EP0151994A2 - Method of preparing an improved sizing agent and novel paper sizing method - Google Patents
Method of preparing an improved sizing agent and novel paper sizing method Download PDFInfo
- Publication number
- EP0151994A2 EP0151994A2 EP85100782A EP85100782A EP0151994A2 EP 0151994 A2 EP0151994 A2 EP 0151994A2 EP 85100782 A EP85100782 A EP 85100782A EP 85100782 A EP85100782 A EP 85100782A EP 0151994 A2 EP0151994 A2 EP 0151994A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- polymer
- succinic anhydride
- alkenyl succinic
- emulsion
- cationic
- 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.)
- Granted
Links
- 238000004513 sizing Methods 0.000 title claims abstract description 25
- 238000000034 method Methods 0.000 title claims description 25
- 229920000642 polymer Polymers 0.000 claims abstract description 110
- 239000000839 emulsion Substances 0.000 claims abstract description 90
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 59
- -1 alkenyl succinic anhydride Chemical compound 0.000 claims abstract description 34
- 229940014800 succinic anhydride Drugs 0.000 claims abstract description 28
- 229920002554 vinyl polymer Polymers 0.000 claims abstract description 24
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 claims abstract description 17
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 15
- 125000002091 cationic group Chemical group 0.000 claims description 50
- 239000007787 solid Substances 0.000 claims description 32
- 229920001577 copolymer Polymers 0.000 claims description 13
- 239000000178 monomer Substances 0.000 claims description 13
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 claims description 12
- 238000009833 condensation Methods 0.000 claims description 12
- 230000005494 condensation Effects 0.000 claims description 12
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 claims description 11
- ROSDSFDQCJNGOL-UHFFFAOYSA-N Dimethylamine Chemical compound CNC ROSDSFDQCJNGOL-UHFFFAOYSA-N 0.000 claims description 8
- 239000003995 emulsifying agent Substances 0.000 claims description 8
- 229920003169 water-soluble polymer Polymers 0.000 claims description 6
- 238000002360 preparation method Methods 0.000 claims description 5
- UZNHKBFIBYXPDV-UHFFFAOYSA-N trimethyl-[3-(2-methylprop-2-enoylamino)propyl]azanium;chloride Chemical compound [Cl-].CC(=C)C(=O)NCCC[N+](C)(C)C UZNHKBFIBYXPDV-UHFFFAOYSA-N 0.000 claims description 5
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 claims description 4
- 229920001519 homopolymer Polymers 0.000 claims description 4
- QHVBLSNVXDSMEB-UHFFFAOYSA-N 2-(diethylamino)ethyl prop-2-enoate Chemical compound CCN(CC)CCOC(=O)C=C QHVBLSNVXDSMEB-UHFFFAOYSA-N 0.000 claims 6
- JKNCOURZONDCGV-UHFFFAOYSA-N 2-(dimethylamino)ethyl 2-methylprop-2-enoate Chemical compound CN(C)CCOC(=O)C(C)=C JKNCOURZONDCGV-UHFFFAOYSA-N 0.000 claims 6
- DPBJAVGHACCNRL-UHFFFAOYSA-N 2-(dimethylamino)ethyl prop-2-enoate Chemical compound CN(C)CCOC(=O)C=C DPBJAVGHACCNRL-UHFFFAOYSA-N 0.000 claims 6
- 238000006683 Mannich reaction Methods 0.000 claims 3
- NJSSICCENMLTKO-HRCBOCMUSA-N [(1r,2s,4r,5r)-3-hydroxy-4-(4-methylphenyl)sulfonyloxy-6,8-dioxabicyclo[3.2.1]octan-2-yl] 4-methylbenzenesulfonate Chemical compound C1=CC(C)=CC=C1S(=O)(=O)O[C@H]1C(O)[C@@H](OS(=O)(=O)C=2C=CC(C)=CC=2)[C@@H]2OC[C@H]1O2 NJSSICCENMLTKO-HRCBOCMUSA-N 0.000 claims 3
- 150000003335 secondary amines Chemical class 0.000 claims 3
- 238000004945 emulsification Methods 0.000 abstract description 8
- YAXXOCZAXKLLCV-UHFFFAOYSA-N 3-dodecyloxolane-2,5-dione Chemical class CCCCCCCCCCCCC1CC(=O)OC1=O YAXXOCZAXKLLCV-UHFFFAOYSA-N 0.000 description 105
- 238000007792 addition Methods 0.000 description 21
- 229920002472 Starch Polymers 0.000 description 20
- 235000019698 starch Nutrition 0.000 description 20
- 239000008107 starch Substances 0.000 description 19
- 239000000123 paper Substances 0.000 description 15
- 239000000243 solution Substances 0.000 description 15
- 239000000463 material Substances 0.000 description 14
- 239000004094 surface-active agent Substances 0.000 description 13
- 239000000203 mixture Substances 0.000 description 12
- 230000014759 maintenance of location Effects 0.000 description 11
- 239000004530 micro-emulsion Substances 0.000 description 8
- 230000015572 biosynthetic process Effects 0.000 description 7
- 238000002156 mixing Methods 0.000 description 7
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 6
- 239000012153 distilled water Substances 0.000 description 6
- 230000000887 hydrating effect Effects 0.000 description 6
- 239000002245 particle Substances 0.000 description 6
- 239000013055 pulp slurry Substances 0.000 description 6
- 239000002002 slurry Substances 0.000 description 6
- 229920006322 acrylamide copolymer Polymers 0.000 description 5
- 239000007864 aqueous solution Substances 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 4
- 125000003342 alkenyl group Chemical group 0.000 description 4
- 230000035515 penetration Effects 0.000 description 4
- 229920001592 potato starch Polymers 0.000 description 4
- 229920000881 Modified starch Polymers 0.000 description 3
- 229910000019 calcium carbonate Inorganic materials 0.000 description 3
- 125000004432 carbon atom Chemical group C* 0.000 description 3
- 239000012895 dilution Substances 0.000 description 3
- 238000010790 dilution Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 239000011121 hardwood Substances 0.000 description 3
- 239000002655 kraft paper Substances 0.000 description 3
- 235000019426 modified starch Nutrition 0.000 description 3
- 239000011122 softwood Substances 0.000 description 3
- LEMBMAKTRVUEBM-UHFFFAOYSA-N 2-(diethylamino)ethyl prop-2-enoate;prop-2-enamide Chemical compound NC(=O)C=C.CCN(CC)CCOC(=O)C=C LEMBMAKTRVUEBM-UHFFFAOYSA-N 0.000 description 2
- JADMAVSCPFDMLP-UHFFFAOYSA-N 2-(dimethylamino)ethyl 2-methylprop-2-enoate;prop-2-enamide Chemical compound NC(=O)C=C.CN(C)CCOC(=O)C(C)=C JADMAVSCPFDMLP-UHFFFAOYSA-N 0.000 description 2
- KZPOHIRTVQMRBY-UHFFFAOYSA-N 2-(dimethylamino)ethyl prop-2-enoate;prop-2-enamide Chemical compound NC(=O)C=C.CN(C)CCOC(=O)C=C KZPOHIRTVQMRBY-UHFFFAOYSA-N 0.000 description 2
- PUAQLLVFLMYYJJ-UHFFFAOYSA-N 2-aminopropiophenone Chemical compound CC(N)C(=O)C1=CC=CC=C1 PUAQLLVFLMYYJJ-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- GXGJIOMUZAGVEH-UHFFFAOYSA-N Chamazulene Chemical group CCC1=CC=C(C)C2=CC=C(C)C2=C1 GXGJIOMUZAGVEH-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical class CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 125000000217 alkyl group Chemical group 0.000 description 2
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 2
- 150000001412 amines Chemical class 0.000 description 2
- 239000012736 aqueous medium Substances 0.000 description 2
- 125000003710 aryl alkyl group Chemical group 0.000 description 2
- 229920006317 cationic polymer Polymers 0.000 description 2
- 239000001913 cellulose Substances 0.000 description 2
- 229920002678 cellulose Polymers 0.000 description 2
- GQOKIYDTHHZSCJ-UHFFFAOYSA-M dimethyl-bis(prop-2-enyl)azanium;chloride Chemical compound [Cl-].C=CC[N+](C)(C)CC=C GQOKIYDTHHZSCJ-UHFFFAOYSA-M 0.000 description 2
- 235000019441 ethanol Nutrition 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 230000036571 hydration Effects 0.000 description 2
- 238000006703 hydration reaction Methods 0.000 description 2
- 125000001165 hydrophobic group Chemical group 0.000 description 2
- 150000003014 phosphoric acid esters Chemical class 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000007762 w/o emulsion Substances 0.000 description 2
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 description 1
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- ZVUNTIMPQCQCAQ-UHFFFAOYSA-N 2-dodecanoyloxyethyl dodecanoate Chemical compound CCCCCCCCCCCC(=O)OCCOC(=O)CCCCCCCCCCC ZVUNTIMPQCQCAQ-UHFFFAOYSA-N 0.000 description 1
- MUHFRORXWCGZGE-KTKRTIGZSA-N 2-hydroxyethyl (z)-octadec-9-enoate Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OCCO MUHFRORXWCGZGE-KTKRTIGZSA-N 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- 240000003183 Manihot esculenta Species 0.000 description 1
