US3525668A - Method for improving the wet strength and water resistance of paper - Google Patents
Method for improving the wet strength and water resistance of paper Download PDFInfo
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- US3525668A US3525668A US582259A US3525668DA US3525668A US 3525668 A US3525668 A US 3525668A US 582259 A US582259 A US 582259A US 3525668D A US3525668D A US 3525668DA US 3525668 A US3525668 A US 3525668A
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- paper
- wax
- emulsion
- materials
- wet strength
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title description 13
- 238000000034 method Methods 0.000 title description 9
- 239000000839 emulsion Substances 0.000 description 31
- 239000000203 mixture Substances 0.000 description 24
- 239000001993 wax Substances 0.000 description 23
- 239000000463 material Substances 0.000 description 21
- 239000000123 paper Substances 0.000 description 17
- 229920000642 polymer Polymers 0.000 description 12
- 229920001577 copolymer Polymers 0.000 description 11
- 239000010426 asphalt Substances 0.000 description 8
- -1 alcohol ester Chemical class 0.000 description 7
- 229930195733 hydrocarbon Natural products 0.000 description 7
- 150000002430 hydrocarbons Chemical class 0.000 description 7
- 239000004215 Carbon black (E152) Substances 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 239000002253 acid Substances 0.000 description 6
- 150000001336 alkenes Chemical class 0.000 description 6
- 239000003995 emulsifying agent Substances 0.000 description 6
- 150000002148 esters Chemical class 0.000 description 6
- 239000006185 dispersion Substances 0.000 description 5
- 239000000835 fiber Substances 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- 125000000129 anionic group Chemical group 0.000 description 4
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 125000002091 cationic group Chemical group 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 150000002762 monocarboxylic acid derivatives Chemical group 0.000 description 3
- 239000011087 paperboard Substances 0.000 description 3
- 239000012188 paraffin wax Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 230000035515 penetration Effects 0.000 description 3
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 2
- 239000005977 Ethylene Substances 0.000 description 2
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 150000001298 alcohols Chemical class 0.000 description 2
- XXROGKLTLUQVRX-UHFFFAOYSA-N allyl alcohol Chemical compound OCC=C XXROGKLTLUQVRX-UHFFFAOYSA-N 0.000 description 2
- 239000000440 bentonite Substances 0.000 description 2
- 229910000278 bentonite Inorganic materials 0.000 description 2
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 2
- 125000004432 carbon atom Chemical group C* 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000004927 clay Substances 0.000 description 2
- 239000011280 coal tar Substances 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000004945 emulsification Methods 0.000 description 2
- 238000007654 immersion Methods 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 239000003784 tall oil Substances 0.000 description 2
- WCASXYBKJHWFMY-NSCUHMNNSA-N 2-Buten-1-ol Chemical compound C\C=C\CO WCASXYBKJHWFMY-NSCUHMNNSA-N 0.000 description 1
- 229920003345 Elvax® Polymers 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- IMROMDMJAWUWLK-UHFFFAOYSA-N Ethenol Chemical compound OC=C IMROMDMJAWUWLK-UHFFFAOYSA-N 0.000 description 1
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical group CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 1
- ACIAHEMYLLBZOI-ZZXKWVIFSA-N Unsaturated alcohol Chemical compound CC\C(CO)=C/C ACIAHEMYLLBZOI-ZZXKWVIFSA-N 0.000 description 1
- RSWGJHLUYNHPMX-ONCXSQPRSA-N abietic acid Chemical compound C([C@@H]12)CC(C(C)C)=CC1=CC[C@@H]1[C@]2(C)CCC[C@@]1(C)C(O)=O RSWGJHLUYNHPMX-ONCXSQPRSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 229940037003 alum Drugs 0.000 description 1
- 239000008346 aqueous phase Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 235000013871 bee wax Nutrition 0.000 description 1
- 239000012166 beeswax Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000011111 cardboard Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- 239000005038 ethylene vinyl acetate Substances 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 239000011094 fiberboard Substances 0.000 description 1
- 235000013611 frozen food Nutrition 0.000 description 1
- WCASXYBKJHWFMY-UHFFFAOYSA-N gamma-methylallyl alcohol Natural products CC=CCO WCASXYBKJHWFMY-UHFFFAOYSA-N 0.000 description 1
- FUZZWVXGSFPDMH-UHFFFAOYSA-N hexanoic acid group Chemical group C(CCCCC)(=O)O FUZZWVXGSFPDMH-UHFFFAOYSA-N 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000002655 kraft paper Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000004200 microcrystalline wax Substances 0.000 description 1
