US3421976A - Process of rosin sizing paper - Google Patents
Process of rosin sizing paper Download PDFInfo
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- US3421976A US3421976A US711166A US3421976DA US3421976A US 3421976 A US3421976 A US 3421976A US 711166 A US711166 A US 711166A US 3421976D A US3421976D A US 3421976DA US 3421976 A US3421976 A US 3421976A
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- pulp
- alum
- added
- size
- slurry
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- 238000000034 method Methods 0.000 title description 18
- 238000004513 sizing Methods 0.000 title description 17
- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 title description 13
- KHPCPRHQVVSZAH-HUOMCSJISA-N Rosin Natural products O(C/C=C/c1ccccc1)[C@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 KHPCPRHQVVSZAH-HUOMCSJISA-N 0.000 title description 13
- KHPCPRHQVVSZAH-UHFFFAOYSA-N trans-cinnamyl beta-D-glucopyranoside Natural products OC1C(O)C(O)C(CO)OC1OCC=CC1=CC=CC=C1 KHPCPRHQVVSZAH-UHFFFAOYSA-N 0.000 title description 13
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 66
- 239000002002 slurry Substances 0.000 description 35
- 239000000243 solution Substances 0.000 description 35
- 229940037003 alum Drugs 0.000 description 24
- 239000000123 paper Substances 0.000 description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 22
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 18
- 229910000329 aluminium sulfate Inorganic materials 0.000 description 18
- 235000011128 aluminium sulphate Nutrition 0.000 description 18
- 238000003756 stirring Methods 0.000 description 15
- 229920001131 Pulp (paper) Polymers 0.000 description 14
- 238000005189 flocculation Methods 0.000 description 14
- 230000016615 flocculation Effects 0.000 description 14
- 239000007787 solid Substances 0.000 description 14
- 238000013019 agitation Methods 0.000 description 13
- 239000000047 product Substances 0.000 description 12
- 239000002655 kraft paper Substances 0.000 description 11
- 230000014759 maintenance of location Effects 0.000 description 11
- 239000012153 distilled water Substances 0.000 description 9
- 235000008331 Pinus X rigitaeda Nutrition 0.000 description 8
- 235000011613 Pinus brutia Nutrition 0.000 description 8
- 241000018646 Pinus brutia Species 0.000 description 8
- 239000011121 hardwood Substances 0.000 description 7
- 239000000126 substance Substances 0.000 description 6
- 238000001035 drying Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- 238000003825 pressing Methods 0.000 description 4
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 3
- 150000001450 anions Chemical class 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 230000001965 increasing effect Effects 0.000 description 3
- 230000035515 penetration Effects 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- 239000002023 wood Substances 0.000 description 3
- HZAXFHJVJLSVMW-UHFFFAOYSA-N 2-Aminoethan-1-ol Chemical compound NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 2
- 239000000908 ammonium hydroxide Substances 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 2
- -1 hydroxide ions Chemical class 0.000 description 2
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000013055 pulp slurry Substances 0.000 description 2
- VZSRBBMJRBPUNF-UHFFFAOYSA-N 2-(2,3-dihydro-1H-inden-2-ylamino)-N-[3-oxo-3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propyl]pyrimidine-5-carboxamide Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C(=O)NCCC(N1CC2=C(CC1)NN=N2)=O VZSRBBMJRBPUNF-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000002939 deleterious effect Effects 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 229940031098 ethanolamine Drugs 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000004310 lactic acid Substances 0.000 description 1
- 235000014655 lactic acid Nutrition 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000011122 softwood Substances 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
- D21H17/62—Rosin; Derivatives thereof
Definitions
- This invention relates to the sizing of paper and to a novel method of increasing the resistance of paper to water penetration and otherwise enhancing the quality of the sizing of the paper.
- EXAMPLE 1 Following standard laboratory procedure, a mixture of pine and 25% hardwood kraft pulp, bleached to GE. brightness, was refined in an experimental beater at 1.75% consistency to 488 Canadian Standard freeness. Forty grams (ovendry basis) of the refined pulp were suspended in distilled water at 3% consistency. Fortified size (commercially available Paper Product 2409) was added to the slurry at a rate of 30 pounds of size solids per ton of pulp. A mechanical stirrer was used to keep the slurry thoroughly mixed during the addition. Stirring was continued. After 5 minutes, papermakers alum was added at the rate of 30 pounds A'l (SO .14H O per ton of pulp. Stirring was continued for 10 minutes. Slurry pH after the addition of alum was 4.2.
- EXAMPLE 2 Twenty grams of pulp similar to that used in Example 1 were suspended in distilled water at 3% consistency. Six-tenths milliliter of 0.5 N hydrochloric acid was slowly added to pH 4.5. Cf., US. Pat. No. 3,112,242 to Jones. After stirring for a few minutes, a solution of papermakers alum was added to the slurry at the rate of 20 pounds Al (S0 .14H O per ton of pulp (ovendry basis). Stirring was continued for 5 minutes, during which time pH dropped to 3.8. A solution of sodium hydroxide (0.5 N) was added from a buret, to pH 5.5 and flocculation occurred. Cf., Curtman, L.
- Handsheets were prepared, pressed, and dried as in Example 1. Each sheet was weighed, dipped in a fresh solution of fortified rosin size (Paper Product 2409), blotted lightly, weighed again, and heated to incipient dryness between a polished plate and blotters on a Carver press at C. The sized sheets were clamped in rings and dried in a forced-draft oven at 105 C. for 30 minutes. Basis weight and caliper averaged 100 pounds and 7.0 mils, respectively. Size solids pickup was equivalent to 5.1 pounds per ton of pulp.
- fortified rosin size Paper Product 2409
- the sized sheets were clamped in rings and dried in a forced-draft oven at 105 C. for 30 minutes.
- Basis weight and caliper averaged 100 pounds and 7.0 mils, respectively. Size solids pickup was equivalent to 5.1 pounds per ton of pulp.
