AU7122100A - Cationically modified polysaccharides - Google Patents
Cationically modified polysaccharides Download PDFInfo
- Publication number
- AU7122100A AU7122100A AU71221/00A AU7122100A AU7122100A AU 7122100 A AU7122100 A AU 7122100A AU 71221/00 A AU71221/00 A AU 71221/00A AU 7122100 A AU7122100 A AU 7122100A AU 7122100 A AU7122100 A AU 7122100A
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- Australia
- Prior art keywords
- cationic
- furnish
- starch
- pulp
- retention
- 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.)
- Abandoned
Links
- 150000004676 glycans Chemical class 0.000 title claims description 46
- 229920001282 polysaccharide Polymers 0.000 title claims description 46
- 239000005017 polysaccharide Substances 0.000 title claims description 46
- 229920002472 Starch Polymers 0.000 claims description 151
- 235000019698 starch Nutrition 0.000 claims description 150
- 239000008107 starch Substances 0.000 claims description 144
- 230000014759 maintenance of location Effects 0.000 claims description 137
- 125000002091 cationic group Chemical group 0.000 claims description 82
- 239000000123 paper Substances 0.000 claims description 50
- 239000002245 particle Substances 0.000 claims description 44
- 239000000835 fiber Substances 0.000 claims description 42
- 125000000129 anionic group Chemical group 0.000 claims description 37
- 239000000654 additive Substances 0.000 claims description 34
- 238000000034 method Methods 0.000 claims description 28
- 230000000996 additive effect Effects 0.000 claims description 27
- 229920002401 polyacrylamide Polymers 0.000 claims description 23
- 229920006317 cationic polymer Polymers 0.000 claims description 16
- 240000003183 Manihot esculenta Species 0.000 claims description 13
- 235000016735 Manihot esculenta subsp esculenta Nutrition 0.000 claims description 13
- 150000001412 amines Chemical group 0.000 claims description 12
- 239000000203 mixture Substances 0.000 claims description 12
- 229920001577 copolymer Polymers 0.000 claims description 8
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 claims description 6
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 claims description 3
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims description 3
- 238000000151 deposition Methods 0.000 claims description 3
- 239000000178 monomer Substances 0.000 claims description 3
- 235000010582 Pisum sativum Nutrition 0.000 claims description 2
- 240000004713 Pisum sativum Species 0.000 claims description 2
- 244000061456 Solanum tuberosum Species 0.000 claims description 2
- 235000002595 Solanum tuberosum Nutrition 0.000 claims description 2
- 240000008042 Zea mays Species 0.000 claims description 2
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 claims description 2
- 235000002017 Zea mays subsp mays Nutrition 0.000 claims description 2
- 235000005822 corn Nutrition 0.000 claims description 2
- 238000001035 drying Methods 0.000 claims 2
- 229920000881 Modified starch Polymers 0.000 description 97
- 235000019426 modified starch Nutrition 0.000 description 96
- 239000004368 Modified starch Substances 0.000 description 91
- 239000000047 product Substances 0.000 description 50
- 239000000243 solution Substances 0.000 description 39
- 238000007792 addition Methods 0.000 description 34
- 239000000945 filler Substances 0.000 description 24
- 239000000523 sample Substances 0.000 description 17
- 230000000717 retained effect Effects 0.000 description 16
- 239000007787 solid Substances 0.000 description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 15
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 14
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 14
- 230000003993 interaction Effects 0.000 description 13
- 238000002156 mixing Methods 0.000 description 13
- 229940088417 precipitated calcium carbonate Drugs 0.000 description 12
- 239000008367 deionised water Substances 0.000 description 11
- 229910021641 deionized water Inorganic materials 0.000 description 11
- 230000000694 effects Effects 0.000 description 11
- 239000000126 substance Substances 0.000 description 10
- 125000003277 amino group Chemical group 0.000 description 9
- 239000002002 slurry Substances 0.000 description 9
- 239000007853 buffer solution Substances 0.000 description 8
- 229920001592 potato starch Polymers 0.000 description 7
- 238000000733 zeta-potential measurement Methods 0.000 description 7
- 230000015572 biosynthetic process Effects 0.000 description 6
- 238000002474 experimental method Methods 0.000 description 6
- 238000005189 flocculation Methods 0.000 description 6
- 230000016615 flocculation Effects 0.000 description 6
- 230000002411 adverse Effects 0.000 description 5
- 230000006835 compression Effects 0.000 description 5
- 238000007906 compression Methods 0.000 description 5
- 238000007865 diluting Methods 0.000 description 5
- 239000011121 hardwood Substances 0.000 description 5
- 238000010979 pH adjustment Methods 0.000 description 5
- 238000004458 analytical method Methods 0.000 description 4
- 230000008901 benefit Effects 0.000 description 4
- 239000000706 filtrate Substances 0.000 description 4
- 238000002360 preparation method Methods 0.000 description 4
- 239000000872 buffer Substances 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 238000003359 percent control normalization Methods 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 239000013055 pulp slurry Substances 0.000 description 3
- 239000011122 softwood Substances 0.000 description 3
- 230000008961 swelling Effects 0.000 description 3
- 238000005054 agglomeration Methods 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 2
- 229920006318 anionic polymer Polymers 0.000 description 2
- 238000007385 chemical modification Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 239000008394 flocculating agent Substances 0.000 description 2
- 238000010348 incorporation Methods 0.000 description 2
- 239000002655 kraft paper Substances 0.000 description 2
- 230000007935 neutral effect Effects 0.000 description 2
- 229920000867 polyelectrolyte Polymers 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000004513 sizing Methods 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 229920001661 Chitosan Polymers 0.000 description 1
- 229920002873 Polyethylenimine Polymers 0.000 description 1
- 241000183024 Populus tremula Species 0.000 description 1
- 241000209140 Triticum Species 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- 208000012826 adjustment disease Diseases 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000013068 control sample Substances 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000004925 denaturation Methods 0.000 description 1
- 230000036425 denaturation Effects 0.000 description 1
- 238000010410 dusting Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000003116 impacting effect Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920000962 poly(amidoamine) Polymers 0.000 description 1
- 229920001281 polyalkylene Polymers 0.000 description 1
- 229920000768 polyamine Polymers 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 229920001059 synthetic polymer Polymers 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L3/00—Compositions of starch, amylose or amylopectin or of their derivatives or degradation products
- C08L3/04—Starch derivatives, e.g. crosslinked derivatives
-
- 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
- D21H17/21—Macromolecular organic compounds of natural origin; Derivatives thereof
- D21H17/24—Polysaccharides
- D21H17/28—Starch
- D21H17/29—Starch cationic
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B31/00—Preparation of derivatives of starch
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B31/00—Preparation of derivatives of starch
- C08B31/08—Ethers
- C08B31/12—Ethers having alkyl or cycloalkyl radicals substituted by heteroatoms, e.g. hydroxyalkyl or carboxyalkyl starch
- C08B31/125—Ethers having alkyl or cycloalkyl radicals substituted by heteroatoms, e.g. hydroxyalkyl or carboxyalkyl starch having a substituent containing at least one nitrogen atom, e.g. cationic starch
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L3/00—Compositions of starch, amylose or amylopectin or of their derivatives or degradation products
- C08L3/02—Starch; Degradation products thereof, e.g. dextrin
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L79/00—Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen with or without oxygen or carbon only, not provided for in groups C08L61/00 - C08L77/00
- C08L79/02—Polyamines
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2666/00—Composition of polymers characterized by a further compound in the blend, being organic macromolecular compounds, natural resins, waxes or and bituminous materials, non-macromolecular organic substances, inorganic substances or characterized by their function in the composition
- C08L2666/02—Organic macromolecular compounds, natural resins, waxes or and bituminous materials
-
- 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
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/06—Paper forming aids
- D21H21/10—Retention agents or drainage improvers
-
- 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
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/14—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
- D21H21/18—Reinforcing agents
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Biochemistry (AREA)
- Materials Engineering (AREA)
- Paper (AREA)
Description