- 235000019808 microcrystalline wax Nutrition 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 150000002763 monocarboxylic acids Chemical class 0.000 description 1
- 239000012170 montan wax Substances 0.000 description 1
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid group Chemical group C(CCCCCCC\C=C/CCCCCCCC)(=O)O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 description 1
- 150000001451 organic peroxides Chemical class 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000012169 petroleum derived wax Substances 0.000 description 1
- 235000019381 petroleum wax Nutrition 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 239000011295 pitch Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 1
- 238000010526 radical polymerization reaction Methods 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 238000004078 waterproofing Methods 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/33—Synthetic macromolecular compounds
- D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/36—Polyalkenyalcohols; Polyalkenylethers; Polyalkenylesters
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/33—Synthetic macromolecular compounds
- D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/35—Polyalkenes, e.g. polystyrene
-
- 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
- D21H17/60—Waxes
-
- 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
- D21H17/61—Bitumen
Definitions
- This invention relates to compositions useful for improving the water resistance of paper. More particularly, it relates to compositions which, when blended in vari ous paper stocks, significantly decrease the water absorption and produce a great increase in wet strength of the paper without impairing its dry strength.
- paper materials of excellent water resistance and having high dry and wet strengths result from the incorporation in the paper or fiber board of minor amounts of a composition comprising an aqueous dispersion of a bitumen, a hydrocarbon wax and a copolymer of an olefin and an olefinic alcohol ester.
- the dispersion which comprises the composition is analogous to anionic or cationic bituminous emulsions.
- These emulsions are well described in the art and are generally prepared by stirring a bituminous phase and an aqueous phase in the presence of an emulsifying agent. Examples of the emulsions and various methods of their preparation may be found in the literature, e.g., in U.S. Pats. 2,481,374, U.S. 2,601,597, U.S. 3,026,266 and U.S. 3,271,240.
- the particular type of emulsion is not im- 'ice portant to this invention, as either cationic or anionic emulsions may be employed and their method of preparation is not of consequence. Thus, any number of materials (acid or bases) may be used for emulsifying agents.
- emulsifiers include fatty acids such as oleic, palmeic, lauric, stearic, naphthenic, and oxidized hydrocarbons, tall oil acid, rosin acid and mixtures of these materials.
- the preferred olefin-olefinic alcohol ester polymers which are employed in the compositions are polymers of olefins of from 2 to 4 and esters of olefinic alcohols of 2 to 4- carbon atoms and monocarboxylic acids of from 1 to 12 carbon atoms.
- the monocarboxylic acid moiety is preferably derived from an alkanoic acid.
- Polymers of this type are well known in the art and are usually derived from the reaction of an olefin with an ester derived from an olefinic alcohol and a monocarboxylic acid.
- Suitable olefins which may be reacted with the ester to produce the polymers include ethylene, propylene, butylene and isobutylene.
- the olefinic alcohols from which the esters is derived include vinyl alcohol, allyl alcohol, 2 butenol, l-butenol, etc.
- the monocarboxylic acid from which the ester derived is an acid of from 1 to 12 carbon atoms.
- suitable acids include formic, acetic, propionic, butanoic, hexanoic, octanoic, lauric, etc.
- asphalts which are characterized by penetration values in the range from about 0 to about 30 at 77 F. (ASTM D5-52) and by softening points in the range from about 160 to about 260 F. (ASTM D36-26, Ring and Ball Method) may be used-
- the asphalts will have a softening point of from about 180 to about 230 F. and a penetration of about 0 to 15.
- Suitable bitumens include all kinds of asphalts which are capable of emulsification when heated to from about 300 to about 450 F., irrespective of the manner of their production; thus, steam-refined, solvent-refined ad airblown asphalts may be used.
- High melting coal-tar pitches such as those recovered in coal-tar production from horizontal coke ovens, gaswork retorts, blast furnaces, etc. having substantially similar penetration values and softening points and similar viscosities which permit emulsification when heated to 300450 F., also may be employed in the compositions of the invention.
