US3880710A - Process for fiber treatment - Google Patents

Process for fiber treatment Download PDF

Info

Publication number
US3880710A
US3880710A US323177A US32317773A US3880710A US 3880710 A US3880710 A US 3880710A US 323177 A US323177 A US 323177A US 32317773 A US32317773 A US 32317773A US 3880710 A US3880710 A US 3880710A
Authority
US
United States
Prior art keywords
percent
aniline
water
paper
pyridine
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
US323177A
Inventor
Victor A Pattison
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.)
Occidental Chemical Corp
Original Assignee
Hooker Chemicals and Plastics Corp
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 Hooker Chemicals and Plastics Corp filed Critical Hooker Chemicals and Plastics Corp
Priority to US323177A priority Critical patent/US3880710A/en
Application granted granted Critical
Publication of US3880710A publication Critical patent/US3880710A/en
Assigned to OCCIDENTAL CHEMICAL CORPORATION reassignment OCCIDENTAL CHEMICAL CORPORATION CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). EFFECTIVE APRIL 1, 1982. Assignors: HOOKER CHEMICALS & PLASTICS CORP.
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G12/00Condensation polymers of aldehydes or ketones with only compounds containing hydrogen attached to nitrogen
    • C08G12/02Condensation polymers of aldehydes or ketones with only compounds containing hydrogen attached to nitrogen of aldehydes
    • C08G12/04Condensation polymers of aldehydes or ketones with only compounds containing hydrogen attached to nitrogen of aldehydes with acyclic or carbocyclic compounds
    • C08G12/06Amines
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G12/00Condensation polymers of aldehydes or ketones with only compounds containing hydrogen attached to nitrogen
    • C08G12/02Condensation polymers of aldehydes or ketones with only compounds containing hydrogen attached to nitrogen of aldehydes
    • C08G12/04Condensation polymers of aldehydes or ketones with only compounds containing hydrogen attached to nitrogen of aldehydes with acyclic or carbocyclic compounds
    • C08G12/06Amines
    • C08G12/08Amines aromatic
    • 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
    • D21H17/46Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/47Condensation polymers of aldehydes or ketones
    • D21H17/49Condensation polymers of aldehydes or ketones with compounds containing hydrogen bound to nitrogen