- 235000016735 Manihot esculenta subsp esculenta Nutrition 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- IGFHQQFPSIBGKE-UHFFFAOYSA-N Nonylphenol Natural products CCCCCCCCCC1=CC=C(O)C=C1 IGFHQQFPSIBGKE-UHFFFAOYSA-N 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 241000274582 Pycnanthus angolensis Species 0.000 description 1
- 244000061456 Solanum tuberosum Species 0.000 description 1
- 235000002595 Solanum tuberosum Nutrition 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 229940037003 alum Drugs 0.000 description 1
- 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 1
- ANBBXQWFNXMHLD-UHFFFAOYSA-N aluminum;sodium;oxygen(2-) Chemical compound [O-2].[O-2].[Na+].[Al+3] ANBBXQWFNXMHLD-UHFFFAOYSA-N 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 235000019270 ammonium chloride Nutrition 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- NEHMKBQYUWJMIP-NJFSPNSNSA-N chloro(114C)methane Chemical compound [14CH3]Cl NEHMKBQYUWJMIP-NJFSPNSNSA-N 0.000 description 1
- 229940055042 chromic sulfate Drugs 0.000 description 1
- GRWVQDDAKZFPFI-UHFFFAOYSA-H chromium(III) sulfate Chemical compound [Cr+3].[Cr+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O GRWVQDDAKZFPFI-UHFFFAOYSA-H 0.000 description 1
- 229910000356 chromium(III) sulfate Inorganic materials 0.000 description 1
- 239000011696 chromium(III) sulphate Substances 0.000 description 1
- 235000015217 chromium(III) sulphate Nutrition 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- XFOSBZOUUACCCN-UHFFFAOYSA-M dimethyl-bis(prop-2-enyl)azanium;prop-2-enamide;chloride Chemical compound [Cl-].NC(=O)C=C.C=CC[N+](C)(C)CC=C XFOSBZOUUACCCN-UHFFFAOYSA-M 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- FQPSGWSUVKBHSU-UHFFFAOYSA-N methacrylamide Chemical compound CC(=C)C(N)=O FQPSGWSUVKBHSU-UHFFFAOYSA-N 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- SNQQPOLDUKLAAF-UHFFFAOYSA-N nonylphenol Chemical compound CCCCCCCCCC1=CC=CC=C1O SNQQPOLDUKLAAF-UHFFFAOYSA-N 0.000 description 1
- 239000007764 o/w emulsion Substances 0.000 description 1
- 239000011087 paperboard Substances 0.000 description 1
- XYFCBTPGUUZFHI-UHFFFAOYSA-O phosphonium Chemical compound [PH4+] XYFCBTPGUUZFHI-UHFFFAOYSA-O 0.000 description 1
- 229920002401 polyacrylamide Polymers 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 229940068917 polyethylene glycols Drugs 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- KEJZDYLNJACYGU-UHFFFAOYSA-N prop-2-enamide;trimethyl-[3-(2-methylprop-2-enoylamino)propyl]azanium;chloride Chemical compound [Cl-].NC(=O)C=C.CC(=C)C(=O)NCCC[N+](C)(C)C KEJZDYLNJACYGU-UHFFFAOYSA-N 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 239000011369 resultant mixture Substances 0.000 description 1
- 229910001388 sodium aluminate Inorganic materials 0.000 description 1
- 239000012258 stirred mixture Substances 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-O sulfonium Chemical compound [SH3+] RWSOTUBLDIXVET-UHFFFAOYSA-O 0.000 description 1
- 229920001897 terpolymer Polymers 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- 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
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/33—Synthetic macromolecular compounds
- D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/41—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups
- D21H17/44—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups cationic
- D21H17/45—Nitrogen-containing groups
- D21H17/455—Nitrogen-containing groups comprising tertiary amine or being at least partially quaternised
Definitions
- ASA Alkenyl succinic anhydrides
- the patentee indicates that for effective utilizat- ion, the sizing agents must be used in conjunction with a material which is either cationic in nature or is, on the other hand, capable of ionizing or disassociating in such a manner to produce one or more cations or other positively charged groups.
- the cationic agents as they are defined in this reference are disclosed as "alum, aluminum chloride, long chain fatty amines, sodium aluminate, polyacrylamide, chromic sulfate, animal glue, cationic thermosetting resins, and polyamide polymers".
- the patenteee particularly points out as preferred cationic agents various cationic starch derivates including primary, secondary, tertiary, or quarternary amine starch derivatives and other cationic nitrogen substi- tuded starch derivatives, as well as cationic sulfonium and phosphonium starch derivatives.
- Such derivatives may be prepared from all types of starches including corn, tapioca, potato, etc.
- ASA sizing materials are not water soluble, and must, accordingly, be uniformly suspended in the pulp so that the size can make adequate contact with the cellulosic fibers and thus create the desired effect on the final product.
- a further object of this invention is the use of water soluble cationic vinyl addition polymers having molecular weights above 10,000 and preferably below 1,000,000 as emulsifiers for ASA sizing materials.
- the invention is to utilize cationic water soluble vinyl addition polymers having molecular weights greater than 10,000 and preferably below 1,000,000 as additives and emulsifying agents for ASA sizes.
- cationic vinyl addition polymers having molecular weights greater than 10,000 and preferably below 1,000,000 as additives and emulsifying agents for ASA sizes.
- the use of such cationic vinyl addition polymers serve as useful emulsifying agents for the ASA size and in addition increases the retention of the size upon the cellulosic sheet.
- ASA sizes to which this invention is applicable include those mentioned in U.S. patents 3,102,061, 4,040,900, 3,968,005, and 3,821,069, all of which are hereinafter incorporated by reference.
- ASA sizes useful in the subject of this invention are generally described by the following structural formula: wherein R represents a dimethylene or trimethylene radical, and wherein R 1 is a hydrophobic group containing more than 5 carbon atoms which may be selected from the group consisting of alkyl, alkenyl, aralkyl or aralkenyl groups.
- a surfactant has also been employed in making the ASA sizes of this invention.
- This surfactant may be anionic, non-ionic, or cationic in nature.
- Surfactants employed are generally water soluble and have HLB values ranging from about 8 to about 30 or higher, and preferably from about 8-15.
- the surfactant is generally used to prepare the ASA size by simply mixing it with the raw ASA material.
- the ASA size used in this invention accordingly, and in a preferred embodiment of this invention, will generally contain 75-99.5 parts by weight of ASA and preferably 90-99 parts by weight of ASA with 0.5-25 parts, preferably .75-10 parts, and most preferably 1.0-5 parts by weight of surfactant.
- the surfactants are preferably added-to the ASA prior to emulsification in the aqueous medium.
- the surfactants can also be added to the aqueous medium prior to the addition of the ASA.
- Classes of materials useful as the surfactants in this invention include: ethoxylated alkyl phenols, such as nonyl phenoxy polyethoxy ethanols and octyl phenoxy polyethoxy ethanols; poly ethyleneglycols such as PEG 400 mono-oleate, and PEG 600 dilaurate; as well as other materials including certain ethoxylated phosphate esters.
- Preferred surfactants for use in our invention are GAFAC RM510 and GAFAC RE610, both free acids of complex organic phosphate esters, manufactured by the GAF Corporation.
- Water soluble polymers which are useful cationic agents in this invention include water soluble vinyl addition homopolymers and copolymers having molecular weights greater than 10,000 and preferably below 1,000,000 where at least 10 weight percent and up to 100 weight percent of the mer content of the polymer is a cationic monomer, or cationically modified monomer. Preferably at least 15 and up to 95 weight percent of the mer units in the polymer may be cationic or cationically modified monomers. Most preferably from 20-75 percent by weight of the mer units in the polymer or copolymer are cationic or cationically modified.