- bituminous materials which may be used are the so-called native asphalts, wurtzilite, Gilsonite and Montan wax; these materials may be emulsified and employed in the compositions in the same manner as the more typical asphalts.
- the polymers may be prepared by any suitable method. Ordinarily, free-radical polymerization is utilized with a free-radical producing catalyst, which is oxygen or an organic peroxide. The materials are reacted at high pressures and temperatures from about 150 to 250 C. However, the most suitable methods of producing these polymers comprise reacting an olefin and the ester of an unsaturated alcohol under free-radical conditions at a pressure from about -200 atmospheres, the temperature in the order of -250" C., and distilling to remove unreacted materials. The preferred polymers have molecular weights of from about 100,000 to 1,000,000.
- polymers are produced by the reaction of ethylene with vinyl acetate.
- the polymers are available in a number of molecular weight ranges, and a range of from 100,000 to 500,000 is suitable for the purposes of this invention.
- the waxes employed in the composition are preferably petroleum waxes or, more preferably, parafiin waxes.
- Parafiin wax is a solid, crystalline, hydrocarbon mixture wholly derived from that portion of crude petroleum commonly designated paraffin distillates, from shale distillates, or from hydrocarbon synthesis, by low temperatures solidification, an expression, or by solvent extraction. It is distinguished by its solid state at room temperature, relatively slight deformation at this temperature, even under considerable pressure, and low viscosity, from 35- 45 SSU at 210 F. when melted.
- paraffinic waxes are most desirable, microcrystalline waxes and mixtures of microcrystalline and paraflinic waxes may also be employed in the compositions of the invention. Natural waxes such as beeswax, etc. may also be used.
- the wax and the copolymer may be blended together and then emulsified and blended further with the bituminous emulsion before the treating composition is added to the paper-making fibers.
- the wax and copolymer may be blended with heat into the bituminous mix and emulsified by conventional methods.
- Emulsifying agents which may be employed include the same cationic and anionic emulsifying agents previously mentioned in conjunction with the bitumens.
- the emulsion or emulsions are dispersed into the wet pulp stock from which the products are made.
- the treating compositions are employed in concentrations sufiicient to give from about 0.5% to by weight of solids in the dry paper.
- the ratio of bitumen to waxcopolymer may vary from about 9:1 to about 1:1.
- the ratio of wax to copolymer in the wax-copolymer combination may vary from about 9:1 to about 3:2.
- the concentration of solids of the respective materials is from about 40 to 90% bitumen, from about 6 to 45% wax and from about 1 to 20% of the copolymer. It is preferred that the bituminous portion comprise from about 75 to 85% of the composition, and the wax from about 60 to 80% of the wax-polymer portion.
- the samples were tested in a Mullen tester to determine dry strength.
- the sheet of each sample was immersed in water for 10 minutes, and the amount of water absorbed by 36 square inches of surface in 10 minutes in centigrams was measured and recorded as immersion number.
- the wet sheet was then tested in the Mullen tester to determine its wet strength.
- the wax employed in the samples was a paraffin wax having a softening point of about 150 F.
- an emulsion was prepared from the following materials: 53.5% of a steam-refined asphalt having an ASTM ring and valve softening point of 190 F.; 2% pinewood resin; .65% bentonite clay; .40% NaOH; 43.5% water.
- the emulsion has a pH of about 10.2.
- An emulsion of a hydrocarbon wax was prepared by blending a paraffin wax having a melting point of 154-156 F. AMP with anionic emulsifiers and water. This emulsion was combined with bituminous emulsions (1) and (2) to form other additives.
- polymer modified asphalt treating compositions of this 1. A method of imparting Wet strength to cellulosic 70 materlals from papermakmg fibrous pulp stock which invention, a Kraft pulp was treated with varying quantities of this emulsion, with a bituminous emulsion and with a wax emulsion. The fiber freeness was 650 and the pH of the pulp was about 4.3. Five percent alum retention acid was employed in this sheet, and sheets were thus prepared from the pulp and dried at 300 F. for 20 ethylene and vinyl acetate, said minor portion of said treating composition being sufiicient to give from about 0.5 to 10 percent by weight of solids in the dry paper.
