter minute CO2/5.77 standard liter minute air) to the second 4-liter reaction vessel until a pH of 7.0 was reached at which time the reaction was completed producing an approximate 3.4 percent by wt CaCO3/fiber composite. The calcium carbonate had a predominantly rhombohedral morphology.
- Scalenohedral—CFSTR
- Reacted 15 liters of water with 3 kilograms CaO at 48 degrees Celsius to produce a Ca(OH)2 slake, added an additional 6 liters of water producing a 20 percent by weight Ca(OH)2 slake. The 20 percent Ca(OH)2 slake was screened at −325 mesh and transferred to a 30-liter double jacketed, stainless steel reaction vessel with an agitation of 615rpm. Added 0.015 percent citric acid, by weight of total theoretical CaCO3 to be produced, to the 30-liter reaction vessel and the temperature of the contents brought to 36 degrees Celsius. Began addition of 20 percent CO2 gas in air (13.72 standard liter minute CO2/54.89 standard liter minute air) to the 30-liter reaction vessel to produce a 5:1 Ca(OH)2/CaCO3 slurry. CO2 gassing was stopped and the Ca(OH)2/CaCO3 slurry was transferred to an agitated 20-liter storage vessel.
- In a 4-liter agitated storage vessel, combined 0.25 liters of the Ca(OH)2/CaCO3 slurry with 0.66 liters of 3.8 percent by weight fibers and with 1.09 liters of water making a Ca(OH)2/CaCO3/fiber material. Transferred 2 liters of the Ca(OH)2/CaCO3/fiber material to a 4-liter agitated (1250 revolutions per minute) reaction vessel and the temperature brought to 55 degrees Celsius and carbonated with 20 percent CO2 in air (1.30 standard liter minute CO2/5.23 standard liter minute air) to a pH of 7.0 producing a CaCO3/fiber composite. Prepared 16-liters of 1.5 percent by weight fibers and a separate 10-liter vessel of water. To the 4-liter reaction vessel began addition of the Ca(OH)2/CaCO3 slurry of the 20-liter agitated storage vessel, along with the 1.5 percent consistency fiber mixture at 172.05 ml per minute, along with 31.21 ml per minute of additional water while maintaining the flow of CO2 gas (1.30 standard liter minute CO2/5.23 standard liter minute air) at a rate to maintain conductivity of approximately 90 percent ionic saturation, while maintaining mass balance of approximately 4 percent to 5 percent total solids.
- This reaction was continued until product physical properties remained essentially unchanged. Addition of material from the storage vessel was stopped while CO2 addition was continued and the material in the 4-liter agitated reaction vessel was brought to a pH of 7.0 at which time CO2 addition was stopped producing a 2.2:1 CaCO3/fiber composite with the CaCO3 having a well defined scalenohedral morphology.
- Scalenohedral CFSTR/Surfactant
- Reacted 15 liters of water with 3 kilograms CaO at 48 degrees Celsius to produce a Ca(OH)2 slake, added an additional 6 liters of water producing a 20 percent by weight Ca(OH)2 slake. The 20 percent Ca(OH)2 slake was screened at −325 mesh and transferred to a 30-liter reaction vessel (615 revolutions per minute). Added 0.015 percent citric acid, by weight of total theoretical CaCO3 to be produced, to the 30-liter reaction vessel and the temperature of the contents brought to 35 degrees Celsius. Began addition of 20 percent CO2 gas in air (14.08 standard liter minute CO2/56.30 standard liter minute air) to the 30-liter reaction vessel producing a 5:1 Ca(OH)2/CaCO3 slurry. At this point, CO2 gassing was stopped and the Ca(OH)2/CaCO3 slurry was transferred to a 20-liter agitated storage vessel.
- In a 4-liter agitated storage vessel, combined 0.25 liters of the Ca(OH)2/CaCO3 slurry with 0.66 liters of 3.8 percent by weight fibers and with 1.09 liters of water making 2 liters of Ca(OH)2/CaCO3/fiber material.
- Transferred 2 liters of the Ca(OH)2/CaCO3/fiber material to a 4-liter stainless steel, double jacketed, agitated (1250 revolutions per minute) reaction vessel and the temperature was brought to 58 degrees Celsius. Reacted the Ca(OH)2/CaCO3/fiber material with 20 percent CO2 in air (1.30 standard liter minute CO2/5.23 standard liter minute air) to a pH of 7.0.