- EXAMPLE 3 In accordance with the present invention, twenty-two grams of pulp similar to that used in Example 1 were suspended in demineralized water at 3.0% consistency. Slurry pH after thorough agitation was 6.7. Addition of a solution of alum equivalent to 40.0 pounds A12(SO4)3.14H2O per ton of pulp lowered pH to 4.1. Half normal sodium hydroxide was added slowly, with agitation, to pH 5.5 and flocculation occurred.
- Cf Curtman, L. J.; Qualitative Chemical Analysis; The MacMillan Company; New York, 1938; P. 181 and Kolthoif et al.; Textbook of Quantitative Inorganic Analysis (3rd Ed); The MacMillan Company; New York, 1952; P. 318.
- EXAMPLE 4 Twenty-two grams of kraft pulp similar to that used in Example 1 were adjusted to 3% consistency with demineralized water. After thorough mixing, pH was 6.7. A solution of papermakers alum equivalent to 62.7 pounds Al (SO -14H O per ton of pulp was added to pH 3.9. A 0.5 N solution of sodium hydroxide was used to adjust pH to 5.2 and flocculation occurred. Cf., Curtman, L. J.; Qualitative Chemical Analysis; The MacMillan Company; New York, 1938; P. 181 and Kolthotf et al.; Textbook of Quantitative Inorganic Analysis (3rd Ed); The MacMillan Company; New York, 1952; P.
- handsheets were prepared and dried as before, dipped in a solution of Paper Product 2409 of such concentration as to give a size solids pickup of 8.8 pounds per ton of pulp.
- Final drying and pressing brought basis weight and caliper into the range reported for earlier experiments.
- Example 4 was repeated, except that pH of the slurry of pulp and alum was adjusted to 5.5 by the addition of sodium hydroxide.
- Example 4 was repeated, except that pH of the slurry of pulp and alum was adjusted to 5.8 by the addition of sodium hydroxide.
- EXAMPLE 7 Pulp similar to that used in Example 1 was suspended in distilled water at 3% consistency. Half normal hydrochloric acid was slowly added, to pH 4.5. Cf., US. Pat. No. 3,112,242 to Jones. After stirring for a few minutes a solution of papermakers alum was added to the slurry at the rate of 62.6 pounds of alum solids per ton of pulp. Stirring was continued for 5 minutes before 0.5 N sodium hydroxide was slowly added, to pH 5.5 and flocculation occurred. Cf., Curtman, L. J Qualitative Chemical Analysis; The MacMillan Company; New York, 1938; P.
- Example 7 was repeated, except that pH of the pulp slurry was adjusted to 6.0 with half normal hydrochloric acid before addition of alum. Cf., US. Pat. No. 3,112,242 to Jones.
- EXAMPLE 9 Forty grams of kraft pulp similar to that used in Example 1 were adjusted to 3% consistency with demineralized water. A solution of papermakers alum equivalent to 62.7 pounds Al (SO -14H O per ton of pulp was added, to pH 3.8. A 0.5 N solution of sodium hydroxide was used to adjust pH to 5.5 and flocculation occurred. Cf., Curtman, L. J.; Qualitative Chemical Analysis; The MacMillan Company; New York, 1938; P. 181 and Kolthoff et al.; Textbook of Quantitative Inorganic Analysis (3rd Ed); The MacMillan Company; New York, 1952; P. 318.
- handsheets were prepared and dried as before, dipped in a solution of Paper Product 2409 of such concentration as to give a size solids pickup of 8.8 pounds per ton of pulp.
- Final drying and pressing brought basis weight and caliper into the range reported for earlier examples.
- Example 9 was repeated, except that a 15-minute retention period was allowed between flocculation of alum, and dilution of slurry to handsheet-making consistency.
- EXAMPLE 1 1 Forty grams of kraft pulp similar to that used in Example 1 were adjusted to 3% consistency with demineralized water. A solution of papermakers alum equivalent to 63.0 pounds Al (SO -14H O per ton of pulp was added, to pH 4.0. The mixture was transferred to a TAPPI standard disintegrator. The disintegrator was started, and as violent agitation began, a 10% solution of sodium hydroxide was poured into the slurry in such volume as to raise pH to 5.5 and flocculation occurred. Cf, Curtman, L. J.; Qualitative Chemical Analysis; The MacMillan Company, New York, 1938; P.
- Example 11 was repeated, except that alum and size were added at the rate of 90 and 11 pounds, respectively, per ton of pulp.
- Example 11 was repeated, except that alum and size were added at the rate of and 20 pounds, respectively, per ton of pulp.
- Example 11 was repeated, except that alum and size were added at the rate of and 22.5 pounds, respectively, per ton of pulp.
- Example 11 was repeated, except that alum and size were added at the rate of 200 and 25 pounds, respectively, per ton of pulp.
- Example 12 was repeated, except that 17 pounds regular pale rosin size was used in place of pounds Paper Product 2409.
- Example 12 was repeated, except that the fiber furnish was bleached softwood sulfite pulp instead of 75% pine and 25% hardwood kraft pulp.
- Example 18 was repeated, except that the fiber furnish was unbleached pine kraft pulp instead of bleached sulfite pulp.
- EXAMPLE 20 Following standard laboratory procedure, a mixture of 45% pine and 55% hardwood kraft pulp, bleached to 85% GE. brightness, was refined in an experimental beater at 1.75% consistency to 502 Canadian Standard freeness. Forty grams (ovendry basis) of the refined pulp were suspended in distilled water at 3% consistency. Fortified size (commercially available Paper Product 2409) was added to the slurry at a rate of 30 pounds of size solids per ton of pulp. A mechanical stirrer was used to keep the slurry thoroughly mixed during the addition. Stirring was continued. After 5 minutes, papermakers alum was added at the rate of 30 pounds Al (SO l4H O per ton of pulp. Stirring was continued for 10 minutes.
- Slurry pH after the addition of alum was 4.2.