- the polymers selected for use in this invention generally have a molecular weight of greater than 10,000 and preferably less than 1,000,000. Polymers of this type should generally be water soluble, and a preferred molecular weight has been found to be between 20,000 and 750,000. Most preferably, the molecular weights of the polymers employed range from 50,000 to 150,000.
- Polymers which can be employed in the practice of this invention include, but are not limited to the following exemplary copolymers and homopolymers: acrylamide-dimethylaminoethylacrylate, acrylamide-dimethylaminoethylacrylate quaternaries, acrylamide-diethylaminoethylacrylate, acrylamide-diethylaminoethylacrylate quaternaries, acrylamide-dimethylaminoethylmethacrylate, acrylamide-dimethylaminoethylmethacrylate quaternaries, acrylamide-diallyldimethyl ammonium chloride, polydiallyl-dimethyl ammonium chloride, polydimethylaminoethylmethacrylate and its quaternaries, polymethacrylamidopropyltrimethyl ammonium chloride; and, acrylamide-methacrylamidopropyltrimethyl ammonium chloride.
- polymers and copolymers of acrylamide which have been subjected to a "Mannich” reaction with formaldehyde and a lower alkyl secondary amine. These polymers may or may not be quaternized.
- condensation polymers such as those prepared by condensing dimethylamine with epi-chlorohydrin. Polymers of this type are described in Reissue Patents 28,807 and 28,808, hereafter incorporated by reference. Polymers of this type typically have intrinsic viscosities in the range of 0.15 to 1.5. Other cationic water soluble condensation polymers such as those prepared from ethylene dichloride and ammonia, which may or may not be quaternized with methylchloride, etc. may also be useful. While the bulk of this specification refers to polymers of this invention as vinyl addition polymers, the description is also applicable to those condensation polymers.
- the polymers employed, as stated above, may be copolymers and even terpolymers of various vinyl addition monomers. While acrylamide is a preferred nonionic monomer for use in preparing copolymers useful in this invention, other nonionic monomers such as methacrylamide and,even certain anionically charged monomers such as acrylic acid, methacrylic acid, various sulfonated water soluble vinyl addition monomers, etc. can be employed.
- Polymers as used in this invention may be in the form of water-in-oil emulsions (such as those described in U.S. Re. patent 28,474 and 28,576, both of which are hereinafter incorporated by reference), dry powders, or dilute aqueous solutions.
- the polymers Preferably form an oil-in-water emulsion of the alkenyl succinic anhydride sizing material.
- an aqueous solution must first be prepared of the polymer.
- the water soluble surfactants used to invert the water-in-oil emulsions have no detrimental effect on the activity of the polymer used to emulsify the ASA size.
- the final size emulsion to be added to the pulp furnish may be polymer.
- the ASA emulsions fed to the pulp slurry according to this invention will generally contain:
- these emulsions will contain:
- the ASA emulsion contains .01 - 5.0 and generally .01 - 1.0 parts polymer and even more preferable, .05 - .9 parts polymer for each part of ASA in the emulsion.
- the ASA emulsion contains .01 - 7.5 and generally .01 - 5.0 parts polymer.
- the polymers are thus used in preparation of the dispersions or emulsions of the ASA sizing material.
- the polymers of this invention may be used to emulsify the ASA, or may be added to previously formed ASA emulsions. In either case, the polymer will increase the performance of ; the emulsion compared to emulsions not containing the polymer.
- conventional emulsifiying agents should be used in addition to the polymer.
- no additional emulsifier need be employed.
- Solution acrylamide copolymers of types DMAEM-MeCl Quat, MAPTAC, and polyDADMAC of molecular weights ranging from 10,000 to 400,000 were evaluated as ASA emulsification and retention aids.
- These novel sizing compositions were compared in terms of ASA particle size, physical emulsion stability and sizing performance to conventional ASA emulsions in water or cationic starch. Description of these polymers are given in Table I.
- ASA emulsions in water were prepared by combining 95 parts of distilled water and 5 parts of ASA in an Eberbach semi-microemulsion cup. The mixture was dispersed for 3 minutes at high speed. The emulsion formed was diluted with distilled water to 0.50 percent ASA solids basis and used in Example 1.
- ASA emulsions in cationic starch were prepared by first hydrating 5 parts of a pregelatinized cationic potato starch in 95 parts of water and agitating for 30 minutes. Size emulsions were then prepared by combining 75 parts of the starch solution with 25 parts of ASA in the emulsion cup and dispersing for 20 seconds. This emulsion was diluted to 0.50 percent ASA solids basis and used in Example 2.
- ASA emulsions in vinyl addition polymers were prepared by dispersing ASA in polymer solutions at a ratio of 5:1 dry solids basis. These emulsions were diluted to 0.50 percent ASA solids basis by the method described above. Examples 3-8 illustrate the novel use of these addition polymers.
- the examples 26 and 27 illustrate the use of dimethylamino epi-chlorohydrin condensation polymers having an intrinsic viscosity of at least 0.15.
- ASA emulsions were tested separately in a paper slurry of composition 50 percent recycled corrugated boxboard, 50 percent recycled newsprint. Other slurry parameters were 0.5 percent consistency, 400 Canadian Standard Freeness, pH 7.5, and 25 degrees Celsius to which was added 12.5 parts per million of hydrated aluminum sulfate. Handsheets of basis weight 50 pounds per 3300 square feet were prepared in accordance with TAPPI T-205 procedures. The sizing compositions listed above were added to the paper slurry shortly before wet-web formation at dosages of 0.10 and 0.15 percent on paper solids. Handsheets were immediately dried on rotary drum to 98 percent solids basis. Results are shown on Table I.
- Vinyl addition polymers such as copolymers of acrylamide with DMAEM-MeCl quat or MAPTAC, and polyDADMAC, were further evaluated as ASA emulsification and retention aids.
- ASA emulsification and retention aids were compared in terms of ASA emulsion particle size, physical emulsion stability with aging, and sizing performance to conventional ASA emulsions in water or cationic starch.
- the molecular weight of these polymers ranged from 10,000 to 400,000. A description of these polymers is shown in Table II.
- ASA emulsions in water were prepared by combining 95 parts of distilled water and 5 parts of ASA in a laboratory 8 ounce Osterizer cup. The mixture was dispersed at high speed for 3 minutes. The emulsion formed was diluted with distilled water to 0.50 percent ASA solids basis and used in Example 9.
- ASA emulsions in cationic starch solutions were prepared by first hydrating 5 parts of a pregelatinized cationic potato starch in 95 parts of water and agitating for 30 minutes. Size emulsions were then prepared by combining 95 parts of the starch solution with 5 parts of ASA in the Osterizer cup and dispersing the size for 25 seconds. This emulsion was diluted to 0.50 percent ASA solids basis and used in Example 10.
- ASA emulsions in vinyl addition polymers were prepared by dispersing ASA in the polymer solutions at a ratio of 1:1 ASA to polymer solids in the O sterizer cup for 5 to 30 seconds. These emulsions are then diluted to 0.50 percent ASA solids as described above. Examples 11-16 illustrate the novel use of these vinyl addition polymers.
- ASA emulsion was tested separately in a paper slurry of composition 50 percent bleached softwood kraft and 50 percent bleached hardwood kraft pulps.
- the other slurry parameters were 0.5 percent consistency, 330 Canadian Standard Freeness, pH 7.3, and 27 degrees Celcius.
- Handsheets of basis weight 50 pounds per 3300 square feet were prepared in accordance with TAPPI T-205 procedures. The sizing compositions listed below were added to the paper slurry shortly before wet web formation at the dosage of 0.20 percent ASA solids on paper solids. Handsheets were immediately pressed to approximately 50 percent residual moisture and dried on a rotary drum dryer to 98 percent paper solids basis. Results are shown in the attached Table II.
- ASA emulsions thus formed were compared in the terms of particle size and sizing performance with respect to ASA water emulsions and conventional emulsions prepared from cationic starch.
- ASA emulsions in water were prepared by combining 95 parts of distilled water and 5 part of ASA in an Eberbach semi-microemulsion cup and dispersing the size for. 60 seconds. The resulting emulsion was diluted to 0.50 percent ASA solids basis with water and used in Example 17.
