US2622960A - Glyoxal treatment of absorbent paper to improve wet strength - Google Patents

Glyoxal treatment of absorbent paper to improve wet strength Download PDF

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US2622960A
US2622960A US15275A US1527548A US2622960A US 2622960 A US2622960 A US 2622960A US 15275 A US15275 A US 15275A US 1527548 A US1527548 A US 1527548A US 2622960 A US2622960 A US 2622960A
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sheet
glyoxal
paper
wet strength
absorbent paper
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US15275A
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Walter E Woods
Schenck Willard Allan
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A P W Products Co Inc
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    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/03Non-macromolecular organic compounds
    • D21H17/05Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
    • D21H17/06Alcohols; Phenols; Ethers; Aldehydes; Ketones; Acetals; Ketals
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S8/00Bleaching and dyeing; fluid treatment and chemical modification of textiles and fibers
    • Y10S8/17Glyoxal and polyaldehyde treatment of textiles

Definitions

  • This invention relates to the production of wet-strengthened absorbent products of unwoven, felted cellulose fibers and more particularly to a method of treating an absorbent paper to produce a product having relatively high wet and dry strengths, as well as good moisture absorbing properties and resistance to linting.
  • the treating agents proposed have been acid media'that tended to corrode the paper-making equipment or to decrease the strength of the cellulose fibers or both.
  • the nature of the wet strengthening process and the reagents used have been such that the resulting product could not be readily disintegrated by alkalis, and thus effective reuse of the broke was precluded.
  • the glyoxal used in carrying out the present process may be either the pure compound or the technical grade. However, where the technical grade is used it is commonly quite strongly acid, and hence before a solution of technical grade glyoxal is applied to the paper its acidity is preferably reduced by addition of sufiicient alkali to produce an approximately neutral solution.
  • the pH of a solution of technical grade glyoxal may be adjusted with a suitable alkali, such as sodium hydroxide, to a pH between about 4.0 and 8.0.
  • the absorbent paper after the application of the aqueous glyoxal solution thereto, be heated to a temperature sufficient to cause the glyoxal to react with the cellulose of the paper to produce the desired degree of wet-strengthening.
  • the temperature used in the present process is higher than that used in certain prior processes which depend for their wet strengthening effect upon a reaction between glyoxal and another reagent capable of condensing with the glyoxal to produce a water-resistant condensation product.
  • the treated paper is preferably heated for a period of time sufficient to reduce the moisture content to say 3% to 7% and to a temperature of not less than about 212 F. While the upper temperature limit is not particularly critical it should, of course, be below the temperature which produces decomposition or excessive dehydration of the paper. In general, the temperatures ordinarily used at the drying end of a paper-making machine are suitable for use in the present process.
  • a 45 lb. basis sheet was prepared containing approximately 50% round wood and 50% unbleached sulphite pulp. The sheet was pressed and dried before application of the treating agent thereto.
  • the sheet was completely immersed for approximately 20 seconds in an aqueous solution of a commercial grade of glyoxal containing 1.6 ml. of the glyoxal, 29.1 ml. of 0.05 normal sodium hydroxide, and 69.3 grams of water, the pH of this solution being about 7.5.
  • the sheet appeared to be completely saturated at the end of 20 seconds and was removed from the solution, placed between blotters, and pressed for one minute at 120 lbs. persq. in. pressure. It was found that this manner of pressing reduced the moisture content of the sheet to about 50%, based on the air-dry weight of the sheet.
  • the sheet was dried for seven minutes on a drier whose surface temperature was 240 F.
  • this sheet showed a dry tensile strength of 13.7 lbs/in. and a wet strength of 2.49 lbs/in.
  • the ratio of wet strength to dry strength was 18.3 (.183 100) which is about two and one-half times as great as the corresponding ratio for this paper when untreated.
  • the concentration of glyoxal in the treating solution may be varied within relatively wide limits. It has been found that the improvement in wet strength depends primarily upon the amount of glyoxal retained in the paper, rather than upon the concentration of the treating solution. However, there does not appear to be any selective absorption of the glyoxal from the solution, nd hence the amount of glyoxal retained in the paper before drying depends upon the amount of solution associated with the paper after it has been pressed or squeezed, and upon the concentration a of the glyoxal in the solution associated with the paper after it has been squeezed. In general, a
  • glyoxal such that between 0.3 and 3.0% of glyoxal, based on the dry weight of the sheet, is retained on the sheet.
