US2764483A - Process for sizing paper - Google Patents

Process for sizing paper Download PDF

Info

Publication number
US2764483A
US2764483A US255133A US25513351A US2764483A US 2764483 A US2764483 A US 2764483A US 255133 A US255133 A US 255133A US 25513351 A US25513351 A US 25513351A US 2764483 A US2764483 A US 2764483A
Authority
US
United States
Prior art keywords
paper
sizing
salt
rosin
polyamine
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US255133A
Inventor
Denis J O'flynn
William H Seymour
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
EIDP Inc
Original Assignee
EI Du Pont de Nemours and Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by EI Du Pont de Nemours and Co filed Critical EI Du Pont de Nemours and Co
Priority to US255133A priority Critical patent/US2764483A/en
Application granted granted Critical
Publication of US2764483A publication Critical patent/US2764483A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • 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
    • D21H17/20Macromolecular organic compounds
    • D21H17/33Synthetic macromolecular compounds
    • D21H17/34Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/41Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups
    • D21H17/44Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups cationic
    • D21H17/45Nitrogen-containing groups
    • D21H17/455Nitrogen-containing groups comprising tertiary amine or being at least partially quaternised

Definitions

  • This invention relates to a novel process for sizing paper, and more particularly to a process for sizing paper by adding a sizing agent to the paper ingredients, e. g. in the beater stage of paper manufacture, or by means of a tub-sizing operation.
  • rosin has been employed as a paper sizing agent. During that period numerous attempts have been made to find a satisfactory substitute for rosin. In general, all such attempts have failed, since no agents Were found which could produce the desired efiect on paper at a relatively low cost as compared with the cost per ton of sizing paper with rosin.
  • One of the chief disadvantages in employing rosin as a paper size is the fact that rosin must be applied in an acidic mixture, and this results in a lack of permanence in the end product, since paper which is made at a pH below 7, and particularly below 5, loses strength at an appreciable rate on storage.
  • rosin employed in sizing paperv varies from about 0.1 to about 5 Paper which is to be employed in outside applications, such as billboard paper and the like, is sized with a relatively high percentage of rosin, namely about 5%. In contrast with this, certain varieties of paper which are to be employed in connection with printing, twisting, etc. are either unsized or carry only a relatively small quantity of rosin, viz. 0.1%.
  • rosin'as a paper size The effectiveness of rosin'as a paper size is believed to reside in part in its ability to form a monomolecular film over the individual fibers due in part to the fact that the rosin exists in the formof small. particles having a magnitude of 1 to 2 microns.
  • Synthetic resinous materials in general, fail to do this, although they are frequently capable of imparting water repellence, e. g. by forming a more or less impermeable coating or layer. To produce optimumsizing action without consuming excessive amounts of resin, it is considered that the resin must be capable of forming a monomolecular film over the fibers, for otherwise large amounts of resin would be r ce needed, and therefore a relatively expensive synthetic resin could not compete with rosin.
  • a water-insoluble resin to meet the requirements of a rosin substitute, would have to be capable of existing in the form of polarized, very small particles, such as those of submicroscopic magnitude, which are capable of coalescing on a fiber surface, such coalescing being caused by some ingredient within the fiber or by attractive forces of some other kind, causing the resin particles to be substantive to the fiber.
  • Ordinary water repellents do not possess these desirable characteristics.
  • An object of this invention is to provide a paper sizing composition which can be employed satisfactorily as a substitute for rosin in paper sizing.
  • a further object is to provide a rosin substitute which can be employed for this purpose without employing an acidic pH in the beater operation.
  • a still further object isto provide a substitute for rosin in clay or carbonate filled paper.
  • a sizing operation which comprises subjecting lignocellulosic fibers, in the beater stage of paper manufacture to the action of an aqueous dispersion of submicroscopic particles of an ethylene-carbon monoxide interpolymer polyamine carboxylate salt, as hereinafter defined, said polyamine salt being unmodified by formaldehyde, the carboxylic acid radical of the saltbeing that of a member of the class consisting of alkanoic and hydroxyalkanoic acids, e. g.
  • acetic, hydroxyacetic, propionic, and lactic acids and mixtures thereof the pH of the aqueous pulp after addition of the said dispersion being maintained at 5.5 to 8.5, preferably 7 to 7.5, the mol ratio of ethylene/ carbon monoxide in the said carboxylate being 3:1 to 15:1, and the nitrogen content of the said carboxylate bring from about 1.0 to 6.0%, preferably 1.5 to 3.0%, until upon subsequent drying of the paper ingredients the paper is loaded with the said salt to the extent of 0.1 to 0.5%, whereby a sizing of the paper is effected.
  • the ethylene-carbon monoxide interpolymer polyamines which are employed in the practice of the present invention are hereinafter referred to by the designation E/CO polyamines.
  • E/CO polyamines are the products which are obtained by hydrogenation of ethylene-carbon monoxide interpolymers in the presence of ammonia.
  • the E/CO polyamines are disclosed in the Hoehn Patent U. S. 2,495,255 (cf. also British 652,566,