- composition is dispersed by emulsifying the bitumen, (A), and a mixture of the hydrocarbon Wax, (B), and the copolymer, (C), separately, and incorporating them Within the pulp stock.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
United States Patent U.S. Cl. 162--169 2 Claims ABSTRACT OF THE DISCLOSURE Applying an aqueous dispersion of 40 to 90% by weight of bitumen, 6. to 45% by weight hydrocarbon wax, and 1 to 20% by weight of a copolymer of an olefin and an olefinic alcohol ester has been found to impart improved wet strength and water resistance to paper.
This invention relates to compositions useful for improving the water resistance of paper. More particularly, it relates to compositions which, when blended in vari ous paper stocks, significantly decrease the water absorption and produce a great increase in wet strength of the paper without impairing its dry strength.
In various applications of paper and paper board, it is exceedingly important that the materials be resistant to water impregnation. For example, in commerce many items are packaged for shipment and sale in paper or cardboard wrappings, etc. When it is probable that the items will come in contact with moisture, a coating is usually applied to the package to prevent passage of moisture into the package with consequent damage to the article and the container. Thus, frozen food containers are usually coated with wax or plastic compositions for this purpose. However, for many applications where moisture contact is not inevitable, the application of coatings to the exterior of packages, etc. is usually uneconomical due to the substantial cost of coating materials and applicators. However, since occasional moisture contact has serious effects on uncoated paper materials, it is highly desirable to incorporate within the matrix of fibers in the paper, substances which will increase the moisture resistance and wet strength of the paper. Among the materials that have been employed for this purpose have been various bituminous (especially asphaltic) materials and waxes. However, none of these materials have been found entirely satisfactory. Asphaltic materials have been found to produce an insufiicient decrease in water absorption and increase in wet strength. Wax, while significantly decreasing water absorption, produces a substantial decrease in the dry strength of the paper and only a nominal increase in wet strength.
It is therefore desirable to incorporate into the paper fibers a material which will provide dry strength retention while increasing water resistance and wet strength.
It has now been found that paper materials of excellent water resistance and having high dry and wet strengths result from the incorporation in the paper or fiber board of minor amounts of a composition comprising an aqueous dispersion of a bitumen, a hydrocarbon wax and a copolymer of an olefin and an olefinic alcohol ester.
The dispersion which comprises the composition is analogous to anionic or cationic bituminous emulsions. These emulsions are well described in the art and are generally prepared by stirring a bituminous phase and an aqueous phase in the presence of an emulsifying agent. Examples of the emulsions and various methods of their preparation may be found in the literature, e.g., in U.S. Pats. 2,481,374, U.S. 2,601,597, U.S. 3,026,266 and U.S. 3,271,240. The particular type of emulsion is not im- 'ice portant to this invention, as either cationic or anionic emulsions may be employed and their method of preparation is not of consequence. Thus, any number of materials (acid or bases) may be used for emulsifying agents.
However, it may be noted that, in accordance with the prior findings of the art, smallparticle size of the emulsions is preferred in order to eliminate plugging of paper equipment and appearance of spots on the paper; thus, the use of agents which result in small particles of the emulsion is preferred. Examples of suitable emulsifiers include fatty acids such as oleic, palmeic, lauric, stearic, naphthenic, and oxidized hydrocarbons, tall oil acid, rosin acid and mixtures of these materials.
The preferred olefin-olefinic alcohol ester polymers which are employed in the compositions are polymers of olefins of from 2 to 4 and esters of olefinic alcohols of 2 to 4- carbon atoms and monocarboxylic acids of from 1 to 12 carbon atoms. The monocarboxylic acid moiety is preferably derived from an alkanoic acid. Polymers of this type are well known in the art and are usually derived from the reaction of an olefin with an ester derived from an olefinic alcohol and a monocarboxylic acid. Suitable olefins which may be reacted with the ester to produce the polymers include ethylene, propylene, butylene and isobutylene. The olefinic alcohols from which the esters is derived include vinyl alcohol, allyl alcohol, 2 butenol, l-butenol, etc. The monocarboxylic acid from which the ester derived is an acid of from 1 to 12 carbon atoms. Thus. suitable acids include formic, acetic, propionic, butanoic, hexanoic, octanoic, lauric, etc.
As examples of suitable bituminous materials which may be employed in the compositions of this invention may be cited asphalts which are characterized by penetration values in the range from about 0 to about 30 at 77 F. (ASTM D5-52) and by softening points in the range from about 160 to about 260 F. (ASTM D36-26, Ring and Ball Method) may be used- Preferably the asphalts will have a softening point of from about 180 to about 230 F. and a penetration of about 0 to 15.