- At this point, prepared 16-liters of 1.5 percent by weight fibers (6.32 liters of fibers at 3.8 percent consistency and 9.68 liters of water) and a separate 10-liter vessel of water. Added 0.04 percent surfactant based on the volume of fibers at 1.5 percent consistency. The surfactant is Tergitol™ MIN-FOAM 2× which is available commercially from Union Carbide, 39 Old Ridgebury Road, Danbury, Conn. 06817.
- Once a pH of 7.0 was achieved in the 4-liter reaction vessel, began addition of the remaining 5:1 Ca(OH)2/CaCO3 slurry from the 20-liter agitated storage vessel, with a flow of the 1.5 percent fiber mixture at 176.48 ml per minute and with 32.00 ml per minute water from the 10-liter vessel to the 4-liter reaction vessel while maintaining the flow of CO2 gas (1.30 standard liter minute CO2/5.23 standard liter minute air) at a rate to maintain conductivity of approximately 90 percent ionic saturation, while maintaining mass balance of approximately 4 percent to 5 percent total solids. Continued addition of the material from the agitated storage vessel to the reaction vessel until product physical properties remained essentially unchanged. At which point, addition of material from the storage vessel was stopped while CO2 addition was continued to a pH of 7.0 at which time CO2 addition was stopped. This produced a 2.33:1 CaCO3/fiber composite with the calcium carbonate having a well defined scalenohedral morphology.
- Scalenohedral CFSTR/Polyacrylamide
- Reacted 15 liters of water with 3 kilograms CaO at 48 degrees Celsius producing a Ca(OH)2 slake, added an additional 6 liters of water producing a 20 percent by weight Ca(OH)2 slake. The 20 percent Ca(OH)2 slake was then screened at −325 mesh producing a screened slake that was transferred to a 30-liter agitated (615 rpm) reaction vessel. Added 0.1 percent citric acid, by weight of total theoretical CaCO3 to be produced, to the 30-liter reaction vessel and the temperature of the contents brought to 50 degrees Celsius. Began addition of 20 percent CO2 gas in air (15.01 standard liter minute CO2/60.06 standard liter minute air) to the 30-liter reaction vessel producing a 5:1 Ca(OH)2/CaCO3 slurry. CO2 gassing was stopped and the slurry was transferred to a 20-liter agitated storage vessel. To a 4-liter agitated vessel added 0.31 liters of the Ca(OH)2/CaCO3 slurry, 0.60 liters of fibers at 3.8 percent consistency and 1.09 liters of water to produce a Ca(OH)2/CaCO3/fiber material. 2 liters of the Ca(OH)2/CaCO3/fiber material was transferred to a 4-liter agitated (1250 revolutions per minute) reaction vessel and the temperature was brought to 51 degrees Celsius. Began addition of 20 percent CO2 in air (1.34 standard liter minute CO2/5.34 standard liter minute air) until a pH of 7.0 was reached producing a CaCO3/fiber composite.
- At this point, prepared 16-liters of 1.5 percent by weight fibers (6.32 liters of fibers at 3.8 percent consistency and 9.68 liters of water) and a separate 10-liter vessel of water. Added 0.05 percent cationic polyacrylamide (Percol 292) based on the volume of fibers at 1.5 per cent consistency. Percol 292 is commercially available from Allied Colloids, 2301 Wilroy Road, Suffolk, Va. 23434.
- Once a pH of 7.0 was achieved in the 4-liter reaction vessel, began addition of the remaining 5:1 Ca(OH)2/CaCO3 slurry from the 20-liter agitated storage vessel, with a flow of the 1.5 percent fiber mixture at 90 ml per minute, along with 48.5 ml per minute of additional water to the 4-liter agitated, double jacketed reaction vessel while maintaining the flow of CO2 gas (1.30 standard liter minute CO2/5.23 standard liter minute air) at a rate to maintain conductivity level of approximately 90 percent ionic saturation, and maintain mass balance of the reaction to maintain product concentration at approximately 4 percent to 5 percent solids. Continued addition of the material from the agitated storage vessel to the reaction vessel until product physical properties remained essentially unchanged. Addition of material from the 20-liter storage vessel was stopped while CO2 addition was continued until a pH of 7.0 was reached at which time CO2 addition was stopped producing a 3.34:1 CaCO3/fiber composite with the PCC having a well defined scalenohedral morphology.