  • Salts of the said polyamines are disclosed in the Cupery application S. N. 48,161 now U. S. Patent 2,579,033, issued December 18, 1951. According to the Cupery application, these salts may be employed as agents for imparting water repellence to textiles. It is to be understood, however, that water repellents for textiles (e. g. paraffin wax, etc.) are generally of no value as rosin substitutes in paper sizing.
  • the reductive amination of the ethylene/carbon monoxide polymers produces polyamines in which the number of amino groups is either equivalent to the number of carbonyl groups initially present in the interpolymer or is somewhat less than the number of carbonyl groups.
  • the preferred polyamines employed in the practice of this invention have nitrogen contents corresponding to amino substitution somewhat less than the number of carbonyl groups initially present in the polymer. Some of the carbonyl groups which are not aminated may be reduced to hydroxyl groups, but this evidently does not seriously affect the sizing ability of the polymer.
  • E/CO polyamines which have been modified with formaldehyde have been disclosed heretofore. Such formaldehyde-modified E/CO polyamines are not employed in the practice of the present invention.
  • the E/CO polyamine salt be employed in an aqueous medium, which may be an aqueous acid medium containing a sufficient amount of organic carboxylic acid to produce the desired pH, as hereinabove disclosed. Excellent results are obtained with aqueous acetic acid as the medium. Aqueous hydroxyacetic acid or lactic acid may be employed for this purpose, if desired. The same acid'which is employed in the aqueous medium may also be used as the source of the carboxylic acid radical of the polyamine salt, but this is not at all essential. Sources of the acid radical in the salt which are highly eflective include acetic, hydroxyacetic, propionic, diglycollic, and lactic acids. Certain mixtures of these acids are outstandingly etfective, as disclosed in further detail hereinafter. The amount of acid introduced need not exceed the amount required for salt formation.
  • One of the outstanding advantages of the present invention is that it permits the use of a non-acidic pH in the beater operation.
  • the sizing efliciency is excellent not only at pH ranges as low as 5.5 but also in substantially neutral mixtures and in mildly alkaline mixtures in which the pH is not greater than about 8.5.
  • a critical feature of the sizing agent of this invention is the magnitude of the polymer particles in the dispersion.
  • These particles, in the dispersions described herein, are of submicroscopic size, i. e. less than about .5 microns. In dilute mixtures (less than 1% concentration) the dispersions appear to be water clear; at a concentration of about they have a slight but perceptible haze; at higher concentrations these dispersions are cloudy in appearance.
  • the particle size is larger, as it is in formaldehyde-modified E/CO polyamines, the low resin loadings employed in the process of this invention fail togive any sizing action.
  • the polyamine carboxylate salts which are highly substantive to the paper pulp include those in which the ratio of ethylene/ carbon monoxide in the interpolymer is from 3:1 to :1 (mol proportions), (outstanding results being obtained at about 10:1 to 11:1), provided the nitrogen content of the polyamine carboxylate salt is from about 1.0 to 6.0%, optimum nitrogen content being about 2.4%. Under these circumstances the loading of the paper with the polymer takes place to the extent of about 0.1% to 0.5% based on the dry weight of the sized paper.
  • the concentration of E/CO polyamine carboxylate salt employed in the beater operation can be varied very widely, and, in view of the substantive nature of the polythese higher concentrations is of course less economical than the use of relatively lower concentrations.
  • Sizing aids such as alum, etc. which are required in l the treatment of pulp with rosin are not necessarily employed in the process of the present invention.
  • the nature of the pulp which may be employed is not particularly critical, and good results are obtained with unbleached kraft, bleached sulfite, groundwood and other pulp.
  • the particles in the dispersion were of sufficiently small size that they could not be discerned under the microscope.
  • the sizing operation was carried out by diluting the dispersion to 0.5% concentration by addition of water, and introducing the resulting diluted dispersion into a mechanical slurry containing 2.5 grams of beaten, bone dry pulp in 100 cc. of water. Mixing of the pulp during addition of the dispersion was continuous, and the mixing was continued for about ten minutes following the addition of the polyamine composition. The pH of the mixture was 7.5.
  • the slurry was placed on a sheet mold, and a wet web of paper was formed. The wet web was squeezed between felt pads to give a wet paper sheet having a consistency of 32.5%. This web was dried on a drum drier for two minutes at a surface temperature of 220 F. The sized paper of high quality was thus obtained.
  • Example 2 Under conditions similar to those described in Example 1, a series of sizing operations was conducted with results as shown in the following table.
  • compositions of this invention produce an equal amount of sizing at loadings which are only one-tenth as great as the rosin loading.
  • aqueous dispersion of submicroscopic particles of an ethylene-carbon monoxide interpolymer polyamine carboxylate salt said polyamine salt being unmodified by formaldehyde, the carboxylic acid radical of the said salt being that of a member of the class consisting of acetic, hydroxyacetic, propionic, diglycollic, and lactic acid, and mixtures thereof, the pH of the aqueous pulp after addition of the said dispersion being maintained at 5.5 to 8.5, the mol ratio of ethylene/CO in the said carboxylate being 3:1 to 15:1, the nitrogen content of the said carboxylate being from about 1.0 to 6.0%, until upon subsequent drying of the paper ingredients the paper is loaded with the said salt to the extent of 0.1% t0'0.5%, whereby a sizing of the paper is effected.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Paper (AREA)