Suitable bitumens include all kinds of asphalts which are capable of emulsification when heated to from about 300 to about 450 F., irrespective of the manner of their production; thus, steam-refined, solvent-refined ad airblown asphalts may be used.
High melting coal-tar pitches such as those recovered in coal-tar production from horizontal coke ovens, gaswork retorts, blast furnaces, etc. having substantially similar penetration values and softening points and similar viscosities which permit emulsification when heated to 300450 F., also may be employed in the compositions of the invention.
Included among other bituminous materials which may be used are the so-called native asphalts, wurtzilite, Gilsonite and Montan wax; these materials may be emulsified and employed in the compositions in the same manner as the more typical asphalts.
The polymers may be prepared by any suitable method. Ordinarily, free-radical polymerization is utilized with a free-radical producing catalyst, which is oxygen or an organic peroxide. The materials are reacted at high pressures and temperatures from about 150 to 250 C. However, the most suitable methods of producing these polymers comprise reacting an olefin and the ester of an unsaturated alcohol under free-radical conditions at a pressure from about -200 atmospheres, the temperature in the order of -250" C., and distilling to remove unreacted materials. The preferred polymers have molecular weights of from about 100,000 to 1,000,000.
Examples of the materials which may be obtained commercially are the Elvax polymers marketed by Du Pont,
Inc. These polymers are produced by the reaction of ethylene with vinyl acetate. The polymers are available in a number of molecular weight ranges, and a range of from 100,000 to 500,000 is suitable for the purposes of this invention.
The waxes employed in the composition are preferably petroleum waxes or, more preferably, parafiin waxes. Parafiin wax is a solid, crystalline, hydrocarbon mixture wholly derived from that portion of crude petroleum commonly designated paraffin distillates, from shale distillates, or from hydrocarbon synthesis, by low temperatures solidification, an expression, or by solvent extraction. It is distinguished by its solid state at room temperature, relatively slight deformation at this temperature, even under considerable pressure, and low viscosity, from 35- 45 SSU at 210 F. when melted. Although the paraffinic waxes are most desirable, microcrystalline waxes and mixtures of microcrystalline and paraflinic waxes may also be employed in the compositions of the invention. Natural waxes such as beeswax, etc. may also be used.
In order to form the aqueous dispersion used for the treating composition, the wax and the copolymer may be blended together and then emulsified and blended further with the bituminous emulsion before the treating composition is added to the paper-making fibers. Alternatively, the wax and copolymer may be blended with heat into the bituminous mix and emulsified by conventional methods. Emulsifying agents which may be employed include the same cationic and anionic emulsifying agents previously mentioned in conjunction with the bitumens. In order to disperse the materials on the cellulosic fibers, the emulsion or emulsions are dispersed into the wet pulp stock from which the products are made.
The treating compositions are employed in concentrations sufiicient to give from about 0.5% to by weight of solids in the dry paper. The ratio of bitumen to waxcopolymer may vary from about 9:1 to about 1:1. The ratio of wax to copolymer in the wax-copolymer combination may vary from about 9:1 to about 3:2. Thus, in the total composition, the concentration of solids of the respective materials is from about 40 to 90% bitumen, from about 6 to 45% wax and from about 1 to 20% of the copolymer. It is preferred that the bituminous portion comprise from about 75 to 85% of the composition, and the wax from about 60 to 80% of the wax-polymer portion.
minutes. The samples were tested in a Mullen tester to determine dry strength. The sheet of each sample was immersed in water for 10 minutes, and the amount of water absorbed by 36 square inches of surface in 10 minutes in centigrams was measured and recorded as immersion number. The wet sheet was then tested in the Mullen tester to determine its wet strength. The wax employed in the samples was a paraffin wax having a softening point of about 150 F.
The following materials were employed:
1) By ordinary emulsion forming methods, such as that described in US. Pat. No. 2,481,374, previously referred to, an emulsion was prepared from the following materials: 53.5% of a steam-refined asphalt having an ASTM ring and valve softening point of 190 F.; 2% pinewood resin; .65% bentonite clay; .40% NaOH; 43.5% water. The emulsion has a pH of about 10.2.