- a solution of half normal sodium hydroxide was added to pH 6.0. pH was adjusted to 5.0 by the addition of papermakers alum (5.5 pounds per ton). Stirring was continued for 1 minute. Consistency was adjusted to 0.375% with water containing enough hydrochloric acid to give pH 5.0.
- Handsheets were formed on a British sheet mold, pressed between a polished metal plate and blotters, clamped in rings, and dried in a forced-draft oven at 105 C. for 30 minutes. Basis weight and caliper averaged 100 pounds and 7.0 mils, respectively. Before testing, sheets were brought into equilibrium with the atmosphere of a room maintained at 50% relatively humidity and 73 F.
- Example 5 was repeated, except that pH of the slurry of pulp and alum was adjusted to 5.5 by the addition of ammonium hydroxide, and that the pulp was the same as that used in Example 20.
- Example 21 was repeated, except that pH of the slurry of pulp and alum was adjusted to 5.5 by the addition of eth-anolamine.
- EXAMPLE 23 Forty grams of pulp similar to that used in Example 1 were suspended in distilled water at 3% consistency. Slurry pH was adjusted to 4.5 by the slow addition of 0.5 N hydrochloric acid. After stirring for a few minutes a 0.5 N solution of sodium hydroxide was added to the slurry at the rate of 6.6 lb. of NaOH per ton of pulp (ovendry basis). After continued stirring for five minutes a solution of papermakers alum was added from a buret, to pH 5.5. Flocculation occurred. After a retention period of 20 minutes (slow agitation), water containing hydrochloric acid to give pH 5.5 was added, to sheet making consistency.
- Handsheets were prepared, pressed, and dried as in Example 1. Each sheet was weighed, dipped in a fresh solution of fortified rosin size (Paper Product 2409), blotted lightly, weighed again, and heated to incipient dryness between a polished plate and blotters on a Pasadena press at 105 C. The sized sheets were clamped in rings and dried in a forced-draft oven at 105 C. for 30 minutes. Basis weight and caliper averaged pounds and 7.0 mils, respectively. Size solids pickup was equivalent to 5.1 pounds per ton of pulp.
- fortified rosin size Paper Product 2409
- the sized sheets were clamped in rings and dried in a forced-draft oven at 105 C. for 30 minutes.
- Basis weight and caliper averaged pounds and 7.0 mils, respectively. Size solids pickup was equivalent to 5.1 pounds per ton of pulp.
- EXAMPLE 24 Forty grams of pulp similar to that used in Example 1 were suspended in distilled water at 3% consistency. Addition of a solution of sodium hydroxide equivalent to 10.7 lb. NaOH per ton of pulp raised pH to 11.2. A solution of papermakers alum (equivalent to 40.0 pounds Al (SO -l4H O per ton of pulp) was added slowly, with agitation, to pH 5.5. Flocculation followed. Stirring was continued during a 25-minute retention period before the pulp was diluted with water, at pH 5.5, and handsheets were prepared and dried as before. Each dried sheet was weighed, and dipped into a fresh solution of fortified rosin size. Sheets were blotted, weighed again, and dried as before. Size solids pickup was equivalent to 8.1 pounds per ton of pulp. Average basis weight was 100 pounds; caliper was 7.0 mils.
- EXAMPLE 25 Forty grams of kraft pulp similar to that used in Example 1 were adjusted to 3% consistency with distilled water. A 0.5 N solution of sodium hydroxide, equivalent to 18.7 lb. NaOH per ton of pulp was added to pH 11.3. After 5 minutes of stirring a solution of papermakers alum equivalent to 62.7 pounds Al (SO -14H O per tonof pulp was added to adjust pH to 5.2. Flocculation occurred. After a retention period of 25 minutes, handsheets were prepared and dried as before, dipped in a solution of Paper Product 2409 of such concentration as to give a size solids pickup of 8.8 pounds per ton of pulp. Final drying and pressing brought basis weight and caliper into the range reported for earlier experiments.
- EPQAMPLE 26 Example 25 was repeated, except that after the addition of sodium hydroxide solution equipvalent to 20.0 lb. of NaOH per ton of pulp, pH of the alkaline slurry was adjusted to 5.8 by the slow addition of a solution of papermakers alum.
- EXAMPLE 27 Forty grams of kraft pulp similar to that used in Example 1 were adpusted to 3% consistency with distilled water. A 10% solution of sodium hydroxide equivalent to 18.9 lb. NaOH per ton of pulp was added to the slurry. The mixture was transferred to a TAPPI Standard disintegrator. The disintegrator was started, and as violent agitation began a solution of papermakers alum was poured into the slurry in such volume as to lower pH to 5.5. Violent agitation was continued for a total of 30 seconds. The treated pulp was retruned to a beaker and stirred at a moderate hate for 20 minutes. Handsheets were prepared, pressed, and dried as in Example 1.
- Each dried sheet was weighed, dipped in a fresh solution of fortified size (Paper Product 2409), blotted lightly, weighed, and heated to incipient dryness between a polished plate and blotters on a Pasadena press at C.
- the sized sheets were clamped in rings and dried in a forced-draft oven at 105 C. for 30 minutes. Size solids pickup was equivalent to 12.7 pounds per ton of pulp.
- EXAMPLE 28 Forty grams of pulp similar to that used in Example 1 were adjusted to 3% consistency with distilled water. A 3 N solution of ammonium hydroxide was added to the slurry and stirred for 5 minutes. pH of the slurry at this point was 10.7. A solution of papermakers alum was slowly added to the slurry to pH 5.5. After a retention period of 25 minutes handsheets were prepared and dried as before. They were dipped in a solution of Paper Product 240 9 of such concentration as to give a 7 a size solids pickup of 8.8 pounds per ton of pulp.
- NorE.-Exa1nplcs 1 through 8 Mobile Mill pulp, 75% pine, 25% hardwood; 85% (LE. brightness; 500 Canadian standard lreeness.
- Examples 9 through 17 Mobile Mill pulp, 75% pine, 25% Hardwood; 85% G.E. brightness; 500 Canadian standard frceness.