  • the improvement in wet strength appears to be an approximately linear function of the amount of glyoxal applied. It has been found that about 10% to 20% of the glyoxal is lost during drying 36 depending on the drying temperature, and hence the amount of glyoxal applied from solution should be somewhat greater than the indicated percentage to provide for retention of 0.3 to 3% on the paper after drying.
  • Quantities of glyoxal 40 less than 0.3% and greater than 3% may be used in particular cases, although where less than 0.3% is used the improvement in wet strength is ordinarily relatively slight, and in cases where more than 3% is used the additional increase in wet strength may not be economically worthwhile.
  • the desired concentration of glyoxal in the sheet may be achieved within limits by varying either the proportion of solution expressed course, be understood that the solution may be applied in other ways than by saturating the sheet, as for example, by spraying a controlled quantity of the solution onto the sheet.
  • the treated paper be heated to a temperature sufiicient to cause the glyoxal to react with the cellulose of the paper.
  • the drying is preferably effected by heating the sheet to a temperature of 240 F. to 250 F. with a drying period of about 15 to 60 seconds.
  • the treated sheet should be heated to a temperature of at least 212 F., since the improvement in wet strength is significantly greater when such temperatures are used than it is when relatively lower temperatures are used.
  • The-effectof the present process upon the absorbency of the treated paper ismore favorable than thatof'certain prior processes.
  • all processes for wet-strengthening paper decrease the absorbency of the paper in some degree.
  • the absorbency of thetreated paper continues to decrease .as..a function of time until at the end of a period .of'months the absorbency has dropped to the: point where thepaperissubstantially useless for? its. intended" purpose.
  • the present process isused; on the: other'hand, there is an initial relatively small decrease in absorbency duringth'e first week or two after treatment, and thereafter'there appears to be no further material decre'ase'in absorbency.
  • an absorbent paper of a small quantity of an aqueous solution of a solute consisting essentially of glyoxal produces a striking improvement in the wet strength of the paper.
  • the treating solution may be applied in any suitable and convenient manner, such as by dipping the paper in a body of the solution or by spraying the solution onto the paper. Since the solution is approximately neutral, it does not corrode or otherwise damage the paper-making machinery or tender the cellulose fibers. The absorbency of the paper is more nearly preserved and the nature of the process is such that any broke that is formed during the paper-making process can be readily and efiectively reused.
  • the process of producing an absorbent paper having improved wet strength comprising the steps of applying to a preformed sheet of ab sorbent paper an aqueous solution containing glyoxal as its sole essential active ingredient to deposit on said sheet a quantity of glyoxal equal to between 0.3% and 3% by weight of said sheet, and heating said sheet to cause said glyoxal to react with the cellulose of said paper to improve the wet strength of said sheet.
  • the process of producing an absorbent paper having improved wet strength comprising the steps of; applying to a preformed sheet of absorbent paper a treating agent which is an aqueous solution containing glyoxal as its sole essential active ingredient, and heating said sheet to a temperature between 212 F. and the decomposition temperature of said sheet to cause said glyoxal to react with the cellulose of said paper to improve the wet strength of said sheet.
  • a treating agent which is an aqueous solution containing glyoxal as its sole essential active ingredient
  • said solution having apH of at least-4.0, and heating said sheet-to a temperature between 212 F. and the decomposition temperature of said sheet to cause said glyoxal to react with the cellulose of said paper to improve the wet strength of said sheet.
  • the process of producing an absorbent paper having improved wet strength comprising the steps of; dipping a preformed sheet of absorbent paper into an aqueous solution containing between 0.1% and 5% by weight of glyoxal as its sole essential active ingredient and having a pH of at least 4.0, squeezing excess solution from said sheet, and heating said sheet to a temperature between 212 F. and the decomposition temperature of said sheet to cause said glyoxal to react with the cellulose of said paper to improve the wet strength of said sheet.
