WO2008086029A2 - Surface sizing with agents and glycol ethers - Google Patents
Surface sizing with agents and glycol ethers Download PDFInfo
- Publication number
- WO2008086029A2 WO2008086029A2 PCT/US2008/000360 US2008000360W WO2008086029A2 WO 2008086029 A2 WO2008086029 A2 WO 2008086029A2 US 2008000360 W US2008000360 W US 2008000360W WO 2008086029 A2 WO2008086029 A2 WO 2008086029A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- paper
- sizing agent
- glycol
- composition
- starch
- Prior art date
Links
- 238000004513 sizing Methods 0.000 title claims abstract description 120
- -1 glycol ethers Chemical class 0.000 title claims description 31
- LYCAIKOWRPUZTN-UHFFFAOYSA-N ethylene glycol Natural products OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 title description 15
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 title description 8
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 94
- 229920002472 Starch Polymers 0.000 claims abstract description 81
- 235000019698 starch Nutrition 0.000 claims abstract description 81
- 239000008107 starch Substances 0.000 claims abstract description 78
- 229920000642 polymer Polymers 0.000 claims abstract description 77
- 239000000203 mixture Substances 0.000 claims abstract description 68
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 claims abstract description 47
- 238000007641 inkjet printing Methods 0.000 claims abstract description 7
- 229920001451 polypropylene glycol Polymers 0.000 claims description 36
- 229920001223 polyethylene glycol Polymers 0.000 claims description 31
- 239000002202 Polyethylene glycol Substances 0.000 claims description 27
- 238000000034 method Methods 0.000 claims description 26
- 239000000539 dimer Substances 0.000 claims description 17
- 150000003839 salts Chemical class 0.000 claims description 17
- GYZLOYUZLJXAJU-UHFFFAOYSA-N diglycidyl ether Chemical compound C1OC1COCC1CO1 GYZLOYUZLJXAJU-UHFFFAOYSA-N 0.000 claims description 14
- 229910052751 metal Inorganic materials 0.000 claims description 14
- 239000002184 metal Substances 0.000 claims description 14
- 230000008569 process Effects 0.000 claims description 13
- AOBIOSPNXBMOAT-UHFFFAOYSA-N 2-[2-(oxiran-2-ylmethoxy)ethoxymethyl]oxirane Chemical compound C1OC1COCCOCC1CO1 AOBIOSPNXBMOAT-UHFFFAOYSA-N 0.000 claims description 6
- 229940014800 succinic anhydride Drugs 0.000 claims description 5
- 125000000524 functional group Chemical group 0.000 claims description 4
- 239000004816 latex Substances 0.000 claims description 3
- 229920000126 latex Polymers 0.000 claims description 3
- 235000021158 dinner Nutrition 0.000 claims description 2
- 150000002561 ketenes Chemical class 0.000 claims 2
- CCGKOQOJPYTBIH-UHFFFAOYSA-N ethenone Chemical compound C=C=O CCGKOQOJPYTBIH-UHFFFAOYSA-N 0.000 claims 1
- 239000000463 material Substances 0.000 abstract description 32
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 28
- 150000001875 compounds Chemical class 0.000 abstract description 14
- 230000008901 benefit Effects 0.000 abstract description 8
- 238000011282 treatment Methods 0.000 description 44
- 238000007792 addition Methods 0.000 description 29
- 239000000654 additive Substances 0.000 description 23
- 230000003287 optical effect Effects 0.000 description 20
- 239000000839 emulsion Substances 0.000 description 16
- 238000000576 coating method Methods 0.000 description 14
- 238000012360 testing method Methods 0.000 description 13
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 12
- 239000007788 liquid Substances 0.000 description 12
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 10
- 239000011230 binding agent Substances 0.000 description 10
- 125000002091 cationic group Chemical group 0.000 description 10
- 239000011248 coating agent Substances 0.000 description 10
- 238000007639 printing Methods 0.000 description 9
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 8
- 239000000126 substance Substances 0.000 description 8
- 239000010410 layer Substances 0.000 description 7
- 230000014759 maintenance of location Effects 0.000 description 7
- 238000004381 surface treatment Methods 0.000 description 7
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 6
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 6
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 6
- 230000000996 additive effect Effects 0.000 description 6
- 238000004458 analytical method Methods 0.000 description 6
- 239000001110 calcium chloride Substances 0.000 description 6
- 229910001628 calcium chloride Inorganic materials 0.000 description 6
- 238000004132 cross linking Methods 0.000 description 6
- 239000000945 filler Substances 0.000 description 6
- 239000011780 sodium chloride Substances 0.000 description 6
- 125000000129 anionic group Chemical group 0.000 description 5
- 239000006185 dispersion Substances 0.000 description 5
- 239000000835 fiber Substances 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- 239000000758 substrate Substances 0.000 description 5
- 239000004372 Polyvinyl alcohol Substances 0.000 description 4
- 238000009990 desizing Methods 0.000 description 4
- 235000014113 dietary fatty acids Nutrition 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000000194 fatty acid Substances 0.000 description 4
- 229930195729 fatty acid Natural products 0.000 description 4
- 239000011121 hardwood Substances 0.000 description 4
- 239000003906 humectant Substances 0.000 description 4
- 230000006872 improvement Effects 0.000 description 4
- 230000001965 increasing effect Effects 0.000 description 4
- 239000011256 inorganic filler Substances 0.000 description 4
- 229920002451 polyvinyl alcohol Polymers 0.000 description 4
- 239000011122 softwood Substances 0.000 description 4
- 238000010998 test method Methods 0.000 description 4
- 239000002023 wood Substances 0.000 description 4
- 239000004593 Epoxy Substances 0.000 description 3
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 3
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical group CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 3
- 229920001131 Pulp (paper) Polymers 0.000 description 3
- 239000002250 absorbent Substances 0.000 description 3
- 230000002745 absorbent Effects 0.000 description 3
- 229940037003 alum Drugs 0.000 description 3
- 239000002216 antistatic agent Substances 0.000 description 3
- 229910000019 calcium carbonate Inorganic materials 0.000 description 3
- 239000001913 cellulose Substances 0.000 description 3
- 229920002678 cellulose Polymers 0.000 description 3
- 239000000975 dye Substances 0.000 description 3
- 150000002170 ethers Chemical class 0.000 description 3
- 238000009472 formulation Methods 0.000 description 3
- 229910003475 inorganic filler Inorganic materials 0.000 description 3
- 229910001629 magnesium chloride Inorganic materials 0.000 description 3
- 239000001254 oxidized starch Substances 0.000 description 3
- 235000013808 oxidized starch Nutrition 0.000 description 3
- 230000035515 penetration Effects 0.000 description 3
- 239000000049 pigment Substances 0.000 description 3
- 229920002401 polyacrylamide Polymers 0.000 description 3
- 229940088417 precipitated calcium carbonate Drugs 0.000 description 3
- 230000001737 promoting effect Effects 0.000 description 3
- PYSRRFNXTXNWCD-UHFFFAOYSA-N 3-(2-phenylethenyl)furan-2,5-dione Chemical compound O=C1OC(=O)C(C=CC=2C=CC=CC=2)=C1 PYSRRFNXTXNWCD-UHFFFAOYSA-N 0.000 description 2
- 235000009899 Agrostemma githago Nutrition 0.000 description 2
- 239000004971 Cross linker Substances 0.000 description 2
- 229920000881 Modified starch Polymers 0.000 description 2
- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 229920000147 Styrene maleic anhydride Polymers 0.000 description 2
- 244000178320 Vaccaria pyramidata Species 0.000 description 2
- 229910000329 aluminium sulfate Inorganic materials 0.000 description 2
- 235000011128 aluminium sulphate Nutrition 0.000 description 2
- 150000001412 amines Chemical class 0.000 description 2
- 229920001400 block copolymer Polymers 0.000 description 2
- 238000005282 brightening Methods 0.000 description 2
- 238000003490 calendering Methods 0.000 description 2
- 235000013339 cereals Nutrition 0.000 description 2
- 239000004927 clay Substances 0.000 description 2
- 230000001143 conditioned effect Effects 0.000 description 2
- 239000013530 defoamer Substances 0.000 description 2
- 150000002118 epoxides Chemical group 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 235000019426 modified starch Nutrition 0.000 description 2
- 239000002736 nonionic surfactant Substances 0.000 description 2
- 239000012766 organic filler Substances 0.000 description 2
- 229920000768 polyamine Polymers 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 150000003856 quaternary ammonium compounds Chemical class 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 150000005846 sugar alcohols Polymers 0.000 description 2
- JNYAEWCLZODPBN-JGWLITMVSA-N (2r,3r,4s)-2-[(1r)-1,2-dihydroxyethyl]oxolane-3,4-diol Chemical class OC[C@@H](O)[C@H]1OC[C@H](O)[C@H]1O JNYAEWCLZODPBN-JGWLITMVSA-N 0.000 description 1
- CVEPFOUZABPRMK-UHFFFAOYSA-N 2-methylprop-2-enoic acid;styrene Chemical compound CC(=C)C(O)=O.C=CC1=CC=CC=C1 CVEPFOUZABPRMK-UHFFFAOYSA-N 0.000 description 1
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 1
- 229920000178 Acrylic resin Polymers 0.000 description 1
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- 229930091051 Arenine Natural products 0.000 description 1
- 241000887125 Chaptalia nutans Species 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 229920002261 Corn starch Polymers 0.000 description 1
- QEVGZEDELICMKH-UHFFFAOYSA-N Diglycolic acid Chemical compound OC(=O)COCC(O)=O QEVGZEDELICMKH-UHFFFAOYSA-N 0.000 description 1
- JOYRKODLDBILNP-UHFFFAOYSA-N Ethyl urethane Chemical compound CCOC(N)=O JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 description 1
- 240000000486 Lepidium draba Species 0.000 description 1
- 235000000391 Lepidium draba Nutrition 0.000 description 1
- 240000003183 Manihot esculenta Species 0.000 description 1
- 235000016735 Manihot esculenta subsp esculenta Nutrition 0.000 description 1
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 239000004902 Softening Agent Substances 0.000 description 1
- 229920002125 Sokalan® Polymers 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
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 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
- 150000001408 amides Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000003115 biocidal effect Effects 0.000 description 1
- 239000003139 biocide Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 description 1
- 125000002843 carboxylic acid group Chemical group 0.000 description 1
- 239000005018 casein Substances 0.000 description 1
- BECPQYXYKAMYBN-UHFFFAOYSA-N casein, tech. Chemical compound NCCCCC(C(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(CC(C)C)N=C(O)C(CCC(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(C(C)O)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(COP(O)(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(N)CC1=CC=CC=C1 BECPQYXYKAMYBN-UHFFFAOYSA-N 0.000 description 1
- 235000021240 caseins Nutrition 0.000 description 1
- 239000004359 castor oil Substances 0.000 description 1
- 235000019438 castor oil Nutrition 0.000 description 1
- 229920006317 cationic polymer Polymers 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 229910052570 clay Inorganic materials 0.000 description 1
- 239000008199 coating composition Substances 0.000 description 1
- 239000011247 coating layer Substances 0.000 description 1
- 239000013065 commercial product Substances 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 239000008120 corn starch Substances 0.000 description 1
- 239000003431 cross linking reagent Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 150000005690 diesters Chemical class 0.000 description 1
- WASQWSOJHCZDFK-UHFFFAOYSA-N diketene Chemical compound C=C1CC(=O)O1 WASQWSOJHCZDFK-UHFFFAOYSA-N 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 125000003700 epoxy group Chemical group 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- QHZOMAXECYYXGP-UHFFFAOYSA-N ethene;prop-2-enoic acid Chemical compound C=C.OC(=O)C=C QHZOMAXECYYXGP-UHFFFAOYSA-N 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 150000002191 fatty alcohols Chemical class 0.000 description 1