- the ASA emulsions in cationic starch were prepared by first hydrating three parts of a pregelatinized cationic potato starch in 97 parts agitated cold water for 30 minutes.
- Emulsions were then prepared at two ASA to starch solid ratios of 10:1 and 3:1 by dispersing 30 parts of ASA in 70 parts of 3 percent cationic starch or 9 parts of ASA in 91 parts of 3 percent cationic starch respectively with the aid of the semi-microemulsion cup.
- the resulting emulsions were diluted to 0.5 percent ASA solids basis with water and used in Examples 19 and 20 accordingly.
- Polymer solutions were prepared by hydrating 0.6 parts (as polymer solids) of those copolymers of acrylamide listed below in 99.4 parts of water respectively, allowing sufficient time and mixing for complete hydration.
- Emulsions were than prepared at two ASA to polymer solids ratios of 10:1 and 3:1 by dispersing 6 parts of ASA in 94 parts of 0.6 percent polymer solids solution or 1.8 parts of ASA in 98.2 parts of 0.6 percent polymer solids solution respectively with the aid of the semi-microemulsion cup.
- ASA emulsions were separately added to a 0.5 percent consistency pulp slurry of composition 40 percent bleached hardwood sulfate pulp, 40 percent bleached softwood sulfate pulp, and 20 percent calcium carbonate of 300 Canadian Standard Freeness (pH 8.2). Handsheets of basis weight 50 pounds per 3300 square feet were prepared in accordance with TAPPI T-205 procedures. Emulsions.of ASA were added to the pulp slurry shortly before wet-web formation at dosages of 0.250 and 2.00 percent on dry pulp solids. Handsheets were immediately dried on a rotary drum dryer to 98 percent solids basis (2 percent residual moisture). Results are shown in Table III.
- polymers in the high molecular weight range can lead to the formation of tacky deposits and unstable emulsions. Further research as exemplified herein has shown that polymers having a molecular weight greater than 10,000 but lower than 1,000,000, and preferably from 20,000 to 750,000, performed essentially equivalent to polymers having higher molecular weight. In addition, the use of polymers having molecular weights in the preferred range of from 50,000 - 150,000 led to the elimination of the deposit formation noted above, and increased the stability of the ASA emulsions so prepared.
- the ASA chosen for this and all subsequent studies is a substituted (alkenyl) cyclic dicarboxylic acid anhydride wherein the alkenyl groups are derived from a mixture of 14-22 carbon atoms.
- the ASA size measure used in these tests was prepared by mixing 196 gms. of the polymer solution with 4.0 gms. of a commercial paper grade alkenyl succinic anhydride size available from Chevron Chemical Company, containing 1.0% by weight of Gafac RM-510 surfactant available from GAF Corporation. The resultant mixture was then emulsified by mixing for 30 seconds in an Eberbach semi-microemulsion cup followed by a final dilution of 0.5% ASA solids. The ASA emulsions were added to a commercial, calcium carbonate filled bleached Kraft furnish dosed at 0.25 % on dry pulp solids.
- the neutral ink penetration test describes the paper's resistance to aqueous fluid penetration and is a measurement of time (in seconds) for ink to penetrate paper to a predetermined degree (80 percent reflectance endpoint). The greater the time, the greater the paper's resistance to ink penetration.
- the following examples further illustrate the novel use of acrylamide copolymers of type DMAEM-MeSQ and DADMAC as emulsifiers and retention aids for alkenyl succinic anhydride sizing compositions.
- the ASA emulsions thus formed were compared in terms of particle size and sizing performance with respect to ASA water emulsions and conventional emulsions prepared from cationic starch.
- ASA emulsions in water were prepared by combining 95 parts of distilled water and 5 parts of ASA in an Eberbach semi-microemulsion cup and dispersing the size for 60 seconds. The resulting emulsion was diluted to 0.50 percent ASA solids basis with water and used for the two sets.
- the ASA emulsions in cationic starch were prepared by first hydrating three parts of a pregelatinized cationic potato starch in 97 parts agitated cold water for 30 minutes.
- Emulsions were then prepared at two ASA to starch solid ratios of 10:1 and 1:1 by dispersing 30 parts of ASA in 70 parts of 3 percent cationic starch or 3 parts of ASA in 97 parts of 3 percent cationic starch respectively with the aid of the semi-microemulsion cup.
- the resulting emulsions were diluted to 0.5 percent ASA solids basis with water and used accordingly.
- Polymer solutions were prepared by hydrating 0.6 parts (as polymer) of those copolymers of acrylamide listed below in 99.4 parts of water respectively, allowing sufficient time and mixing for complete hydration.
- Emulsions of ASA in polymer were then prepared by dispersing 6 parts of ASA in 94 parts of 0.6 percent polymer for 60 seconds with the aid of the semi-microemulsion cup. A further dilution to 0.5 percent ASA solids was then taken.
- this example illustrates the advantages offered by this invention: the ability of these cationic water soluble acrylamide copolymers to initiate and maintain a stable ASA emulsion and to render the ASA emulsion particles cellulose substantive.
- Polymers tested include the following:
- ASA emulsions were separately added to a 0.5 percent consistency pulp slurry of compostion 40 percent bleached hardwood sulfate pulp, 40 percent bleached softwood sulfate pulp, and 20 percent calcium carbonate of 300 Canadian Standard Freeness (pH 8.2).
- Handsheets of basis weight 50 pounds per 3300 square feet were prepared in accordance with TAPPI T-205 procedures.
- Emulsions of ASA were added to the pulp slurry shortly before wet-web formation at dosages ranging from 0.125 to 2.00 percent. Handsheets were immediately dried on a rotary drum dryer to 98 percent solids basis (2 percent residual moisture). In another variation of this procedure, 0.025 percent of a polymer was added to the pulp slurry separately after addition of sizing emulsions. Results are shown in Table V.
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Abstract
Description
- Alkenyl succinic anhydrides (ASA) useful in the sizing of cellulosic materials have gained considerable commercial success. These materials were first fully disclosed in U.S. patent 3,102,064 which is hereinafter incorporated by reference. This patent discloses a certain class of chemical materials generally having the structural formula
- In describing the use of the ASA sizes disclosed in this re- ference, the patentee indicates that for effective utilizat- ion, the sizing agents must be used in conjunction with a material which is either cationic in nature or is, on the other hand, capable of ionizing or disassociating in such a manner to produce one or more cations or other positively charged groups. The cationic agents as they are defined in this reference are disclosed as "alum, aluminum chloride, long chain fatty amines, sodium aluminate, polyacrylamide, chromic sulfate, animal glue, cationic thermosetting resins, and polyamide polymers". The patentee particularly points out as preferred cationic agents various cationic starch derivates including primary, secondary, tertiary, or quarternary amine starch derivatives and other cationic nitrogen substi- tuded starch derivatives, as well as cationic sulfonium and phosphonium starch derivatives. Such derivatives, as stated by the patentee, may be prepared from all types of starches including corn, tapioca, potato, etc.
- With the growing commercial use of sizes of the type above described, serious problems have remained in the application of the sizes to paper stock or pulp prior to its formation into sheet or other useful forms. Part of the problem has been that the ASA sizing materials are not water soluble, and must, accordingly, be uniformly suspended in the pulp so that the size can make adequate contact with the cellulosic fibers and thus create the desired effect on the final product.
- While the cationic agents disclosed in U.S. patent 3,103,061 have met with success, there has been a need within the paper industry to produce a more effective, "cationic agent" for ASA sizes. In addition, such cationic agent would preferably aid in the retention of the size on the fiber, and would increase, where desired, the wet and/or dry strength of the final sheet material.
- It is accordingly an object of this invention to provide to the art a group of additives which will serve to emulsify or disperse the ASA size in the pulp and allow for retention of the size onto the fiber.
- A further object of this invention is the use of water soluble cationic vinyl addition polymers having molecular weights above 10,000 and preferably below 1,000,000 as emulsifiers for ASA sizing materials.
- Further objects will appear hereinafter.
- The invention, as briefly stated above, is to utilize cationic water soluble vinyl addition polymers having molecular weights greater than 10,000 and preferably below 1,000,000 as additives and emulsifying agents for ASA sizes. The use of such cationic vinyl addition polymers serve as useful emulsifying agents for the ASA size and in addition increases the retention of the size upon the cellulosic sheet.