- The control fiber of the present invention was refined at the Empire State Paper Research Institute (ESPRI) using an Escher-Wyss (conical) refiner to an 80° SR (freeness). Measured by a fiber quality analyzer (using arithmatic means) the control fiber measured 200-400 microns
- How Control Filler-Fiber was Made
- Produce a 15% solids slake and mix with fibers (˜1.5% consistency) React in the presence of CO2 to endpoint of pH of 7.0 producing a filler-fiber composite with a surface area of 6-11 m2/g (˜60 to 80% PCC but can have more or less in composite)
TABLE 1 Breaking Length Physical Properties in Meters Filler Loading Scalenohedral Aragonitic Rhombohedral Control Levels Filler-fiber Filler-fiber Filler-fiber Filler-fiber 20 4,021 4,599 4,312 4,245 25 3,799 4,358 3,813 3,715 30 3,280 3,674 3,871 2,998 -
TABLE 2 Tensile Strength Physical Properties in kN/m Filler Loading Scalenohedral Aragonitic Rhombohedral Control Levels Filler-fiber Filler-fiber Filler-fiber Filler-fiber 20 3.062 3.555 3.397 3.382 25 3.124 3.324 2.999 3.021 30 2.658 2.785 3.005 2.448 -
TABLE 3 Internal Bond Strength Physical Properties in ft-lb Filler Loading Scalenohedral Aragonitic Rhombohedral Control Levels Filler-fiber Filler-fiber Filler-fiber Filler-fiber 20 237.70 264.07 283.13 255.67 25 263.20 285.95 251.65 256.95 30 242.63 248.60 273.65 249.53 - The morphology controlled filler-fiber composite showed equivalent or greater physical properties (i.e. tensil strength, breaking length, and internal bond strength) as compared with the control filler-fiber.
TABLE 4 ISO Opacity Optical Properties Filler Loading Scalenohedral Aragonitic Rhombohedral Control Levels Filler-fiber Filler-fiber Filler-fiber Filler-fiber 20 89.20 88.20 87.38 88.18 25 89.93 89.15 88.78 89.55 30 90.95 90.40 89.68 90.83 -
TABLE 5 Pigment Scatter Optical Properties Filler Loading Scalenohedral Aragonitic Rhombohedral Control Levels Filler-fiber Filler-fiber Filler-fiber Filler-fiber 20 60.15 55.47 55.08 58.55 25 64.90 62.40 61.10 65.40 30 70.55 69.55 65.80 73.13 - The morphology controlled filler-fiber composite showed equivalent optical properties (i.e. ISO Opacity and Pigment Scatter) as compared with the control filler-fiber.
Claims (48)
1. A filler-fiber composite comprising:
(a) feeding slake containing citric acid to a first stage reactor
(b) reacting the slake containing citric acid in the first stage reactor in the presence of carbon dioxide to produce a first partially converted calcium hydroxide calcium carbonate slurry
(c) reacting the first partially converted calcium hydroxide calcium carbonate slurry in a second stage reactor in the presence of carbon dioxide to produce a second partially converted calcium hydroxide calcium carbonate slurry and
(d) reacting the second partially converted calcium hydroxide calcium carbonate slurry in a third stage reactor in the presence of carbon dioxide and fibrils to produce a filler-fiber composite.
2. The filler-fiber composite of claim 1 wherein the fiber is from about 0.1 microns to about 2 microns in thickness and from about 10 microns to about 400 microns in length.
3. The filler-fiber composite of claim 2 wherein the filler is scalenohedral having a specific surface area of from about 5 meters squared per gram to about 11 meters squared per gram.
4. The filler-fiber composite of claim 3 wherein the calcium hydroxide calcium carbonate slurry is converted from about 20 percent to about 40 percent.
5. The filler-fiber composite of claim 4 wherein the first partially converted calcium hydroxide calcium carbonate slurry is converted from about 41 percent to about 99 percent.
6. The filler-fiber composite of claim 5 wherein the second partially converted calcium hydroxide calcium carbonate slurry is converted to a filler-fiber composite.