- 150000002194 fatty esters Chemical class 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- ZEMPKEQAKRGZGQ-XOQCFJPHSA-N glycerol triricinoleate Natural products CCCCCC[C@@H](O)CC=CCCCCCCCC(=O)OC[C@@H](COC(=O)CCCCCCCC=CC[C@@H](O)CCCCCC)OC(=O)CCCCCCCC=CC[C@H](O)CCCCCC ZEMPKEQAKRGZGQ-XOQCFJPHSA-N 0.000 description 1
- 239000001046 green dye Substances 0.000 description 1
- LNEPOXFFQSENCJ-UHFFFAOYSA-N haloperidol Chemical compound C1CC(O)(C=2C=CC(Cl)=CC=2)CCN1CCCC(=O)C1=CC=C(F)C=C1 LNEPOXFFQSENCJ-UHFFFAOYSA-N 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 238000010191 image analysis Methods 0.000 description 1
- 238000003703 image analysis method Methods 0.000 description 1
- 239000001023 inorganic pigment Substances 0.000 description 1
- 238000009533 lab test Methods 0.000 description 1
- 238000011005 laboratory method Methods 0.000 description 1
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 229920000962 poly(amidoamine) Polymers 0.000 description 1
- 229920001515 polyalkylene glycol Polymers 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 239000004848 polyfunctional curative Substances 0.000 description 1
- 229920000151 polyglycol Polymers 0.000 description 1
- 239000010695 polyglycol Substances 0.000 description 1
- 229920005862 polyol Polymers 0.000 description 1
- 150000003077 polyols Chemical class 0.000 description 1
- 229920002689 polyvinyl acetate Polymers 0.000 description 1
- 239000011118 polyvinyl acetate Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- HXHCOXPZCUFAJI-UHFFFAOYSA-N prop-2-enoic acid;styrene Chemical compound OC(=O)C=C.C=CC1=CC=CC=C1 HXHCOXPZCUFAJI-UHFFFAOYSA-N 0.000 description 1
- 238000004537 pulping Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 229920013730 reactive polymer Polymers 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 229920001909 styrene-acrylic polymer Polymers 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 239000012815 thermoplastic material Substances 0.000 description 1
- 238000010023 transfer printing Methods 0.000 description 1
- 230000002087 whitening effect Effects 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
- 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
- D21H21/16—Sizing or water-repelling agents
-
- 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
- D21H17/16—Addition products thereof with hydrocarbons
-
- 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
- D21H17/17—Ketenes, e.g. ketene dimers
-
- 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
- D21H19/00—Coated paper; Coating material
- D21H19/36—Coatings with pigments
- D21H19/44—Coatings with pigments characterised by the other ingredients, e.g. the binder or dispersing agent
- D21H19/54—Starch
-
- 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
- D21H19/00—Coated paper; Coating material
- D21H19/36—Coatings with pigments
- D21H19/44—Coatings with pigments characterised by the other ingredients, e.g. the binder or dispersing agent
- D21H19/56—Macromolecular organic compounds or oligomers thereof obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D21H19/60—Polyalkenylalcohols; Polyalkenylethers; Polyalkenylesters
Definitions
- This invention describes the improvement of uncoated fine paper by treatment of the surface of the paper with polymers based on glycol ethers used in combination with starch and paper sizing agents.
- the invention results in paper with enhanced ink-jet print quality.
- the enhanced qualities include less mottle on the printed images, less strike-through to the back side of the paper when printed, and enhanced optical density of printed images.
- Glycol ether based polymers including those end capped with epoxy groups have been added to paper for many years.
- US Patent 3873354A (1972) describes the addition of humectants along with salts, such as sodium chloride and calcium chloride, to paper to be used for electroreprographic (or electrostatic) printing, that is copy paper.
- the humectant must be water soluble or water miscible.
- the size press is mentioned as a means of application and "another additive which will typically be added to the size press solution is a conventional binder such as a starch, gum, casein, polyvinyl alcohol or acetate, animal glue, etc.”.
- the goal was to reduce the static build-up on the paper.
- the level of addition of salts was recited but not the level of humectant. However, in an example, about 0.05% of the paper weight of polyethylene glycol was added. This is greater than the level use by applicant herein.
- the use of adducts of polyethylene glycol are not mentioned nor is the use of polypropylene glycol or adducts of polypropylene glycol mentioned. The latter two are not water soluble. There is no mention of the use of sizing agents in the paper.
- US Patent 4210412 describes the use of "polyhydric alcohol” in cellulose based textiles.
- the additive is used to swell the cellulose so it will accept dyes during a transfer printing operation.
- What is called polyhydric alcohol includes "polyalkylene glycols such as polyethylene glycol of average molecular weight of 200 to 4000, polypropylene glycol of average molecular weight of 400 to 5000, polyethylene glycol / polypropylene glycol block copolymers of average molecular weight of 400 to 5000 . . . mono- and diethers . . . and diesters . . .”
- the addition levels were not given; but, the addition levels used in the examples were higher than the current invention. For example, the level used in Example 2 had polyethylene glycol added at 7.5% of the substrate. This is far greater than used in the current invention
- US Patent application 20050104947 A1 describes treatments for paper to reduce the amount of cockle and curl and also to provide an ink-jet image recording method.
- the treated paper is defined by its level of water absorption and a ratio of wet to dry tensile strength.
- the cockle and curl tendencies are lowered by decreasing the hydrogen bonds between fibers in the paper.
- the desired paper is obtained by two methods.
- One method deals with the treatment of the pulp fibers before the sheet is formed such that the treatment compounds are located between fibers.
- the compounds that can be used are polyethylene glycol polypropylene glycol block copolymers, polyoxyethylene fatty acid esters, and other nonionic surfactant type materials. Also materials such as monoglycidyl ethers can be used.
- a second method is to add to the paper a heat-curable material or a thermoplastic material. Again the material must be located between fibers and in this case adhere fibers together.
- Epoxy resins are given as one class of suitable additives.
- the treatment is also said to preferably include polyvalent metal salts such as calcium chloride or a cationic polymer such as cationic starch. Either material can be added at levels that provide 0.1 to 2 g/m 2 of material to the sheet.
- the sheet weights of interest are 60 to 128 g/m 2 . Therefore, the range of percentage addition is from 0.08 to 3.3%.
- coated papers are very different from the paper of the current invention.
- a coated paper has one or more relatively thick layers of treatment on one or both sides of a preformed paper.
- Such papers find use in high-end printing application including high-end ink-jet printing applications such as photographic paper.
- coated grades have an absorbent layer composed of either a polymer that absorbs a high volume of liquid ink or a high level of filler that can adsorb a high volume of liquid ink.
- glycol ether based polymers used in such coatings. First they may be added as an absorbent material and secondly, diglycidyl ethers of glycol based polymers may be added to improve surface strength.
- European Patent 0634284 discusses both such uses.
- the instant invention does not cover coated papers.
- polyglycol ethers in paper coatings.
- US Patent 5746814 describes the addition of the following compounds as desizing agents in a more complex composition for coating of paper: poly(alkylene glycol); poly(propylene oxide) - poly(ethylene oxide) copolymers; fatty ester modified compounds of glycerol and poly(ethylene glycol); and poly(oxyalkyene)modified compounds of sorbitan esters, fatty amines, alkanol amides, castor oil, fatty acid, fatty alcohol.
- the overall composition contains solvent, binder, desizing agent, anticurl agent, defoamer, biocide, antistatic agent, lightfastness promoting agent, and a filler. All of the coating applications fall into a different class of paper from the current invention and the coating compositions are significantly different as noted above.
- Base paper employed for the paper support of the present invention is made employing wood pulp as a main raw material . . . It is possible to incorporate into base paper sizing agents such as . . . strengthening agents such as starch . . . moisture retention agents such as polyethylene glycol, dispersing agents and softening agents . . .”
- US Patent 6203899B1 describes a printing medium comprising a liquid absorbent base material, an ink-receiving layer provided on the base material, which comprises a pigment, a binder and a cationic substance, and a surface layer provided on the ink receiving layer.
- a coated paper It is described as fibrous pulp and a filler impregnated with a crosslinking substance.
- the crosslinking substance is crosslinked to form nonswelling paper.
- the crosslinking substance can be an epoxy.
- PPGDGE is specifically described.
- the crosslinking substance can be a polymer having a reactive group. Starch is one example of the polymer. The amount of starch is in the range that can be applied by a size press.
- the ratio of crosslinking substance, starch, to crosslinking agent, PPGDGE, is from 100:1 to 1 :1 by weight. The range is different from the current invention where our ratio under preferred conditions is about 400 to 1 or less.
- a polyvalent metal salt is mentioned as an option for crosslinking certain materials.
- the divalent metal ions that are optional additives of the invention of this disclosure do not crosslink starch.
- US 6706320B2 describes modifying a surface containing a polymeric material.
- the substrate can be cellulosic and in another claim it is said the modifying agent can be a crosslinker.
- the crosslinker can be an epoxy compound such as diglycidyl ethers of polyols.
- the process of the patent requires the presence of a polyamine as a surface modifying agent and that the polyamine vaporize in the process. The epoxy compound reacts with the amine.
- US Patent 5746814A includes polyethyleneglycol diglycidyl ether as one of the compounds that can be added to prevent paper from curling.
- An elaborate composition for treating paper is described with a wide range of levels of each component. There are nine components in the composition and they can include water, starch as a binder, and PEGDGE as an anticurl or a desizing agent. Taking the maximum of starch in the composition and the minimum of PEGDGE one gets a ratio of 150:1. This is different from that of the current invention. Furthermore the current invention does not require many of the other components listed such as antistatic agent or desizing agent or lightfastness promoting agent.
- the composition is for treating paper that has already been imaged.
- Hercules Incorporated has a patent (US6207258 B1) on the use of divalent metal salts with sizing agents. It also had a patent (US6051107A) on mixtures of reactive and nonreactive sizing agents as pre-mixes and in paper treatment compositions. The later patent was not maintained.
- one embodiment of the invention involves a paper composition having applied to its surface a composition comprising a glycol ether based polymer that provides enhanced ink-jet print quality.
- the advantage of the paper composition is improved ink-jet printing without significant loss of water hold-out.
- this first embodiment of the invention is an uncoated paper (based on wood pulp or other cellulose product based) that has been treated on the surface with at least the following materials and dried to the point of usefulness. These materials are:
- the sizing agent will be present in an amount of 0.01% to 0.3% based on dry weight of paper.
- the starch will be present in an amount of 1 to 8% based on dry weight of paper.
- glycol ether based polymer will be present in an amount of less than 0.025% based on dry weight of paper.
- One preferred composition is paper surface-treated with starch, sizing material, a glycol ether based polymer and a divalent metal salt.