(2) An experimental, small-particle-size emulsion was prepared employing the same asphaltic bases as in emulsion 1, 1% of the pinewood resin, 1% tall oil, .5% bentonite clay, .4% NaOH. This emulsion contains an ingredient designed to effect small particle size in the finished emulsion. The average particle size above 0.9 micron was 1.1 microns.
(3) An emulsion of a hydrocarbon wax was prepared by blending a paraffin wax having a melting point of 154-156 F. AMP with anionic emulsifiers and water. This emulsion was combined with bituminous emulsions (1) and (2) to form other additives.
(4) 30% by weight of an ethylene-vinyl acetate copolymer having a melt index of 5-7 (ASTM D12-38 modified) was combined with of the same wax as in emulsion (3).
(5) The wax emulsion described in (3) was combined with the asphaltic emulsion of 1).
(6) The wax-copolymer emulsion of (4) was combined with the asphaltic emulsion of (1).
(7) The wax-copolymer emulsion of (4) was combined with the asphaltic emulsion of (2).
In preparing the samples the various emulsions were used to size the hand sheets.
Data from the above-mentioned test are included in Table I. Ratios of the various sizing constituents are given. Additionally, the wet strength to dry strength ratio times 100 is included, this figure being a reliable determinant of the eifectiveness of the waterproofing size.
TABLE I.EFFECT OF TREATING AGENTS UPON PAPER Treating agent, weight percent of Wet total dispersion strength] Drain Dry Wet dry Test Additive ry time, Mullen, Mullen, Immersion strength No. No Bitumen Wax Copolymer sheet seconds p.s.i. p.s.i. No. X100 0 25 117 22 222 18. s 3 0 100 0 1 34 86 26 110 30.2 3 0 100 0 3 32 96 36 112 37.5 3 0 100 0 5 31 74 24 as 32.4 4 0 70 3o 1 32 115 51 106 44. 4 4 0 70 30 3 31 53 101 62.4 4 0 70 30 5 31 9s 70 71 71.5 1 0 0 1 28 116 33 121 28. 4 1 100 0 0 3 33 115 45 112 39.1 1 100 0 0 5 34 120 56 103 46. 6 5 s0 20 0 5 33 54 89 51.4 5 60 40 0 5 32 96 41 89 42.7 5 40 60 0 5 32 82 31 93 37.8 6 s0 14 6 5 32 114 66 79 58.0 6 60 2s 12 5 32 104 60 77 57.6 6 40 42 1s 5 33 86 69 70 80.2 2 100 0 0 1 2s 87 51 127 58.6 2 100 0 0 3 31 84 42 115 50.0 2 100 0 0 5 34 99 43 43.4 7 s0 14 6 5 33 85 88 69 97.8 7 60 2s 12 5 34 78 59 79 75.6 7 40 42 1s 5 34 72 72 78 100.0
In order to demonstrate the advantage of the wax- What 1scla1med1s: polymer modified asphalt treating compositions of this 1. A method of imparting Wet strength to cellulosic 70 materlals from papermakmg fibrous pulp stock which invention, a Kraft pulp was treated with varying quantities of this emulsion, with a bituminous emulsion and with a wax emulsion. The fiber freeness was 650 and the pH of the pulp was about 4.3. Five percent alum retention acid was employed in this sheet, and sheets were thus prepared from the pulp and dried at 300 F. for 20 ethylene and vinyl acetate, said minor portion of said treating composition being sufiicient to give from about 0.5 to 10 percent by weight of solids in the dry paper.
2. The method of claim 1 wherein the composition is dispersed by emulsifying the bitumen, (A), and a mixture of the hydrocarbon Wax, (B), and the copolymer, (C), separately, and incorporating them Within the pulp stock.
References Cited UNITED STATES PATENTS 6 3,158,531 11/1964 Rohrer 162-171 XR 3,291,767 12/ 1966 Zaayenga.
OTHER REFERENCES Casey, Pulp and Paper, Interscience Publishers, Inc., 2nd edition, vo1.II (1960), p. 1154.