Description

United States Patent PROCESS FOR SIZING PAPER No Drawing. Application November 6, 1951, Serial No. 255,133
3 Claims. (Cl. 92-21) This invention relates to a novel process for sizing paper, and more particularly to a process for sizing paper by adding a sizing agent to the paper ingredients, e. g. in the beater stage of paper manufacture, or by means of a tub-sizing operation.
For about 150 years rosin has been employed as a paper sizing agent. During that period numerous attempts have been made to find a satisfactory substitute for rosin. In general, all such attempts have failed, since no agents Were found which could produce the desired efiect on paper at a relatively low cost as compared with the cost per ton of sizing paper with rosin. One of the chief disadvantages in employing rosin as a paper size is the fact that rosin must be applied in an acidic mixture, and this results in a lack of permanence in the end product, since paper which is made at a pH below 7, and particularly below 5, loses strength at an appreciable rate on storage. For certain purposes permanence is highly desirable and, While ordinary rosinsized paper is serviceable over a period of many years, improvements in the ageing properties of paper, especially paper made under conditions heretofore requiring a low pH, is desirable. Moreover, it has been a common experience in paper manufacturing to observe that for reasons not fully understood inconsistent results are ,obtained from time to time in rosin-sizing operation, and therefore the trade has adopted the practice, during such periods of difficulty, of making unsized paper and returning to the production of sized paper only after the condition which affects the sizing operation adversely disappears.
In this country the average quantity of rosin employed in sizing papervvaries from about 0.1 to about 5 Paper which is to be employed in outside applications, such as billboard paper and the like, is sized with a relatively high percentage of rosin, namely about 5%. In contrast with this, certain varieties of paper which are to be employed in connection with printing, twisting, etc. are either unsized or carry only a relatively small quantity of rosin, viz. 0.1%.
In view of the large quantities of rosin required in the paper industry, and also in view. of the deficiencies which, as mentioned hereinabove, frequently occur in connection with the use of rosin as a paper size, a need has arisen for' synthetic materials which can be employed effectively and economically as paper sizing agents.
The effectiveness of rosin'as a paper size is believed to reside in part in its ability to form a monomolecular film over the individual fibers due in part to the fact that the rosin exists in the formof small. particles having a magnitude of 1 to 2 microns. Synthetic resinous materials, in general, fail to do this, although they are frequently capable of imparting water repellence, e. g. by forming a more or less impermeable coating or layer. To produce optimumsizing action without consuming excessive amounts of resin, it is considered that the resin must be capable of forming a monomolecular film over the fibers, for otherwise large amounts of resin would be r ce needed, and therefore a relatively expensive synthetic resin could not compete with rosin. Thus it appears that a water-insoluble resin, to meet the requirements of a rosin substitute, would have to be capable of existing in the form of polarized, very small particles, such as those of submicroscopic magnitude, which are capable of coalescing on a fiber surface, such coalescing being caused by some ingredient within the fiber or by attractive forces of some other kind, causing the resin particles to be substantive to the fiber. Ordinary water repellents do not possess these desirable characteristics.
An object of this invention is to provide a paper sizing composition which can be employed satisfactorily as a substitute for rosin in paper sizing. A further object is to provide a rosin substitute which can be employed for this purpose without employing an acidic pH in the beater operation. A still further object isto provide a substitute for rosin in clay or carbonate filled paper. Other objects of the invention will appear hereinafter.
These objects are accomplished in accordance with the present invention by means of a sizing operation which comprises subjecting lignocellulosic fibers, in the beater stage of paper manufacture to the action of an aqueous dispersion of submicroscopic particles of an ethylene-carbon monoxide interpolymer polyamine carboxylate salt, as hereinafter defined, said polyamine salt being unmodified by formaldehyde, the carboxylic acid radical of the saltbeing that of a member of the class consisting of alkanoic and hydroxyalkanoic acids, e. g. acetic, hydroxyacetic, propionic, and lactic acids and mixtures thereof, the pH of the aqueous pulp after addition of the said dispersion being maintained at 5.5 to 8.5, preferably 7 to 7.5, the mol ratio of ethylene/ carbon monoxide in the said carboxylate being 3:1 to 15:1, and the nitrogen content of the said carboxylate bring from about 1.0 to 6.0%, preferably 1.5 to 3.0%, until upon subsequent drying of the paper ingredients the paper is loaded with the said salt to the extent of 0.1 to 0.5%, whereby a sizing of the paper is effected. The ethylene-carbon monoxide interpolymer polyamines which are employed in the practice of the present invention are hereinafter referred to by the designation E/CO polyamines. These E/CO polyamines are the products which are obtained by hydrogenation of ethylene-carbon monoxide interpolymers in the presence of ammonia. The E/CO polyamines are disclosed in the Hoehn Patent U. S. 2,495,255 (cf. also British 652,566,