  • the process of producing an absorbent paper having improved wet strength comprising the steps of; applying to a preformed sheet of absorbent paper a treating agent which is an aqueous soiution containing glyoxal as its sole essential active ingredient, said solution having a pH between 4.0 and 8.0 and a glyoxal content between 0.1% and 5.0% by weight, and drying said sheet by heating it for between 15 and seconds to a final temperature of about 250 F. to cause said glyoxal to react with the cellulose of said paper to improve the wet strength of said sheet.
  • a treating agent which is an aqueous soiution containing glyoxal as its sole essential active ingredient, said solution having a pH between 4.0 and 8.0 and a glyoxal content between 0.1% and 5.0% by weight
  • a felted sheet of absorbent paper having a high wet strength resulting from the application thereto of a treating agent which is an aqueous solution containing glyoxal as its sole essential active ingredient and having a pH between 4.0 and 8.0 to deposit in said sheet a quantity of glyoxal equal to between 0.3% and 3% by weight of said sheet, and the subsequent drying of said sheet at a temperature between 212 F. and the decomposition temperature of said sheet to cause said glyoxal to react with the cellulose of said paper and thereby produce said improvement in the wet strength of said sheet.
  • a treating agent which is an aqueous solution containing glyoxal as its sole essential active ingredient and having a pH between 4.0 and 8.0 to deposit in said sheet a quantity of glyoxal equal to between 0.3% and 3% by weight of said sheet
  • the process of producing an absorbent paper having improved wet strength comprising the steps of applying to a preformed sheet of absorbent paper a treating agent which is an aqueous solution containing from 0.1% to 5% by weight of glyoxal as its sole essential active ingredient and having a pH of at least 4.0, and heating said sheet to a temperature between 212 and the decomposition temperature of said sheet to cause said glyoxal to react with the cellulose of said paper to improve the wet strength of said sheet.
  • a treating agent which is an aqueous solution containing from 0.1% to 5% by weight of glyoxal as its sole essential active ingredient and having a pH of at least 4.0
  • the process of producing an absorbent paper having improved wet strength comprising the steps of applying to a preformed sheet of absorbent paper a treating agent which is an aqueous solution containing from 0.1% to 5% by weight of glyoxal as its sole essential active ingredient and having a pH between 4.0 and 8.0, and heating said sheet to a temperature between 212 F. and the decomposition temperature of said sheet to cause said glyoxal to react with the cellulose of said paper to improve the wet strength of said paper.
  • a treating agent which is an aqueous solution containing from 0.1% to 5% by weight of glyoxal as its sole essential active ingredient and having a pH between 4.0 and 8.0

Description

Patented Dec. 23, 1952 UNITED STATES PATENT OFFICE GLYOXAL TREATMENT OF ABSORBENT PAPER TO IMPROVE WET STRENGTH No Drawing. Application March 16, 1948, Serial No. 15,275
10 Claims.
This invention relates to the production of wet-strengthened absorbent products of unwoven, felted cellulose fibers and more particularly to a method of treating an absorbent paper to produce a product having relatively high wet and dry strengths, as well as good moisture absorbing properties and resistance to linting. This application is a continuation-in-part of our prior application Serial No. 561,506, filed November 1, 1944, now abandoned.
One of the principal problems encountered in the manufacture of absorbent papers, such as paper toweling, absorbent tissue, paper diapers and the like, arises out of the fact that such papers when wet normally possess relatively little strength, and hence tear or rupture easily. Numerous efiorts have been made to overcome this difiiculty and various substances have been proposed for improving the wet strength of absorbent papers, either by incorporation of the substance in the paper stock during its preparation or by its application to preformed sheets. In general, these prior processes hav been open to one or more of several objections. Thus in some cases they have excessively decreased the absorbency or adversely affected other desirable properties of the sheet. In other cases they have been excessively expensive. In still other cases the treating agents proposed have been acid media'that tended to corrode the paper-making equipment or to decrease the strength of the cellulose fibers or both. In other cases the nature of the wet strengthening process and the reagents used have been such that the resulting product could not be readily disintegrated by alkalis, and thus effective reuse of the broke was precluded.