- Examples 20 through 22 Springhill Mill pulp, 45% pine, 55% hardwood; 85% GE. brightness; 500 0.5. Ireeuess.
- Examples 23 through 28 Mobile 1111. pulp, 7.3% pine, hardwood; 85% brightness, 500 Canadian standard iroencss.
- a process for sizing paper made from wood pulp has been developed. Sizing by the present flocculated comprising a step of adding papermalt'ers alum to an alum-rosin size procedure has produced handsheets supeaqueous slurry of wood pulp in an amount sufiicient to rior in the characteristics evaluated to similar sheets prebring the pH of the aqueous slurry of wood pulp to about pared by orthodox meansat less than half the size furn- 5 and below, a step of adding a material yielding hyish cost.
- the flocculated alum-sized amount suflicient to flocculate the papcrmakers alum sheets outperformed standard sheets by an impressive without raising the pH of the aqueous slurry of the wood margin.
- a process for sizing paper made from wood pulp The data also show that the sequence of steps comcomprising a first step of adding papermakers alum to prising the method of the invention can be reversed.
- Data not shown reveal that the internal addition of part to bring the pH of the aqueous slurry of wood pulp to of the size after flocculation of alum, and part after the about 5 and below, a second step of adding a material formation and drying of the sheet results in sizing that yielding hydroxide ions to the aqueous slurry of wood compares favorably with that obtained by adding the V pulp in an amount sufiicient to flocculate the papermakcrs total amount in a simulated size press application.
- Variations in flocculation pH between 5.2 and 5.8 have 3.
- the process of claim 1 wherein the material is soresistance to penetration by hot coflee. Other characterdium hydroxide. istics were not greatly affected (Examples 5, 7, and 8); 5.
- Bleached sulfite and unbleached kraft pulps may be US, Cl, X,R
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Description
United States Patent Ofifice Patented Jan. 14, 1969 Claims ABSTRACT OF THE DISCLQSURE A process of sizing paper in which papermakers alum and a material yielding hydroxide ions (e.g., sodium hydroxide) are added to aqueous wood pulp, the pH thereof is kept at 7 or below, and rosin size is applied to the surface of paper made from the pulp.
This invention relates to the sizing of paper and to a novel method of increasing the resistance of paper to water penetration and otherwise enhancing the quality of the sizing of the paper.
This application is a continuation-in-part of copending US. Ser. No. 456,515, filed May 17, 1965, now abandoned.
US. Pat. No. 3,074,843, issued to Lagally et al. shows a process of producing paper having high dry strength and good wet strength wherein aluminum hydroxide is precipitated by mixing an aluminum-containing compound and an acid, a base, or an aluminum salt in the absence of nonaluminum-containing polyvalent anions (e.g., the sulfate ion). Optimum results were achieved at a pH within the range of 6 to 9. See, particularly, column 6, lines 29 to 32, and column 2, lines 61 to 63, of the Lagally et al. patent. Lagally et al. stress their need to be free of nonaluminum-containing polyvalent anions by calling it essential to their invention. See column 2, lines 27 and 28, of the Lagally et al. patent.
It has now been found, however, that the stated need of Lagally et al. for the attainment of strength when wet can be obviated, and that remarkable levels of sizing can be obtained concurrently with the development of strength. It has been found that, if papermakers alum is added to an aqueous wood pulp slurry until its pH is 5 and below and if a base such as sodium hydroxide is then added to the pulp and alum mixture without bringing the overall pH to 7 and above, aluminum hydroxide will precipitate in such a manner and to such a degree as to assure excellent levels of sizing once rosin size or the like is added to complete the process. It has also been found that, if these steps are reversed, i.e., if the hydroxide is added first and the alum added second, similar advantageous results are achieved. In short, then, it has been found that, if the pH of the wood pulp is attended to correctly, the presence of the non-aluminum-containing polyvalent anions of papermakers alumAl (SO .l4H Ois of little or no deleterious effect. The following examples, which describe a standard sizing method (Examples 1 and 20) and variations of the method of present invention (Examples 2 to 28, excepting 20), and tables, which compile data of tests made on products of the examples, confirm this finding:
EXAMPLE 1 Following standard laboratory procedure, a mixture of pine and 25% hardwood kraft pulp, bleached to GE. brightness, was refined in an experimental beater at 1.75% consistency to 488 Canadian Standard freeness. Forty grams (ovendry basis) of the refined pulp were suspended in distilled water at 3% consistency. Fortified size (commercially available Paper Product 2409) was added to the slurry at a rate of 30 pounds of size solids per ton of pulp. A mechanical stirrer was used to keep the slurry thoroughly mixed during the addition. Stirring was continued. After 5 minutes, papermakers alum was added at the rate of 30 pounds A'l (SO .14H O per ton of pulp. Stirring was continued for 10 minutes. Slurry pH after the addition of alum was 4.2. A solution of half normal sodium hydroxide was added to pH 6.0. pH was adjusted to 5.0 by the addition of papermakers alum (5.5 pounds per ton). Stirring was continued for 1 minute. Consistency was adjusted to 0.375% with water containing enough hydrochloric acid to give pH 5.0. Handsheets were formed on a British sheet mold, pressed between a polished metal plate and blotters, clamped in rings, and dried in a forced-draft oven at 105 C. for 30 minutes. Basis weight and caliper averaged pounds and 7.0 mils, respectively. Before testing, sheets were brought into equilibrium with the atmosphere of a room maintained at 50% relative humidity and 73 F.
EXAMPLE 2 Twenty grams of pulp similar to that used in Example 1 were suspended in distilled water at 3% consistency. Six-tenths milliliter of 0.5 N hydrochloric acid was slowly added to pH 4.5. Cf., US. Pat. No. 3,112,242 to Jones. After stirring for a few minutes, a solution of papermakers alum was added to the slurry at the rate of 20 pounds Al (S0 .14H O per ton of pulp (ovendry basis). Stirring was continued for 5 minutes, during which time pH dropped to 3.8. A solution of sodium hydroxide (0.5 N) was added from a buret, to pH 5.5 and flocculation occurred. Cf., Curtman, L. J.; Qualitative Chemical Analysis; The MacMillan Company; New York, 1938; P. 181 and Kolthoif et al.; Textbook of Quantitative Inorganic Analysis (3rd Ed.); The MacMillan Company; New York, 1952; P. 318. After a retention period of 20 minutes (slow agitation), consistency was adjusted to 0.375% with water containing enough hydrochloric acid to give pH 5.5.