French 975,461, Belgian 486,101). Salts of the said polyamines are disclosed in the Cupery application S. N. 48,161 now U. S. Patent 2,579,033, issued December 18, 1951. According to the Cupery application, these salts may be employed as agents for imparting water repellence to textiles. It is to be understood, however, that water repellents for textiles (e. g. paraffin wax, etc.) are generally of no value as rosin substitutes in paper sizing.
In general, the reductive amination of the ethylene/carbon monoxide polymers produces polyamines in which the number of amino groups is either equivalent to the number of carbonyl groups initially present in the interpolymer or is somewhat less than the number of carbonyl groups. The preferred polyamines employed in the practice of this invention have nitrogen contents corresponding to amino substitution somewhat less than the number of carbonyl groups initially present in the polymer. Some of the carbonyl groups which are not aminated may be reduced to hydroxyl groups, but this evidently does not seriously affect the sizing ability of the polymer. E/CO polyamines which have been modified with formaldehyde have been disclosed heretofore. Such formaldehyde-modified E/CO polyamines are not employed in the practice of the present invention.
It is essential, in the process of this invention, that the E/CO polyamine salt be employed in an aqueous medium, which may be an aqueous acid medium containing a sufficient amount of organic carboxylic acid to produce the desired pH, as hereinabove disclosed. Excellent results are obtained with aqueous acetic acid as the medium. Aqueous hydroxyacetic acid or lactic acid may be employed for this purpose, if desired. The same acid'which is employed in the aqueous medium may also be used as the source of the carboxylic acid radical of the polyamine salt, but this is not at all essential. Sources of the acid radical in the salt which are highly eflective include acetic, hydroxyacetic, propionic, diglycollic, and lactic acids. Certain mixtures of these acids are outstandingly etfective, as disclosed in further detail hereinafter. The amount of acid introduced need not exceed the amount required for salt formation.
One of the outstanding advantages of the present invention is that it permits the use of a non-acidic pH in the beater operation. The sizing efliciency is excellent not only at pH ranges as low as 5.5 but also in substantially neutral mixtures and in mildly alkaline mixtures in which the pH is not greater than about 8.5.
A critical feature of the sizing agent of this invention is the magnitude of the polymer particles in the dispersion. These particles, in the dispersions described herein, are of submicroscopic size, i. e. less than about .5 microns. In dilute mixtures (less than 1% concentration) the dispersions appear to be water clear; at a concentration of about they have a slight but perceptible haze; at higher concentrations these dispersions are cloudy in appearance. When the particle size is larger, as it is in formaldehyde-modified E/CO polyamines, the low resin loadings employed in the process of this invention fail togive any sizing action.
The polyamine carboxylate salts which are highly substantive to the paper pulp include those in which the ratio of ethylene/ carbon monoxide in the interpolymer is from 3:1 to :1 (mol proportions), (outstanding results being obtained at about 10:1 to 11:1), provided the nitrogen content of the polyamine carboxylate salt is from about 1.0 to 6.0%, optimum nitrogen content being about 2.4%. Under these circumstances the loading of the paper with the polymer takes place to the extent of about 0.1% to 0.5% based on the dry weight of the sized paper.
The concentration of E/CO polyamine carboxylate salt employed in the beater operation can be varied very widely, and, in view of the substantive nature of the polythese higher concentrations is of course less economical than the use of relatively lower concentrations.
Sizing aids such as alum, etc. which are required in l the treatment of pulp with rosin are not necessarily employed in the process of the present invention.
The nature of the pulp which may be employed is not particularly critical, and good results are obtained with unbleached kraft, bleached sulfite, groundwood and other pulp.