It is accordingly an object of the invention to provide a process for improving the wet strength of an absorbent pa er with a minimum decrease in the absorbency thereof. It is a further object of the invention to provide a process of this type which uses reagents that do not adversely eifect the paper-making machinery or tender the cellulose fibers. It is still another object of the invention to provide a wet-strengthened absorbentpaper that is capable of being readily disintegrated by alkalis for re-use in the paper-making process. Other objects of the invention will be'in part obvious and-in part pointed out hereafter.
We have discovered that the foregoing objects can beachieved by applying to a preformed absorbent'sheet of paper an aqueous solution of a solute consisting essentially of glyoxaLand then heating the treated sheet to a temperature surficient to cause the glyoxal to react with the cellulose. We have found that, contrary to certain prior teachings, it is not necessary to utilize a mixture of glyoxal and another reagent capable of reacting with the glyoxal to produce wet strengthening of the paper, but on the contrary that by following the procedure described hereafter, the desired wet strengthening of the paper may be achieved by employing an aqueous solution of glyoxal wherein glyoxal alone is the agent producing wet strength.
The glyoxal used in carrying out the present process may be either the pure compound or the technical grade. However, where the technical grade is used it is commonly quite strongly acid, and hence before a solution of technical grade glyoxal is applied to the paper its acidity is preferably reduced by addition of sufiicient alkali to produce an approximately neutral solution. The pH of a solution of technical grade glyoxal may be adjusted with a suitable alkali, such as sodium hydroxide, to a pH between about 4.0 and 8.0.
It has been found to be important that the absorbent paper, after the application of the aqueous glyoxal solution thereto, be heated to a temperature sufficient to cause the glyoxal to react with the cellulose of the paper to produce the desired degree of wet-strengthening. In general, the temperature used in the present process is higher than that used in certain prior processes which depend for their wet strengthening effect upon a reaction between glyoxal and another reagent capable of condensing with the glyoxal to produce a water-resistant condensation product. Thus in the present process the treated paper is preferably heated for a period of time sufficient to reduce the moisture content to say 3% to 7% and to a temperature of not less than about 212 F. While the upper temperature limit is not particularly critical it should, of course, be below the temperature which produces decomposition or excessive dehydration of the paper. In general, the temperatures ordinarily used at the drying end of a paper-making machine are suitable for use in the present process.
Our experiments indicate that glyoxal is unique in its capacity to increase the wet strength of absorbent papers. The unique and unexpected efficacy of glyoxal for this purpose and the failure of chemically related compounds to give a comparable result under the same conditions, is
brought out by the data given in Tables I and II below. In the experiments which form the basis of Table I, preformed sheets of absorbent paper were immersed in aqueous solutions containing about 1% by weight of the treating agent and were squeezed to remove excess solution, after which they were dried on a drier whose surface temperature was 240 F. In each case the dry and wet strengths of the sheet were determined by the well-known Schopper tensile test. The data given in Table I represent average values obtained by treating several samples with each treating agent.
The data given in Table II were obtained using the same procedure as in Table I, but the paper used in the second set of tests had a greater initial tensile strength and therefore the data of Table I cannot be directly compared with the data of Table II.
Table I Dry Tensile Wet Tensile Ratio: Treating Agent Stren th, Strength, fitxloo lbs. in. lbs/in. dry
Untreated..." l2. 9 0. 99 7. 65 Glyoxalic acid. 12. 6 0. 72 5. 7 Glycollic acid..- 12.8 0. 56 4. 4 Glyoxal l3. 7 2. 43 17. 7
Table II Dry Tensile Wet Tensile Ratio: Treating Agent Strength, Strength, EXIOO lbs/in. lbs/m. dry
Untreated l9. 5 2 2 ll. 3 Benzil a.! 2% Meth lglyox Form ldehyde 17. 9 1 3 7. 3 Glyoxal 18.1 8 1 4t 8 From the foregoing tables it is apparent that such substances as formaldehyde, glyoxalic acid, glycollic acid, methylglyoxal and benzil, when used under the same conditions as glyoxal, either do not increase the ratio of wet strength to dry strength at all or increase it only very slightly, whereas when glyoxal is used the wet strengthdry strength ratio is increased between twoand four-fold. Thus glyoxal is strikingly superior to these other substances in improving the wet strength of absorbent papers,
In order to point out more fully the nature of the present invention, the following specific example is given of an illustrative procedure that may be used in carrying out the invention:
A 45 lb. basis sheet was prepared containing approximately 50% round wood and 50% unbleached sulphite pulp. The sheet was pressed and dried before application of the treating agent thereto.