- the sizing materials and glycol ether based polymers are defined below along with the addition levels.
- the paper of the invention has improved ink-jet print qualities of less mottle of printed areas, less strike-through of ink, and possibly increased optical density over paper not treated with all the components of the invention.
- the sizing agents provide water hold-out. They may also improve the sharpness and optical density of ink-jet printed images.
- the addition of sizing agents to paper is common.
- starch is a standard additive to paper and thus, the invention in one embodiment is the addition of sizing agent and starch with glycol ether based polymers, such as polypropylene glycol diglycidyl ether.
- glycol ether based polymers such as polypropylene glycol diglycidyl ether.
- the paper as described above also contains a divalent metal salt as described in Hercules patent US6207258 B1 , incorporated by reference.
- Any uncoated paper can be used, but a preferred paper is uncoated "fine" paper for printing and writing applications.
- Such paper typically contains bleached wood pulp, precipitated calcium carbonate, and starch along with other materials deemed beneficial for preparing the paper or enhancing paper properties or reducing the cost of the paper.
- a typical uncoated fine paper has a , basis weight of 70 to 80 grams per square meter.
- the three or four components of the invention, listed above, may be added either separately or together to the surface of the paper. Fine paper for printing and writing is usually treated before it leaves the paper machine on which it was m maordloe.
- the internal chemistry may affect the application of the coating but does not have a direct effect on the final properties of the paper.
- internal sizing is covered up by a coating and will not directly change the surface tension of the final coating unless it migrates through the coating.
- the method of applying the materials used in this invention is not crucial as long as the application method for the materials is controllable and leads to the desired results.
- the most preferred method of addition is for the starch to be dissolved in water by cooking and for the other components to be added to the starch solution and then for the resulting composition (the treatment composition) to be applied to the paper with a paper machine size press.
- a second embodiment of the invention is the composition used to treat the paper. It is defined as a starch based solution containing at least one paper sizing agent and at least one glycol ether based polymer and optionally a soluble divalent metal salt such as calcium chloride and optionally other additives common to the treatment of paper.
- the treatment composition allows for all of the additives to be applied simultaneously to the paper.
- This is an aqueous composition that contains : sizing agent in an amount of 0.03-1%, starch present in an amount of 1.5-12%, glycol present in an amount of less than 0.25%.
- the treatment composition consists predominantly of water in which a binder is dissolved.
- the binder is the predominant component aside from the water.
- the binder for this invention is predominantly starch.
- Other binders such a polyvinyl alcohol can be used in combination with the starch.
- other additives are typically added such as sizing agents that hold out water and improve printing properties; optical brightening agents; dyes; and antistatic agents.
- materials such as inorganic fillers are added. When fillers are added they do not constitute more than about 40% of the composition on a dry weight percent basis of the non-water components.
- compositions can also contain other common additives such as sodium chloride and defoamer.
- the advantage offered by the second embodiment of the invention is the simultaneous treatment of the paper with a composition that leads to the improvements listed above in the first embodiment of the invention.
- the composition must be such that it is uniform and it can be applied to the paper in a uniform manner.
- glycol ether based polymers will be added to the treatment composition so that they are applied to the paper with the paper machine at the same time as the starch and sizing agent.
- a third aspect of the current invention is a pre-mixture of the sizing agents and glycol ether based polymers and optionally a divalent metal salt.
- the pre-mixture is then added to the starch based solution just described.
- the pre-mixtures may be water based solutions or emulsions or dispersions.
- the glycol ether polymer will be 3-50% based on the amount of sizing agent.
- a third embodiment of the invention comprises pre-mixtures of some of the additives that go into the surface treatment composition thus offering the convenience of adding several materials simultaneously to the mixture used to treat the paper.
- the pre- mixtures that are of interest for this disclosure will contain the following materials:
- a water-based composition i.e. a solution, latex, and or dispersion of one or more paper sizing agents, and one or more glycol ether based polymers.
- the glycol ether based polymers used in this invention include polymers with repeat units of ethylene glycol or propylene glycol or combinations of them. There may be other functional groups along the backbone provided they do not account for more than approximately ten percent by weight of the final polymer structure. There may be branching along the backbone.
- the polymers can be end-capped with hydroxyl groups, ethers, gylcidyl ethers, esters, carboxylic acid groups, and other functionality so long as the end groups do not account for more than 25% of the weight of the average polymer molecule.
- the polymer compositions may have one, two, or more types of functional end groups other than hydroxyl groups. There may also be one of more types of functional groups within the polymer backbone or grafted on to it.
- glycol ether based surfactants that fit the above criteria are part of this invention provided they meet the remaining conditions given below.
- Glycidyl ether end- capped polymers such as polyethyleneglycol digycidyl ether and polypropyleneglycol digycidyl ether are useful also.
- the average molecular weight of the glycol ether based polymers of this invention shall be from approximately 350 g/mole to approximately 200,000.
- the polymer must be soluble or readily dispersible in water.
- the preferable average molecular weight is between 380 and 20,000 and most preferably between 500 and 2000 g/mole.
- the addition level of the glycol ether based polymers of the invention is defined by the impact on sizing as defined in this invention and by concentration.
- the glycol ether based polymers of the invention should not cause greater than a 25% reduction in the level of sizing when utilized under at least some portion of the conditions of this invention.
- polypropylene glycol (PPG) may be used at a low level but at a high level it interferes with sizing.
- the level of addition of the glycol ether polymers to the aqueous composition for surface treating the paper shall be less than 0.25%.
- the level of addition in a premix with sizing agent should be less than 50% of the active sizing agent by weight.
- the paper substrate which is treated in the current invention can contain wood based pulp from ground wood to chemically bleached wood or a non-wood based pulp or a combination of pulps.
- the paper can also contain usual paper making inorganic fillers such as calcium carbonate or clay and may also contain organic fillers.
- the paper can also contain strength additives, retention additives, internal sizing agents and other common paper additives such as alum.
- the preferred grade of paper can be any type suitable for ink- jet printing which can include fine paper to white-top liner board.
- the basis weight of the paper can be anywhere from 40g/m 2 to 350g/m 2 .
- the preferred paper is any type of printing and writing paper including roll fed to sheet fed papers. The most preferred is uncoated fine paper with a basis weight between 60 and 100 g/m 2 .
- the starches that are suitable as part of the paper treatment can be of any kind provided they can be dissolved in water and applied to the paper.
- the starches can be from a variety of sources including corn, potato, rice, cassava root, and others used in paper making. Unmodified and modified starches can be used. Modified starches include oxidized, ethylated, cationic, anionic, amphoteric, hydrophobically modified, and others used in paper making.
- the preferred starches have reduced viscosities such that solutions of greater than 6% solids can be used on a paper machine size press. The most preferred are those with reduced viscosity that are also are oxidized, ethylated, cationic, or amphoteric.
- the range of starch treatment based on the dry weight of the final paper is 1 % to 8.0%. More preferably from 2% to 7% and most preferably from 3% to 6%.
- the range of starch concentration in the treatment composition can be from 1.5% to 12% provided the viscosity allows for application to the paper substrate. More preferably the concentration will be between 3% and 11% and most preferably between 5% and 10%.
- the surface treatment sizing agents suitable for the current invention include those that are termed reactive such as alkyl ketene dimers, alkenyl ketene dinners, and alkyl succinic anhydrides.
- Unreactive sizing agents are also suitable and may be mixed or used with the reactive sizing agents as described in a previous Hercules' patent (US6051107A). Unreactive sizing agents may be used on their own. Unreactive sizing agents include soluble polymers such as styrene - maleic anhydride based polymers, styrene - esterified maleic anhydride based polymers, styrene acrylic acid and styrene methacrylic acid based polymers and insoluble polymers such as polymer latexes commonly used in paper making such as poly(styrene/acrylic) resins, acrylonitrile/acylic resins and urethane polymers and insoluble polymer dispersions such as of ethylene/acrylic acid polymers.
- soluble polymers such as styrene - maleic anhydride based polymers, styrene - esterified maleic anhydride based polymers, st
- the level of surface treatment sizing agent in the final dry paper will range from 0.01 % to 0.3% on a dry weight basis. Preferably the level is 0.02 to 0.2% and most preferably it is 0.03 to 0.1%.
- All of the above levels are based on both sides of a base paper being treated. However, the invention is applicable to treatment of one or both sides. When only one side is being treated all of the above levels relating to the paper will be one half of the values listed.
- the final paper may contain other additives that were included in the formation of the paper or were applied along with the surface treatment or separately from the surface treatment.
- the additives applicable are those which are usually utilized in paper. They include but are not limited to the following: inorganic and organic fillers such as calcium carbonate or hollow sphere pigments; optical brightening agents which are also known as fluorescent whitening aids, pigments; dyes, strength additives such as polyamidoamines, promoter resins such as polydimethyldiallylammonium chloride; adhesion promoting polymers such as styrene acrylic latexes and styrene maleic anhydride based polymers; and inorganic salts such as sodium chloride and calcium chloride.
- the final paper contains a divalent metal salt it should be less than 0.25% of the paper weight.
- the methods of applying the paper treatment composition of the current invention are not limited provided uniform controlled application is obtained.
- the treatment may be made to paper formed on a paper machine and then only partially dried or it can be made on a paper machine to dried paper or the treatment can be done separate from the paper machine to paper that was formed, dried, and moved.
- the preferred process is for paper to be formed with a paper machine, partially dried, and treated using a paper machine size press, and then for the paper to be dried again.
- the paper may be further modified by calendering.
- the treatment composition has the same components just described.
- the starch solution in water must be of dissolved starch and the viscosity must be such that the solution, containing other components, can be applied to the paper.
- the viscosity and not the solids of the starch solution is the most critical factor; however, some starch materials can only be dissolved at very low concentrations before they become too thick to use.
- a paper maker will select a starch based on the properties it imparts to the paper as well as its ease of use and the ability to apply the desired level with the equipment being used.
- a preferred level of starch in the treatment composition is 3 to 12% and a most preferred level is 5 to 10%.
- Other materials such as polyvinyl alcohol may be used with the starch, if desired.
- the additional binder level will be less than the starch level.
- Suitable sizing agents are described above. They are added to the starch solution.
- the level of sizing agent in the composition will depend on two factors: the level of the starch composition applied to the paper and the desired level of sizing treatment. Typically the level of starch addition is selected along with the starch solution concentration and then the level of sizing agent in the starch solution is adjusted to get the desired level of treatment.
- the level of sizing agent in the starch composition will be between 0.03 and 1% of the paper treatment composition based on the active component of the sizing agent.
- the level of glycol ether based polymer in the treatment composition will be determined in the same manner as described for the sizing agent level.
- the level of glycol ether based polymer will be determined by the amount of starch solution applied and the desired level of the polymer to be applied.
- the level of glycol ether polymer in the paper treatment composition will be less than 0.25%.
- the treatment composition may contain other materials as noted above for the paper.
- a soluble divalent metal salt such as calcium chloride and magnesium chloride the level of the salt will be less than 20% of the starch level.
- the sizing agents of interest were described above.
- One or more sizing agents can be combined.
- the form of the sizing agent will be as a solution emulsion or dispersion in water with suitable additives used to obtain desired stability.
- One or more glycol ether based polymers can be combined with the sizing agents.
- the sizing agent formulation may also contain a water soluble divalent metal salt such as calcium chloride or magnesium chloride.