The invention is illustrated further by means of the following examples. 7
Example 1.A dispersion is prepared by mixing 20 grams of E/CO polyamine (ethylene:carbon monoxide ratio=1l, N2=2.38%, 2 grams hydroxyacetic acid, and 178 grams of water. This was accomplished by adding the polyamine very slowly to the hydroxyacetic acid, and later dissolving the resulting mixture in water, and maintaining the composition thus produced at a temperature of C. with constant agitation. Finally the mixture was heated for five minutes at refluxing temperature and then cooled to room temperature. To 20 grams of the 100 cc. of water. Mixing of the pulp during addition of diglycollic acid. The resulting mixture was heated under boiling conditions for about 20 minutes. The relatively stable dispersion was thus obtained, which after two months storage did not change in appearance and continued to have unchanged sizing properties. The particles in the dispersion were of sufficiently small size that they could not be discerned under the microscope. The sizing operation was carried out by diluting the dispersion to 0.5% concentration by addition of water, and introducing the resulting diluted dispersion into a mechanical slurry containing 2.5 grams of beaten, bone dry pulp in 100 cc. of water. Mixing of the pulp during addition of the dispersion was continuous, and the mixing was continued for about ten minutes following the addition of the polyamine composition. The pH of the mixture was 7.5. The slurry was placed on a sheet mold, and a wet web of paper was formed. The wet web was squeezed between felt pads to give a wet paper sheet having a consistency of 32.5%. This web was dried on a drum drier for two minutes at a surface temperature of 220 F. The sized paper of high quality was thus obtained.
Example 2.-Under conditions similar to those described in Example 1, a series of sizing operations was conducted with results as shown in the following table.
TABLE I Sizing effect of E/C'O Pair amines in the absence of formaldehyde E/CO Polyamine 1 Dispersion pH Drying Conditions TAPPI Size Dry- Indicator Acid Test,
Resin Head- Time, Temper- Sea- Added, Beater Box Min. ature, Average Type Cone, percent F. for a series percent of tests 1 E/OO polyamine analyzed. E/CO Ratio 11/1. Used as 10% aqueous dispersions. Pulp used was unbleached kraft.
mer, it is not critical to employ a relatively high concentration. Concentrations as low as about 0.1% are effective, but of course much higher concentrations, up to For comparison with the results given in the above examples it was found that 3% rosin size gave a size test (TAPPI) of 31; in other words, the data prove that the about 5 or more, can be employed if desired. Use of compositions of this invention produce an equal amount of sizing at loadings which are only one-tenth as great as the rosin loading.
It will be understood, of course, that the foregoing examples are illustrative only, and that numerous methods for carrying out the process of the invention will occur to those who are skilled in the art. For example, numerous ingredients in addition to the polyamines may be employed if desired. The introduction of paraffin wax, for example, is permissible in the process of the present invention. Dispersing agents, in general, are not required, although they are sometimes of value, especially when waxes, etc. are also present in the dispersion. All such modifications to the extent that they are within the terms of the appended claims are regarded as being within the scope of the present invention.
We claim:
1. In a process for manufacturing sized paper the steps which comprise introducing into the aqueous pulp in the beater stage of paper manufacture an aqueous dispersion of submicroscopic particles of an ethylene-carbon monoxide interpolymer polyamine carboxylate salt, said polyamine salt being unmodified by formaldehyde, the carboxylic acid radical of the said salt being that of a member of the class consisting of acetic, hydroxyacetic, propionic, diglycollic, and lactic acid, and mixtures thereof, the pH of the aqueous pulp after addition of the said dispersion being maintained at 5.5 to 8.5, the mol ratio of ethylene/CO in the said carboxylate being 3:1 to 15:1, the nitrogen content of the said carboxylate being from about 1.0 to 6.0%, until upon subsequent drying of the paper ingredients the paper is loaded with the said salt to the extent of 0.1% t0'0.5%, whereby a sizing of the paper is effected. v
2. Process of claim 1 wherein the pH of the beater contents is 7 to 8.5.
3. Process of claim 2 wherein the carboxylic acid includes both hydroxyacetic and diglycollic acid.
References Cited in the file of this patent UNITED STATES PATENTS 2,325,302 Britt July 27, 1943 2,338,602 Schur Jan. 4, 1944 2,343,090 Smith a Feb. 29, 1944 2,343,095 Smith Feb. 29, 1944 2,487,899 Sherman Nov. 15, 1949 2,495,255 Hoehn Jan. 24, 1950 2,526,637 Cupery Oct. 24, 1950 2,526,638 Cupery Oct. 24, 1950 2,526,639 Cupery Oct. 24, 1950