After drying, the sheet was completely immersed for approximately 20 seconds in an aqueous solution of a commercial grade of glyoxal containing 1.6 ml. of the glyoxal, 29.1 ml. of 0.05 normal sodium hydroxide, and 69.3 grams of water, the pH of this solution being about 7.5. The sheet appeared to be completely saturated at the end of 20 seconds and was removed from the solution, placed between blotters, and pressed for one minute at 120 lbs. persq. in. pressure. It was found that this manner of pressing reduced the moisture content of the sheet to about 50%, based on the air-dry weight of the sheet. After the excess solution had been expressed in this manner, the sheet was dried for seven minutes on a drier whose surface temperature was 240 F. When tested by the Schopper tensile test, this sheet showed a dry tensile strength of 13.7 lbs/in. and a wet strength of 2.49 lbs/in. Thus the ratio of wet strength to dry strength was 18.3 (.183 100) which is about two and one-half times as great as the corresponding ratio for this paper when untreated.
It is of course to be understood that the foregoing example is illustrative and that the various operating conditions set forth may be modified 10 within the scope of the invention. For example,
the concentration of glyoxal in the treating solution may be varied within relatively wide limits. It has been found that the improvement in wet strength depends primarily upon the amount of glyoxal retained in the paper, rather than upon the concentration of the treating solution. However, there does not appear to be any selective absorption of the glyoxal from the solution, nd hence the amount of glyoxal retained in the paper before drying depends upon the amount of solution associated with the paper after it has been pressed or squeezed, and upon the concentration a of the glyoxal in the solution associated with the paper after it has been squeezed. In general, a
useful degree of improvement in wet strength may be achieved by applying to the sheet a quantity of glyoxal such that between 0.3 and 3.0% of glyoxal, based on the dry weight of the sheet, is retained on the sheet. Within this range, and for relatively constant drying conditions, the improvement in wet strength appears to be an approximately linear function of the amount of glyoxal applied. It has been found that about 10% to 20% of the glyoxal is lost during drying 36 depending on the drying temperature, and hence the amount of glyoxal applied from solution should be somewhat greater than the indicated percentage to provide for retention of 0.3 to 3% on the paper after drying. Quantities of glyoxal 40 less than 0.3% and greater than 3% may be used in particular cases, although where less than 0.3% is used the improvement in wet strength is ordinarily relatively slight, and in cases where more than 3% is used the additional increase in wet strength may not be economically worthwhile.
In cases where the solution is applied by saturating the sheet and then expressing the excess solution, the desired concentration of glyoxal in the sheet may be achieved within limits by varying either the proportion of solution expressed course, be understood that the solution may be applied in other ways than by saturating the sheet, as for example, by spraying a controlled quantity of the solution onto the sheet.
As pointed out above, since in the present process glyoxal is used in the absence of any added reagent capable of condensing therewith, it is important that the treated paper be heated to a temperature sufiicient to cause the glyoxal to react with the cellulose of the paper. The drying is preferably effected by heating the sheet to a temperature of 240 F. to 250 F. with a drying period of about 15 to 60 seconds. As indicated above, the treated sheet should be heated to a temperature of at least 212 F., since the improvement in wet strength is significantly greater when such temperatures are used than it is when relatively lower temperatures are used.
The use of glyoxal in accordance with the present process appears to improve the wet 7 strength of papers made from all different types 5' of pulps. Our tests have shown significant increases in :the wet strength of. papers. prepared from both bleached and unbleachedsulphiteand kraft pulps, bleachedv soda,.alpha, and ground wood pulps. The improvement in the wet strength of papers prepared from groundwood pulps is particularly striking.
The-effectof the present process upon the absorbency of the treated paper ismore favorable than thatof'certain prior processes. In general, all processes for wet-strengthening paper decrease the absorbency of the paper in some degree. In thecase of many-of the prior processes, the absorbency of thetreated paper continues to decrease .as..a function of time until at the end of a period .of'months the absorbency has dropped to the: point where thepaperissubstantially useless for? its. intended" purpose. Where the present process isused; on the: other'hand, there is an initial relatively small decrease in absorbency duringth'e first week or two after treatment, and thereafter'there appears to be no further material decre'ase'in absorbency.