WO 01/29313 PCT/USOO/24561 -1 CATIONICALLY MODIFIED POLYSACCHARIDES Field of the Invention 5 The present invention relates to modified polysaccharide as a filler and strengthening aid for paper and board products and, more particularly, to modified polysaccharide having enhanced surface charge. Background of the Invention 10 One goal in papermaking is to increase the amount of filler in the ultimate product so as to reduce the amount of fiber, a relatively expensive component. Increasing the amount of filler must not have an adverse effect on the paper's sizing and other necessary properties. Among fillers, starch is attractive because of its low cost and availability. In general, unmodified raw starch is not well retained in 15 papermaking furnishes due to the lack of an effective interaction with fibers and retention aids. Despite this disadvantage, methods have been devised that utilize starch as a filler in papermaking. In most paper and board manufacturing, starch is fully cooked and used at a size press. Size press starch can include additives that impart desirable properties to a 20 paper or board such as improved printing, stiffness, bond, dusting, surface pick, among others. Cationic starch is typically added at the papermachine wet end and can improve a paper's strength properties and fine particle retention. Other charged synthetic polymers can be combined with cationic starch to improve overall fine particle retention. 25 Raw uncooked and unmodified starch particles are not added to the wet end of a paper machine due to their unacceptably low retention. Raw starch has a particle surface charge near zero when slurried in water. This lack of surface charge results in a weak interaction with charged retention aids and/or fibers. Without strong interaction (e.g., chemical attachment), starch cannot be retained well in a papermaking 30 system. Mechanical filtration of starch particles can result in some starch retention in a fibrous web, but such retention requires a specific type of headbox configuration. However, by adding a surface charge to the raw starch particles, it is possible to dramatically increase starch retention in a web. Such increased starch retention is achieved through the use of retention aids that form a bridging attachment between the 35 charged starch particles and fiber surfaces. Adding charge to raw starch has been previously accomplished by chemical modification of starch through the covalent WO 01/29313 PCT/USOO/24561 -2 attachment of certain functional groups, for example, quaternary amine groups, to the starch. In papermaking, these chemically modified starches are typically fully cooked and then added in the papermachine's wet end. Such a chemical modification process adds considerable cost to the starch and, furthermore, does not result in a starch 5 having sufficient surface charge to improve retention of uncooked starch significantly beyond that of raw unmodified starch. Accordingly, there exists a need for an economical filler for use in papermaking methods that provides for increased particle retention without adversely impacting sizing. A need also exists for fillers having increased retention and, in addition, impart 10 strength to paper products into which they are incorporated. The present invention seeks to fulfill these needs and provides further related advantages. Summary of the Invention In one aspect, the present invention provides a modified polysaccharide having 15 enhanced surface charge. The polysaccharide of the invention is a polysaccharide that has been modified to include a cationic polymer. The modified starch formed in accordance with the present invention has a surface charge from about +5 to about +20 mV. The modified polysaccharide can be advantageous incorporated into a papermaking furnish with enhanced retention. 20 In another aspect of the invention, paper products that include the modified polysaccharide having enhanced surface charge are provided. Paper products that include the modified polysaccharide have increased strength compared to similarly constituted paper products that do not include the modified polysaccharide. In one embodiment, the paper product includes cellulosic fibers and the modified 25 polysaccharide. In another embodiment, in addition to cellulosic fibers and modified polysaccharide, the paper product further includes a retention aid that enhances the retention of the modified polysaccharide to the fibers. The retention aid can be either a positively or a negatively charged retention aid. In further aspects, the invention provides methods for forming the modified 30 polysaccharide having enhanced surface charge and methods for forming paper products having increased filler retention and increased strength through the incorporation of the modified polysaccharide. Brief Description of the Drawings 35 The foregoing aspects and many of the attendant advantages of this invention will become more readily appreciated as the same become better understood by WO 01/29313 PCTUSOO/24561 -3 reference to the following detailed description, when taken in conjunction with the accompanying drawings, wherein: FIGURE 1 is a schematic illustration of a representative modified polysaccharide formed in accordance with the present invention. 5 Detailed Description of the Preferred Embodiment In one aspect, the present invention provides polysaccharide having enhanced surface charge. The polysaccharide has been modified to include a cationic additive that imparts a positive charge to the polysaccharide surface. As used herein, the terms 10 "polysaccharide" and "starch" are interchangeable, and the terms "modified starch" and "modified polysaccharide" refer to a polysaccharide having enhanced surface charge formed in accordance with the present invention. Suitable cationic additives include materials that can be irreversibly and/or strongly associated with starch and, when associated with starch, enhance its surface 15 charge. Cationic additives include cationic organic polyelectrolytes and polymers. Preferably, the cationic additive includes a cationic polymer such as a polyquaternary amine. In a preferred embodiment, the cationic additive is a relatively low molecular weight, highly positively charged polyquaternary amine having a molecular weight in the range from about 1 to 5 million grams per mole and about 3 milliequivalents 20 quaternary amine per gram. Such a polyquaternary amine is commercially available under the designation Nalco 7527 from Nalco Chemical Co., Naperville, IL. The cationic additive is present on the starch in an amount from about 1 to about 15 pounds/ton starch on a dry basis and, preferably, about 5 pounds/ton starch. Other cationic additives that are useful in forming the modified starches of the 25 invention include cationic polyacrylamides, aluminum sulfate, chitosan, polyamines, polyamidoamines, polyethylenimines, polyamide-epichlorohydrin (PAE), polyalkylene polyamine-epichlorohydrin (PAPAE), and amine polymer-epichlorohydrin (APE). The modified starch formed in accordance with the present invention has a surface charge in the range from about +1 mV to about +100 mV and, preferably from 30 about +5 to about +20 mV as determined by the zeta potential measurement. Starches from a variety of sources can be modified to provide starches having enhanced surface charge. Suitable starches are available from corn, potato, tapioca, pea and wheat, among other sources. The modified starch of the invention can be formed from a slurry of raw 35 uncooked starch and cationic additive in water. In one embodiment, raw uncooked starch is added to pH 10 water to provide a slurry having about 7% solids. The starch WO 01/29313 PCT/USOO/24561 -4 swells in the alkaline solution which appears as a milky paste. Although swelling occurs, the starch remains in the form of discrete particles. However, at higher pH, the starch can gel as a result of denaturation (i.e., chemical cooking). Gelatinization during modified starch formation is to be avoided. Without being bound by the 5 following theory, it is proposed that the cationic additive diffuses into the surface of the swollen starch particle to provide a surface charged particle. The cationic additive is then entrapped within the starch particle on adjusting the pH of the cationic additive treated starch slurry to about neutral pH. On addition of the cationic additive, the starch changes in appearance from a milky paste to granular sand-like particles. 10 Alternatively, in another embodiment, the modified starch can be formed by adding to the cationic additive to a starch slurry at about pH 7. Although the amount of swelling at neutral pH is less than that which occurs at alkaline pH, the swelling is sufficient to provide a modified starch having enhanced surface charge. In a preferred embodiment, the modified polysaccharide is a granular polysaccharide. 15 A schematic illustration of a representative starch particle formed in accordance with the present invention is illustrated in FIGURE 1. Referring to FIGURE 1, modified starch particle 10 includes cationic additives 12 adhered to starch particle 14. The preparation and properties of representative modified starches having enhanced surface charge are described in Example 1. The measurement of the surface 20 charge of representative surface charged enhanced starch particles formed in accordance with the present invention is described in Example 2. The modified starch of the invention can be advantageously incorporated into a papermaking furnish. As described below, the modified starch is highly retained by pulp thereby rendering the modified starch an economic filler for paper products. 