- the amount of glycol ether based polymer versus sizing agents can be from 3% to 50% polymer to active sizing agent. More preferably the level of glycol ether based polymer to active sizing agent will be from 4% to 35%. When added the level of divalent metal salt will be less than two times the total level of sizing agents.
- Paper sizing refers to the ability of a paper to hold out a liquid or from preventing it from penetrating into or through the paper. Generally the liquid held out is water. Sizing values are specific to the test used. Compounds that are designed to increased the hold-out of liquids are known as sizing agents. Sometimes a specific type of sizing is referred to such as an oil sizing agent. For the current work, the sizing and sizing agents are defined in terms of the ability to hold out the water based ink solution used in the Hercules Sizing Test. The test is defined below. For a discussion on sizing, see Principles of Wet End Chemistry by William E. Scott, Tappi Press 1996, Atlanta, ISBN 0-89852-286-2
- Optical density is a measure of the inverse of the amount of reflected light off a surface. Generally and for the purpose of this invention, it is a measure of light reflecting off of a black printed area on a sheet of paper.
- Optical Density (OD) equals -Iog 10 (reflectance). The test method utilized was to use commercial hand-held densitometer. It is further described below. The concept of optical density is explained in detail in an article by Allen Rushing found on the internet at www.logliqht.com/concepts&tools.htm.
- Mottle or more accurately print mottle, refers to the unevenness of a printed area. It can be blotchiness or variations in optical density. They are visible to the eye. The method used to measure the mottle will determine what value it has. The test method used is provided below. An example of print mottle is shown in Fig. 19.17 of Printing Fundamentals ed. Alex Glassman, Tappi 1985, Atlanta, ISBN 0-89852-045-2.
- Strike-through refers to the uneven penetration of ink through to the back side of a printed paper. It is not show through which is the ability to see the printed image from the back side of the sheet but rather is penetration of the ink through or almost through the sheet. The ink penetration is often uneven and the strike-through will have a speckled appearance on the back side of a large printed area. The method used to measure the mottle will determine what value it has. The test method used in the current invention is provided below.
- Paper samples for the examples below were prepared by either a laboratory method or with a pilot paper machine. The general procedures are described here. Specific details are listed with each example.
- base papers were prepared ahead of time at Western Michigan University on their pilot paper machine.
- the papers were made without any size press treatment, that is no starch, sizing agent, or other additive was applied to the surface of the formed paper.
- the pulp used to make the papers was a 75%/25% by weight mixture of hardwood and softwood bleached craft pulp as is typical of what would be used to produce commercial copy paper.
- the papers also contained precipitated calcium carbonate, cationic starch, aluminum sulfate and a retention aid. Once made and dried the papers were cut into sheets and stored. The paper was later treated at the Hercules Research Center with a laboratory bench top puddle size press.
- the size press consisted of a horizontal set of ten inch pinched rollers, one rubber coated and one metal, through which the paper was fed. A puddle of the size press treatment was held by the rollers and dams on the top side of the rollers. The rollers were held together with 14 pounds of air pressure. The paper passed through the puddle as it was pulled by the rollers, and through the rollers, to give a controlled and uniform level of treatment. The level of treatment was controlled by the concentration of the treatment chemicals in the treatment solution which was generally a dissolved starch solution. The paper was captured below the two rollers and immediately dried on a drum drier set at about 100 0 C. The paper was dried to about a 3-5% moisture level.
- the size press formulations were prepared by dissolving starch for 45 minutes at 95°C, cooling, holding the starch at 65°C. Generally the starch pH was adjusted to 7.5. To the starch was added other additives for this treatment such as salt, sizing agents, and the glycol ether based polymers used in this invention. Once the additives were in the starch solution the solution pH was readjusted to a pH of 7.5. Then the starch solution, still at 65 0 C was used to treat the paper. For each base paper used the amount of solution picked up through the rollers was determined and the additive levels set accordingly. After drying, each sample was conditioned by aging at room temperature for seven days. The samples were also conditioned for at least 12 hours prior to being tested under the conditions they would be tested.
- Paper samples were printed with a Hewlett Packard HP6122 printer using HP45 black ink cartridges. The settings for the printer were: plain paper, normal print quality, color, no color enhancement. On each sample a solid black five inch by five inch square was printed and allowed to dry before being stacked.
- Mottle and strike-through are both variations of uniformity, mottle of black print and strike-through of the white back side of paper that has been printed.
- An image analysis method was used to quantify the variations. Images were captured by a dual light scanner at a resolution of 600 dpi in bit-map format. The images were then analyzed with a mottle analysis software package from Verity IA 2004 Multifunction Version 1.4.1 designed by Roy R. Rosenberger. The software does a stochastic analysis. Mottle values can be obtained for various target sizes. A paper by Roy R. Rosenberger of Appleton, Wisconsin explains the analysis. The paper "Stochastic Frequency Distribution Analysis as Applied to Mottle Measurement" can be obtained on the VeritylA web site www.veritvia.com.
- one target size is reported. First the 600 dpi images were taken. Then each image was analyzed as a collection of squares (a target size) of 16 dots by 16 dots (a 0.67mm by 0.67mm square) across approximately a 55mm by 55mm area. Across the image, groups of four squares were combined into a larger square. Each large square was a target of 1.4mm by 1.4mm. The numbers for the analysis of the mottle was determined for the collection of 1.4 by 1.4mm squares across the selected image area. The software provided a mottle number for the 1.4 X 1.4mm targets. In the analysis, a higher value indicates more mottle. A lower value represents a more uniform image and is desirable. [0061]The same procedure was used for quantifying strike-through.
- optical density is a reflectance measurement.
- an optical densitometer from Graphics Microsystems Inc. was used. The model was a Cosar 200. Black optical densities were measured and reported. Six readings were taken for each sample and averaged. A higher optical density value represents less reflectance and thus a darker looking print.
- Example 1 Demonstration of the problem of lowering internal sizing levels when no glycol based polymer is present.
- the paper was made with 70:30 ratio of bleached craft hardwood and softwood as suitable for fine paper. 15% of a medium size precipitated calcium carbonate (Albacar 5970) was added based on the pulp solids. Likewise 0.75% cationic starch, 0.25% papermakers alum (AI2O3 * 14H20), 0.015% of an anionic polyacrylamide retention aid, and three different levels of alkyl succinic anhydride (ASA) sizing agent were added on the same basis. The ASA was added as a stable emulsion typical for papermaking. At the size press, each sample was treated with a water solution of 8% oxidized starch and 0.5% sodium chloride to give an addition of 4% starch and 0.25% sodium chloride to the final dry paper.
- a medium size precipitated calcium carbonate Albacar 5970
- ASA alkyl succinic anhydride
- HST Hercules Sizing test Example 2 Demonstration of the problem of increasing surface sizing levels with no glycol based polymer.
- Example 2 The same conditions of Example 1 were used. At the size press, Hercules imPress ® ST900 sizing agent (ST900) was added along with the starch. ST900 is an emulsion containing alkenyl ketene dimer as a sizing agent. The levels of addition on a dry basis of the dimer to the final paper were 0 and 0.05%.
- ST900 Hercules imPress ® ST900 sizing agent
- Samples were prepared in the laboratory using a bench top size press and pre-made base sheet by the process described above.
- the base sheet contained 1.25#/ton of a solid AKD sizing agent applied as an emulsion (Hercules' Hercon ® 70 sizing emulsion). It also contained 10% Albacar HO PCC filler.
- the compositions of the paper treatments applied at the size press were based on a 9% solution, in water, of a low viscosity oxidized starch (D-15F from Grain Processing Corporation). The pick-up of the base sheet of the starch solution was 54.0%.
- the final paper contained approximately (54 X 0.09)/(100 + (54 x 0.09) x100 % or 4.64% starch. Addition levels of additives were based on this pick-up. To each formulation enough NaCI was added to give a final paper content of 0.25%. Enough reactive sizing agent, non-reactive sizing agent, glycol ether polymer and MgCI 2 was added to give the desired levels of addition as listed in the following table. The reactive sizing agent used was a stable emulsion of liquid dimer based on a saturated alkyl fatty acid (AKD).
- ALD alkyl fatty acid
- the unreactive sizing agent was a styrene acidic emulsion type (SAE) consisting of a poly(styrene/butyl acrylate) emulsion (Hercules' Chromaset 800 product).
- SAE styrene acidic emulsion type
- the glycol ether polymer was a polyethylene glycol (PEG) of 1000g/mole average molecular weight. Both the MgCI2 and PEG were pre-mixed with the dimer emulsion before being added to the starch solution.
- OD optical density
- the cationic starch used was Stalok 400 from Staley
- the level of cationic starch was 0.75% of the final paper weight
- AKD Alkyl Ketene Dimer Sizing Agent
- Hercules Hercon 70 sizing agent Hercules Hercon 70 sizing agent.
- the alum level was 0.25% based on final paper weight
- the level of anionic polyacrylamide retention aid was 0.015% based on final paper weight
- the temperature was 5O 0 C
- the pH was 7.0
- the basis weight of the paper formed was 75grams per square meter of paper
- the starch used was an oxidized corn starch called D15F from Grain Processing
- the starch was cooked for 40 minutes at 95 0 C
- the starch solution concentration was 7.5%
- the temperature of the size press solution was 65 0 C
- the liquid dimer sizing agent used was Hercules imPress ST900 sizing agent.
- the level of PPG added is listed below in the table of results.
- the PPG had an average molecular weight of 700g/mole.
- PPG was only slightly effective at lowering mottle. It was effective at reducing strike-through. However, at 0.01% and 0.02% in the paper it reduced the level of sizing.
- Example 5 Addition of polyethyleneglycol diglycidyl ether and polypropylene glycol diglycidyl ether.
- Paper was made with two levels of ASA 1 0.036 and 0.041 %. A 75/25 hard wood / soft wood mixture was used with 16% PCC filler, 0.75% cationic starch, 0.5% paper makers alum, and 0.015% anionic retention aid. The paper was then treated on the paper machine at the size press.
- PEGDGE Polyethyleneglycol diglycidyl ether
- PPGDGE polypropylene glycol diglycidyl ether
- the sizing agent was added as an emulsion to the starch solution.
- the glycol ether polymers were also added to the starch solution.
- the level of starch added to the paper was 4%. As is typical in fine paper manufacturing 0.25% NaCI was added to the paper by also adding NaCI to the size press starch solution.
- the levels of dimer and glycol ether polymers in the final papers are noted below.
- Both PEGDGE and PPGDGE reduced mottle and strike-through. The benefit depends on the amount of mottle and strike-through of the paper without them. The samples with more internal ASA had less mottle and strike-through and therefore the amount of improvement was less. PPGDGE was more effective than PEGDGE. However, when 0.02% PPGDGE was used the sizing was reduced. At lower levels, it may also have a negative effect on sizing when a low level of sizing agent is used. As an added benefit, both epoxides enhanced optical density. PPGDGE was again more effective than PEGDGE.
- PEGBCME reduced mottle and strike-through.
- Example 7 Use of a pre-mixture.
- ImPress ® ST900 sizing emulsion of Hercules was used as the sizing agent on its own and in pre-mixtures with PPG.
- the PPG was predispersed in water, 10% PPG and 90% water, with a sonicator.