Our tests have further shown that the Wet strength of paper treated by the present process improves over a period of time. Also the nature of the treated product is such that it is capable of being disintegrated by strong alkali so that the broke normally accumulating as an incident of the paper-making process can be readily disintegrated and reprocessed.
From the foregoing description it is apparent that the present process is capable of achieving the several objects set forth above. The application to an absorbent paper of a small quantity of an aqueous solution of a solute consisting essentially of glyoxal produces a striking improvement in the wet strength of the paper. The treating solution may be applied in any suitable and convenient manner, such as by dipping the paper in a body of the solution or by spraying the solution onto the paper. Since the solution is approximately neutral, it does not corrode or otherwise damage the paper-making machinery or tender the cellulose fibers. The absorbency of the paper is more nearly preserved and the nature of the process is such that any broke that is formed during the paper-making process can be readily and efiectively reused.
We claim:
1. The process of producing an absorbent paper having improved wet strength, comprising the steps of applying to a preformed sheet of ab sorbent paper an aqueous solution containing glyoxal as its sole essential active ingredient to deposit on said sheet a quantity of glyoxal equal to between 0.3% and 3% by weight of said sheet, and heating said sheet to cause said glyoxal to react with the cellulose of said paper to improve the wet strength of said sheet.
2. The process of producing an absorbent paper having improved wet strength, comprising the steps of; applying to a preformed sheet of absorbent paper a treating agent which is an aqueous solution containing glyoxal as its sole essential active ingredient, and heating said sheet to a temperature between 212 F. and the decomposition temperature of said sheet to cause said glyoxal to react with the cellulose of said paper to improve the wet strength of said sheet.
3. The process of producing an absorbent paper having improved wet strength, comprising the steps of; applying to a preformed sheet of absorbent paper an aqueous solution containing glyoxal as its sole essential active ingredient to deposit on said sheet a quantity of "glyoxaliequalfto between 0.3% and 3% by weightof said sheet,
said solution having apH of at least-4.0, and heating said sheet-to a temperature between 212 F. and the decomposition temperature of said sheet to cause said glyoxal to react with the cellulose of said paper to improve the wet strength of said sheet.
4. The process of producing an absorbent paper having improved wet strength, comprising the steps of; spraying on a preformed sheet of absorbent paper an aqueous solution containing glyoxal as its sole essential active'ingredientand having a pH. of at least 4.0 to deposit in said.
sheet a quantity of glyoxal equal to between 0.3
and 3 by weight of said sheet, and heating said:
sheet to a temperature between 212? F. and the decomposition temperature of said sheetto'cause said glyoxal to react with the cellulose ofsaid paper to improve the wet strength of said sheet.
5. The process of producing an absorbent paper having improved wet strength, comprising the steps of; dipping a preformed sheet of absorbent paper into an aqueous solution containing between 0.1% and 5% by weight of glyoxal as its sole essential active ingredient and having a pH of at least 4.0, squeezing excess solution from said sheet, and heating said sheet to a temperature between 212 F. and the decomposition temperature of said sheet to cause said glyoxal to react with the cellulose of said paper to improve the wet strength of said sheet.
6. The process of producing an absorbent paper having improved wet strength, comprising the steps of; applying to a preformed sheet of absorbent paper a treating agent which is an aqueous soiution containing glyoxal as its sole essential active ingredient, said solution having a pH between 4.0 and 8.0 and a glyoxal content between 0.1% and 5.0% by weight, and drying said sheet by heating it for between 15 and seconds to a final temperature of about 250 F. to cause said glyoxal to react with the cellulose of said paper to improve the wet strength of said sheet.
7. As a new article of manufacture, a felted sheet of absorbent paper having a high wet strength resulting from the application thereto of a treating agent which is an aqueous solution containing glyoxal as its sole essential active ingredient and having a pH between 4.0 and 8.0 to deposit in said sheet a quantity of glyoxal equal to between 0.3% and 3% by weight of said sheet, and the subsequent drying of said sheet at a temperature between 212 F. and the decomposition temperature of said sheet to cause said glyoxal to react with the cellulose of said paper and thereby produce said improvement in the wet strength of said sheet.