- The ASA sizes to which this invention is applicable include those mentioned in U.S. patents 3,102,061, 4,040,900, 3,968,005, and 3,821,069, all of which are hereinafter incorporated by reference.
- The ASA sizes useful in the subject of this invention are generally described by the following structural formula:
- In a particular useful embodiment of this invention, a surfactant has also been employed in making the ASA sizes of this invention. This surfactant may be anionic, non-ionic, or cationic in nature. Surfactants employed are generally water soluble and have HLB values ranging from about 8 to about 30 or higher, and preferably from about 8-15. The surfactant is generally used to prepare the ASA size by simply mixing it with the raw ASA material. The ASA size used in this invention accordingly, and in a preferred embodiment of this invention, will generally contain 75-99.5 parts by weight of ASA and preferably 90-99 parts by weight of ASA with 0.5-25 parts, preferably .75-10 parts, and most preferably 1.0-5 parts by weight of surfactant.
- The surfactants are preferably added-to the ASA prior to emulsification in the aqueous medium. The surfactants can also be added to the aqueous medium prior to the addition of the ASA.
- The surfactants useful in this invention are further described in U.S. patent 4,040,900 previously incorporated by reference into this specification. The relevant parts of U.S. patent 4,040,900 begin at column 4, line 54 continue through column 5, line 46. Other portions of this patent are, however, relevant.
- Classes of materials useful as the surfactants in this invention include: ethoxylated alkyl phenols, such as nonyl phenoxy polyethoxy ethanols and octyl phenoxy polyethoxy ethanols; poly ethyleneglycols such as PEG 400 mono-oleate, and PEG 600 dilaurate; as well as other materials including certain ethoxylated phosphate esters.
- Preferred surfactants for use in our invention are GAFAC RM510 and GAFAC RE610, both free acids of complex organic phosphate esters, manufactured by the GAF Corporation.
- Water soluble polymers which are useful cationic agents in this invention include water soluble vinyl addition homopolymers and copolymers having molecular weights greater than 10,000 and preferably below 1,000,000 where at least 10 weight percent and up to 100 weight percent of the mer content of the polymer is a cationic monomer, or cationically modified monomer. Preferably at least 15 and up to 95 weight percent of the mer units in the polymer may be cationic or cationically modified monomers. Most preferably from 20-75 percent by weight of the mer units in the polymer or copolymer are cationic or cationically modified.
- The polymers selected for use in this invention generally have a molecular weight of greater than 10,000 and preferably less than 1,000,000. Polymers of this type should generally be water soluble, and a preferred molecular weight has been found to be between 20,000 and 750,000. Most preferably, the molecular weights of the polymers employed range from 50,000 to 150,000.
- Polymers which can be employed in the practice of this invention include, but are not limited to the following exemplary copolymers and homopolymers: acrylamide-dimethylaminoethylacrylate, acrylamide-dimethylaminoethylacrylate quaternaries, acrylamide-diethylaminoethylacrylate, acrylamide-diethylaminoethylacrylate quaternaries, acrylamide-dimethylaminoethylmethacrylate, acrylamide-dimethylaminoethylmethacrylate quaternaries, acrylamide-diallyldimethyl ammonium chloride, polydiallyl-dimethyl ammonium chloride, polydimethylaminoethylmethacrylate and its quaternaries, polymethacrylamidopropyltrimethyl ammonium chloride; and, acrylamide-methacrylamidopropyltrimethyl ammonium chloride.
- Also useful are polymers and copolymers of acrylamide which have been subjected to a "Mannich" reaction with formaldehyde and a lower alkyl secondary amine. These polymers may or may not be quaternized.
- Also useful in the practice of this invention are certain condensation polymers such as those prepared by condensing dimethylamine with epi-chlorohydrin. Polymers of this type are described in Reissue Patents 28,807 and 28,808, hereafter incorporated by reference. Polymers of this type typically have intrinsic viscosities in the range of 0.15 to 1.5. Other cationic water soluble condensation polymers such as those prepared from ethylene dichloride and ammonia, which may or may not be quaternized with methylchloride, etc. may also be useful. While the bulk of this specification refers to polymers of this invention as vinyl addition polymers, the description is also applicable to those condensation polymers.
- As seen, all of the polymers useful in this invention are cationically charged and are water-soluble. Many are prepared from vinyl addition monomers, although condensation polymers will also work. Since the number of possible cationically charged monomers that will produce a water soluble polymer is essentially unlimited, and it is expected that all water-soluble cationically charged vinyl addition polymers having a molecular weight of 10,000 or more but less than 1,000,000 will work, we do not wish to be limited to the above given list. However, the mentioned compounds are preferred ones.
- The polymers employed, as stated above, may be copolymers and even terpolymers of various vinyl addition monomers. While acrylamide is a preferred nonionic monomer for use in preparing copolymers useful in this invention, other nonionic monomers such as methacrylamide and,even certain anionically charged monomers such as acrylic acid, methacrylic acid, various sulfonated water soluble vinyl addition monomers, etc. can be employed.
- Polymers as used in this invention may be in the form of water-in-oil emulsions (such as those described in U.S. Re. patent 28,474 and 28,576, both of which are hereinafter incorporated by reference), dry powders, or dilute aqueous solutions. Preferably the polymers form an oil-in-water emulsion of the alkenyl succinic anhydride sizing material.
- In order to employ the polymers of the subject invention in the emulsification of ASA sizes, an aqueous solution must first be prepared of the polymer. In the case of the water-in-oil emulsions of vinyl addition polymers, we have found the water soluble surfactants used to invert the water-in-oil emulsions have no detrimental effect on the activity of the polymer used to emulsify the ASA size. When preparing a polymer solution from a water-in-oil emulsion polymer, a useful method or device for forming the solution is exemplified in U.S. Patent 4,057,223 which discloses a mixing block.
- Depending upon the molecular weight and cationic charge of the polymer, from 0.01.% to 25 %, and preferably .01-10 % by weight of the final size emulsion to be added to the pulp furnish may be polymer.
- The ASA emulsions fed to the pulp slurry according to this invention will generally contain:
- 50 - 99.9 % by weight water
- .01 - 50 % by weight ASA
- .001 - 25,0 % by weight (preferably .005 - 3,0 %) of the water soluble polymer
- Preferably, these emulsions will contain:
- 60 - 99.9 % water
- .01 - 40 % ASA
- .010 - 10 % polymer
- Most preferably the ASA emulsion contains .01 - 5.0 and generally .01 - 1.0 parts polymer and even more preferable, .05 - .9 parts polymer for each part of ASA in the emulsion.
- Most preferably the ASA emulsion contains .01 - 7.5 and generally .01 - 5.0 parts polymer.
- The polymers are thus used in preparation of the dispersions or emulsions of the ASA sizing material.
- The polymers of this invention may be used to emulsify the ASA, or may be added to previously formed ASA emulsions. In either case, the polymer will increase the performance of ; the emulsion compared to emulsions not containing the polymer. When the polymer is added to an ASA emulsion that has already been formed, conventional emulsifiying agents should be used in addition to the polymer. When added or used during the make-up of the ASA emulsion, no additional emulsifier need be employed.
- In order to test the subject invention, the following experiments were conducted. The polymers listed below were obtained commercially or prepared in the form indicated.
- Solution acrylamide copolymers of types DMAEM-MeCl Quat, MAPTAC, and polyDADMAC of molecular weights ranging from 10,000 to 400,000 were evaluated as ASA emulsification and retention aids. These novel sizing compositions were compared in terms of ASA particle size, physical emulsion stability and sizing performance to conventional ASA emulsions in water or cationic starch. Description of these polymers are given in Table I.
- ASA emulsions in water were prepared by combining 95 parts of distilled water and 5 parts of ASA in an Eberbach semi-microemulsion cup. The mixture was dispersed for 3 minutes at high speed. The emulsion formed was diluted with distilled water to 0.50 percent ASA solids basis and used in Example 1. ASA emulsions in cationic starch were prepared by first hydrating 5 parts of a pregelatinized cationic potato starch in 95 parts of water and agitating for 30 minutes. Size emulsions were then prepared by combining 75 parts of the starch solution with 25 parts of ASA in the emulsion cup and dispersing for 20 seconds. This emulsion was diluted to 0.50 percent ASA solids basis and used in Example 2. Lastly, ASA emulsions in vinyl addition polymers were prepared by dispersing ASA in polymer solutions at a ratio of 5:1 dry solids basis. These emulsions were diluted to 0.50 percent ASA solids basis by the method described above. Examples 3-8 illustrate the novel use of these addition polymers.