7. A method for producing a filler-fiber composite comprising:
(a) feeding slake containing citric acid to a first stage reactor
(b) reacting the slake containing citric acid in the first stage reactor in the presence of carbon dioxide to produce a first partially converted calcium hydroxide calcium carbonate slurry
(c) reacting the first partially converted calcium hydroxide calcium carbonate slurry in a second stage reactor in the presence of carbon dioxide to produce a second partially converted calcium hydroxide calcium carbonate slurry and
(d) reacting the second partially converted calcium hydroxide calcium carbonate slurry in a third stage reactor in the presence of carbon dioxide and fibers to produce a filler-fiber composite.
8. The method of producing the filler-fiber composite of claim 7 wherein the fiber is from about 0.1 microns to about 2 microns in thickness and from about 10 microns to about 400 microns in length.
9. The method of producing the filler-fiber composite of claim 8 wherein the filler is scalenohedral and has a specific surface area of from about 5 meters squared gram to about 11 meters squared per gram.
10. The method of producing the filler-fiber composite of claim 9 wherein the calcium hydroxide calcium carbonate slurry is converted from about 20 percent to about 40 percent.
11. The method of producing the filler-fiber composite of claim 10 wherein the first partially converted calcium hydroxide calcium carbonate slurry is converted from about 41 percent to about 99 percent.
12. The filler-fiber composite of claim 11 wherein the second partially converted calcium hydroxide calcium carbonate slurry is converted to a filler-fiber composite.
13. The filler-fiber composite of claim 1 utilized in paper or paperboard
14. The filler-fiber composite of claim 7 utilized in paper or paperboard.
15. The paper produced utilizing the filler-fiber of claim 1 .
16. The paper produced utilizing the filler-fiber of claim 7 .
17. A filler-fiber composite comprising:
(a) feeding slake containing citric acid to a first stage reactor
(b) reacting the slake containing citric acid in the first stage reactor in the presence of carbon dioxide to produce a first partially converted calcium hydroxide calcium carbonate slurry
(c) taking a first portion of the partially converted calcium hydroxide calcium carbonate slurry adding fibrils and reacting such in a second stage reactor in the presence of carbon dioxide to produce a calcium carbonate\fibril composite to serve as a heel and
(d) taking a second portion of the partially converted calcium hydroxide calcium carbonate slurry adding fibrils and surfactant and reacting in the presence of CO2 to produce a second partially converted Ca(OH)2/CaCO3/fibril material and
(e) reacting the second partially converted Ca(OH)2/CaCO3/fibril material in the presence of CO2 in a third stage reactor to produce a filler-fiber composite.
18. The filler-fiber composite of claim 17 wherein the fiber is from about 0.1 microns to about 2 microns in thickness and from about 10 microns to about 400 microns in length.
19. The filler-fiber composite of claim 18 wherein the filler is scalenohedral having a specific surface area of from about 5 meters squared per gram to about 11 meters squared per gram.
20. The filler-fiber composite of claim 19 wherein the calcium hydroxide calcium carbonate slurry is converted from about 20 percent to about 40 percent.
21. The filler-fiber composite of claim 20 wherein the first partially converted calcium hydroxide calcium carbonate slurry is converted from about 41 percent to about 99 percent.
22. The filler-fiber composite of claim 21 wherein the second partially converted calcium hydroxide calcium carbonate slurry is converted to a filler-fiber composite.
23. A method for producing a filler-fiber composite comprising:
(a) feeding slake containing citric acid to a first stage reactor
(b) reacting the slake containing citric acid in the first stage reactor in the presence of carbon dioxide to produce a first partially converted calcium hydroxide calcium carbonate slurry
(c) taking a first portion of the partially converted calcium hydroxide calcium carbonate slurry adding fibrils and reacting such in a second stage reactor in the presence of carbon dioxide to produce a calcium carbonate\fibril composite to serve as a heel and
(d) taking a second portion of the partially converted calcium hydroxide calcium carbonate slurry adding fibrils and surfactant and reacting in the presence of CO2 to produce a second partially converted Ca(OH)2/CaCO3/fibril material and reacting the second partially converted Ca(OH)2/CaCO3/fibril material in the presence of CO2 in a third stage reactor to produce a filler-fiber composite.