25 Moreover, the paper products that incorporate the modified starch pulp have improved strength. The retention of the modified starch in pulp is increased compared to raw uncooked starch. As described in Example 3, Britt Jar experiments demonstrated that the modified starch can be retained by pulp to an equal or greater extent compared to 30 precipitated calcium carbonate (PCC), a conventional filler. Generally, for a fine paper furnish, from about 60 to about 70 percent modified starch was retained under conditions that resulted in the retention of about 45 percent PCC. The modified starch can be highly retained by pulp to provide a pulp that can yield a paper product having high filler retention. Alternatively, in addition to the 35 modified starch, other retention aids can be added to the pulp to further increase WO 01/29313 PCT/USOO/24561 -5 modified starch retention. Retention aids include those known in the papermaking art and the anionic and cationic retention aids described below. An anionic retention aid or additive can be utilized to increase modified starch retention. Anionic retention aids include anionic organic polyelectrolytes and 5 polymers. Preferably, the anionic retention aid includes an anionic polymer such as, for example, anionic polyacrylamide (APAM). In a preferred embodiment, the anionic retention aid is a relatively high molecular weight, slightly negatively charged polyacrylamide. The preferred polyacrylamide has a molecular weight in the range from about 8 to about 15 million grams/mole and is a copolymer of acrylic acid (30 10 mole percent) and acrylamide (70 mole percent). Such a polyacrylamide is commercially available under the designation Accurac 171 from Cytec Industries Inc., West Patterson, NJ. Alternatively, the anionic polyacrylamide is commercially available under the designation Nugen 24 from Northwest Specialty Chemicals, Vancouver, WA. The anionic retention aid is present in the fibrous pulp in an amount 15 from about 0.1 to about 3.0 pounds/ton fiber and, preferably, about 0.5 pounds/ton fiber. Other suitable anionic retention aids include high molecular weight anionic flocculants. As described in Example 3, a representative anionic retention aid (e.g., APAM) 20 is preferably added to the pulp at the wet end of the papermaking machine and can be added to the pulp prior to modified starch addition, simultaneous with modified starch addition, or after modified starch addition. As illustrated in Table 9, the greatest retention (72 percent by weight) was achieved with the addition of the APAM to the pulp followed by the addition of the modified starch. The second greatest retention 25 (58 percent by weight) was the addition of the modified starch to the pulp followed by the APAM addition. Both of these conditions provided a higher filler retention than the typical alkaline fine paper system (45 percent by weight). Other additives can also advantageously increase the retention of the modified starch by pulp. For example, cationic retention aids and additives can increase pulp 30 retention of the modified starch. Preferably, the cationic retention aid includes a cationic polymer such as, for example, a cationic polyacrylamide (CPAM), which has a relatively high molecular weight and is slightly positively charged. The preferred polyacrylamide has a molecular weight in the range from about 8 to about 15 million grams/mole and is a copolymer of acrylamide (90 mole percent) and a quaternary 35 amine monomer (10 mole percent). Such a polyacrylamide is commercially available under the designation Accurac 182RS from Cytec Industries Inc., West Patterson, NJ.
WO 01/29313 PCT/USOO/24561 -6 The cationic retention aid is present in the fibrous pulp in an amount from about 0.1 to about 12 pounds/ton fiber and, preferably, from about 0.4 to about 6 pounds/ton fiber. Combinations of anionic and cationic retention aids can be used with the modified starch to increase pulp retention. 5 Other suitable cationic retention aids include high molecular weight cationic flocculants such as, for example, cationic polyacrylamides commercially available from Nalco Chemical Co., Naperville, IL under the designations Nalco 7530 and 7520. Pulps containing the highly retained modified starches can be formed into paper products characterized by having advantageously high filler retention and increased 10 strength. Paper products that benefit from the advantageous incorporation of the modified starch include fine paper, newsprint, bleached board, liner board, medium board, and old corrugated cardboard (OCC), among others. Paper products containing modified starch and, optionally, one or more of the retention aids described above can be formed by adding the modified starch and, if 15 desired, the retention aid(s), to a pulp furnish at the wet end of a papermaking machine. Depending on the desired properties of the paper product, the modified starch can be added to the pulp furnish in an amount from about 0.5 to about 20 percent by weight, and preferably from about 3 to about 10 percent by weight based on the total weight of fibers. 20 The flow characteristics of a pulp furnish, including the furnish's ability to be dewatered, is an important factor in high speed papermaking methods and machines. One advantage of the invention is that the addition of modified starch to a pulp furnish does not adversely affect the furnish's flow characteristics despite the furnish's high retention of modified starch. Furthermore, the furnish is not adversely affected by the 25 addition of the modified starch when the pulp is treated with an anionic retention aid in accordance with the invention. The wet end addition of the modified starch to a pulp furnish treated with an anionic retention aid does not result in the formation of a gum like precipitate, which would negatively impact the quality of the pulp furnish and limit its utility in high speed papermaking. Similarly, the addition of a cationic retention aid 30 to a pulp furnish containing an anionic retention aid and/or modified starch does not adversely affect the pulp furnish. The formation and properties of a representative paper product, OCC, containing modified starch is described in Example 4. The strength properties of the representative OCC product is summarized in Table 11. The results demonstrate that 35 the Mullen burst strength for an OCC product containing 3 percent by weight modified starch is increased by about 20% compared to a similarly constituted OCC product WO 01/29313 PCTIUSOO/24561 -7 lacking modified starch. Increases in short span compression STFI, tensile, and stretch were also observed. The OCC product had an increase in short span compression STFI of about 5%, an increase in tensile of about 9%, and an increase in stretch of about 16% compared to a similarly constituted OCC product lacking modified starch. 5 Representative OCC products were also formed varying (a) the amount of cationic additive used to prepare the modified starch, (b) the amount of modified starch added to the pulp furnish, and (c) the type and amount of retention aid(s) added to the pulp furnish. The percentage starch retention results for various representative OCC products is summarized in Table 12. Referring to Table 12, the results 10 demonstrate that modified starch is highly retained by pulp and that modified starch retention can be increased through the use of retention aids. The anionic retention aid provided an enhancement in retention greater than the cationic retention aid. EXAMPLES 15 Example 1 The Preparation of Representative Surface Charge Enhanced Starch In this example, the preparation and physical properties of representative starches having enhanced surface charge are described. The representative starches including a cationic polymer, a polyquaternary amine (PQA) were prepared as 20 described for Set 1. Representative starches including a polyquaternary amine and further including a retention aid (APAM) were prepared as described for Set 2. Set 1. A cationic potato starch (Accosize 80, commercially available from Cytec Industries Inc., West Patterson, NJ) was cooked at 3.85% solids in a laboratory cooker (44 g, 86% solids) in 1000 mL of deionized water. A 0.1% solution of a 25 representative cationic polymer (a low molecular weight, highly positively charged polyquaternary amine, PQA, commercially available under the designation Nalco 7527 from Nalco Chemical Co., Naperville, IL) was diluted to 0.1% actives (1.43 g diluted to 500 mL). In each of beakers 1, 2 and 3, 5.71 g of tapioca unmodified starch (5.0 g of 30 O.D.) was diluted to 50 mL with pH 10 buffer solution and allowed to sit for thirty minutes. In beaker 2, 0.95% cooked cationic potato starch was added (1.25 g of 3.78% solution) and mixed well. In beaker 3, 5 lb/ton Nalco 7527 was added (12.5 g of 0.1% solution) and mixed well. All three beakers equilibrated for thirty minutes prior to microscopic observation. 35 All three beakers were then adjusted to pH 7 with 1 N sulfuric acid and observed using a microscope. Ten percent by weight (O.D. pulp basis) of the three WO 01/29313 PCTIUSOO/24561 -8 starch samples (1 mL of starch at about 7% solids) was added each to 1.0 g O.D. pulp (hardwood bleached kraft pulp, HWBK, Aspen, disintegrated, commercially available from Weyerhaeuser Co.) at a 0.5% consistency and mixed. The starch samples were microscopically observed. 5 Set 2. Cationic potato starch (Accosize 80), was cooked at 4.5% solids in a laboratory cooker (69 g, at 86% solids in 1340 mL of deionized water). A 0.1% solution of Nalco 7527 was diluted to 0.1% actives (1.43 g diluted to 500 mL). A 0.1% solution of a representative retention aid (a high molecular weight, slightly negatively charged polyacrylamide, APAM, commercially available under the 10 designation Accurac 171 from Cytec Industries Inc., West Patterson, NJ) was diluted to 0.01% actives (1.43 g diluted to 500 mL and diluted 10 times): In each of beakers 1, 2 and 3, 5.0 g of tapioca unmodified starch (4.4 g of O.D.) was diluted to 50 mL, with pH 10 buffer solution and allowed to equilibrate for fifteen minutes. In beaker 2, 1.3% cationic potato starch (Accosize 80) was added 15 (1.25 g of 4.5% solution) and mixed well. In beaker 3, 5.7 lb/ton PQA (Nalco 7527) was added (12.5 g of 0.1% solution) and mixed well. After the chemical additions, the solutions were equilibrated for thirty minutes. All three beakers were then adjusted to pH 7 with 1 N sulfuric acid and allowed to stand for one hour. Pulp treatment. Hardwood bleached kraft pulp (HWBK) was disintegrated and 20 diluted to 0.25% consistency with deionized water. To each of six beakers, 0.5 g pulp at 0.25% consistency was added. Three of the pulp samples were pretreated with APAM by adding 0.5 lb/ton (1.25 g of 0.01% solution). The pulp was well mixed and then starch solutions were added to the pulp samples. To the pulp samples that were not pretreated, 0.5 lb/ton APAM (1.25 g of 0.01% solution) was then added and 25 mixed. All six conditions were qualitatively analyzed using a microscope. The first experiment was designed to qualitatively compare unmodified tapioca starch with the addition of cooked cationic potato starch or a cationic polymer, polyquaternary amine (PQA). A microscope was used to observe any physical changes or reactions with other starch particles or fibers. The microscope observations are 30 summarized in Table 1.