- the PPG dispersion was mixed with the dimer emulsion.
- the ratio of dimer to PPG in the pre-mixtures was 10 to 1 and 5 to 1.
- PPG was premixed with a dimer emulsion and the mottle and strike-through performance of the treated paper was improved. With the lowest level of PPG, 0.0035%, there was little or no improvement of mottle but strikethrough improved. At a higher level the mottle and strikethrough performance of the paper improved. As noted in a previous example, the addition of too much PPG will reduce the level of sizing.
Landscapes
- Paper (AREA)
- Ink Jet Recording Methods And Recording Media Thereof (AREA)
Abstract
In this invention a composition is applied to the surface of paper comprising a glycol ether based polymer that provides enhanced ink-jet print quality. The advantage of using the composition is that it improves ink-jet printing on the paper without significant loss of water hold-out. More specifically, the paper is uncoated and has been treated on the surface with the following materials and dried to the point of usefulness. These materials are: 1) one or more compounds that increase water hold-out. These are known as sizing agents, 2) starch, 3) A glycol ether based polymer.
Description
SURFACE SIZING WITH SIZING AGENTS AND GLYCOL ETHERS
FIELD OF THE INVENTION
[0001] This invention describes the improvement of uncoated fine paper by treatment of the surface of the paper with polymers based on glycol ethers used in combination with starch and paper sizing agents. The invention results in paper with enhanced ink-jet print quality. The enhanced qualities include less mottle on the printed images, less strike-through to the back side of the paper when printed, and enhanced optical density of printed images.
BACKGROUND OF THE INVENTION
[0002] Glycol ether based polymers including those end capped with epoxy groups have been added to paper for many years. As far back as at least 1972, US Patent 3873354A (1972) describes the addition of humectants along with salts, such as sodium chloride and calcium chloride, to paper to be used for electroreprographic (or electrostatic) printing, that is copy paper. The humectants named included "polyethylene glycols and polymers . . .". The humectant must be water soluble or water miscible. The size press is mentioned as a means of application and "another additive which will typically be added to the size press solution is a conventional binder such as a starch, gum, casein, polyvinyl alcohol or acetate, animal glue, etc.". The goal was to reduce the static build-up on the paper. The level of addition of salts was recited but not the level of humectant. However, in an example, about 0.05% of the paper weight of polyethylene glycol was added. This is greater than the level use by applicant herein. In addition the use of adducts of polyethylene glycol are not mentioned nor is the use of polypropylene glycol or adducts of polypropylene glycol mentioned. The latter two are not water soluble. There is no mention of the use of sizing agents in the paper.
[0003] US Patent 4210412 describes the use of "polyhydric alcohol" in cellulose based textiles. The additive is used to swell the cellulose so it will accept dyes during a transfer printing operation. What is called polyhydric alcohol includes "polyalkylene glycols such as polyethylene glycol of average molecular weight of 200 to 4000, polypropylene glycol of average molecular weight of 400 to 5000, polyethylene glycol / polypropylene glycol block copolymers of average molecular weight of 400 to 5000 . . . mono- and diethers . . . and diesters . . ." The addition levels were not given; but, the addition levels used in the examples were higher than the current invention. For example, the level used in Example 2 had polyethylene glycol added at 7.5% of the substrate. This is far greater than used in the
current invention
[0004] US Patent application 20050104947 A1 describes treatments for paper to reduce the amount of cockle and curl and also to provide an ink-jet image recording method. The treated paper is defined by its level of water absorption and a ratio of wet to dry tensile strength. The cockle and curl tendencies are lowered by decreasing the hydrogen bonds between fibers in the paper. The desired paper is obtained by two methods. One method deals with the treatment of the pulp fibers before the sheet is formed such that the treatment compounds are located between fibers. Among the compounds that can be used are polyethylene glycol polypropylene glycol block copolymers, polyoxyethylene fatty acid esters, and other nonionic surfactant type materials. Also materials such as monoglycidyl ethers can be used. A second method is to add to the paper a heat-curable material or a thermoplastic material. Again the material must be located between fibers and in this case adhere fibers together. Epoxy resins are given as one class of suitable additives. Thus, there is no surface treatment of a paper sheet. The application expands on what can be done by saying that the sheet can be treated by surface sizing to apply a nonionic surfactant. Furthermore, the treatment is also said to preferably include polyvalent metal salts such as calcium chloride or a cationic polymer such as cationic starch. Either material can be added at levels that provide 0.1 to 2 g/m2 of material to the sheet. The sheet weights of interest are 60 to 128 g/m2. Therefore, the range of percentage addition is from 0.08 to 3.3%.
[0005] The addition of polyethylene glycol and polypropylene glycol to the wet end of a paper machine is described in US Patent 5240562 (issued in 1993 to Procter and Gamble). The patent points out that polyhyroxy compounds like polyethylene glycols and polypropylene glycols having weight average molecular weights from about 200 to 4000 can be used with quaternary ammonium compounds to give tissue paper a good combination of softness and absorbency. This patent only covers the wet-end addition of the polyhydroxy compounds before the paper is dried. There is no mention of the impact on ink-jet printing. The quaternary ammonium compound and the polyhydroxy compound were premixed.
[0006] There are numerous patents concerning coated paper where a reactive polymer hardener is added to the ink absorptive layer. A wide variety of materials to crosslink the absorptive layer are known and they include diglycidyl ethers of glycol ether based polymers, such as polyethylene glycol digylcidyl ether (PEGDGE). In US Patent 20050202188A1 PEGDGE is used in a ink-jet absorptive coating layer to crosslink polyvinyl
alcohol.
[0007] However, coated papers are very different from the paper of the current invention. A coated paper has one or more relatively thick layers of treatment on one or both sides of a preformed paper. Such papers find use in high-end printing application including high-end ink-jet printing applications such as photographic paper. For ink-jet applications, coated grades have an absorbent layer composed of either a polymer that absorbs a high volume of liquid ink or a high level of filler that can adsorb a high volume of liquid ink. There are two uses of glycol ether based polymers used in such coatings. First they may be added as an absorbent material and secondly, diglycidyl ethers of glycol based polymers may be added to improve surface strength. European Patent 0634284 discusses both such uses. The instant invention does not cover coated papers.
[0008] There are also other uses for polyglycol ethers in paper coatings. US Patent 5746814 describes the addition of the following compounds as desizing agents in a more complex composition for coating of paper: poly(alkylene glycol); poly(propylene oxide) - poly(ethylene oxide) copolymers; fatty ester modified compounds of glycerol and poly(ethylene glycol); and poly(oxyalkyene)modified compounds of sorbitan esters, fatty amines, alkanol amides, castor oil, fatty acid, fatty alcohol. The overall composition contains solvent, binder, desizing agent, anticurl agent, defoamer, biocide, antistatic agent, lightfastness promoting agent, and a filler. All of the coating applications fall into a different class of paper from the current invention and the coating compositions are significantly different as noted above.
[0009] US application, 20050013949 A1 concerns a coated paper. However, its description of the base paper on which an ink absorbing layer would be applied is described as. " Base paper employed for the paper support of the present invention is made employing wood pulp as a main raw material . . . It is possible to incorporate into base paper sizing agents such as . . . strengthening agents such as starch . . . moisture retention agents such as polyethylene glycol, dispersing agents and softening agents . . ."
[001O] US Patent 6203899B1 describes a printing medium comprising a liquid absorbent base material, an ink-receiving layer provided on the base material, which comprises a pigment, a binder and a cationic substance, and a surface layer provided on the ink receiving layer. Here again the concern is a coated paper. It is described as fibrous pulp
and a filler impregnated with a crosslinking substance. The crosslinking substance is crosslinked to form nonswelling paper. The crosslinking substance can be an epoxy. PPGDGE is specifically described. Along with the crosslinking substance can be a polymer having a reactive group. Starch is one example of the polymer. The amount of starch is in the range that can be applied by a size press. The ratio of crosslinking substance, starch, to crosslinking agent, PPGDGE, is from 100:1 to 1 :1 by weight. The range is different from the current invention where our ratio under preferred conditions is about 400 to 1 or less. A polyvalent metal salt is mentioned as an option for crosslinking certain materials. The divalent metal ions that are optional additives of the invention of this disclosure do not crosslink starch.
[0011] US 6706320B2 describes modifying a surface containing a polymeric material. In one claim, it is said the substrate can be cellulosic and in another claim it is said the modifying agent can be a crosslinker. The crosslinker can be an epoxy compound such as diglycidyl ethers of polyols. However, the process of the patent requires the presence of a polyamine as a surface modifying agent and that the polyamine vaporize in the process. The epoxy compound reacts with the amine.
[0012] US Patent 5746814A includes polyethyleneglycol diglycidyl ether as one of the compounds that can be added to prevent paper from curling. An elaborate composition for treating paper is described with a wide range of levels of each component. There are nine components in the composition and they can include water, starch as a binder, and PEGDGE as an anticurl or a desizing agent. Taking the maximum of starch in the composition and the minimum of PEGDGE one gets a ratio of 150:1. This is different from that of the current invention. Furthermore the current invention does not require many of the other components listed such as antistatic agent or desizing agent or lightfastness promoting agent. The composition is for treating paper that has already been imaged.
[0013] Hercules Incorporated has a patent (US6207258 B1) on the use of divalent metal salts with sizing agents. It also had a patent (US6051107A) on mixtures of reactive and nonreactive sizing agents as pre-mixes and in paper treatment compositions. The later patent was not maintained.
SUMMARY OF THE INVENTION
[0014] In general one embodiment of the invention involves a paper composition having applied to its surface a composition comprising a glycol ether based polymer that provides enhanced ink-jet print quality. The advantage of the paper composition is improved ink-jet printing without significant loss of water hold-out.
[0015] More specifically, this first embodiment of the invention is an uncoated paper (based on wood pulp or other cellulose product based) that has been treated on the surface with at least the following materials and dried to the point of usefulness. These materials are:
1) one or more compounds that increase water hold-out. These are known as sizing agents,
2)starch,
3) a glycol ether based polymer.
[0016] The sizing agent will be present in an amount of 0.01% to 0.3% based on dry weight of paper.
[0017] The starch will be present in an amount of 1 to 8% based on dry weight of paper.
[0018] The glycol ether based polymer will be present in an amount of less than 0.025% based on dry weight of paper.
[0019] One preferred composition is paper surface-treated with starch, sizing material, a glycol ether based polymer and a divalent metal salt. The sizing materials and glycol ether based polymers are defined below along with the addition levels.
[0020] The paper of the invention has improved ink-jet print qualities of less mottle of printed areas, less strike-through of ink, and possibly increased optical density over paper not treated with all the components of the invention.
[0021] The sizing agents, as defined below, provide water hold-out. They may also
improve the sharpness and optical density of ink-jet printed images. The addition of sizing agents to paper is common. Likewise starch is a standard additive to paper and thus, the invention in one embodiment is the addition of sizing agent and starch with glycol ether based polymers, such as polypropylene glycol diglycidyl ether. Another option is that the paper as described above also contains a divalent metal salt as described in Hercules patent US6207258 B1 , incorporated by reference.
[0022] Any uncoated paper can be used, but a preferred paper is uncoated "fine" paper for printing and writing applications. Such paper typically contains bleached wood pulp, precipitated calcium carbonate, and starch along with other materials deemed beneficial for preparing the paper or enhancing paper properties or reducing the cost of the paper. A typical uncoated fine paper has a, basis weight of 70 to 80 grams per square meter.