Definitions

  • ABSTRACT Compositions of the formula are used to impart wet-strengthening and waterrepellency properties of fibers and fibrous materials.
  • This invention relates to the treatment of fibrous materials. More particularly, this invention relates to the improvement of wet strength and water repellency characteristics of paper and paper products.
  • R, R and R are organic radicals generally having from 1 to about 12 carbon atoms;
  • R, is an alkyl radical having from about 5 to about 24 carbon atoms;
  • X is halogen;
  • a, b and c are numbers having a value of from zero to 3;
  • x is a number having a value of from about 1 to about 10 and
  • y is a number having a value of from about 0.8 to about 4.
  • the fibers which may be treated in according with the process of the present invention include textile and paper fibers, and the process is particularly useful in treating paper pulp and paper products.
  • the fibrous materials are treated by applying thereto the resins hereinbefore as aqueous dispersions, generally the dispersions containing from about 0.1 to about 10 percent by weight resin, preferably from about 1 to about 5 weight percent.
  • the dispersions may contain the resins in greater amounts; however, it has been found that subjecting the fibrous materials to treatment with aqueous dispersions of resin containing from about 1 to about 5 percent by weight resin, for a time sufficient to provide an addon of resin from about 0.2 to about 2 percent by weight, preferably from about 0.2 to about 1.5 percent by weight, based on the dry weight of the fibrous material treated.
  • the dispersion may be added to the material to be treated by any method known to the art.
  • the dispersions are particularly suited to the treatment of paper pulp.
  • the dispersion is added to the pulp slurry, with stirring, in amounts to obtain the desired addon, the pulp is sheeted out by conventional methods and dried.
  • the resins utilized in treating the fibrous materials are those of the formula:
  • R, R and R are organic radicals generally having from 1 to about 12 carbon atoms; R is an alkyl radical having from about 5 to about 24 carbon atoms; X is halogen; a, b and c are numbers having a value of from zero to 3; x is a number having a value of from about 1 to about and y is a number having a value of from about 0.8 to about 4.
  • the molecular weight of the resins may vary from about 500 to'about 2,500, or higher.
  • the resins used in the present process are prepared by:
  • N-methyl aniline, or a substituted N-methyl anilines, or mixtures thereof are condensed with formaldehyde and a non-N-substituted aniline or mixtures thereof;
  • the resin obtained from (a) is reacted with a carbonic dihalide to convert the N-methyl amino groups to carbamoyl halide groups and the amino groups to isocyanate groups;
  • the resin of (c) is reacted with pyridine N-oxide, substituted pyridine N-oxides, or suitable mixtures thereof to obtain the resins.
  • Suitable carbonic dihalides are phosgene, carbonic dibromide, and the like.
  • phosgene is the carbonic dihalide utilized.
  • Suitable N-methyl anilines for use in formulating the resinous compositions of the present invention include N-methyl aniline; 3,5-dimethyl N-methyl aniline; 4- dodecyl N-methyl aniline; 4-phenyl N-methyl aniline; 4-naphthyl N-methyl aniline; 3-(2-chloro) propyl N- methyl aniline; 3,4,5-trimethyl N-methyl aniline, and the like, as well as a mixtures thereof.
  • the most preferred N-methyl aniline is the unsubstituted N-methyl anilines.
  • Suitable pyridine N-oxides for formulating the resinous compositions of the present invention include 3,5- dimethyl pyridine N-oxide; 3,5-dipropyl pyridine N- oxide; 3-methyl pyridine N-oxide; 4-naphthyl pyridine N-oxide; 4-phenyl pyridine N-oxide; 3-hexyl pyridine N-oxide; 4-(3-chloropropyl) pyridine N-oxide and the like, or mixtures thereof.
  • the most preferred reactant is unsubstituted pyridine N-oxide.
  • the formaldehyde employed may be obtained from such sources as aqueous solutions of formaldehyde, trioxane, paraformaldehyde, and the like.
  • the formaldehyde is used as an aqueous solution, about 37 percent by weight formaldehyde.
  • Suitable non-N-substituted anilines useful in preparing the resins of the present invention include 3,5- dimethyl aniline; 3,5-dipropyl aniline; 4-phenyl aniline; 4-naphthyl aniline; 4-(4-chloro phenyl) aniline; 3-hexyl aniline; 4-dodecylaniline and the like, or mixtures thereof.
  • the most preferred reactant is unsubstituted aniline.
  • the reaction of the aniline compound, the N-methyl aniline compound and formaldehyde is conducted by adding the fomaldehyde on a continuous basis to the aniline compounds in a system acidified to a low pH of a suitable mineral acid such as hydrochloric acid, the formaldehyde added in sufficient amounts to effect condensation of the anilines present.
  • a suitable alkaline agent as for example, aqueous sodium hydroxide
  • the liquid phase is removed by decantation, and the residue heated to remove any remaining water.
  • the pH of the reaction system, during the addition of the formaldehyde, is generally maintained at l or less.
  • the temperature during the step (a) reaction is generally maintained at from about to about 160C, preferably from about 130 to about 160C, with the time required to effect the condensation being on the order of from about 60 to about 90 minutes.
  • step (a) is then reacted with the selected carbonic dihalide, preferably phosgene, by adding a suitable solvent to the resin, heating to temperatures sufficient to remove any water present, cooling to less than about 35C, and adding the carbonic dihalide continuously, in about stoichiometric amounts to react with the N-methyl amino groups, converting the groups to carbamoyl chloride groups, and the amino groups to isocyanate groups.
  • the selected carbonic dihalide preferably phosgene
  • Heat is applied to move the temperature gradually up to about 150C, evolving hydrochloric acid.
  • the temperature is generally moved through a range of from about 35 to about 150C over a period of about 90 minutes.
  • the solvent is removed by distillation, generally at about C under reduced pressures.
  • Suitable solvents include the halogenated hydrocarbons, such as chlorobenzene, dichlorobenzene and the like.
  • reaction is completed within a period of from about 90 to 120 minutes.
  • step (b) is then reacted with the fatty alcohol by adding the alcohol, with stirring, to the resin in amounts sufficient to convert the isocyanate groups to carbamoyl ester groups, generally at a temperature of about 90C, the reaction being essentially completed within a period of about 30 minutes.
  • reaction product from step (c) is then reacted with the selected pyridine N-oxide by adding the pyridine N-oxide in about stoichiometric amounts, based on the carbamoyl halide groups present, stirring and allowing the reaction mixture to stand for about 2-8 hours, maintaining the temperature at ambient temperatures; however, the reaction may be conducted at elevated temperatures, on the order of about 90C.
  • N-methyl aniline (257 parts by weight) is condensed with aniline (149 parts by weight) and formaldehyde at a pH of about 1 and at a temperature of about C.
  • the reaction product is added to dichlorobenzene and heated to remove water-present.
  • Phosgene is added to the reaction system, after cooling, and the temperature gradually increased to about 150C over a period of about 90 minutes.
  • 48.6 grams of the product'and 32.5 grams of stearyl alcohol is heated at 90C for 120 minutes.
  • the reaction mixture is dissolved in chloroform and added to a solution of pyridine'N-oxide in chloroform (17 grams pyridine N-oxide in 102 grams chloroform). The reaction mixture is stirred for 60 minutes and on solvent evaporation, a water dispersible product is obtained.
  • kraft pulp of 450 ml freeness, and 0.30 consistancy is admixed with a 5 percent aqueous dispersion of a resin prepared in accordance with the procedure of Example 1, and the concentration is adjusted to the indicated level.
  • hand sheets are prepared and cured for 30 minutes, at 105C and conditioned overnight at about 25C and 50 percent relative humidity. The results are set forth in the following table.
  • x is a number having a value of from 1 to 10 and y is a number having a value of from 0.8 to 4.
  • samples of l-5 when subjected to a standard water-methanol water repellency test, are unwetted by 10, 40, 60, 60 and 80 percent methanol-water solutions, respectively.
  • a process for rendering fibrous materials wetstrengthened and water repellent which comprises treating said fibrous material with a wet-strengthening and 0.1 to 10 percent of water repelling amount of an aqueous dispersion comprising water and a resinous composition of the formula CH O wherein R, R and R are alkyl or aryl organic radicals 45 addon is from 0.2 to 1.5 percent by weight.
  • R is an alkyl radical having from 5 to 24 carbon atoms
  • X is halogen