- The examples 26 and 27 illustrate the use of dimethylamino epi-chlorohydrin condensation polymers having an intrinsic viscosity of at least 0.15.
- The ASA emulsions were tested separately in a paper slurry of composition 50 percent recycled corrugated boxboard, 50 percent recycled newsprint. Other slurry parameters were 0.5 percent consistency, 400 Canadian Standard Freeness, pH 7.5, and 25 degrees Celsius to which was added 12.5 parts per million of hydrated aluminum sulfate. Handsheets of basis weight 50 pounds per 3300 square feet were prepared in accordance with TAPPI T-205 procedures. The sizing compositions listed above were added to the paper slurry shortly before wet-web formation at dosages of 0.10 and 0.15 percent on paper solids. Handsheets were immediately dried on rotary drum to 98 percent solids basis. Results are shown on Table I.
- Vinyl addition polymers, such as copolymers of acrylamide with DMAEM-MeCl quat or MAPTAC, and polyDADMAC, were further evaluated as ASA emulsification and retention aids. These novel sizing compositions were compared in terms of ASA emulsion particle size, physical emulsion stability with aging, and sizing performance to conventional ASA emulsions in water or cationic starch. The molecular weight of these polymers ranged from 10,000 to 400,000. A description of these polymers is shown in Table II.
- ASA emulsions in water were prepared by combining 95 parts of distilled water and 5 parts of ASA in a laboratory 8 ounce Osterizer cup. The mixture was dispersed at high speed for 3 minutes. The emulsion formed was diluted with distilled water to 0.50 percent ASA solids basis and used in Example 9. ASA emulsions in cationic starch solutions were prepared by first hydrating 5 parts of a pregelatinized cationic potato starch in 95 parts of water and agitating for 30 minutes. Size emulsions were then prepared by combining 95 parts of the starch solution with 5 parts of ASA in the Osterizer cup and dispersing the size for 25 seconds. This emulsion was diluted to 0.50 percent ASA solids basis and used in Example 10. ASA emulsions in vinyl addition polymers were prepared by dispersing ASA in the polymer solutions at a ratio of 1:1 ASA to polymer solids in the Osterizer cup for 5 to 30 seconds. These emulsions are then diluted to 0.50 percent ASA solids as described above. Examples 11-16 illustrate the novel use of these vinyl addition polymers.
- Each ASA emulsion was tested separately in a paper slurry of composition 50 percent bleached softwood kraft and 50 percent bleached hardwood kraft pulps. The other slurry parameters were 0.5 percent consistency, 330 Canadian Standard Freeness, pH 7.3, and 27 degrees Celcius. Handsheets of basis weight 50 pounds per 3300 square feet were prepared in accordance with TAPPI T-205 procedures. The sizing compositions listed below were added to the paper slurry shortly before wet web formation at the dosage of 0.20 percent ASA solids on paper solids. Handsheets were immediately pressed to approximately 50 percent residual moisture and dried on a rotary drum dryer to 98 percent paper solids basis. Results are shown in the attached Table II.
- The following examples further illustrate the novel use of acrylamide copolymers of type DMAEM-MeSQ, DMAEA-MeSQ, DEAEA-MeSQ and DADMAC of molecular weights greater than 1,000,000 as emulsifiers and retention aids for alkenyl succinic anhydride sizing compositions. The ASA emulsions thus formed were compared in the terms of particle size and sizing performance with respect to ASA water emulsions and conventional emulsions prepared from cationic starch.
- For comparison, ASA emulsions in water were prepared by combining 95 parts of distilled water and 5 part of ASA in an Eberbach semi-microemulsion cup and dispersing the size for. 60 seconds. The resulting emulsion was diluted to 0.50 percent ASA solids basis with water and used in Example 17. The ASA emulsions in cationic starch were prepared by first hydrating three parts of a pregelatinized cationic potato starch in 97 parts agitated cold water for 30 minutes. Emulsions were then prepared at two ASA to starch solid ratios of 10:1 and 3:1 by dispersing 30 parts of ASA in 70 parts of 3 percent cationic starch or 9 parts of ASA in 91 parts of 3 percent cationic starch respectively with the aid of the semi-microemulsion cup. The resulting emulsions were diluted to 0.5 percent ASA solids basis with water and used in Examples 19 and 20 accordingly.
- Polymer solutions were prepared by hydrating 0.6 parts (as polymer solids) of those copolymers of acrylamide listed below in 99.4 parts of water respectively, allowing sufficient time and mixing for complete hydration. Emulsions were than prepared at two ASA to polymer solids ratios of 10:1 and 3:1 by dispersing 6 parts of ASA in 94 parts of 0.6 percent polymer solids solution or 1.8 parts of ASA in 98.2 parts of 0.6 percent polymer solids solution respectively with the aid of the semi-microemulsion cup.
- A further dilution to 0.5 percent ASA solids was then taken. The following examples illustrate the advantages offered by this invention: the ability of these cationic water soluble acrylamide copolymers to initiate an ASA emulsion and to render the ASA emulsion particles cellulose substantive.
- Each of the below cited ASA emulsions were separately added to a 0.5 percent consistency pulp slurry of composition 40 percent bleached hardwood sulfate pulp, 40 percent bleached softwood sulfate pulp, and 20 percent calcium carbonate of 300 Canadian Standard Freeness (pH 8.2). Handsheets of basis weight 50 pounds per 3300 square feet were prepared in accordance with TAPPI T-205 procedures. Emulsions.of ASA were added to the pulp slurry shortly before wet-web formation at dosages of 0.250 and 2.00 percent on dry pulp solids. Handsheets were immediately dried on a rotary drum dryer to 98 percent solids basis (2 percent residual moisture). Results are shown in Table III.
- This example clearly illustrates the novel use of cationic vinyl addition copolymers as ASA emulsification aids and retention aids. Improved water resistance is realized over conventional ASA in water or cationic starch emulsions. Secondly, the improved water resistance offered by this invention cannot be attributed simply to improved papermachine retention as demonstrated by separate additions of these same cationic polymers to the paper furnish.
- The use of polymers in the high molecular weight range, however, can lead to the formation of tacky deposits and unstable emulsions. Further research as exemplified herein has shown that polymers having a molecular weight greater than 10,000 but lower than 1,000,000, and preferably from 20,000 to 750,000, performed essentially equivalent to polymers having higher molecular weight. In addition, the use of polymers having molecular weights in the preferred range of from 50,000 - 150,000 led to the elimination of the deposit formation noted above, and increased the stability of the ASA emulsions so prepared.
- The effect of various other polymers on the emulsification of ASA sizing materials and the results obtained using such polymers were investigated. In this group of experiments, 3 different classes of polymers were employed (see below). All of these materials were prepared as water-in-oil emulsions of the polymer. Aqueous solutions of the polymers were prepared to yield an approximate 2% product basis or approximately .6% by weight aqueous polymer solution. The polymer solution was prepared by mixing together 288 grams of deionized water, 6.0 mls. of a 2% by weight aqueous solution of an ethoxylated (9) nonyl phenol surfactant followed by adding approximately 6 cc of the water-in-oil emulsion to the stirred mixture. The aqueous solutions were then adjusted to yield 2% by weight polymer product.
- The ASA chosen for this and all subsequent studies is a substituted (alkenyl) cyclic dicarboxylic acid anhydride wherein the alkenyl groups are derived from a mixture of 14-22 carbon atoms.
- The ASA size measure used in these tests was prepared by mixing 196 gms. of the polymer solution with 4.0 gms. of a commercial paper grade alkenyl succinic anhydride size available from Chevron Chemical Company, containing 1.0% by weight of Gafac RM-510 surfactant available from GAF Corporation. The resultant mixture was then emulsified by mixing for 30 seconds in an Eberbach semi-microemulsion cup followed by a final dilution of 0.5% ASA solids. The ASA emulsions were added to a commercial, calcium carbonate filled bleached Kraft furnish dosed at 0.25 % on dry pulp solids.
- The neutral ink penetration test describes the paper's resistance to aqueous fluid penetration and is a measurement of time (in seconds) for ink to penetrate paper to a predetermined degree (80 percent reflectance endpoint). The greater the time, the greater the paper's resistance to ink penetration. Those skilled in the art will readily recognize this test as the generally practiced Hercules'Size Penetration Test. Results are found in Table IV.