[0023] For the present invention, the three or four components of the invention, listed above, may be added either separately or together to the surface of the paper. Fine paper for printing and writing is usually treated before it leaves the paper machine on which it was m maordloe.
[0024] A clear distinction should be made between surface treatments and coatings. Both are applied to paper that is already formed. Both can be used to enhance printing properties. A treatment is meant to modify the surface of the paper but the general structure remains mostly unchanged. A coating creates a new surface. More material is applied with a coating than a treatment. Coatings are usually made up of a large percentage of inorganic filler or pigment such as silica or clay or calcium carbonate. A coating covers the entire surface of the paper substrate blocking the porous nature of the paper and leveling the surface. With a "treatment", the composition of the base sheet still has a large influence on final properties. For example, more wet-end sizing leads to a higher surface tension in the final paper versus a low level of sizing. With a "coating", the internal chemistry may affect the application of the coating but does not have a direct effect on the final properties of the paper. For example, internal sizing is covered up by a coating and will not directly change the surface tension of the final coating unless it migrates through the coating.
[0025] The method of applying the materials used in this invention is not crucial as long as the application method for the materials is controllable and leads to the desired results. The most preferred method of addition is for the starch to be dissolved in water by
cooking and for the other components to be added to the starch solution and then for the resulting composition (the treatment composition) to be applied to the paper with a paper machine size press.
[0026] A second embodiment of the invention is the composition used to treat the paper. It is defined as a starch based solution containing at least one paper sizing agent and at least one glycol ether based polymer and optionally a soluble divalent metal salt such as calcium chloride and optionally other additives common to the treatment of paper. The treatment composition allows for all of the additives to be applied simultaneously to the paper. This is an aqueous composition that contains : sizing agent in an amount of 0.03-1%, starch present in an amount of 1.5-12%, glycol present in an amount of less than 0.25%.
[0027] The treatment composition consists predominantly of water in which a binder is dissolved. The binder is the predominant component aside from the water. The binder for this invention is predominantly starch. Other binders such a polyvinyl alcohol can be used in combination with the starch. With the binder, other additives are typically added such as sizing agents that hold out water and improve printing properties; optical brightening agents; dyes; and antistatic agents. Sometimes materials such as inorganic fillers are added. When fillers are added they do not constitute more than about 40% of the composition on a dry weight percent basis of the non-water components.
[0028] These compositions can also contain other common additives such as sodium chloride and defoamer. The advantage offered by the second embodiment of the invention (the treatment composition) is the simultaneous treatment of the paper with a composition that leads to the improvements listed above in the first embodiment of the invention. The composition must be such that it is uniform and it can be applied to the paper in a uniform manner.
[0029] Preferably, the glycol ether based polymers will be added to the treatment composition so that they are applied to the paper with the paper machine at the same time as the starch and sizing agent.
A third aspect of the current invention is a pre-mixture of the sizing agents and glycol ether
based polymers and optionally a divalent metal salt. The pre-mixture is then added to the starch based solution just described. The pre-mixtures may be water based solutions or emulsions or dispersions. The glycol ether polymer will be 3-50% based on the amount of sizing agent.
[0030] A third embodiment of the invention comprises pre-mixtures of some of the additives that go into the surface treatment composition thus offering the convenience of adding several materials simultaneously to the mixture used to treat the paper. The pre- mixtures that are of interest for this disclosure will contain the following materials:
A water-based composition (i.e. a solution, latex, and or dispersion) of one or more paper sizing agents, and one or more glycol ether based polymers.
DETAILED DESCRIPTION OF THE INVENTION
[0031] The glycol ether based polymers used in this invention include polymers with repeat units of ethylene glycol or propylene glycol or combinations of them. There may be other functional groups along the backbone provided they do not account for more than approximately ten percent by weight of the final polymer structure. There may be branching along the backbone. The polymers can be end-capped with hydroxyl groups, ethers, gylcidyl ethers, esters, carboxylic acid groups, and other functionality so long as the end groups do not account for more than 25% of the weight of the average polymer molecule.
[0032] The polymer compositions may have one, two, or more types of functional end groups other than hydroxyl groups. There may also be one of more types of functional groups within the polymer backbone or grafted on to it.
[0033] Use of glycol ether based surfactants that fit the above criteria are part of this invention provided they meet the remaining conditions given below. Glycidyl ether end- capped polymers such as polyethyleneglycol digycidyl ether and polypropyleneglycol digycidyl ether are useful also.
[0034] The average molecular weight of the glycol ether based polymers of this invention shall be from approximately 350 g/mole to approximately 200,000. The polymer must be soluble or readily dispersible in water. The preferable average molecular weight is
between 380 and 20,000 and most preferably between 500 and 2000 g/mole.
[0035] The addition level of the glycol ether based polymers of the invention is defined by the impact on sizing as defined in this invention and by concentration. The glycol ether based polymers of the invention should not cause greater than a 25% reduction in the level of sizing when utilized under at least some portion of the conditions of this invention. For example, polypropylene glycol (PPG) may be used at a low level but at a high level it interferes with sizing. The level of addition of the glycol ether polymers to the aqueous composition for surface treating the paper shall be less than 0.25%. The level of addition in a premix with sizing agent should be less than 50% of the active sizing agent by weight.
[0036] The paper substrate which is treated in the current invention can contain wood based pulp from ground wood to chemically bleached wood or a non-wood based pulp or a combination of pulps. The paper can also contain usual paper making inorganic fillers such as calcium carbonate or clay and may also contain organic fillers. The paper can also contain strength additives, retention additives, internal sizing agents and other common paper additives such as alum. The preferred grade of paper can be any type suitable for ink- jet printing which can include fine paper to white-top liner board. The basis weight of the paper can be anywhere from 40g/m2 to 350g/m2. The preferred paper is any type of printing and writing paper including roll fed to sheet fed papers. The most preferred is uncoated fine paper with a basis weight between 60 and 100 g/m2.
[0037] The starches that are suitable as part of the paper treatment can be of any kind provided they can be dissolved in water and applied to the paper. The starches can be from a variety of sources including corn, potato, rice, cassava root, and others used in paper making. Unmodified and modified starches can be used. Modified starches include oxidized, ethylated, cationic, anionic, amphoteric, hydrophobically modified, and others used in paper making. The preferred starches have reduced viscosities such that solutions of greater than 6% solids can be used on a paper machine size press. The most preferred are those with reduced viscosity that are also are oxidized, ethylated, cationic, or amphoteric. The range of starch treatment based on the dry weight of the final paper is 1 % to 8.0%. More preferably from 2% to 7% and most preferably from 3% to 6%. The range of starch concentration in the treatment composition can be from 1.5% to 12% provided the viscosity allows for application to the paper substrate. More preferably the concentration will be between 3% and 11% and most preferably between 5% and 10%.
[0038] The surface treatment sizing agents suitable for the current invention include those that are termed reactive such as alkyl ketene dimers, alkenyl ketene dinners, and alkyl succinic anhydrides. Sizing agents termed unreactive are also suitable and may be mixed or used with the reactive sizing agents as described in a previous Hercules' patent (US6051107A). Unreactive sizing agents may be used on their own. Unreactive sizing agents include soluble polymers such as styrene - maleic anhydride based polymers, styrene - esterified maleic anhydride based polymers, styrene acrylic acid and styrene methacrylic acid based polymers and insoluble polymers such as polymer latexes commonly used in paper making such as poly(styrene/acrylic) resins, acrylonitrile/acylic resins and urethane polymers and insoluble polymer dispersions such as of ethylene/acrylic acid polymers.
[0039] The level of surface treatment sizing agent in the final dry paper will range from 0.01 % to 0.3% on a dry weight basis. Preferably the level is 0.02 to 0.2% and most preferably it is 0.03 to 0.1%.
[0040] All of the above levels are based on both sides of a base paper being treated. However, the invention is applicable to treatment of one or both sides. When only one side is being treated all of the above levels relating to the paper will be one half of the values listed.
[0041] The final paper may contain other additives that were included in the formation of the paper or were applied along with the surface treatment or separately from the surface treatment. The additives applicable are those which are usually utilized in paper. They include but are not limited to the following: inorganic and organic fillers such as calcium carbonate or hollow sphere pigments; optical brightening agents which are also known as fluorescent whitening aids, pigments; dyes, strength additives such as polyamidoamines, promoter resins such as polydimethyldiallylammonium chloride; adhesion promoting polymers such as styrene acrylic latexes and styrene maleic anhydride based polymers; and inorganic salts such as sodium chloride and calcium chloride. When the final paper contains a divalent metal salt it should be less than 0.25% of the paper weight.
[0042] The methods of applying the paper treatment composition of the current invention are not limited provided uniform controlled application is obtained. The treatment may be made to paper formed on a paper machine and then only partially dried or it can be
made on a paper machine to dried paper or the treatment can be done separate from the paper machine to paper that was formed, dried, and moved. The preferred process is for paper to be formed with a paper machine, partially dried, and treated using a paper machine size press, and then for the paper to be dried again. The paper may be further modified by calendering.
[0043] The treatment composition, the second embodiment of the invention described above, has the same components just described. The starch solution in water must be of dissolved starch and the viscosity must be such that the solution, containing other components, can be applied to the paper. The viscosity and not the solids of the starch solution is the most critical factor; however, some starch materials can only be dissolved at very low concentrations before they become too thick to use. A paper maker will select a starch based on the properties it imparts to the paper as well as its ease of use and the ability to apply the desired level with the equipment being used. A preferred level of starch in the treatment composition is 3 to 12% and a most preferred level is 5 to 10%. Other materials such as polyvinyl alcohol may be used with the starch, if desired. The additional binder level will be less than the starch level.
[0044] Suitable sizing agents are described above. They are added to the starch solution. The level of sizing agent in the composition will depend on two factors: the level of the starch composition applied to the paper and the desired level of sizing treatment. Typically the level of starch addition is selected along with the starch solution concentration and then the level of sizing agent in the starch solution is adjusted to get the desired level of treatment. The level of sizing agent in the starch composition will be between 0.03 and 1% of the paper treatment composition based on the active component of the sizing agent.
[0045] The level of glycol ether based polymer in the treatment composition will be determined in the same manner as described for the sizing agent level. The level of glycol ether based polymer will be determined by the amount of starch solution applied and the desired level of the polymer to be applied. The level of glycol ether polymer in the paper treatment composition will be less than 0.25%.
[0046] The treatment composition may contain other materials as noted above for the paper. When the treatment composition contains a soluble divalent metal salt such as calcium chloride and magnesium chloride the level of the salt will be less than 20% of the
starch level.
[0047] The sizing agents of interest were described above. One or more sizing agents can be combined. The form of the sizing agent will be as a solution emulsion or dispersion in water with suitable additives used to obtain desired stability. One or more glycol ether based polymers can be combined with the sizing agents. The sizing agent formulation may also contain a water soluble divalent metal salt such as calcium chloride or magnesium chloride.
[0048] The amount of glycol ether based polymer versus sizing agents can be from 3% to 50% polymer to active sizing agent. More preferably the level of glycol ether based polymer to active sizing agent will be from 4% to 35%. When added the level of divalent metal salt will be less than two times the total level of sizing agents.