WO 01/29313 PCT/USOO/24561 -9 Table 1. Qualitative microscopic observations. After Chemical After pH Beaker Addition Adjustment Reaction with Fibers 1 (Control) No flocculation No flocculation No interaction 2 (Cationic starch) Some flocculation Some flocculation Some interaction 3 (PQA) No flocculation No flocculation Some interaction (Highly dispersed) After the addition of the PQA and reduction of the pH, there was a noticeable difference in the behavior of the starch slurry. The starch granules appeared highly 5 dispersed. There was also some interaction between the modified starch and the fibers before and after the pH adjustment. The addition of both cooked starch and PQA caused the starch particles to have some interaction when added to fiber. The effect of post- or pretreating fibers with an anionic polymer (APAM) on the reaction of the modified starch solutions was also determined. In one case, APAM 10 was added to the fiber before addition of the starch slurry, and in the second case, APAM was added after the addition of the starch to the fibers. The observations are summarized in Table 2. Table 2. Qualitative microscopic observations. Fibers Pretreated with Fibers Post-Treated with Beaker APAM APAM 1 (Control) No fiber interaction Starch particles lying uniformly on fiber Some starch Some starch 2 (Cationic starch) agglomeration/fiber agglomeration/fiber interaction interaction 3 (PQA) No fiber interaction No fiber interaction 15 Treatment with APAM had an insignificant effect on the appearance of fibers treated with either the cationic starch and PQA-modified starch.
WO 01/29313 PCT/USOO/24561 -10 Example 2 The Measurement of Surface Charge of Representative Surface Charge Enhanced Starch Particles In this example, the measurement of the surface charge of representative starch 5 particles having enhanced surface charge are described. The surface charged was determined by zeta potential measurement. Sets 1 and 2: Control and Modified Starches. Unmodified tapioca starch was used for each test. To each starch sample (5.0 g) was added 50 mL pH 10 buffer solution and the solution was allowed to stand for one hour. After standing for one 10 hour, 5 lb/ton (actives basis) PQA (Nalco 7527) was added to the starch and mixed well to provide the "modified sample". In the control sample, no polymer was added. The samples were allowed to stand for an additional hour before adjusting to pH 7 with 1 N sulfuric acid. The samples were allowed to stand for an additional hour prior to analysis. 15 Set 3: Modified Starches from pH Variance. The modified sample was prepared by adding 5.0 g of unmodified tapioca starch in 50 mL of pH 10 buffer (as described above) and allowed to stand for one hour before adding 5 lb/ton PQA (Nalco 7527). After one hour, the pH was adjusted to pH 7 with 1 N sulfuric acid and allowed to stand for one final hour. A second sample was prepared by adding pH 10 20 buffer to 5.0 g of tapioca starch as received and then allowed to stand. After the hour, 5 lb/ton PQA (Nalco 7527) was added and was allowed to stand for another two hours with no further pH adjustment. A third sample was prepared as described above except that pH 7 buffer was added to the starch with no further pH adjustment. Zeta Potential Measurement. The zeta potentials for all samples were 25 measured using a Delsa 440 (Coulter Electronics, Inc., Hialeah, FL) run at a frequency range of± 500 Hz, and with a current equal to one-half the value of the conductivity of the sample. The sample was run at two cell heights (16 and 84). Due to the addition of the PQA, the samples stayed fairly well dispersed and were allowed to settle for one hour prior to analysis. 30 The zeta potential results from the Set 1 samples are shown in Table 3. The charge is an average at 8.6, 17.1, 25.6, and 34.20 angles at both the 16 and 84 cell heights. The control (unmodified sample) was run in triplicate and the modified sample was run in duplicate. The results demonstrate that the addition of the cationic polyacrylamide gave the modified sample a significantly enhanced charge compared to 35 the control.
WO 01/29313 PCTUSOO/24561 -11 Table 3. Starch zeta potential measurement results. PQA Conductivity Average Sample (lb/ton) pH (ms/cm) (mV) Control 0 7 6.1 1.59 Control 0 7 9.5 2.67 Control 0 7 9.8 -2.95 Modified 5 7 7.7 17.35 Modified 5 7 9.1 18.22 The zeta potential results from the Set 2 samples are shown in Table 4. Because settling in a zeta potential cell can shift the stationary plane, an experiment 5 was conducted testing samples of various consistency to determine the effect on the charge analysis. The consistencies were varied by varying settling times of the starch slurries prior to analysis. The same samples were prepared as with the first set, and included a control and a modified sample. The modified sample was also washed with deionized water to determine whether the charge was on the particle surface or merely 10 weakly associated with the surface. Table 4. Starch zeta potential measurement results. PQA Conductivity Settling Averag Starch (lb/ton) pH Condition (ms/cm) Time (min) e (mV) Control 0 7 Unwashed 6.96 0 -2.08 Control 0 7 Unwashed 9.75 9 -2.19 Control 0 7 Unwashed 9.82 15 -2.47 Modified 5 7 Unwashed 6.86 0 10.72 Modified 5 7 Unwashed 7.95 9 15.24 Modified 5 7 Washed 8.40 9 10.10 WO 01/29313 PCT/USOO/24561 -12 The results show that settling time does effect the zeta potential measurement. The results further indicate that the charge is on the particle surface and not merely weakly associated with the surface, and that washing the starch particles has an insignificant effect on zeta potential measurement. 5 To determine the effect of pH on modified starch formation and on the overall particle charge, three samples (Set 3 samples prepared as described above) were compared. The results are shown in Table 5. Table 5. Effect of pH adjustment on charge e. 7527 Initial Final Conductivity Settling Average Starch (lb/ton) pH pH (ms/cm) Time (min.) (my) Modified 5 7 7 6.79 60 17.25 Modified 5 10 10 8.00 60 15.86 Modified 5 10 7 8.05 60 18.29 10 All of the modified samples had a similar cationic charge. It does not appear that the pH adjustment had a significant effect on the modification process surface charge. Example 3 15 Pulp Retention of Representative Surface Charge Enhanced Starch In this example, the retention of representative starch having enhanced surface charge by pulp is described. To determine whether the modified starch can be retained in high shear conditions, a Britt Jar was used for retention studies. Pulp Preparation. Prince Albert hardwood was refined to a 400 mL CSF with 20 the Escher Wyss conical refiner (Bird Escher Wyss, Manfield, MA) using the following conditions: 3.0% consistency, 1.0 W-s/m specific edge load, 1250 rpm, 0.583 km/s cutting length, and 60 degree bar angle. Prince Albert softwood was also refined to a 600 mL CSF with the Escher Wyss using the same conditions except that the specific edge load was 3.0 W-s/m. The net power specific energy for the hardwood was 48.6 25 kW-h/t and for the softwood was 1.75 kW-h/t. A pulp blend of 60% hardwood and 40% softwood was prepared. The fines were removed using a 200 mesh screen box. The final freeness value of the pulp mixture without fines was 695 mL at a 2.2% consistency.