S. LEON BASHORE, Primary Examiner R. H. TUSHIN, Assistant Examiner U.S. Cl. X.R.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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US58225966A | 1966-09-27 | 1966-09-27 |
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US3525668A true US3525668A (en) | 1970-08-25 |
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US582259A Expired - Lifetime US3525668A (en) | 1966-09-27 | 1966-09-27 | Method for improving the wet strength and water resistance of paper |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3912669A (en) * | 1973-01-15 | 1975-10-14 | Hill & Griffith Company | Bituminous coating system and articles produced thereby |
US5865953A (en) * | 1996-08-30 | 1999-02-02 | Merrimac Paper Company, Inc. | Paper for corrugating medium |
US20040091585A1 (en) * | 2002-11-08 | 2004-05-13 | Theisen John A. | Treated paper product, combination food and treated paper product, and methods for manufacturing and using treated paper product |
US20060263495A1 (en) * | 2005-05-23 | 2006-11-23 | David Langton | Food interleaver, method for imparting flavor to food product, and combination food product and food interleaver |
US20170009400A1 (en) * | 2015-07-10 | 2017-01-12 | Minxuan TAN | Method for manufacturing transfer paper |
US10751900B2 (en) * | 2017-07-03 | 2020-08-25 | Weber Maschinenbau Gmbh Breidenbach | Providing a cutting area with web-like interleaver material |
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Publication number | Priority date | Publication date | Assignee | Title |
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US601597A (en) * | 1898-03-29 | Fly-poison plate | ||
US3158531A (en) * | 1961-08-18 | 1964-11-24 | Rohrer Ernst | Process for the production of waterproof materials from waste paper containing bitumen and/or wax |
US3272690A (en) * | 1963-06-26 | 1966-09-13 | Continental Oil Co | Method of improving the wet strength of paper by addition of ethylene-vinyl acetate copolymer thereto |
US3291767A (en) * | 1963-07-16 | 1966-12-13 | Sun Oil Co | Asphaltic filament comprising asphalt, ethylene-vinyl acetate copolymer and paraffinwax |
-
1966
- 1966-09-27 US US582259A patent/US3525668A/en not_active Expired - Lifetime
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
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US601597A (en) * | 1898-03-29 | Fly-poison plate | ||
US3158531A (en) * | 1961-08-18 | 1964-11-24 | Rohrer Ernst | Process for the production of waterproof materials from waste paper containing bitumen and/or wax |
US3272690A (en) * | 1963-06-26 | 1966-09-13 | Continental Oil Co | Method of improving the wet strength of paper by addition of ethylene-vinyl acetate copolymer thereto |
US3291767A (en) * | 1963-07-16 | 1966-12-13 | Sun Oil Co | Asphaltic filament comprising asphalt, ethylene-vinyl acetate copolymer and paraffinwax |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3912669A (en) * | 1973-01-15 | 1975-10-14 | Hill & Griffith Company | Bituminous coating system and articles produced thereby |
US5865953A (en) * | 1996-08-30 | 1999-02-02 | Merrimac Paper Company, Inc. | Paper for corrugating medium |
US20040091585A1 (en) * | 2002-11-08 | 2004-05-13 | Theisen John A. | Treated paper product, combination food and treated paper product, and methods for manufacturing and using treated paper product |
US7189308B2 (en) * | 2002-11-08 | 2007-03-13 | Wausau Paper Corp. | Treated paper product |
US20070160716A1 (en) * | 2002-11-08 | 2007-07-12 | Wausau Paper Specialty Products, Llc | Treated paper product, combination food and treated paper product, and methods for manufacturing and using treated paper product |
US8337919B2 (en) | 2002-11-08 | 2012-12-25 | Wausau Paper Mills, Llc | Treated paper product, combination food and treated paper product, and methods for manufacturing and using treated paper product |
US20060263495A1 (en) * | 2005-05-23 | 2006-11-23 | David Langton | Food interleaver, method for imparting flavor to food product, and combination food product and food interleaver |
US7601375B2 (en) | 2005-05-23 | 2009-10-13 | Wausau Paper Specialty Products, Llc | Food interleaver, method for imparting flavor to food product, and combination food product and food interleaver |
US8080271B2 (en) | 2005-05-23 | 2011-12-20 | Wausau Paper Mills, Llc | Food interleaver, method for imparting flavor to food product, and combination food product and food interleaver |
US20170009400A1 (en) * | 2015-07-10 | 2017-01-12 | Minxuan TAN | Method for manufacturing transfer paper |
US10751900B2 (en) * | 2017-07-03 | 2020-08-25 | Weber Maschinenbau Gmbh Breidenbach | Providing a cutting area with web-like interleaver material |
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