DEFINITIONS
SIZING
[0049] Paper sizing refers to the ability of a paper to hold out a liquid or from preventing it from penetrating into or through the paper. Generally the liquid held out is water. Sizing values are specific to the test used. Compounds that are designed to increased the hold-out of liquids are known as sizing agents. Sometimes a specific type of sizing is referred to such as an oil sizing agent. For the current work, the sizing and sizing agents are defined in terms of the ability to hold out the water based ink solution used in the Hercules Sizing Test. The test is defined below. For a discussion on sizing, see Principles of Wet End Chemistry by William E. Scott, Tappi Press 1996, Atlanta, ISBN 0-89852-286-2
OPTICAL DENSITY
[0050] Optical density is a measure of the inverse of the amount of reflected light off a surface. Generally and for the purpose of this invention, it is a measure of light reflecting off of a black printed area on a sheet of paper. Optical Density (OD) equals -Iog10(reflectance). The test method utilized was to use commercial hand-held densitometer. It is further described below. The concept of optical density is explained in detail in an article by Allen Rushing found on the internet at www.logliqht.com/concepts&tools.htm.
MOTTLE
[0051] Mottle, or more accurately print mottle, refers to the unevenness of a printed area. It can be blotchiness or variations in optical density. They are visible to the eye. The method used to measure the mottle will determine what value it has. The test method used is provided below. An example of print mottle is shown in Fig. 19.17 of Printing Fundamentals ed. Alex Glassman, Tappi 1985, Atlanta, ISBN 0-89852-045-2.
STRIKETHROUGH
[0052] Strike-through refers to the uneven penetration of ink through to the back side of a printed paper. It is not show through which is the ability to see the printed image from the back side of the sheet but rather is penetration of the ink through or almost through the sheet. The ink penetration is often uneven and the strike-through will have a speckled appearance on the back side of a large printed area. The method used to measure the mottle will determine what value it has. The test method used in the current invention is provided below.
TEST METHODS
PREPARATION OF SAMPLES
[0053] Paper samples for the examples below were prepared by either a laboratory method or with a pilot paper machine. The general procedures are described here. Specific details are listed with each example.
[0054] For the laboratory test, base papers were prepared ahead of time at Western Michigan University on their pilot paper machine. The papers were made without any size press treatment, that is no starch, sizing agent, or other additive was applied to the surface of the formed paper. The pulp used to make the papers was a 75%/25% by weight mixture of hardwood and softwood bleached craft pulp as is typical of what would be used to produce commercial copy paper. The papers also contained precipitated calcium carbonate, cationic starch, aluminum sulfate and a retention aid. Once made and dried the papers were cut into sheets and stored. The paper was later treated at the Hercules Research Center with a laboratory bench top puddle size press. The size press consisted of a horizontal set of ten inch pinched rollers, one rubber coated and one metal, through which the paper was fed. A puddle of the size press treatment was held by the rollers and dams on the top side of the rollers. The rollers were held together with 14 pounds of air pressure. The paper passed through the puddle as it was pulled by the rollers, and through the rollers, to give a controlled
and uniform level of treatment. The level of treatment was controlled by the concentration of the treatment chemicals in the treatment solution which was generally a dissolved starch solution. The paper was captured below the two rollers and immediately dried on a drum drier set at about 1000C. The paper was dried to about a 3-5% moisture level.
[0055] The size press formulations were prepared by dissolving starch for 45 minutes at 95°C, cooling, holding the starch at 65°C. Generally the starch pH was adjusted to 7.5. To the starch was added other additives for this treatment such as salt, sizing agents, and the glycol ether based polymers used in this invention. Once the additives were in the starch solution the solution pH was readjusted to a pH of 7.5. Then the starch solution, still at 650C was used to treat the paper. For each base paper used the amount of solution picked up through the rollers was determined and the additive levels set accordingly. After drying, each sample was conditioned by aging at room temperature for seven days. The samples were also conditioned for at least 12 hours prior to being tested under the conditions they would be tested.
[0056] Other samples used in the examples below were prepared on Hercules' pilot paper machine. The paper was made with conditions similar to those described above for Western Michigan University. Again the goal was to make standard copy paper. On the Hercules paper machine the first drier section was followed by a size press and then another drier section and then a set of calendering rolls. The treatments of the invention were applied to the paper at the size press. A puddle size press mode was used. In the puddle mode, the liquid treatment solution was held along the rolls as a puddle through which the paper passed. The pilot machine process imitated the process of a large paper machine. As with laboratory studies a solution of cooked (dissolved) starch was used as the carrier for treatment chemicals.
Sizing Test
[0057] Descriptions of various sizing tests can be found in The Handbook of Pulping and Papermakinq by Christopher J. Biermann Acedemic Press 1996, San Diego, ISBN 0-12- 097362-6. Properties of Paper: An Introduction ed. William E. Scott and James C. Abbott Tappi Press 1995, Atlanta, ISBN 0-89852-062-2. The Hercules Sizing Test (HST) was used for the current work. It is described by Tappi Method T530. For the test results presented in this disclosure a solution containing 1% napthalene green dye and 1% formic acid was used as the penetrant. The end point of the test was set at 80% reflectance.
Ink-Jet Printing Conditions
[0058] Paper samples were printed with a Hewlett Packard HP6122 printer using HP45 black ink cartridges. The settings for the printer were: plain paper, normal print quality, color, no color enhancement. On each sample a solid black five inch by five inch square was printed and allowed to dry before being stacked.
Image Analysis for Mottle and Strike-Through
[0059] Mottle and strike-through are both variations of uniformity, mottle of black print and strike-through of the white back side of paper that has been printed. An image analysis method was used to quantify the variations. Images were captured by a dual light scanner at a resolution of 600 dpi in bit-map format. The images were then analyzed with a mottle analysis software package from Verity IA 2004 Multifunction Version 1.4.1 designed by Roy R. Rosenberger. The software does a stochastic analysis. Mottle values can be obtained for various target sizes. A paper by Roy R. Rosenberger of Appleton, Wisconsin explains the analysis. The paper "Stochastic Frequency Distribution Analysis as Applied to Mottle Measurement" can be obtained on the VeritylA web site www.veritvia.com. For the results presented in this disclosure black printed samples were used and the luminance values of the printed areas were evaluated on a grey scale. In the analysis, three values are obtained: 1) the standard deviation of the standard deviation of luminance values of each target on a grey scale; 2) the mean of the standard deviation of the luminance values; and 3) the standard deviation of the means of the standard deviation of the luminance values. These values are multiplied together to obtain what is called a Mottle Number.
[0060] For the examples presented in this disclosure, one target size is reported. First the 600 dpi images were taken. Then each image was analyzed as a collection of squares (a target size) of 16 dots by 16 dots (a 0.67mm by 0.67mm square) across approximately a 55mm by 55mm area. Across the image, groups of four squares were combined into a larger square. Each large square was a target of 1.4mm by 1.4mm. The numbers for the analysis of the mottle was determined for the collection of 1.4 by 1.4mm squares across the selected image area. The software provided a mottle number for the 1.4 X 1.4mm targets. In the analysis, a higher value indicates more mottle. A lower value represents a more uniform image and is desirable.
[0061]The same procedure was used for quantifying strike-through.
Measuring Optical Density
[0062] As noted above, optical density is a reflectance measurement. For the values of the current disclosure, an optical densitometer from Graphics Microsystems Inc. was used. The model was a Cosar 200. Black optical densities were measured and reported. Six readings were taken for each sample and averaged. A higher optical density value represents less reflectance and thus a darker looking print.
[0063] In all of the above tests, it is not so much the absolute values that are of importance but rather the relative values versus control samples that were included in all tests. The control samples are described in each example.
EXAMPLES
Example 1 Demonstration of the problem of lowering internal sizing levels when no glycol based polymer is present.
[0064] Using the pilot paper machine process described earlier and the conditions listed here three different paper samples were prepared with different levels of internal sizing and only starch and sodium chloride applied at the size press. The sizing (liquid hold-out property) of the final paper was determined by the Hercules Sizing Test described above. The mottle and strike-through were determined on ink-jet printed black squares as described earlier.
[0065] The paper was made with 70:30 ratio of bleached craft hardwood and softwood as suitable for fine paper. 15% of a medium size precipitated calcium carbonate (Albacar 5970) was added based on the pulp solids. Likewise 0.75% cationic starch, 0.25% papermakers alum (AI2O3*14H20), 0.015% of an anionic polyacrylamide retention aid, and three different levels of alkyl succinic anhydride (ASA) sizing agent were added on the same basis. The ASA was added as a stable emulsion typical for papermaking. At the size press, each sample was treated with a water solution of 8% oxidized starch and 0.5% sodium chloride to give an addition of 4% starch and 0.25% sodium chloride to the final dry paper.
[0066] The following table lists the results. Less ASA sizing agent resulted in less sizing and more mottle and strike-through when printed.
Sample ASA level HST(sec) Mottle Strike-Through
1. 0.036% 3 5.84 12.0
2. 0.046% 69 5.15 11.2
3. 0.060% 131 2.68 2.61
HST= Hercules Sizing test
Example 2 Demonstration of the problem of increasing surface sizing levels with no glycol based polymer.
[0067] The same conditions of Example 1 were used. At the size press, Hercules imPress® ST900 sizing agent (ST900) was added along with the starch. ST900 is an emulsion containing alkenyl ketene dimer as a sizing agent. The levels of addition on a dry basis of the dimer to the final paper were 0 and 0.05%.
[0068] The results for sizing mottle and strike-through are listed in the following table. Adding some surface sizing increased the sizing but the mottle and strike-through were worse.
Sample dimer level HST(sec) Mottle Strike-Through
1. 0 3 5.84 12.0
2. 0.050 189 27.0 18.3
Example 3 Addition of premixed polyethyleneglycol and magnesium chloride
[0069] Samples were prepared in the laboratory using a bench top size press and pre-made base sheet by the process described above. The base sheet contained 1.25#/ton of a solid AKD sizing agent applied as an emulsion (Hercules' Hercon® 70 sizing emulsion). It also contained 10% Albacar HO PCC filler. The compositions of the paper treatments applied at the size press were based on a 9% solution, in water, of a low viscosity oxidized starch (D-15F from Grain Processing Corporation). The pick-up of the base sheet of the starch solution was 54.0%. Therefore, the final paper contained approximately (54 X 0.09)/(100 + (54 x 0.09) x100 % or 4.64% starch. Addition levels of additives were based on this pick-up. To each formulation enough NaCI was added to give a final paper content of 0.25%. Enough reactive sizing agent, non-reactive sizing agent, glycol ether polymer and MgCI2 was added to give the desired levels of addition as listed in the following table. The reactive sizing agent used was a stable emulsion of liquid dimer based on a saturated alkyl fatty acid (AKD). The unreactive sizing agent was a styrene acidic emulsion type (SAE) consisting of a poly(styrene/butyl acrylate) emulsion (Hercules' Chromaset 800 product). The glycol ether polymer was a polyethylene glycol (PEG) of 1000g/mole average molecular weight. Both the MgCI2 and PEG were pre-mixed with the dimer emulsion before being added to the starch solution. The results for the final paper sizing, mottle, strike-through and optical density (OD) are also listed in the table.