Handsheets were prepared, pressed, and dried as in Example 1. Each sheet was weighed, dipped in a fresh solution of fortified rosin size (Paper Product 2409), blotted lightly, weighed again, and heated to incipient dryness between a polished plate and blotters on a Carver press at C. The sized sheets were clamped in rings and dried in a forced-draft oven at 105 C. for 30 minutes. Basis weight and caliper averaged 100 pounds and 7.0 mils, respectively. Size solids pickup was equivalent to 5.1 pounds per ton of pulp.
EXAMPLE 3 In accordance with the present invention, twenty-two grams of pulp similar to that used in Example 1 were suspended in demineralized water at 3.0% consistency. Slurry pH after thorough agitation was 6.7. Addition of a solution of alum equivalent to 40.0 pounds A12(SO4)3.14H2O per ton of pulp lowered pH to 4.1. Half normal sodium hydroxide was added slowly, with agitation, to pH 5.5 and flocculation occurred. Cf, Curtman, L. J.; Qualitative Chemical Analysis; The MacMillan Company; New York, 1938; P. 181 and Kolthoif et al.; Textbook of Quantitative Inorganic Analysis (3rd Ed); The MacMillan Company; New York, 1952; P. 318. Stirring was continued during a 25-minute retention period before the pulp was diluted with water at pH 5.5, and handsheets were prepared and dried as in Example 2. Each dried sheet was weighed, and dipped into a fresh solution of fortified rosin size. Sheets were blotted, weighed again, and dried as before. Size solids pickup was equivalent to 8.1 pounds per ton of pulp. Average basis weight was 100 pounds; caliper was 7.0 mils.
EXAMPLE 4 Twenty-two grams of kraft pulp similar to that used in Example 1 were adjusted to 3% consistency with demineralized water. After thorough mixing, pH was 6.7. A solution of papermakers alum equivalent to 62.7 pounds Al (SO -14H O per ton of pulp was added to pH 3.9. A 0.5 N solution of sodium hydroxide was used to adjust pH to 5.2 and flocculation occurred. Cf., Curtman, L. J.; Qualitative Chemical Analysis; The MacMillan Company; New York, 1938; P. 181 and Kolthotf et al.; Textbook of Quantitative Inorganic Analysis (3rd Ed); The MacMillan Company; New York, 1952; P. 318, After a retention period of 25 minutes, handsheets were prepared and dried as before, dipped in a solution of Paper Product 2409 of such concentration as to give a size solids pickup of 8.8 pounds per ton of pulp. Final drying and pressing brought basis weight and caliper into the range reported for earlier experiments.
EXAMPLE 5 Example 4 was repeated, except that pH of the slurry of pulp and alum was adjusted to 5.5 by the addition of sodium hydroxide.
EXAMPLE 6 Example 4 was repeated, except that pH of the slurry of pulp and alum was adjusted to 5.8 by the addition of sodium hydroxide.
EXAMPLE 7 Pulp similar to that used in Example 1 was suspended in distilled water at 3% consistency. Half normal hydrochloric acid was slowly added, to pH 4.5. Cf., US. Pat. No. 3,112,242 to Jones. After stirring for a few minutes a solution of papermakers alum Was added to the slurry at the rate of 62.6 pounds of alum solids per ton of pulp. Stirring was continued for 5 minutes before 0.5 N sodium hydroxide was slowly added, to pH 5.5 and flocculation occurred. Cf., Curtman, L. J Qualitative Chemical Analysis; The MacMillan Company; New York, 1938; P. 181 and Kolthotf et al.; Textbook of Quantitative Inorganic Analysis 3rd Ed); The MacMillan Company; New York, 1952; P. 318. After a retention period of minutes (slow agitation), consistency was adjusted to 0.375% with water containing enough hydrochloric acid to give pH 5.5. Handsheets were prepared as in Example 1, dipped in a solution of fortified rosin size, blotted, and dried as in earlier experiments. Size solids pickup was 8.8 pounds per ton of pulp.
4 EXAMPLE 8 Example 7 was repeated, except that pH of the pulp slurry was adjusted to 6.0 with half normal hydrochloric acid before addition of alum. Cf., US. Pat. No. 3,112,242 to Jones.
EXAMPLE 9 Forty grams of kraft pulp similar to that used in Example 1 were adjusted to 3% consistency with demineralized water. A solution of papermakers alum equivalent to 62.7 pounds Al (SO -14H O per ton of pulp was added, to pH 3.8. A 0.5 N solution of sodium hydroxide was used to adjust pH to 5.5 and flocculation occurred. Cf., Curtman, L. J.; Qualitative Chemical Analysis; The MacMillan Company; New York, 1938; P. 181 and Kolthoff et al.; Textbook of Quantitative Inorganic Analysis (3rd Ed); The MacMillan Company; New York, 1952; P. 318. After a retention period of 5 minutes, handsheets were prepared and dried as before, dipped in a solution of Paper Product 2409 of such concentration as to give a size solids pickup of 8.8 pounds per ton of pulp. Final drying and pressing brought basis weight and caliper into the range reported for earlier examples.
EXAMPLE 10 Example 9 was repeated, except that a 15-minute retention period was allowed between flocculation of alum, and dilution of slurry to handsheet-making consistency.