24. The method for producing filler-fiber composite of claim 23 wherein the fiber is from about 0.1 microns to about 2 microns in thickness and from about 10 microns to about 400 microns in length.
25. The method for producing filler-fiber composite of claim 24 wherein the filler is scalenohedral having a specific surface area of from about 5 meters squared per gram to about 11 meters squared per gram.
26. The method for producing filler-fiber composite of claim 25 wherein the calcium hydroxide calcium carbonate slurry is converted from about 20 percent to about 40 percent.
27. The method for producing filler-fiber composite of claim 26 wherein the first partially converted calcium hydroxide calcium carbonate slurry is converted from about 41 percent to about 99 percent.
28. The method for producing filler-fiber composite of claim 27 wherein the second partially converted calcium hydroxide calcium carbonate slurry is converted to a filler-fiber composite.
29. The filler-fiber composite of claim 17 utilized in paper or paperboard
30. The filler-fiber composite of claim 23 utilized in paper or paperboard.
31. The paper produced utilizing the filler-fiber of claim 17 .
32. The paper produced utilizing the filler-fiber of claim 23 .
33. A filler-fiber composite comprising:
(a) feeding slake containing citric acid to a first stage reactor
(b) reacting the slake containing citric acid in the first stage reactor in the presence of carbon dioxide to produce a first partially converted calcium hydroxide calcium carbonate slurry
(c) taking a first portion of the partially converted calcium hydroxide calcium carbonate slurry adding fibrils and reacting such in a second stage reactor in the presence of carbon dioxide to produce a calcium carbonate/fibril composite to serve as a heel and
(d) taking a second portion of the partially converted calcium hydroxide calcium carbonate slurry adding fibrils and polyacrylamide and reacting in the presence of CO2 to produce a second partially converted Ca(OH)2/CaCO3/fibril material and
(e) reacting the second partially converted Ca(OH)2/CaCO3/fibril material in the presence of CO2 in a third stage reactor to produce a filler/fiber composite.
34. The filler-fiber composite of claim 33 wherein the fiber is from about 0.1 microns to about 2 microns in thickness and from about 10 microns to about 400 microns in length.
35. The filler-fiber composite of claim 34 wherein the filler is scalenohedral having a specific surface area of from about 5 meters squared per gram to about 11 meters squared per gram.
36. The filler-fiber composite of claim 35 wherein the calcium hydroxide calcium carbonate slurry is converted from about 20 percent to about 40 percent.
37. The filler-fiber composite of claim 36 wherein the first partially converted calcium hydroxide calcium carbonate slurry is converted from about 41 percent to about 99 percent.
38. The filler-fiber composite of claim 37 wherein the second partially converted calcium hydroxide calcium carbonate slurry is converted to a filler-fiber composite.
39. A method of producing a filler-fiber composite comprising:
(a) feeding slake containing citric acid to a first stage reactor
(b) reacting the slake containing citric acid in the first stage reactor in the presence of carbon dioxide to produce a first partially converted calcium hydroxide calcium carbonate slurry
(c) taking a first portion of the partially converted calcium hydroxide calcium carbonate slurry adding fibrils and reacting such in a second stage reactor in the presence of carbon dioxide to produce a calcium carbonate\fibril composite to serve as a heel and
(d) taking a second portion of the partially converted calcium hydroxide calcium carbonate slurry adding fibrils and polyacrylamide and reacting in the presence of CO2 to produce a second partially converted Ca(OH)2/CaCO3/fibril material and
(e) reacting the second partially converted Ca(OH)2/CaCO3/fibril material in the presence of CO2 in a third stage reactor to produce a filler/fiber composite.
40. The method for producing filler-fiber composite of claim 39 wherein the fiber is from about 0.1 microns to about 2 microns in thickness and from about 10 microns to about 400 microns in length.
41. The method for producing filler-fiber composite of claim 40 wherein the filler is scalenohedral having a specific surface area of from about 5 meters squared per gram to about 11 meters squared per gram.
42. The method for producing filler-fiber composite of claim 41 wherein the calcium hydroxide calcium carbonate slurry is converted from about 20 percent to about 40 percent.