[0070] Values listed for materials are percent of final paper weight. The HST values are in seconds.
Dimer SAE PEG MgCI 2 HST Mottle St.Thr. OD
A. 0.035 0.018 0 0 496 16.2 8.29 1.23
B. ' 0.045 0.023 0 0 515 18.0 2.78 1.32
C. 0.035 0.018 0.007 0 449 10.2 2.24 1.37
D 0.045 0.023 0.009 0 477 2.1 0.60 1.42
E 0.035 0.018 0 0.053 477 22.9 4.58 1.29
F. 0.045 0.023 0 0.068 513 11.0 2.04 1.45
G 0.035 0.018 0.007 0.053 378 23.0 4.31 1.32
H 0.045 0.023 0.009 0.068 431 0.7 0.42 1.47
[0071] The addition of PEG improved mottle, strike-through, and optical density. The
sizing was not compromized. Addition of MgCI2 lowered sizing a little but also improved mottle, strike-through, and optical density. Addition of both materials had a significant effect on sizing and at the lower level did not improve mottle. However, at the higher level mottle, strike-through, and optical density improved. The benefits of MgCI2 were known from previous work but the benefit obtained from PEG was surprising. Surprisingly, the benefits of divalent metals salts and PEG were additive.
Example 4 Addition of polypropylene glycol
[0072] Using the pilot paper machine described earlier with wet-end conditions consisting of 75/25 hard wood/ soft wood, 16% PCC, 0.07% dimer from an AKD emulsion, alum, cationic starch, and anionic polyacrylamide retention aid the effect of the additions of starch with NaCI, liquid dimer emulsion and polypropyleneglycol (PPG) were tested. The level of starch, NaCI, and dimer in the final paper samples were constant and were 4%, 0.25%, and 0.035%, respectively.
[0073] The wet-end conditions were as follows:
The cationic starch used was Stalok 400 from Staley
The level of cationic starch was 0.75% of the final paper weight
AKD stands for Alkyl Ketene Dimer Sizing Agent. The commercial product used was
Hercules Hercon 70 sizing agent.
The alum level was 0.25% based on final paper weight
The level of anionic polyacrylamide retention aid was 0.015% based on final paper weight
The temperature was 5O0C
The pH was 7.0
The basis weight of the paper formed was 75grams per square meter of paper
[0074] The size press conditions were as follows:
The starch used was an oxidized corn starch called D15F from Grain Processing
Corporation
The starch was cooked for 40 minutes at 950C
The starch solution concentration was 7.5%
The temperature of the size press solution was 650C
The liquid dimer sizing agent used was Hercules imPress ST900 sizing agent.
[0075] The level of PPG added is listed below in the table of results. The PPG had an average molecular weight of 700g/mole.
Sample PPG(%) HST(sec) Mottle Str-Thr
A. 0 268 16.4 51.6
B 0.01 % 229 14.6 37.4
C 0.02% 70 12.0 17.2
[0076] PPG was only slightly effective at lowering mottle. It was effective at reducing strike-through. However, at 0.01% and 0.02% in the paper it reduced the level of sizing.
Example 5 Addition of polyethyleneglycol diglycidyl ether and polypropylene glycol diglycidyl ether.
[0077] The pilot paper machine described above was used to test the effectiveness of PEG and PPG with glycidyl ether (epoxide) end groups. The conditions were the same as in example 4, except the wet-end sizing was alkyl succinic anhydride (ASA). The pH was 7.8 instead of 7.0
[0078] Paper was made with two levels of ASA1 0.036 and 0.041 %. A 75/25 hard wood / soft wood mixture was used with 16% PCC filler, 0.75% cationic starch, 0.5% paper makers alum, and 0.015% anionic retention aid. The paper was then treated on the paper machine at the size press.
[0079] Polyethyleneglycol diglycidyl ether (PEGDGE) with an average molecular weight of about 350 g/mole and polypropylene glycol diglycidyl ether (PPGDGE) with an
average molecular weight of about 400 g/mole were mixed with an oxidized starch and a liquid ketene dimer sizing agent made from an unsaturated alkyl fatty acid. The sizing agent was added as an emulsion to the starch solution. The glycol ether polymers were also added to the starch solution. The level of starch added to the paper was 4%. As is typical in fine paper manufacturing 0.25% NaCI was added to the paper by also adding NaCI to the size press starch solution. The levels of dimer and glycol ether polymers in the final papers are noted below.
[0080] (the levels of materials are listed in dry percent of the final paper weight.)
I. 0.036% ASA in the base sheet
Sample Dimer Polymer HST Mottle Str.Th. OD
A 0.05 none 181 8.38 3.18 1.27
B 0.065 none 195 13.6 3.35 1.32
C 0.05 0.01 PEGDGE 169 9.79 3.22 1.34
D 0.065 0.01 PEGDGE 181 2.80 0.735 1.41
E 0.05 0.02 PEGDGE 154 2.16 1.05 1.38
F 0.065 0.02 PEGDGE 192 2.24 0.814 1.39
G 0.05 0.01 PPGDGE 162 1.16 0.921 1.43
H 0.05 0.02 PPGDGE 126 1.51 0.722 1.43
II. 0.041 %ASA in the base sheet
Sample Dimer Polymer HST Mottle Str.Th. OD
A 0.04 none 174 2.39 1.36 1.41
B 0.055 none 185 1.13 0.57 1.43
C 0.04 0.0075 PEGDGE 158 1.17 0.62 1.42
D 0.055 0.0075 PEGDGE 180 0.905 0.53 1.43
E 0.04 0.015 PEGDGE 156 1.02 0.83 1.41
F 0.055 0.015 PEGDGE 148 0.88 0.54 1.42
G 0.04 0.0075 PPGDGE 164 0.82 0.71 1.43
H 0.055 0.0075 PPGDGE 201 0.94 0.65 1.43
[0081] Both PEGDGE and PPGDGE reduced mottle and strike-through. The benefit depends on the amount of mottle and strike-through of the paper without them. The samples with more internal ASA had less mottle and strike-through and therefore the amount of
improvement was less. PPGDGE was more effective than PEGDGE. However, when 0.02% PPGDGE was used the sizing was reduced. At lower levels, it may also have a negative effect on sizing when a low level of sizing agent is used. As an added benefit, both epoxides enhanced optical density. PPGDGE was again more effective than PEGDGE.
Example 6 Addition of alternative functionalized glycol ether polymers
[0082] Using the same conditions as Example 3, except for use of an 8% rather than a 9% starch solution, poly(ethylene glycol) bis (carboxymethyl) ether (PEGBCME) was evaluated. The polymer was obtained from Alrich and had an average molecular weight of 600. The results are displayed in the following table.
[0083] Values listed for materials are percent of final paper weight. The HST values are in seconds.
Dimer PEGBCME Mottle St.Thr
A. 0.04 0 15.0 10.5
B. 0.04 0.0075 4.75 14.3
C. 0.04 0.015 1.13 5.25
PEGBCME reduced mottle and strike-through.
Example 7 Use of a pre-mixture.
[0084] Using the same conditions as Example 3, except for use of a 10% starch solution instead of a 9% starch solution, a pre-mixture of sizing agent and glycol ether polymer was evaluated.
[0085] ImPress® ST900 sizing emulsion of Hercules was used as the sizing agent on its own and in pre-mixtures with PPG. The PPG was predispersed in water, 10% PPG and 90% water, with a sonicator. The PPG dispersion was mixed with the dimer emulsion. The ratio of dimer to PPG in the pre-mixtures was 10 to 1 and 5 to 1. The results of the evaluation are summarized in the following table.
Dimer PPG HST Mottle St.Thr.
A. 0.035 0 384 28.9 8.56
C. 0.035 0.0035 392 29.4 5.56
E. 0.035 0.007 349 16.6 4.83
[0086] PPG was premixed with a dimer emulsion and the mottle and strike-through performance of the treated paper was improved. With the lowest level of PPG, 0.0035%, there was little or no improvement of mottle but strikethrough improved. At a higher level the mottle and strikethrough performance of the paper improved. As noted in a previous example, the addition of too much PPG will reduce the level of sizing.
Claims
1. An uncoated cellulosic paper having a front and a back surface, having been treated on at least one surface with: a) at least one sizing agent present in an amount of between 0.01 to 0.3% based on dry weight of paper; b) starch present in an amount of between 1 to 8% based on dry weight of paper c) a glycol ether based polymer present in an amount less than 0.025% based on dry weight of paper; and optionally, a divalent metal salt.
2. The cellulosic paper of claim 1 wherein the glycol ether based polymers primary backbone is selected from polyethylene glycol, or polypropylene glycol.
3. The cellulosic paper of claim 1 wherein the glycol ether based polymers have glycidyether functional groups.
4. The cellulosic paper of claim 1 wherein the glycol ether based polymers primary backbone is selected from polyethyleneglycol diglycidyl ether or polypropylene glycol diglycidyl ether.
5. The cellulosic paper of claim 1 wherein the sizing agent is selected from alkyl succinic anhydride, ketene dinners, or alkenyl ketene dimers.
6. An aqueous composition for surface treating paper through a size press, which composition contains: a) Sizing agent in an amount of 0.03-1.0%, b) starch present in an amount of 1.5-12% c) a glycol ether based polymer present in an amount of less than 0.25% of the composition.
7. The composition of Claim 6 wherein the glycol ether polymers primary backbone is either polyethylene glycol or polypropylene glycol.
8. The composition of claim 6 wherein the glycol ether polymers primary backbone is selected from polyethyleneglycol diglycidyl ether or polypropylene glycol diglycidyl ether.
9. The composition of claim 6 wherein the glycol ether based polymers have glycidyl ether based functional groups.
10. The composition of claim 6 wherein the sizing agent is selected from alkyl succinic anhydride, ketene dimers, or alkenyl ketene dimers.
11. Process for improving ink-jet printing properties of paper which comprises treating paper with a composition of claim 6.
12. Process of claim 11 wherein the glycol ether based polymer is selected from polyethylene glycol, polypropylene glycol, polyethyleneglycol diglycidyl ether, or polypropylene glycol diglycidyl ether.
13. Process of claim 11 wherein the glycol ether based polymers have glycidyl ether functionality.
14. The process of claim 12 wherein the sizing agent is a reactive sizing agent.
15. Process of claim 11 wherein the sizing agent is selected from alkyl succinic anhydride, ketene dimers, or alkenyl ketene dimers.
16. The cellulosic paper of claim 1 wherein the sizing agent is a combination of a reactive dimer sizing agent and a polymeric latex sizing agent.
17. The process of claim 12 wherein the sizing agent is a combination of a reactive dimer sizing agent and a polymeric latex sizing agent.
8. Aqueous composition containing a glycol ether based polymer and an emulsified sizing agent, where the glycol ether based polymer is present in an amount of 3- 50% based on amount of sizing agent.
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WO2010011646A2 (en) * | 2008-07-24 | 2010-01-28 | Hercules Incorporated | Enhanced surface sizing of paper |
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WO2010039996A1 (en) * | 2008-10-01 | 2010-04-08 | International Paper Company | A paper substrate containing a wetting agent and having improved printability |
US20100129553A1 (en) * | 2008-11-27 | 2010-05-27 | International Paper Company | Optical Brightening Compositions For High Quality Inkjet Printing |
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