EXAMPLE 1 1 Forty grams of kraft pulp similar to that used in Example 1 were adjusted to 3% consistency with demineralized water. A solution of papermakers alum equivalent to 63.0 pounds Al (SO -14H O per ton of pulp was added, to pH 4.0. The mixture was transferred to a TAPPI standard disintegrator. The disintegrator was started, and as violent agitation began, a 10% solution of sodium hydroxide was poured into the slurry in such volume as to raise pH to 5.5 and flocculation occurred. Cf, Curtman, L. J.; Qualitative Chemical Analysis; The MacMillan Company, New York, 1938; P. 181 and Koltholf et al.; Textbook of Quantitative Inorganic Analysis (3rd Ed.); The Mac- Millan Company; New York, 1952; P. 318. Violent agitation was continued for a total of 30 seconds. The treated pulp was returned to a beaker and stirred at a moderate rate for 20 minutes. Handsheets were prepared, pressed, and dried as in Example 1. Each dried sheet was weighed, dipped in a fresh solution of fortified size (Paper Product 2409), blotted lightly, weighed, and heated to incipient dryness between a polished plate and blotters on a Carver press at C. The sized sheets were clamped in rings and dried in a forced-draft oven at 105 C. for 30 minutes. Size solids pickup was equivalent to 12.7 pounds per ton of pulp.
EXAMPLE 12 Example 11 was repeated, except that agitation during and after flocculation was slow.
EXAMPLE 13 Example 11 was repeated, except that alum and size were added at the rate of 90 and 11 pounds, respectively, per ton of pulp.
EXAMPLE 14 Example 11 was repeated, except that alum and size were added at the rate of and 20 pounds, respectively, per ton of pulp.
EXAMPLE 15 Example 11 was repeated, except that alum and size were added at the rate of and 22.5 pounds, respectively, per ton of pulp.
EXAMPLE 16 Example 11 was repeated, except that alum and size were added at the rate of 200 and 25 pounds, respectively, per ton of pulp.
EXAMPLE 17 Example 12 was repeated, except that 17 pounds regular pale rosin size was used in place of pounds Paper Product 2409.
EXAMPLE 18 Example 12 was repeated, except that the fiber furnish was bleached softwood sulfite pulp instead of 75% pine and 25% hardwood kraft pulp.
EXAMPLE 19 Example 18 was repeated, except that the fiber furnish was unbleached pine kraft pulp instead of bleached sulfite pulp.
EXAMPLE 20 Following standard laboratory procedure, a mixture of 45% pine and 55% hardwood kraft pulp, bleached to 85% GE. brightness, was refined in an experimental beater at 1.75% consistency to 502 Canadian Standard freeness. Forty grams (ovendry basis) of the refined pulp were suspended in distilled water at 3% consistency. Fortified size (commercially available Paper Product 2409) was added to the slurry at a rate of 30 pounds of size solids per ton of pulp. A mechanical stirrer was used to keep the slurry thoroughly mixed during the addition. Stirring was continued. After 5 minutes, papermakers alum was added at the rate of 30 pounds Al (SO l4H O per ton of pulp. Stirring was continued for 10 minutes. Slurry pH after the addition of alum was 4.2. A solution of half normal sodium hydroxide was added to pH 6.0. pH was adjusted to 5.0 by the addition of papermakers alum (5.5 pounds per ton). Stirring was continued for 1 minute. Consistency was adjusted to 0.375% with water containing enough hydrochloric acid to give pH 5.0. Handsheets were formed on a British sheet mold, pressed between a polished metal plate and blotters, clamped in rings, and dried in a forced-draft oven at 105 C. for 30 minutes. Basis weight and caliper averaged 100 pounds and 7.0 mils, respectively. Before testing, sheets were brought into equilibrium with the atmosphere of a room maintained at 50% relatively humidity and 73 F.
EXAMPLE 21 Example 5 was repeated, except that pH of the slurry of pulp and alum was adjusted to 5.5 by the addition of ammonium hydroxide, and that the pulp was the same as that used in Example 20.
EXAMPLE 22 Example 21 was repeated, except that pH of the slurry of pulp and alum was adjusted to 5.5 by the addition of eth-anolamine.
EXAMPLE 23 Forty grams of pulp similar to that used in Example 1 were suspended in distilled water at 3% consistency. Slurry pH was adjusted to 4.5 by the slow addition of 0.5 N hydrochloric acid. After stirring for a few minutes a 0.5 N solution of sodium hydroxide was added to the slurry at the rate of 6.6 lb. of NaOH per ton of pulp (ovendry basis). After continued stirring for five minutes a solution of papermakers alum was added from a buret, to pH 5.5. Flocculation occurred. After a retention period of 20 minutes (slow agitation), water containing hydrochloric acid to give pH 5.5 was added, to sheet making consistency.
Handsheets were prepared, pressed, and dried as in Example 1. Each sheet was weighed, dipped in a fresh solution of fortified rosin size (Paper Product 2409), blotted lightly, weighed again, and heated to incipient dryness between a polished plate and blotters on a Pasadena press at 105 C. The sized sheets were clamped in rings and dried in a forced-draft oven at 105 C. for 30 minutes. Basis weight and caliper averaged pounds and 7.0 mils, respectively. Size solids pickup was equivalent to 5.1 pounds per ton of pulp.
EXAMPLE 24 Forty grams of pulp similar to that used in Example 1 were suspended in distilled water at 3% consistency. Addition of a solution of sodium hydroxide equivalent to 10.7 lb. NaOH per ton of pulp raised pH to 11.2. A solution of papermakers alum (equivalent to 40.0 pounds Al (SO -l4H O per ton of pulp) was added slowly, with agitation, to pH 5.5. Flocculation followed. Stirring was continued during a 25-minute retention period before the pulp was diluted with water, at pH 5.5, and handsheets were prepared and dried as before. Each dried sheet was weighed, and dipped into a fresh solution of fortified rosin size. Sheets were blotted, weighed again, and dried as before. Size solids pickup was equivalent to 8.1 pounds per ton of pulp. Average basis weight was 100 pounds; caliper was 7.0 mils.