8. The process of producing an absorbent paper having improved wet strength comprising the steps of applying to a preformed sheet of absorbent paper a treating agent which is an aqueous solution containing from 0.1% to 5% by weight of glyoxal as its sole essential active ingredient and having a pH of at least 4.0, and heating said sheet to a temperature between 212 and the decomposition temperature of said sheet to cause said glyoxal to react with the cellulose of said paper to improve the wet strength of said sheet.
9. The process of producing an absorbent paper having improved wet strength comprising the steps of applying to a preformed sheet of absorbent paper a treating agent which is an aqueous solution containing from 0.1% to 5% by weight of glyoxal as its sole essential active ingredient and having a pH between 4.0 and 8.0, and heating said sheet to a temperature between 212 F. and the decomposition temperature of said sheet to cause said glyoxal to react with the cellulose of said paper to improve the wet strength of said paper.
10. The process of producing an absorbent paper having improved wet strength comprising the steps of applying to a preformed sheet of absorbent paper a treating agent which is an approximately neutral aqueous solution containing from 0.1% to 5% by weight of glyoxal as its sole active ingredient, and heating said sheet to 15 WALTER E. WOODS. ILLARD ALLAN SCHENCK.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 1,546,211 Dreyfus July 14, 1925 1,816,973 Kantorowicz Aug. 4, 1931 1,857,263 Sponsel et al. May 10, 1932 2,203,492 Evans June 4, 1940 2,285,490 Broderick June 9, 1942 2,322,888 Schwartz June 29, 1943 2,436,076 Pfefier et a1 Feb. 17, 1948 FOREIGN PATENTS Number Country Date 317,085 Great Britain Dec. .8, 1930 439,294 Great Britain Dec. 4, 1935 460,201 Great Britain Jan. 22, 1937 484,691 Great Britain Spec. not accepted,
published 1938. 502,724 Great Britain Mar. 21, 1939 547,846 Great Britain Sept. 15, 1942

Claims (1)

1. THE PROCESS OF PRODUCING AN ABSORBENT PAPER HAVING IMPROVED WET STRENGTH, COMPRISING THE STEPS; APPLYING TO A PREFORMED SHEET OF ABSORBENT PAPER AN AQUEOUS SOLUTION CONTAINING GLYOXAL AS ITS SOLE ESSENTIAL ACTIVE INGREDIENT TO DEPOSIT ON SAID SHEET A QUANTITY OF GLYOXAL EQUAL TO BETWEEN 0.3% AND 3% BY WEIGHT OF SAID SHEET, AND HEATING SAID SHEET TO CAUSE SAID GLYOXAL TO REACT WITH THE CELLULOSE OF SAID PAPER TO IMPROVE THE WET STRENGTH OF SAID SHEET.