Claims (1)

1. IN A PROCESS FOR MANUFACTURING SIZED PAPER THE STEPS WHICH COMPRISE INTRODUCING INTO THE AQUEOUS PULP IN THE BEATER STAGE OF PAPER MANUFACTURE AN AQUEOUS DISPERSION OF SUBMICROSCOPIC PARTICLES OF AN ETHYLENE-CARBON MONOXIDE INTERPOLYMER POLYAMINE CARBOXYLATE SALT, SAID POLYAMINE SALT BEING UNMODIFIED BY FORMALDEHYDE, THE CARBOXYLIC ACID RADICAL OF THE SAID SALT BEING THAT OF A MEMBER OF THE CLASS CONSISTING OF ACETIC, HYDROXYACETIC, PROPIONIC, DIGLYCOLLIC, AND LACTIC ACID, AND MIXTURES THEREOF, THE PH OF THE AQUEOUS PULP AFTER ADDITION OF THE SAID DISPERSION BEING MAINTAINED AT 5.5 TO 8.5, THE MOL RATIO OF ETHYLENE/CO IN THE SAID CARBOXYLATE BEING 3:1 TO 15:1, THE NITROGEN CONTENT OF THE SAID CARBOXYLATE BEING FROM ABOUT 1.0 TO 6.0%, UNTIL UPON SUBSEQUENT DRYING OF THE PAPER INGREDIENTS THE PAPER IS LOADED WITH THE SAID SALT TO THE EXTENT OF 0.1% TO 0.5%, WHEREBY A SIZING OF THE PAPER IS EFFECTED.
US255133A 1951-11-06 1951-11-06 Process for sizing paper Expired - Lifetime US2764483A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US255133A US2764483A (en) 1951-11-06 1951-11-06 Process for sizing paper

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US255133A US2764483A (en) 1951-11-06 1951-11-06 Process for sizing paper

Publications (1)

Publication Number Publication Date
US2764483A true US2764483A (en) 1956-09-25

Family

ID=22966976

Family Applications (1)

Application Number Title Priority Date Filing Date
US255133A Expired - Lifetime US2764483A (en) 1951-11-06 1951-11-06 Process for sizing paper

Country Status (1)

Country Link
US (1) US2764483A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2882184A (en) * 1955-01-17 1959-04-14 Trachet Jacques Jean Paraffinic anti-corrosive coatings in the form of a strip or tape
DE1150865B (en) * 1958-04-14 1963-06-27 Schweizerische Viscose Process for the production of cellulose and polyamide-containing flat structures from fiber material using polyamides as binders