EXAMPLE 25 Forty grams of kraft pulp similar to that used in Example 1 were adjusted to 3% consistency with distilled water. A 0.5 N solution of sodium hydroxide, equivalent to 18.7 lb. NaOH per ton of pulp was added to pH 11.3. After 5 minutes of stirring a solution of papermakers alum equivalent to 62.7 pounds Al (SO -14H O per tonof pulp was added to adjust pH to 5.2. Flocculation occurred. After a retention period of 25 minutes, handsheets were prepared and dried as before, dipped in a solution of Paper Product 2409 of such concentration as to give a size solids pickup of 8.8 pounds per ton of pulp. Final drying and pressing brought basis weight and caliper into the range reported for earlier experiments.
EPQAMPLE 26 Example 25 was repeated, except that after the addition of sodium hydroxide solution equipvalent to 20.0 lb. of NaOH per ton of pulp, pH of the alkaline slurry was adjusted to 5.8 by the slow addition of a solution of papermakers alum.
EXAMPLE 27 Forty grams of kraft pulp similar to that used in Example 1 were adpusted to 3% consistency with distilled water. A 10% solution of sodium hydroxide equivalent to 18.9 lb. NaOH per ton of pulp was added to the slurry. The mixture was transferred to a TAPPI Standard disintegrator. The disintegrator was started, and as violent agitation began a solution of papermakers alum was poured into the slurry in such volume as to lower pH to 5.5. Violent agitation was continued for a total of 30 seconds. The treated pulp was retruned to a beaker and stirred at a moderate hate for 20 minutes. Handsheets were prepared, pressed, and dried as in Example 1. Each dried sheet was weighed, dipped in a fresh solution of fortified size (Paper Product 2409), blotted lightly, weighed, and heated to incipient dryness between a polished plate and blotters on a Pasadena press at C. The sized sheets were clamped in rings and dried in a forced-draft oven at 105 C. for 30 minutes. Size solids pickup was equivalent to 12.7 pounds per ton of pulp.
EXAMPLE 28 Forty grams of pulp similar to that used in Example 1 were adjusted to 3% consistency with distilled water. A 3 N solution of ammonium hydroxide was added to the slurry and stirred for 5 minutes. pH of the slurry at this point was 10.7. A solution of papermakers alum was slowly added to the slurry to pH 5.5. After a retention period of 25 minutes handsheets were prepared and dried as before. They were dipped in a solution of Paper Product 240 9 of such concentration as to give a 7 a size solids pickup of 8.8 pounds per ton of pulp. Final Both fortified rosin size and regular pale rosm size are pressing and drying brought basls we1ght and cahper mto compatible with the flocculated alum system (Exthe range reported for earlter experunents. ample 17).
TABLE I Cotiee Lactic acid Hercules Dry Cobb, Water Tensile Size Example number peuescope, penescope, 111k, indicator, Wet break g./sq. in. absorption, wet/dry, furnish,
minutes minutes seconds seconds percent percent dollar/ton 12.1 1.4 214 122 2.5111in 38 58.1 5.0 4. 94 24. 3 7.5 248 1226 1.9111111. 34 56. o 4. t) 1. 43 35. 8 111.5 587 12s 3.0111111- 25 47. a 5. t1 2. 34 90+ 31. s 736 14 .1 4.1111111 25 4s. 2 0. 5 3. 21 110+ 41.0 737 145 3.7 mm 25 47. 6. s 90+ 31. 0 830 142 3.1, nnn 25 4s. 2 13.1) 3. 14. 9 31 1, 514 14!; (3.8 min, 25 4s. (1 u. o 3 15. 3 33 1,177 142 8.8 mm 24 47. 7 7. 1 4c. 9 40 1, 005 148 12.5 mm 24 40. 2 o. 4 3. 18. 2 30 702 144 11.7 min 25 4o. 9 7. 0 3. 110+ 23. 8 1, 182 142 12.2 min. 26 47.7 7. 4 1. 21. 0 1G. 8 J34 140 1 8 111111. 26 49. 4 7.0 3. 90+ .59 0 1,165 144 1o 0 min 24 47. s s. 2 4. 4 90+ 90+ 1, 704 170 31+ l1r 23 45.5 10.19 8. 90+ 1,530 1615 24+ hr, 24 44. 7 11. J 9. 90+ 10+ 1,453 155 "4+ hr 24 45. 7 12. 7 10. 1D. 3 90+ 1,444 151 131 mm 25 49. 2 8. 4 4. 90+ 23. 4 1,172 140 5 4 mm 22 3.1 7. 7 4. 90+ 71.0 5, 000+ 156 47 7 min 27 53. 7 7. 4 4. u. 2 1. 5 140 2.7 min 38 113.2 4. 3 4. 1 61.2 16. 2 7 141 4.8 min. 2t] 50. 2 5. 7 3. 22.0 20.8 1, 419 172 3.4 min 28 71.0 5. 8 12. 18.1 15. 5 3 209 1 0 H1111 25 50.8 7. 5 1. 36.8 38. 5 1, 437 219 3 1 mm. 25 48. 0 8. 8 2. 90+ 42. 2 1, 314 213 4 6 111111 24 48. 4 5 .9 3. 43. 5 37. 5 1, 501 221 3.2 min. 24 47. 2 l). 2 3. 50.1 75. 2 1, 421 219 6.5 min. 24 46. 7 10.7 4. 23. 3 22.1 1, 446 191 6.5 min 24 48. 6 .t. 1 2.
NorE.-Exa1nplcs 1 through 8: Mobile Mill pulp, 75% pine, 25% hardwood; 85% (LE. brightness; 500 Canadian standard lreeness. Examples 9 through 17: Mobile Mill pulp, 75% pine, 25% Hardwood; 85% G.E. brightness; 500 Canadian standard frceness. Examples 20 through 22: Springhill Mill pulp, 45% pine, 55% hardwood; 85% GE. brightness; 500 0.5. Ireeuess. Examples 23 through 28: Mobile 1111. pulp, 7.3% pine, hardwood; 85% brightness, 500 Canadian standard iroencss.