- The following examples further illustrate the novel use of acrylamide copolymers of type DMAEM-MeSQ and DADMAC as emulsifiers and retention aids for alkenyl succinic anhydride sizing compositions. The ASA emulsions thus formed were compared in terms of particle size and sizing performance with respect to ASA water emulsions and conventional emulsions prepared from cationic starch.
- For comparison, ASA emulsions in water were prepared by combining 95 parts of distilled water and 5 parts of ASA in an Eberbach semi-microemulsion cup and dispersing the size for 60 seconds. The resulting emulsion was diluted to 0.50 percent ASA solids basis with water and used for the two sets. The ASA emulsions in cationic starch were prepared by first hydrating three parts of a pregelatinized cationic potato starch in 97 parts agitated cold water for 30 minutes. Emulsions were then prepared at two ASA to starch solid ratios of 10:1 and 1:1 by dispersing 30 parts of ASA in 70 parts of 3 percent cationic starch or 3 parts of ASA in 97 parts of 3 percent cationic starch respectively with the aid of the semi-microemulsion cup. The resulting emulsions were diluted to 0.5 percent ASA solids basis with water and used accordingly.
- Polymer solutions were prepared by hydrating 0.6 parts (as polymer) of those copolymers of acrylamide listed below in 99.4 parts of water respectively, allowing sufficient time and mixing for complete hydration. Emulsions of ASA in polymer were then prepared by dispersing 6 parts of ASA in 94 parts of 0.6 percent polymer for 60 seconds with the aid of the semi-microemulsion cup. A further dilution to 0.5 percent ASA solids was then taken. Also this example illustrates the advantages offered by this invention: the ability of these cationic water soluble acrylamide copolymers to initiate and maintain a stable ASA emulsion and to render the ASA emulsion particles cellulose substantive. Polymers tested include the following:
- Each of the below cited ASA emulsions were separately added to a 0.5 percent consistency pulp slurry of compostion 40 percent bleached hardwood sulfate pulp, 40 percent bleached softwood sulfate pulp, and 20 percent calcium carbonate of 300 Canadian Standard Freeness (pH 8.2). Handsheets of basis weight 50 pounds per 3300 square feet were prepared in accordance with TAPPI T-205 procedures. Emulsions of ASA were added to the pulp slurry shortly before wet-web formation at dosages ranging from 0.125 to 2.00 percent. Handsheets were immediately dried on a rotary drum dryer to 98 percent solids basis (2 percent residual moisture). In another variation of this procedure, 0.025 percent of a polymer was added to the pulp slurry separately after addition of sizing emulsions. Results are shown in Table V.
- This example clearly illustrates the novel use of cationic vinyl addition copolymers as ASA emulsification aids and emulsion retention aids. Improved water resistance is realized over conventional ASA in water or cationic starch emulsions. Secondly, the improved water resistance offered by this invention cannot be attributed simply to improved papermachine retention as demonstrated by separate additions of these same cationic polymers to the paper furnish.
Claims (20)
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AT85100782T ATE66028T1 (en) | 1984-01-27 | 1985-01-25 | METHOD FOR PREPARING A SIZE AND PAPER SIZING METHOD. |
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US57432484A | 1984-01-27 | 1984-01-27 | |
US574324 | 1984-01-27 | ||
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US625476 | 1984-06-25 |
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AU (1) | AU577735B2 (en) |
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CS (1) | CS264115B2 (en) |
DE (1) | DE3583688D1 (en) |
DK (1) | DK172016B1 (en) |
ES (1) | ES8609428A1 (en) |
FI (1) | FI81860C (en) |
GR (1) | GR850215B (en) |
MX (1) | MX166763B (en) |
NZ (1) | NZ210958A (en) |
PL (1) | PL148735B1 (en) |
Cited By (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0177260A1 (en) * | 1984-09-25 | 1986-04-09 | Seiko Kagaku Kogyo Co., Ltd. | Aqueous dispersed solution of substituted succinic anhydride and process for producing the same |
EP0743394A2 (en) * | 1995-05-17 | 1996-11-20 | National Starch and Chemical Investment Holding Corporation | Method of paper sizing using modified cationic starch |
WO1999055962A2 (en) * | 1998-04-27 | 1999-11-04 | Akzo Nobel N.V. | A process for the production of paper |
US6207719B1 (en) * | 1998-08-19 | 2001-03-27 | Dennis G. Pardikes | Method and system for preparing ASA emulsion |
WO2004059082A1 (en) * | 2002-12-17 | 2004-07-15 | Lanxess Corporation | Alkenylsuccinic anhydride compositions and method for using the same |
WO2012007364A1 (en) | 2010-07-13 | 2012-01-19 | Akzo Nobel Chemicals International B.V. | Surface sizing of paper |
WO2012061384A3 (en) * | 2010-11-02 | 2012-07-19 | Nalco Company | Method of using aldehyde-functionalized polymers to increase papermachine performance and enhance sizing |
US8840759B2 (en) | 2010-11-02 | 2014-09-23 | Ecolab Usa Inc. | Method of using aldehyde-functionalized polymers to increase papermachine performance and enhance sizing |
WO2014164380A1 (en) * | 2013-03-13 | 2014-10-09 | Nalco Company | Method of using aldehyde-functionalized polymers to increase papermachine performance and enhance sizing |
EP2920364A4 (en) * | 2012-11-15 | 2016-07-13 | Ecolab Usa Inc | Emulsification of alkenyl succinic anhydride with an amine-containing homopolymer or copolymer |
US9487916B2 (en) | 2007-09-12 | 2016-11-08 | Nalco Company | Method of improving dewatering efficiency, increasing sheet wet web strength, increasing sheet wet strength and enhancing filler retention in papermaking |
US9702086B2 (en) | 2014-10-06 | 2017-07-11 | Ecolab Usa Inc. | Method of increasing paper strength using an amine containing polymer composition |
US9752283B2 (en) | 2007-09-12 | 2017-09-05 | Ecolab Usa Inc. | Anionic preflocculation of fillers used in papermaking |
US9920482B2 (en) | 2014-10-06 | 2018-03-20 | Ecolab Usa Inc. | Method of increasing paper strength |
US9951475B2 (en) | 2014-01-16 | 2018-04-24 | Ecolab Usa Inc. | Wet end chemicals for dry end strength in paper |
CN110407973A (en) * | 2018-04-27 | 2019-11-05 | 上海东升新材料有限公司 | A kind of preparation method of gum rosin cationic emulsifier |
US10648133B2 (en) | 2016-05-13 | 2020-05-12 | Ecolab Usa Inc. | Tissue dust reduction |
US10889939B2 (en) | 2015-12-25 | 2021-01-12 | Ecolab Usa Inc. | Sizing method for making paper and paper prepared thereof |
CN113403874A (en) * | 2021-06-25 | 2021-09-17 | 山东太阳纸业股份有限公司 | ASA pickering emulsion with stable microcrystalline cellulose and preparation method thereof |
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US4279794A (en) * | 1979-04-26 | 1981-07-21 | Hercules Incorporated | Sizing method and sizing composition for use therein |
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DE3002687A1 (en) * | 1980-01-25 | 1981-07-30 | Bayer Ag, 5090 Leverkusen | CATIONIC SIZE FOR PAPER |
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- 1985-01-23 AU AU38004/85A patent/AU577735B2/en not_active Ceased
- 1985-01-23 FI FI850296A patent/FI81860C/en not_active IP Right Cessation
- 1985-01-25 NZ NZ21095885A patent/NZ210958A/en unknown
- 1985-01-25 ES ES539847A patent/ES8609428A1/en not_active Expired
- 1985-01-25 BR BR8500339A patent/BR8500339A/en not_active IP Right Cessation
- 1985-01-25 MX MX20414885A patent/MX166763B/en unknown