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2325302A (en) * 1938-11-03 1943-07-27 Scott Paper Co High-wet-strength paper
US2338602A (en) * 1939-12-04 1944-01-04 Reconstruction Finance Corp Fabrication of wet-strengthened papers
US2343095A (en) * 1940-08-03 1944-02-29 Du Pont Resin dispersion useful in the textile and paper industries
US2343090A (en) * 1940-08-03 1944-02-29 Du Pont Treatment of textiles and composition useful therefor
US2487899A (en) * 1945-05-10 1949-11-15 Nopco Chem Co Process of wax sizing papermaking fibers using a cationic surface active agent
US2495255A (en) * 1948-01-28 1950-01-24 Du Pont Polymeric polyamines
US2526639A (en) * 1949-08-01 1950-10-24 Du Pont Polymeric materials from formaldehyde and a hydrogenated butadiene-1, 3-acrylonitrile copolymer
US2526637A (en) * 1948-04-02 1950-10-24 Du Pont Shrinkproofed wool and method of producing same
US2526638A (en) * 1949-03-03 1950-10-24 Du Pont Paper treated with formaldehyde and a polymeric polyamine

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2325302A (en) * 1938-11-03 1943-07-27 Scott Paper Co High-wet-strength paper
US2338602A (en) * 1939-12-04 1944-01-04 Reconstruction Finance Corp Fabrication of wet-strengthened papers
US2343095A (en) * 1940-08-03 1944-02-29 Du Pont Resin dispersion useful in the textile and paper industries
US2343090A (en) * 1940-08-03 1944-02-29 Du Pont Treatment of textiles and composition useful therefor
US2487899A (en) * 1945-05-10 1949-11-15 Nopco Chem Co Process of wax sizing papermaking fibers using a cationic surface active agent
US2495255A (en) * 1948-01-28 1950-01-24 Du Pont Polymeric polyamines
US2526637A (en) * 1948-04-02 1950-10-24 Du Pont Shrinkproofed wool and method of producing same
US2526638A (en) * 1949-03-03 1950-10-24 Du Pont Paper treated with formaldehyde and a polymeric polyamine
US2526639A (en) * 1949-08-01 1950-10-24 Du Pont Polymeric materials from formaldehyde and a hydrogenated butadiene-1, 3-acrylonitrile copolymer

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2882184A (en) * 1955-01-17 1959-04-14 Trachet Jacques Jean Paraffinic anti-corrosive coatings in the form of a strip or tape
DE1150865B (en) * 1958-04-14 1963-06-27 Schweizerische Viscose Process for the production of cellulose and polyamide-containing flat structures from fiber material using polyamides as binders

Similar Documents

Publication Publication Date Title
JP7097356B2 (en) How to Form a Coating Layer Containing Microfibrillated Cellulose
DE1546369C3 (en) Process for making paper, paperboard and the like with improved wet strength. Eliminated from: 1177824
US11525211B2 (en) Bio-based polyelectrolyte complex compositions comprising non-water soluble particles
US3138473A (en) Compositions and process to increase the wet strength of paper
JP6931659B2 (en) A method for producing a composite containing MFC and a composite produced by this method.
US4214948A (en) Method of sizing paper
CN111479858B (en) Method for producing a film with good barrier properties and film with good barrier properties
US2739058A (en) Process for sizing paper with polyethylene
US2022004A (en) Paper sizing
US3006806A (en) Sized paper and process therefor
JP3032601B2 (en) Improved inorganic filler for papermaking
US3311532A (en) Ketene dimer paper sizing compositions including acyl compound extender and paper sized therewith
EP0193111B1 (en) Process for producing paper with a high dry strength
US2582840A (en) Sizing fibrous materials with modified urea-formaldehyde resin
US3081219A (en) Prevention of deposition of pitch in papermaking
SE1651027A1 (en) Method for manufacturing intermediate product for conversioninto microfibrillated cellulose
US2961367A (en) Sized paper and method of making same
US3139373A (en) Process for the internal sizing of paper with a salt of a substituted succinic acid
US2764483A (en) Process for sizing paper
US2365813A (en) Process for treating fibrous products and products thereof
JP2021507130A (en) Method for manufacturing textile products containing microfibrillated cellulose
US3017291A (en) Wet-strength paper and method of producing same
US3035965A (en) Paper composed of synthetic fibers, and fibrous binder for use in the manufacture thereof
US1998758A (en) Treatment of paper pulp
US3151017A (en) Selected treatment of fiber blends with resins