WO 01/29313 PCTIUSOO/24561 -13 Britt Jar Conditions. A Britt Jar having a 100 mesh conical mesh screen was used in the retention determination. The pulp was added into a vaned Britt Jar with the stopper close and mixed with the starch at various speeds. After time had elapsed for sampling, the stopper was opened and the filtrate was collected in a tared aluminum 5 pan (around 100 mL). The pan was immediately weighed on the same four-place balance that was used for the tare. The pan was put into a 105*C oven until the following day. The dried sample was placed into a desiccator before reweighing the pan. The consistency of the unretained slurry was calculated from Equation 1. 0. D. grams residue Filtrate Consistency = Tota eFle(1) Total Gramis Filtrate 10 The percent retained from the pulp slurry was calculated using Equation 2. Percent Retained = Pulp Slurry Consistency - Filtrate Consistency (2) Pulp Slurry Consistency To determine the correct degree of shear or mixing speed, an initial study was done with a typical alkaline fine paper furnish. The retention of starch formed in accordance with the present invention was compared to the retention of precipitated 15 calcium carbonate. Chemicals. The pulp prepared as described above was diluted to 0.65% consistency with deionized water. Precipitated calcium carbonate (PCC) was obtained from Specialty Minerals, Inc., Bethlehem, PA and had 31.6% solids. A highly charged, high molecular weight anionic polyacrylamide (APAM, Accurac 171) solution was 20 prepared by diluting 1.43 g APAM to 500 mL with deionized water. The solution was mixed with a Braun hand blender for fifteen seconds to provide a 0.1% APAM solution and then diluted 1OX by diluting 50 mL of 0.1% to 500 mL with deionized water to provide a 0.01% solution. A cationic potato starch (Accosize 80) solution was prepared by mixing 69.9 g of starch (86% solids) with 1340 mL of deionized 25 water at 4.5% solid. Britt Jar Procedure. Pulp (2.5 g, 385 g of 0.65% consistency) was added to the Britt Jar. Table 6 shows the chemical additions and the amounts made to the pulp samples with the mixing times following each addition.
WO 01/29313 PCTIUSOO/24561 -14 Table 6. Chemical order of addition and mixing times. Chemical Mixing Time (seconds) 17 lb/ton cationic starch 15 (0.47 g of 4.5%) 20% PCC (1.58 g of 31.6%) 15 0.5 lb/ton APAM (6.25 g of 0.01%) 30 The above conditions were run at three different mixing speeds, 500, 100, and 1500 rpm, with the ultimate goal of obtaining realistic filler retention. Typical filler 5 retention on a fine paper machine is between 50-55% retention. Table 7 provides the mixing speed results. Table 7. Britt Jar filler retention: Mixing speed variance. Mixing speed (rpm) Percent filler retention 500 50.4 1000 8.95 1500 4.5 Referring to Table 7, the 500 rpm data set provides effective retention while 10 the higher mixing speed conditions show inadequate retention. Modified Starch Retention The retention of the modified starch of the present invention was compared to a typical alkaline fine paper furnish with PCC. The APAM and cationic starch solutions were prepared the same as described above. In addition, a PQA solution 15 (Nalco 7527) was prepared by diluting 1.43 g stock to 500 mL with deionized water. The PQA solution was 0.1% actives and was mixed for fifteen seconds with a Braun hand blender. PCC was as described above. The pulp was diluted to 0.42% consistency with deionized water. The modified starch was prepared by diluting 5.0 g (12.5% solids) of 20 unmodified tapioca starch to 50 mL with pH 10 buffer solution. The starch was well mixed and allowed to stand for one hour. A volume of 12.5 mL of 0.1% PQA (Nalco 7527) was added and mixed well. The solution was allowed to stand for another hour. The pH was then adjusted to pH 7 with 1 N sulfuric acid (about 2.7 mL). The final consistency of the starch solution was 6.7%. 25 The control starch was prepared by diluting 5.0 g (12.5% solids) of unmodified tapioca starch to 50 mL with pH 10 buffer solution. The starch was mixed well and WO 01/29313 PCT/USOO/24561 -15 was allowed to stand for one hour. A volume of 12.5 mL of deionized water was added and mixed well. The solution was allowed to stand for another hour. The pH was then adjusted to pH 7 with 1 N sulfuric acid (about 2.7 mL). The final consistency of the starch solution was 6.7%. 5 Britt Jar Procedure. For each Britt Jar experiment, 2.5 g pulp (595 g at 0.42% consistency) was added and mixed using 500 rpm. For the control starch and the modified starch, 6.5 g of 6.7% starch was added (17.4%). For the APAM, 6.25 mL of a 0.01% solution was added (0.5 lb/ton) and for the cationic potato starch, 0.5 g of 4.5% solids was added (17 lb/ton). For the PCC, 1.6 g of 31.6% solution was added 10 (20%). The conditions are summarized in Table 8. Each condition was run in triplicate and the entire experiment was randomized (except for the alkaline fine paper furnish which was completed first in triplicate.) Table 8. Britt Jar chemical conditions. First Addition Mixing Time (s) Second Addition Mixing Time (s) 17.4% Modified Starch 30 None 30 17.4% Modified Starch 30 0.5 lb/ton APAM 30 0.5 lb/ton APAM 30 17.4% Modified Starch 30 17.4% Control Starch 30 None 30 17.4% Control Starch 30 0.5 lb/ton APAM 30 0.5 lb/ton APAM 30 17.4% Control Starch 30 17 lb/ton Cationic Starch/ 15/15 0.5 lb/ton APAM 30 20% PCC WO 01/29313 PCTIUSOO/24561 -16 The filler (modified starch or PCC) retentions are summarized in Table 9. Table 9. Britt Jar filler retention: Order of addition variance. Sample (First/Second Addition) Percent filler retention Control/APAM 5 Modified/APAM 58 Cationic starch/PCC/APAM 45 APAM/Control 3 APAM/Modified 72 Control/None 1 Modified/None 10 The highest retention was achieved with the addition of the APAM to the pulp 5 followed by the addition of the modified starch. The second highest retention was the addition of the modified starch to the pulp followed by the APAM addition. Both of these conditions had a higher filler retention than the typical alkaline fine paper system. Effect of Treatment pH on Modified Starch Retention Pulp having the greatest starch retention was obtained using pulp fibers that 10 had been pretreated with APAM. To evaluate the effect of pH on the modified starch retention by pulp, pulp was treated with the modified starch under three different pH conditions. The pulp, APAM, and PQA solutions were prepared as described above. The original pulp mixture was diluted to 0.41% consistency with deionized water. To add 2.5 g of 0.D. pulp, 605 g of the 0.41% solution was used for each condition. 15 Three starch solutions were prepared as follows. Modified Starch pH 10-7. Five grams (12.5% solids) of unmodified tapioca starch was diluted to 50 mL with pH 10 buffer solution. The starch was mixed well and was allowed to stand for one hour. A volume of 12.5 mL of 0.1% Nalco 7527 was added and mixed well. The solution was allowed to stand for another hour. The 20 pH was then adjusted to pH 7 with 1 N sulfuric acid (about 2.7 mL). The solutions equilibrated for one more hour. The final consistency of the starch solution was 6.7%. Modified Starch pH 10-10. Five grams (12.5% solids) of unmodified tapioca starch was diluted to 50 mL with pH 10 buffer solution. The starch was mixed well and was allowed to stand for one hour. A volume of 12.5 niL of 0.1% Nalco 7527 25 was added and mixed well. The solution was allowed to stand for two hours. The final consistency of the starch solution was 6.7%.