- 1985-01-25 DE DE8585100782T patent/DE3583688D1/en not_active Expired - Lifetime
- 1985-01-25 EP EP19850100782 patent/EP0151994B2/en not_active Expired - Lifetime
- 1985-01-25 DK DK34085A patent/DK172016B1/en not_active IP Right Cessation
- 1985-01-25 GR GR850215A patent/GR850215B/el unknown
- 1985-01-26 PL PL25170485A patent/PL148735B1/en unknown
- 1985-01-28 CS CS85583A patent/CS264115B2/en unknown
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US3666512A (en) * | 1970-03-25 | 1972-05-30 | American Cyanamid Co | Compositions of fatty acid anhydrides containing catalyst |
US4040900A (en) * | 1974-05-20 | 1977-08-09 | National Starch And Chemical Corporation | Method of sizing paper |
US4279794A (en) * | 1979-04-26 | 1981-07-21 | Hercules Incorporated | Sizing method and sizing composition for use therein |
DE3105903A1 (en) * | 1981-02-18 | 1982-09-09 | Basf Ag, 6700 Ludwigshafen | Process for pulp sizing paper |
EP0085330A1 (en) * | 1982-01-30 | 1983-08-10 | Bayer Ag | Sizing agent and its use |
EP0122617A1 (en) * | 1983-04-16 | 1984-10-24 | Nippon Petrochemicals Company, Limited | Paper sizing composition |
Cited By (36)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4882087A (en) * | 1984-09-25 | 1989-11-21 | Seiko Kagaku Kogyo Co., Ltd. | Aqueous dispersed solution of substituted succinic anhydride and process for producing the same |
EP0177260A1 (en) * | 1984-09-25 | 1986-04-09 | Seiko Kagaku Kogyo Co., Ltd. | Aqueous dispersed solution of substituted succinic anhydride and process for producing the same |
EP0743394A2 (en) * | 1995-05-17 | 1996-11-20 | National Starch and Chemical Investment Holding Corporation | Method of paper sizing using modified cationic starch |
EP0743394A3 (en) * | 1995-05-17 | 1997-11-05 | National Starch and Chemical Investment Holding Corporation | Method of paper sizing using modified cationic starch |
WO1999055962A2 (en) * | 1998-04-27 | 1999-11-04 | Akzo Nobel N.V. | A process for the production of paper |
WO1999055962A3 (en) * | 1998-04-27 | 1999-12-16 | Akzo Nobel Nv | A process for the production of paper |
AU750335B2 (en) * | 1998-04-27 | 2002-07-18 | Akzo Nobel N.V. | A process for the production of paper |
CZ301693B6 (en) * | 1998-04-27 | 2010-05-26 | Akzo Nobel N. V. | Process for producing paper and cationic vinyl addition polymer used in the process |
US7750054B2 (en) | 1998-08-19 | 2010-07-06 | Dennis G. Pardikes | Means for and methods of using a selected energy factor to apply a paper coating |
US6207719B1 (en) * | 1998-08-19 | 2001-03-27 | Dennis G. Pardikes | Method and system for preparing ASA emulsion |
US6951892B2 (en) * | 1998-08-19 | 2005-10-04 | Norchem Industries, Inc. | Means for and methods of using a selected energy factor to apply a paper coating |
WO2004059082A1 (en) * | 2002-12-17 | 2004-07-15 | Lanxess Corporation | Alkenylsuccinic anhydride compositions and method for using the same |
US10145067B2 (en) | 2007-09-12 | 2018-12-04 | Ecolab Usa Inc. | Method of improving dewatering efficiency, increasing sheet wet web strength, increasing sheet wet strength and enhancing filler retention in papermaking |
US9752283B2 (en) | 2007-09-12 | 2017-09-05 | Ecolab Usa Inc. | Anionic preflocculation of fillers used in papermaking |
US9487916B2 (en) | 2007-09-12 | 2016-11-08 | Nalco Company | Method of improving dewatering efficiency, increasing sheet wet web strength, increasing sheet wet strength and enhancing filler retention in papermaking |
WO2012007364A1 (en) | 2010-07-13 | 2012-01-19 | Akzo Nobel Chemicals International B.V. | Surface sizing of paper |
RU2595681C2 (en) * | 2010-11-02 | 2016-08-27 | Налко Компани | Method of using aldehyde-functionalised polymers to increase efficiency of paper-making machine and improvement of sizing |
US8840759B2 (en) | 2010-11-02 | 2014-09-23 | Ecolab Usa Inc. | Method of using aldehyde-functionalized polymers to increase papermachine performance and enhance sizing |
AU2011323531B2 (en) * | 2010-11-02 | 2017-02-02 | Nalco Company | Method of using aldehyde-functionalized polymers to increase papermachine performance and enhance sizing |
AU2011323531A9 (en) * | 2010-11-02 | 2017-02-09 | Nalco Company | Method of using aldehyde-functionalized polymers to increase papermachine performance and enhance sizing |
EP2635634B1 (en) | 2010-11-02 | 2017-03-22 | Nalco Company | Method of using aldehyde-functionalized polymers to increase papermachine performance and enhance sizing |
US9624623B2 (en) | 2010-11-02 | 2017-04-18 | Ecolab Usa Inc. | Emulsification of alkenyl succinic anhydride with an amine-containing homopolymer or copolymer |
TWI582290B (en) * | 2010-11-02 | 2017-05-11 | 奈寇公司 | Method of using aldehyde-functionalized polymers to increase papermachine performance and enhance sizing |
US10227731B2 (en) | 2010-11-02 | 2019-03-12 | Ecolab Usa Inc. | Emulsification of alkenyl succinic anhydride with an amine-containing homopolymer of copolymer |
US8709207B2 (en) | 2010-11-02 | 2014-04-29 | Nalco Company | Method of using aldehyde-functionalized polymers to increase papermachine performance and enhance sizing |
WO2012061384A3 (en) * | 2010-11-02 | 2012-07-19 | Nalco Company | Method of using aldehyde-functionalized polymers to increase papermachine performance and enhance sizing |
EP2920364A4 (en) * | 2012-11-15 | 2016-07-13 | Ecolab Usa Inc | Emulsification of alkenyl succinic anhydride with an amine-containing homopolymer or copolymer |
WO2014164380A1 (en) * | 2013-03-13 | 2014-10-09 | Nalco Company | Method of using aldehyde-functionalized polymers to increase papermachine performance and enhance sizing |
US9951475B2 (en) | 2014-01-16 | 2018-04-24 | Ecolab Usa Inc. | Wet end chemicals for dry end strength in paper |
US9920482B2 (en) | 2014-10-06 | 2018-03-20 | Ecolab Usa Inc. | Method of increasing paper strength |
US9840810B2 (en) | 2014-10-06 | 2017-12-12 | Ecolab Usa Inc. | Method of increasing paper bulk strength by using a diallylamine acrylamide copolymer in a size press formulation containing starch |
US9702086B2 (en) | 2014-10-06 | 2017-07-11 | Ecolab Usa Inc. | Method of increasing paper strength using an amine containing polymer composition |
US10889939B2 (en) | 2015-12-25 | 2021-01-12 | Ecolab Usa Inc. | Sizing method for making paper and paper prepared thereof |
US10648133B2 (en) | 2016-05-13 | 2020-05-12 | Ecolab Usa Inc. | Tissue dust reduction |
CN110407973A (en) * | 2018-04-27 | 2019-11-05 | 上海东升新材料有限公司 | A kind of preparation method of gum rosin cationic emulsifier |
CN113403874A (en) * | 2021-06-25 | 2021-09-17 | 山东太阳纸业股份有限公司 | ASA pickering emulsion with stable microcrystalline cellulose and preparation method thereof |
Also Published As
Publication number | Publication date |
---|---|
FI850296A0 (en) | 1985-01-23 |
NZ210958A (en) | 1988-08-30 |
DK34085A (en) | 1985-07-28 |
DK34085D0 (en) | 1985-01-25 |
MX166763B (en) | 1993-02-02 |
AU577735B2 (en) | 1988-09-29 |
FI81860B (en) | 1990-08-31 |
CS264115B2 (en) | 1989-06-13 |
EP0151994B1 (en) | 1991-08-07 |
PL251704A1 (en) | 1985-10-08 |
DK172016B1 (en) | 1997-09-15 |
ES539847A0 (en) | 1986-09-01 |
EP0151994B2 (en) | 1995-04-19 |
AU3800485A (en) | 1985-08-01 |
EP0151994A3 (en) | 1985-11-27 |
ES8609428A1 (en) | 1986-09-01 |
FI850296L (en) | 1985-07-28 |
GR850215B (en) | 1985-05-17 |
PL148735B1 (en) | 1989-11-30 |
FI81860C (en) | 1990-12-10 |
DE3583688D1 (en) | 1991-09-12 |
CS58385A2 (en) | 1988-09-16 |
BR8500339A (en) | 1985-09-03 |
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