43. The method for producing filler-fiber composite of claim 42 wherein the first partially converted calcium hydroxide calcium carbonate slurry is converted from about 41 percent to about 99 percent.
44. The method for producing filler-fiber composite of claim 43 wherein the second partially converted calcium hydroxide calcium carbonate slurry is converted to a filler-fiber composite.
45. The filler-fiber composite of claim 33 utilized in paper or paperboard
46. The filler-fiber composite of claim 39 utilized in paper or paperboard.
47. The paper produced utilizing the filler-fiber of claim 33 .
48. The paper produced utilizing the filler-fiber of claim 39.
Priority Applications (15)
Application Number | Priority Date | Filing Date | Title |
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US10/314,584 US20040108081A1 (en) | 2002-12-09 | 2002-12-09 | Filler-fiber composite |
AU2003293225A AU2003293225A1 (en) | 2002-12-09 | 2003-12-03 | Filler-fiber composite |
RU2005121567/04A RU2005121567A (en) | 2002-12-09 | 2003-12-03 | COMPOSITE MATERIAL FILLER-FIBER |
CNA200380105511XA CN1723314A (en) | 2002-12-09 | 2003-12-03 | Filler-fiber composite |
CA002509514A CA2509514A1 (en) | 2002-12-09 | 2003-12-03 | Filler-fiber composite |
EP03790217A EP1576236A1 (en) | 2002-12-09 | 2003-12-03 | Filler-fiber composite |
PCT/US2003/038218 WO2004053229A1 (en) | 2002-12-09 | 2003-12-03 | Filler-fiber composite |
BR0316926-0A BR0316926A (en) | 2002-12-09 | 2003-12-03 | Fiber-filler composite, method for producing a fiber-filler composite, and paper |
JP2004559205A JP2006509118A (en) | 2002-12-09 | 2003-12-03 | Filler-fiber composite |
CL200302529A CL2003002529A1 (en) | 2002-12-09 | 2003-12-04 | METHOD FOR PRODUCING A FILLING AND FIBER MATERIAL COMPOUND, WHICH INCLUDES FEEDING A REACTOR A HYDROTED CALCIUM ION MATERIAL TO WHICH CITRUS ACID IS ADDED AND SO MAKES REACTION IN THE PRESENCE OF CO2 GAS TO FINALLY PRECIPITATE |
ARP030104509A AR042328A1 (en) | 2002-12-09 | 2003-12-05 | A FILLING COMPOUND - FIBER, METHOD TO PRODUCE IT AND THE PAPER OR CARTON CONTAINING SUCH COMPOUND |
UY28107A UY28107A1 (en) | 2002-12-09 | 2003-12-05 | FILLING-FIBER COMPOUND |
KR1020030088374A KR20040050051A (en) | 2002-12-09 | 2003-12-06 | Filler-fiber composite |
TW092134687A TW200500534A (en) | 2002-12-09 | 2003-12-09 | Filler-fiber composite |
NO20053138A NO20053138L (en) | 2002-12-09 | 2005-06-27 | Filler-fiber composite. |
Applications Claiming Priority (1)
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US10/314,584 US20040108081A1 (en) | 2002-12-09 | 2002-12-09 | Filler-fiber composite |
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US20040108081A1 true US20040108081A1 (en) | 2004-06-10 |
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US10/314,584 Abandoned US20040108081A1 (en) | 2002-12-09 | 2002-12-09 | Filler-fiber composite |
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US (1) | US20040108081A1 (en) |
EP (1) | EP1576236A1 (en) |
JP (1) | JP2006509118A (en) |
KR (1) | KR20040050051A (en) |
CN (1) | CN1723314A (en) |
AR (1) | AR042328A1 (en) |
AU (1) | AU2003293225A1 (en) |
BR (1) | BR0316926A (en) |
CA (1) | CA2509514A1 (en) |
CL (1) | CL2003002529A1 (en) |
NO (1) | NO20053138L (en) |
RU (1) | RU2005121567A (en) |
TW (1) | TW200500534A (en) |
UY (1) | UY28107A1 (en) |
WO (1) | WO2004053229A1 (en) |
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US20040168781A1 (en) * | 2002-08-05 | 2004-09-02 | Petri Silenius | Noil for use in paper manufacture, method for its production, and paper pulp and paper containing such noil |
WO2006032333A1 (en) * | 2004-09-17 | 2006-03-30 | Voith Patent Gmbh | Method and device for charging a fibre material suspension |