WO 01/29313 PCT/USOO/24561 -17 Modified Starch pH 7- 7. Five grams (12.5% solids) of unmodified tapioca starch was diluted to 50 mL with pH 7 buffer solution. The starch was mixed well and was allowed to stand for one hour. 12.5 mL of 0.1% Nalco 7527 was added and mixed well. The solution was allowed to stand for two hours. The final consistency of the 5 starch solution was 6.7%. Britt Jar Procedure. APAM was added to the pulp in the Britt Jar followed by mixing for 30 seconds followed by the addition of the starch slurry. For each run, 0.5 lb/ton APAM (6.25 mL 0.01% solution) and 20% starch (7.4 mL of a 6.74% solution) were added. The experiment was randomized and each condition was run in 10 triplicate. The results of pH variance are summarized in Table 10. Table 10. Britt jar filler retention: pH variance. APAM/Modified Percent filler retention pHlO/pHlO 69 pHl0/pH7 75 pH7/pH7 77 All of the tested conditions show a high retention of starch with the pH 7/pH 7 method providing slightly greater retention than the pH 1 0/pH 10 condition. 15 Example 4 The Formation and Properties of OCC Containing Representative Surface Charge Enhanced Starch In this example, the formation and properties of old corrugated cardboard (OCC) containing modified starch is described. The properties of representative OCC 20 products was determined and compared to OCC products that did not include modified starch. The OCC product was formed from a fibrous furnish containing 100 percent OCC. Modified starch was prepared as described above by adding 5 lb PQA (Nalco 7527)/ton starch. The pulp furnish was treated with 0.5 lb APAM (Accurac 171)/ton 25 fiber followed by the addition of 3 percent by weight modified starch based on the total weight of fiber, and then 5 lb CPAM (Accurac 182RS)/ton fiber. After depositing the pulp furnish containing the modified starch onto a foraminous support, the deposited pulp was dewatered, and then dried to provide the OCC product. The properties of the OCC product prepared as described above are 30 summarized in Table 11. In the table, Sample 1 refers to an OCC product that was formed without the inclusion of modified starch and Sample 2 refers to an OCC WO 01/29313 PCT/USOO/24561 -18 product that includes 3 percent by weight modified starch based on the total weight of fiber. In the table, SSC STFI and TEA refer to short span compression STFI and tensile energy adsorption, respectively.
WO 01/29313 PCT/USOO/24561 -19 ON t 03 - 0N c0 cc WO 01/29313 PCTIUSOO/24561 -20 Referring to Table 11, the Mullen burst strength for OCC product Samples 1 and 2 represent an increase of about 20% compared to similarly constituted OCC lacking modified starch. Increases in short span compression STFI, tensile, and stretch 5 were also observed. The OCC product containing modified starch had an increase in short span compression STFI of about 5%, an increase in tensile of about 9%, and an increase in stretch of about 16% compared to a similarly constituted OCC product lacking modified starch. The weight percentage of starch retained in representative OCC products were 10 compared to each other and compared to OCC products containing unmodified starch. The results are summarized in Tables 12-15. Several representative OCC products were formed varying the amount of cationic additive used to prepare the modified starch, the amount of modified starch added to the pulp furnish, and the type and amount of retention aid(s) added to the 15 pulp furnish. The percentage starch retention results for various representative OCC products is summarized in Table 12. In these products, the cationic additive used in forming the modified starch was PQA (Nalco 7527), the anionic retention aid was APAM (Accurac 171), and the cationic retention aid was CPAM (Accurac 182). The following terms are used in Table 12: 20 Modified Starch refers to starch modified with 5 lb PQA (Nalco 7527)/ton starch; Variable PQA refers to an OCC product prepared by pretreating the pulp furnish with 0.5 lb APAM (Accurac 171)/ton fiber prior to treatment with modified starch prepared from starch and variable amounts of PQA (Nalco 7527): A, B, C, and 25 D refer to OCC products containing modified starch prepared from 1, 2, 3, 5, and 7 lb PQA (Nalco 7527)/ton starch; Variable APAM refers to an OCC product prepared by pretreating the pulp furnish with variable amounts of APAM (Accurac 171) followed by treatment with modified starch prepared from starch and 5 lb PQA (Nalco 7527)/ton starch: E, F, and 30 G refer to OCC products in which the pulp furnish was pretreated with 0.25, 0.50, and 0.75 lb APAM (Accurac 171)/ton fiber; APAM/PQA/APAM refers to an OCC product in which the pulp furnish was pretreated with 0.25 lb APAM (Accurac 171), and then treated with modified starch prepared from starch and 5 lb PQA (Nalco 7527)/ton starch and 0.25 lb APAM 35 (Accurac 171)/ton fiber; WO 01/29313 PCT/USOO/24561 -21 APAM/PQA/CPAM refers to an OCC product in which the pulp furnish was pretreated with 0.25 lb APAM (Accurac 171), then treated with modified starch prepared from starch and 5 lb PQA (Nalco 7527)/ton starch followed by 2.0 lb CPAM (Accurac 182)/ton fiber; and 5 Variable CPAM refers to an OCC product prepared by treating the pulp furnish with variable amounts of CPAM (Accurac 182) after treatment with modified starch prepared from starch and 5 lb PQA (Nalco 7527)/ton starch: H, I, and J refer to OCC products in which the pulp furnish was treated with 1.0, 2.0, and 3.0 lb CPAM (Accurac 182)/ton fiber; 10 Table 12. OCC starch retention comparison. OCC Filler Percent Retention Starch 1.45 Modified starch 20.82 Variable PQA A 79.19 B 95.63 C 94.52 D 88.20 Variable APAM E 82.83 F 94.52 G 88.65 APAM/PQA/APAM 81.29 APAM/PQA/CPAM 76.45 Variable CPAM H 37.50 1 42.31 J 45.42 The results in Table 12 demonstrate that modified starch is highly retained by pulp and that modified starch retention can be increased through the use of retention aids. The anionic retention aid provided an enhancement in retention greater than the 15 cationic retention aid. The weight percentage of modified starch retained in representative OCC products as a function of the amount of starch cationic additive (PQA, Nalco WO 01/29313 PCT/USOO/24561 -22 7527)/ton starch, with pretreatment with 0.5 lb anionic retention aid (APAM, Accurac 171)/ton fiber was determined. The results are summarized in Table 13. Table 13. OCC starch retention: PQA variance. PQA (lb/ton) Percent Retention 1 84.5 1 73.9 3 87.7 3 103.6 5 94.5 5 94.6 7 88.8 7 87.6 5 The results demonstrate that significant retention was achieved using from 1 to 7 lb PQA/ton starch, with about 5 lb PQA/ton starch providing near optimum retention. The weight percentage of modified starch (5 lb PQA/ton starch) retained in representative OCC products as a function of pretreatment with varying amounts of 10 anionic retention aid (APAM, Accurac 171) was determined. The results are summarized in Table 14. Table 14. OCC starch retention: APAM variance. APAM (lb/ton) Percent Retention 0.25 79.5 0.25 86.1 0.50 94.5 0.50 94.6 0.75 89.0 0.75 88.3 The results demonstrate that optimum retention was achieved for pretreatment 15 with 0.50 lb anionic retention aid/ton fiber. The weight percentage of modified starch (5 lb PQA/ton starch) retained in representative OCC products as a function of treatment with varying amounts of WO 01/29313 PCT/USOO/24561 -23 cationic retention aid (CPAM, Accurac 182) was determined. The results are summarized in Table 14. Table 15. OCC starch retention: CPAM variance. CPAM (lb/ton) Percent Retention 1 27.1 1 47.9 2 42.5 2 42.2 3 44.4 3 46.5. 5 The results demonstrate that significant retention was achieved using from 1 to 3 lb CPAM/ton starch. While the preferred embodiment of the invention has been illustrated and described, it will be appreciated that various changes can be made therein without departing from the spirit and scope of the invention.