The data presented in the above table suggest that a What is claimed: unique and remarkably effective method of sizing paper 1. A process for sizing paper made from wood pulp has been developed. Sizing by the present flocculated comprising a step of adding papermalt'ers alum to an alum-rosin size procedure has produced handsheets supeaqueous slurry of wood pulp in an amount sufiicient to rior in the characteristics evaluated to similar sheets prebring the pH of the aqueous slurry of wood pulp to about pared by orthodox meansat less than half the size furn- 5 and below, a step of adding a material yielding hyish cost. At costs approaching those required by a standdroxide ions to the aqueous slurry of Wood pulp in an ard laboratory procedure, the flocculated alum-sized amount suflicient to flocculate the papcrmakers alum sheets outperformed standard sheets by an impressive without raising the pH of the aqueous slurry of the wood margin. Increasing the alum and size content of the stock 40 to about 7 and above, and a step of adding a rosin size improved sizing up to a total size furnish cost at current to the wood pulp after it is transformed from the aqueous prices of approximately $8 per ton of pulp, at which level slurry into a web of paper. \6l' V hard sizing was realized. 2. A process for sizing paper made from wood pulp The data also show that the sequence of steps comcomprising a first step of adding papermakers alum to prising the method of the invention can be reversed. an aqueous slurry of wood pulp in an amount sufficient Data not shown reveal that the internal addition of part to bring the pH of the aqueous slurry of wood pulp to of the size after flocculation of alum, and part after the about 5 and below, a second step of adding a material formation and drying of the sheet results in sizing that yielding hydroxide ions to the aqueous slurry of wood compares favorably with that obtained by adding the V pulp in an amount sufiicient to flocculate the papermakcrs total amount in a simulated size press application. Little 5U alum without raising the pH of the aqueous slurry of the benefit is realized by adding all the size internally. Wood to about 7 and above, and a third step of adding The following additional observations are worthy of a rosin size to the wood pulp after it is transformed from note: the aqueous slurry into a web of paper.
Variations in flocculation pH between 5.2 and 5.8 have 3. The process of claim 1 wherein the amount of paperlittle influence on sizing (Examples 4, 5, and 6, Table I); makers alum added to the aqueous slurry of wood pulp Prc-alum adjustment of pH to 4.5 and 6.0 improved is sufiicient to bring the pH thereof to about 4 and below. resistance to penetration by ink, but was damaging to 4. The process of claim 1 wherein the material is soresistance to penetration by hot coflee. Other characterdium hydroxide. istics were not greatly affected (Examples 5, 7, and 8); 5. The process of claim 1 wherein a portion of the Extended ret ntion der ild agitation follQwjng rosin size is added to the aqueous slurry of the wood pulp. flocculation improves resistance to hot coflee (Examples 5, 9, and 10). A 20-minute retention period is satisfac- References Cit d tory;
Violent agitation during and immediately after floc- H UNITED STATES PATENTS culation improves sizing (Examples 11 and 12);
Sizing appears to reach a maximum at a size furnish 1,663,976 3/1928 De Cew 162-180 cost at current prices between $8 and $9 per ton: wet/dry 1,753,775 4/1930 De Cew 162-480 tensile increased progressively as size furnish cost at currflgnt prices approached p ton (Examples 13, 14, s. LEON BASHORE Primary Emmi/1w 1 and 16); t
Bleached sulfite and unbleached kraft pulps may be US, Cl, X,R
sized as effectively with flocculated alum-rosin size as bleached kraft pulps (Examples 18 and 19); and, 162-181, 183,
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US71116668A | 1968-03-07 | 1968-03-07 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3421976A true US3421976A (en) | 1969-01-14 |
Family
ID=24857021
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US711166A Expired - Lifetime US3421976A (en) | 1968-03-07 | 1968-03-07 | Process of rosin sizing paper |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US3421976A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3511630A (en) * | 1967-05-09 | 1970-05-12 | Corning Glass Works | Glass melting and refining furnace with glass level control means |
| US3540980A (en) * | 1968-10-30 | 1970-11-17 | Int Paper Co | Process of rosin sizing paper |
| EP0005419A1 (en) * | 1978-05-03 | 1979-11-14 | Boliden Aktiebolag | Aluminium sulphate compositions containing polynuclear complexes and a method of producing the same and the use thereof |
| US4333795A (en) * | 1979-05-23 | 1982-06-08 | Tenneco Chemicals, Inc. | Chemical compositions useful as paper sizing agents and method of making same |
| US6027611A (en) * | 1996-04-26 | 2000-02-22 | Kimberly-Clark Worldwide, Inc. | Facial tissue with reduced moisture penetration |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1663976A (en) * | 1926-09-22 | 1928-03-27 | Cew Judson A De | Method of sizing paper |
| US1753775A (en) * | 1929-05-24 | 1930-04-08 | Process Engineers Inc | Method of sizing paper pulp |
-
1968
- 1968-03-07 US US711166A patent/US3421976A/en not_active Expired - Lifetime
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1663976A (en) * | 1926-09-22 | 1928-03-27 | Cew Judson A De | Method of sizing paper |
| US1753775A (en) * | 1929-05-24 | 1930-04-08 | Process Engineers Inc | Method of sizing paper pulp |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3511630A (en) * | 1967-05-09 | 1970-05-12 | Corning Glass Works | Glass melting and refining furnace with glass level control means |
| US3540980A (en) * | 1968-10-30 | 1970-11-17 | Int Paper Co | Process of rosin sizing paper |
| EP0005419A1 (en) * | 1978-05-03 | 1979-11-14 | Boliden Aktiebolag | Aluminium sulphate compositions containing polynuclear complexes and a method of producing the same and the use thereof |
| US4333795A (en) * | 1979-05-23 | 1982-06-08 | Tenneco Chemicals, Inc. | Chemical compositions useful as paper sizing agents and method of making same |
| US6027611A (en) * | 1996-04-26 | 2000-02-22 | Kimberly-Clark Worldwide, Inc. | Facial tissue with reduced moisture penetration |
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