WO2010029403A1 (en) * | 2008-09-09 | 2010-03-18 | Omya Development Ag | Compositions of calcium carbonates/pigments for paper formulations, showing print through reduction |
WO2011134939A1 (en) * | 2010-04-27 | 2011-11-03 | Omya Development Ag | Process for the manufacture of structured materials using nano-fibrillar cellulose gels |
WO2011134938A1 (en) * | 2010-04-27 | 2011-11-03 | Omya Development Ag | Process for the production of gel-based composite materials |
US8871057B2 (en) | 2009-03-30 | 2014-10-28 | Omya International Ag | Process for the production of nano-fibrillar cellulose suspensions |
US8871056B2 (en) | 2009-03-30 | 2014-10-28 | Omya International Ag | Process for the production of nano-fibrillar cellulose gels |
US9127405B2 (en) | 2009-05-15 | 2015-09-08 | Imerys Minerals, Limited | Paper filler composition |
US10112844B2 (en) | 2014-03-31 | 2018-10-30 | Nippon Paper Industries Co., Ltd. | Calcium carbonate microparticles and processes for preparing them |
US10214859B2 (en) | 2016-04-05 | 2019-02-26 | Fiberlean Technologies Limited | Paper and paperboard products |
US10253457B2 (en) | 2010-11-15 | 2019-04-09 | Fiberlean Technologies Limited | Compositions |
US10577469B2 (en) | 2015-10-14 | 2020-03-03 | Fiberlean Technologies Limited | 3D-formable sheet material |
EP3604671A4 (en) * | 2017-03-31 | 2020-04-15 | Nippon Paper Industries Co., Ltd. | Method for manufacturing inorganic particle composite fiber sheet |
US10794006B2 (en) | 2016-04-22 | 2020-10-06 | Fiberlean Technologies Limited | Compositions comprising microfibrilated cellulose and polymers and methods of manufacturing fibres and nonwoven materials therefrom |
US11846072B2 (en) | 2016-04-05 | 2023-12-19 | Fiberlean Technologies Limited | Process of making paper and paperboard products |
US11970817B2 (en) | 2009-05-15 | 2024-04-30 | Fiberlean Technologies Limited | Paper filler composition |
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JP7034864B2 (en) * | 2017-10-31 | 2022-03-14 | 日本製紙株式会社 | Functional materials and their use |
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- 2003-12-03 RU RU2005121567/04A patent/RU2005121567A/en not_active Application Discontinuation
- 2003-12-03 CN CNA200380105511XA patent/CN1723314A/en active Pending
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- 2003-12-03 EP EP03790217A patent/EP1576236A1/en not_active Withdrawn
- 2003-12-03 BR BR0316926-0A patent/BR0316926A/en not_active IP Right Cessation
- 2003-12-04 CL CL200302529A patent/CL2003002529A1/en unknown
- 2003-12-05 AR ARP030104509A patent/AR042328A1/en not_active Application Discontinuation
- 2003-12-05 UY UY28107A patent/UY28107A1/en not_active Application Discontinuation
- 2003-12-06 KR KR1020030088374A patent/KR20040050051A/en not_active Application Discontinuation
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US8580082B2 (en) | 2008-09-09 | 2013-11-12 | Omya International Ag | Compositions of calcium carbonates/pigments for paper formulations, showing print through reduction |
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Also Published As
Publication number | Publication date |
---|---|
RU2005121567A (en) | 2006-01-20 |
CA2509514A1 (en) | 2004-06-24 |
EP1576236A1 (en) | 2005-09-21 |
TW200500534A (en) | 2005-01-01 |
KR20040050051A (en) | 2004-06-14 |
BR0316926A (en) | 2005-10-18 |
UY28107A1 (en) | 2004-08-31 |
AR042328A1 (en) | 2005-06-15 |
AU2003293225A1 (en) | 2004-06-30 |
WO2004053229A1 (en) | 2004-06-24 |
NO20053138L (en) | 2005-06-27 |
CN1723314A (en) | 2006-01-18 |
CL2003002529A1 (en) | 2005-01-28 |
JP2006509118A (en) | 2006-03-16 |
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