Claims (55)
1. A composition comprising a polysaccharide particle and a cationic 5 additive, wherein the cationic additive is adhered to the polysaccharide particle to provide a polysaccharide particle having a positive surface charge.
2. The composition of Claim 1 wherein the cationic additive comprises a cationic polymer.
3. The composition of Claim 2 wherein the cationic polymer comprises a 10 polyquaternary amine.
4. The composition of Claim 3 wherein the polyquaternary amine has a molecular weight in the range from about 1 million to about 5 million grams per mole.
5. The composition of Claim 3 wherein the polyquaternary amine has about 3 meq quaternary amine per gram. 15
6. The composition of Claim 1 wherein the cationic additive is present in the composition in an amount from about 1 to about 15 pounds per ton polysaccharide.
7. The composition of Claim 1 wherein the surface charge is in the range from about +1 mV to about +100 mV. 20
8. The composition of Claim 1 wherein the polysaccharide is selected from the group consisting of corn, potato, tapioca, pea, and wheat starches.
9. A pulp furnish comprising a polysaccharide particle having a positive surface charge, wherein the polysaccharide particle having a positive surface charge comprises a cationic additive adhered to the polysaccharide particle. 25
10. The furnish of Claim 9 wherein the cationic additive comprises a cationic polymer.
11. The furnish of Claim 10 wherein the cationic polymer comprises a polyquaternary amine. WO 01/29313 PCT/USOO/24561 -25
12. The furnish of Claim 9 wherein the polysaccharide particle has a surface charge in the range from about +1 mV to about +100 mV.
13. The furnish of Claim 9 further comprising an anionic retention aid.
14. The furnish of Claim 9 further comprising a cationic retention aid. 5
15. The furnish of Claim 13 further comprising a cationic retention aid.
16. The furnish of Claim 13 wherein the anionic retention aid comprises an anionic polyacrylamide.
17. The furnish of Claim 16 wherein the anionic polyacrylamide comprises a copolymer of acrylic acid and acrylamide. 10
18. The furnish of Claim 17 wherein the copolymer comprises about 30 mole percent acrylic acid and about 70 mole percent acrylamide.
19. The furnish of Claim 17 wherein the copolymer has a molecular weight in the range from about 8 to about 15 million grams per mole.
20. The furnish of Claim 13 wherein the anionic retention aid is present in 15 the furnish in an amount from about 0.1 to about 3.0 pounds per ton fiber.
21. The furnish of Claim 14 wherein the cationic retention aid comprises a cationic polyacrylamide.
22. The furnish of Claim 21 wherein the cationic polyacrylamide comprises a copolymer of acrylamide and a quaternary amine monomer. 20
23. The furnish of Claim 22 wherein the copolymer comprises about 90 mole percent acrylamide and about 10 mole percent quaternary amine monomer.
24. The furnish of Claim 22 wherein the copolymer has a molecular weight in the range from about 8 to about 15 million grams per mole.
25. The furnish of Claim 14 wherein the cationic retention aid is present in 25 the furnish in an amount from about 0.1 to about 12 pounds per ton fiber. WO 01/29313 PCTIUSOO/24561 -26
26. A paper product comprising a polysaccharide particle having a positive surface charge, wherein the polysaccharide particle having a positive surface charge comprises a cationic additive adhered to the polysaccharide particle.
27. The paper product of Claim 26 wherein the cationic additive comprises 5 a cationic polymer.
28. The paper product of Claim 27 wherein the cationic polymer comprises a polyquaternary amine.
29. The paper product of Claim 26 wherein the polysaccharide particle has a surface charge in the range from about +1 mV to about +100 mV. 10
30. The paper product of Claim 26 further comprising an anionic retention aid.
31. The paper product of Claim 26 further comprising a cationic retention aid.
32. The paper product of Claim 30 further comprising a cationic retention 15 aid.
33. The paper product of Claim 30 wherein the anionic retention aid comprises an anionic polyacrylamide.
34. The paper product of Claim 31 wherein the cationic retention aid comprises a cationic polyacrylamide. 20
35. The paper product of Claim 26 wherein the paper product is selected from the group consisting of fine paper, newsprint, bleached board, liner board, medium board, and old corrugated cardboard.
36. A method for forming a paper product comprising: adding a polysaccharide particle having a positive surface charge to a first pulp 25 furnish to provide a second pulp furnish, wherein the polysaccharide particle having a positive surface charge comprises a cationic additive adhered to the polysaccharide particle; depositing the second pulp furnish onto a foraminous support to provide a wet web; and 30 dewatering and drying the wet web to provide the paper product. WO 01/29313 PCT/USOO/24561 -27
37. The method of Claim 36 wherein the cationic additive comprises a cationic polymer.
38. The method of Claim 37 wherein the cationic polymer comprises a polyquaternary amine. 5
39. The method of Claim 36 wherein the starch particle has a surface charge in the range from about +1 mV to about +100 mV.
40. The method of Claim 36 further comprising adding an anionic retention aid to the first pulp furnish.
41. The method of Claim 36 further comprising adding a cationic retention 10 aid to the first pulp furnish.
42. The method of Claim 40 further comprising adding a cationic retention aid to the first pulp furnish.
43. The method of Claim 40 wherein the anionic retention aid comprises an anionic polyacrylamide. 15
44. The method of Claim 41 wherein the cationic retention aid comprises a cationic polyacrylamide.
45. The method of Claim 36 wherein the paper product is selected from the group consisting of fine paper, newsprint, bleached board, liner board, medium board, and old corrugated cardboard. 20
46. A method for increasing the strength of a paper product comprising: adding a polysaccharide particle having a positive surface charge to a first pulp furnish to provide a second pulp furnish, wherein the polysaccharide particle having a positive surface charge comprises a cationic additive adhered to the polysaccharide particle; 25 depositing the second pulp furnish onto a foraminous support to provide a wet web; and dewatering and drying the wet web to provide the paper product having increased strength compared to a similarly constituted paper lacking a polysaccharide particle having a positive surface charge. WO 01/29313 PCTUSOO/24561 -28
47. The method of Claim 46 wherein the cationic additive comprises a cationic polymer.
48. The method of Claim 47 wherein the cationic polymer comprises a polyquaternary amine. 5
49. The method of Claim 47 wherein the polysaccharide particle has a surface charge in the range from about +1 mV to about +100 mV.