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Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2816833A (en) * 1954-06-22 1957-12-17 Synvar Corp Wet strength paper
US2869973A (en) * 1954-08-25 1959-01-20 Du Pont Synthetic paper sheet of chemically bonded synthetic polymer fibers and process of making the same
US3096228A (en) * 1961-01-09 1963-07-02 Kimberly Clark Co Manufacture of cellulosic product
DE1260959B (en) * 1963-01-09 1968-02-08 Nobel Bozel Method for stiffening the corrugations of corrugated cardboard
US3395072A (en) * 1964-05-13 1968-07-30 Nobel Bozel Paper coating compositions of synthetic latex and glyoxal and paper coated therewith
US4269602A (en) * 1979-05-07 1981-05-26 Riegel Textile Corporation Buffered non-formaldehyde durable press textile treatment
US4269603A (en) * 1979-05-04 1981-05-26 Riegel Textile Corporation Non-formaldehyde durable press textile treatment
US5080754A (en) * 1990-07-20 1992-01-14 The Research Foundation Of State University Of Ny Method for reducing brightness reversion in lignin-containing pulps and article of manufacture thereof
US5330622A (en) * 1991-07-25 1994-07-19 Aussedat-Rey Composition for rendering a paper or textile base resistant to water, oil and solvents, treated base and process for the production of the treated base
US5958187A (en) * 1994-03-18 1999-09-28 Fort James Corporation Prewettable high softness paper product having temporary wet strength
US6059928A (en) * 1995-09-18 2000-05-09 Fort James Corporation Prewettable high softness paper product having temporary wet strength
US6176973B1 (en) * 1995-07-07 2001-01-23 Stora Kopparbergs Bergslags Aktiebolag (Publ) Absorbent material, absorbent body of the material, and method for preparation of the same
US20070027149A1 (en) * 2001-02-15 2007-02-01 Sugen, Inc. 3-(4-amidopyrrol-2-ylmethylidene)-2-indolinone der derivatives as protein kinase inhibitors

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GB502724A (en) * 1936-07-22 1939-03-21 Scott Paper Co Improvements in the manufacture of papers having a high wet strength
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US2322888A (en) * 1940-11-16 1943-06-29 Du Pont Process for producing high wet strength paper
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US1816973A (en) * 1926-10-30 1931-08-04 Kantorowicz Julius Process of increasing the strength and resistibility against moisture of high molecular carbohydrates
GB317085A (en) * 1928-08-10 1930-12-08 I.G. Farbenindustrie Aktiengesellschaft
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GB460201A (en) * 1935-07-22 1937-01-22 Calico Printers Ass Ltd Improvements in the finishing of textile materials
GB484691A (en) * 1935-08-02 1938-05-05 Raduner & Co Ag Improvements in or relating to methods of refining textiles
GB502724A (en) * 1936-07-22 1939-03-21 Scott Paper Co Improvements in the manufacture of papers having a high wet strength
US2203492A (en) * 1937-06-30 1940-06-04 Ici Ltd Dyed cellulosic material
GB547846A (en) * 1939-03-04 1942-09-15 Cilander Ag Improvements in or relating to the aldehyde treatment of cellulosic textile materials
US2322888A (en) * 1940-11-16 1943-06-29 Du Pont Process for producing high wet strength paper
US2285490A (en) * 1941-03-21 1942-06-09 Carbide & Carbon Chem Corp Felted article and process for its production
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Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2816833A (en) * 1954-06-22 1957-12-17 Synvar Corp Wet strength paper
US2869973A (en) * 1954-08-25 1959-01-20 Du Pont Synthetic paper sheet of chemically bonded synthetic polymer fibers and process of making the same
US3096228A (en) * 1961-01-09 1963-07-02 Kimberly Clark Co Manufacture of cellulosic product
DE1260959B (en) * 1963-01-09 1968-02-08 Nobel Bozel Method for stiffening the corrugations of corrugated cardboard
US3395072A (en) * 1964-05-13 1968-07-30 Nobel Bozel Paper coating compositions of synthetic latex and glyoxal and paper coated therewith
US4269603A (en) * 1979-05-04 1981-05-26 Riegel Textile Corporation Non-formaldehyde durable press textile treatment
US4269602A (en) * 1979-05-07 1981-05-26 Riegel Textile Corporation Buffered non-formaldehyde durable press textile treatment
US5080754A (en) * 1990-07-20 1992-01-14 The Research Foundation Of State University Of Ny Method for reducing brightness reversion in lignin-containing pulps and article of manufacture thereof
US5330622A (en) * 1991-07-25 1994-07-19 Aussedat-Rey Composition for rendering a paper or textile base resistant to water, oil and solvents, treated base and process for the production of the treated base
US5958187A (en) * 1994-03-18 1999-09-28 Fort James Corporation Prewettable high softness paper product having temporary wet strength
US6176973B1 (en) * 1995-07-07 2001-01-23 Stora Kopparbergs Bergslags Aktiebolag (Publ) Absorbent material, absorbent body of the material, and method for preparation of the same
US6059928A (en) * 1995-09-18 2000-05-09 Fort James Corporation Prewettable high softness paper product having temporary wet strength
US20070027149A1 (en) * 2001-02-15 2007-02-01 Sugen, Inc. 3-(4-amidopyrrol-2-ylmethylidene)-2-indolinone der derivatives as protein kinase inhibitors

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