50. The method of Claim 47 further comprising adding an anionic retention aid to the first pulp furnish.
51. The method of Claim 47 further comprising adding a cationic retention 10 aid to the first pulp furnish.
52. The method of Claim 50 further comprising adding a cationic retention aid to the first pulp furnish.
53. The method of Claim 50 wherein the anionic retention aid comprises an anionic polyacrylamide. 15
54. The method of Claim 52 wherein the cationic retention aid comprises a cationic polyacrylamide.
55. The method of Claim 46 wherein the paper product is selected from the group consisting of fine paper, newsprint, bleached board, liner board, medium board, and old corrugated cardboard.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
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US42162199A | 1999-10-19 | 1999-10-19 | |
US09421621 | 1999-10-19 | ||
PCT/US2000/024561 WO2001029313A1 (en) | 1999-10-19 | 2000-09-07 | Cationically modified polysaccharides |
Publications (1)
Publication Number | Publication Date |
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AU7122100A true AU7122100A (en) | 2001-04-30 |
Family
ID=23671321
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AU71221/00A Abandoned AU7122100A (en) | 1999-10-19 | 2000-09-07 | Cationically modified polysaccharides |
Country Status (9)
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US (2) | US20020139501A1 (en) |
JP (1) | JP2003512541A (en) |
KR (1) | KR20020060204A (en) |
CN (1) | CN1377436A (en) |
AU (1) | AU7122100A (en) |
CA (1) | CA2386403A1 (en) |
MX (1) | MXPA02003881A (en) |
SE (1) | SE521309C2 (en) |
WO (1) | WO2001029313A1 (en) |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
PT1492923E (en) * | 2002-04-09 | 2008-06-12 | Fpinnovations | Swollen starch-latex compositions for use in papermaking |
US7494566B2 (en) | 2002-09-13 | 2009-02-24 | University Of Pittsburgh - Of The Commonwealth System Of Higher Education | Composition for increasing cellulosic product strength and method of increasing cellulosic product strength |
US7090745B2 (en) | 2002-09-13 | 2006-08-15 | University Of Pittsburgh | Method for increasing the strength of a cellulosic product |
FR2854898B1 (en) * | 2003-05-12 | 2007-07-13 | Roquette Freres | PROCESS FOR CATIONIZATION OF AMIDONS FROM LEGUMES, CATIONIC STARCH SO OBTAINED AND THEIR APPLICATIONS |
BRPI0508227A (en) | 2004-02-27 | 2007-07-17 | Univ Pittsburgh | interconnected polymer gels and use of such polymer gels in hydrocarbon recovery |
JP2009249785A (en) * | 2008-04-09 | 2009-10-29 | Sansho Kk | Starch-based interlayer adhesive, and method for papermaking using the same |
CN102585097B (en) * | 2012-02-26 | 2013-06-12 | 河南工业大学 | Method for preparing amphoteric starch |
CN112251918B (en) * | 2020-10-12 | 2022-10-11 | 惠州市好好爱日化用品有限公司 | Silk mask base cloth, preparation method thereof and silk mask |
US20230002974A1 (en) * | 2021-07-02 | 2023-01-05 | Knauf Gips Kg | Compositions and methods for making paper using uncooked starch for gypsum panels |
CN115322294A (en) * | 2022-10-10 | 2022-11-11 | 江苏富淼科技股份有限公司 | Starch synergist and preparation method and application thereof |
CN116971202A (en) * | 2023-06-29 | 2023-10-31 | 联盛纸业(龙海)有限公司 | OCC slurry fiber reinforcement modification method and application |
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US3884909A (en) * | 1973-09-24 | 1975-05-20 | Standard Brands Inc | Gelatinizable crosslinked cationic starch and method for its manufacture |
US4609432A (en) * | 1981-05-21 | 1986-09-02 | Brooks Rand Ltd. | Method of making paper having improved tearing strength |
US4347100A (en) * | 1981-05-21 | 1982-08-31 | The Chemithon Corporation | Strength of paper from mechanical or thermomechanical pulp |
SE8306739L (en) * | 1983-12-06 | 1985-06-07 | Svenska Traeforskningsinst | SET TO MAKE PAPERS WITH HIGH FILLER CONTENT |
US4568721A (en) * | 1985-04-01 | 1986-02-04 | Nalco Chemical Company | Starch cationization |
US4913775A (en) * | 1986-01-29 | 1990-04-03 | Allied Colloids Ltd. | Production of paper and paper board |
US4643801A (en) * | 1986-02-24 | 1987-02-17 | Nalco Chemical Company | Papermaking aid |
US5349089A (en) * | 1989-07-07 | 1994-09-20 | National Starch And Chemical Investment Holding Corporation | Reagent for preparing polycationic polysaccharides |
SE8903752D0 (en) * | 1989-11-09 | 1989-11-09 | Eka Nobel Ab | PROCEDURES FOR PREPARING PAPER |
US5126014A (en) * | 1991-07-16 | 1992-06-30 | Nalco Chemical Company | Retention and drainage aid for alkaline fine papermaking process |
US5584966A (en) * | 1994-04-18 | 1996-12-17 | E. I. Du Pont De Nemours And Company | Paper formation |
US5876563A (en) * | 1994-06-01 | 1999-03-02 | Allied Colloids Limited | Manufacture of paper |
US5595631A (en) * | 1995-05-17 | 1997-01-21 | National Starch And Chemical Investment Holding Corporation | Method of paper sizing using modified cationic starch |
US5595630A (en) * | 1995-08-31 | 1997-01-21 | E. I. Du Pont De Nemours And Company | Process for the manufacture of paper |
US5690790A (en) * | 1996-03-28 | 1997-11-25 | The Procter & Gamble Company | Temporary wet strength paper |
JPH09291103A (en) * | 1996-04-25 | 1997-11-11 | Sanwa Kosan Kk | Papermaking starch |
AUPO017196A0 (en) * | 1996-05-30 | 1996-06-27 | George Weston Foods Limited | Novel wet end processing aid |
GB9624031D0 (en) * | 1996-11-19 | 1997-01-08 | Allied Colloids Ltd | Manufacture of paper |
CA2248479A1 (en) * | 1997-09-29 | 1999-03-29 | Calvin T. Tobison | Starch/cationic polymer combinations as coagulants for the mining industry |
US5859128A (en) * | 1997-10-30 | 1999-01-12 | E. I. Du Pont De Nemours And Company | Modified cationic starch composition for removing particles from aqueous dispersions |
US5942087A (en) * | 1998-02-17 | 1999-08-24 | Nalco Chemical Company | Starch retention in paper and board production |
-
2000
- 2000-09-07 CA CA002386403A patent/CA2386403A1/en not_active Abandoned
- 2000-09-07 AU AU71221/00A patent/AU7122100A/en not_active Abandoned
- 2000-09-07 JP JP2001532287A patent/JP2003512541A/en active Pending
- 2000-09-07 CN CN00813784A patent/CN1377436A/en active Pending
- 2000-09-07 WO PCT/US2000/024561 patent/WO2001029313A1/en active Application Filing
- 2000-09-07 MX MXPA02003881A patent/MXPA02003881A/en unknown
- 2000-09-07 KR KR1020027004984A patent/KR20020060204A/en not_active Application Discontinuation
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2002
- 2002-01-17 US US10/052,230 patent/US20020139501A1/en not_active Abandoned
- 2002-04-19 SE SE0201183A patent/SE521309C2/en not_active IP Right Cessation
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2003
- 2003-04-23 US US10/423,043 patent/US20040031579A1/en not_active Abandoned
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SE0201183D0 (en) | 2002-04-19 |
KR20020060204A (en) | 2002-07-16 |
US20020139501A1 (en) | 2002-10-03 |
MXPA02003881A (en) | 2002-10-23 |
CA2386403A1 (en) | 2001-04-26 |
JP2003512541A (en) | 2003-04-02 |
CN1377436A (en) | 2002-10-30 |
US20040031579A1 (en) | 2004-02-19 |
SE0201183L (en) | 2002-06-19 |
SE521309C2 (en) | 2003-10-21 |
WO2001029313A1 (en) | 2001-04-26 |
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