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Paper (AREA)

Abstract

ARE USED TO IMPART WET-STRENGTHENING AND WATER-REPELLENCY PROPERTIES OF FIBERS AND FIBROUS MATERIALS.

Compositions of the formula

Description

United States Patent [191 Pattison [451 Apr. 29, 1975 PROCESS FOR FIBER TREATMENT [75] Inventor: Victor A. Pattison, Tonawanda,
[73] Assignee: Hooker Chemicals & Plastics Corporation, Niagara Falls, NY.
[22] Filed: Jan. 12, 1973 [21] Appl. No.: 323,177
[52] US. Cl. 162/167; 260/295 AM; 260/295 CA [51] Int. Cl D21h 3/12 [58] Field of Search. 260/295 CA, 295 C, 295 Q,
[56] References Cited UNITED STATES PATENTS 2,518,266 8/1950 Baird et a1. 260/295 AM 2,518,267 8/1950 Baird et a1 260/295 AM Primary Examiner-Robert L. Lindsay, Jr.
Assistant ExaminerWilliam F. Smith Attorney, Agent, or Firm-Peter F. Casella; John M. Petruncio [57] ABSTRACT Compositions of the formula are used to impart wet-strengthening and waterrepellency properties of fibers and fibrous materials.
8 Claims, No Drawings PROCESS FOR FIBER TREATMENT This invention relates to the treatment of fibrous materials. More particularly, this invention relates to the improvement of wet strength and water repellency characteristics of paper and paper products.
For many years, no commercially available wet' strength resins were available which would function effectively at pHs much above about 5.5. As a consequence, many grades of paper and paper products made on the alkaline side for various reasons, including strength, softness, use of alkaline fillers or the like, could not be effectively wet-strengthened.
Attempts to allievate this and other problems have been made in the past. Recently, the wet-strengthening of paper and paper products by the use of polymeric reaction products of epichlorohydrin and polyamides derived from polyalkylene polyamines and saturated aliphatic dicarboxylic acids containing from 3 to carbon atoms has been prepared. Such resins have been proposed for use under pH conditions on the alkaline side in the production of alkaline papers, and in applications to fibers while the fibers are in dilute aqueous suspensions of the consistancy generally used in paper mills.
It is also known to produce paper having a measure of wet strength by mixing fibrous pulp with suspensions of polyvinyl alcohol, or with latex, and to produce paper from the thus formed mixture.
Unsaturated aliphatic dibasic acids, reacted with ammonia, a polyamine and epichlorohydrin have also been proposed for use in imparting wet strength to paper and paper products. However, universal acceptance of the wet-strengthening materials of the prior art has been less than total.
It is an object of the present invention to provide paper products having improved wet strength and water repellency characteristics.
This and other objects and advantages of the present invention will become apparent from a reading of the description which follows and the appended claims.
Briefly stated, the wet strength and water-repellency characteristics of fibrous materials, such as paper and paper products, are improved by treating such materials with resinous treating materials of the formula wherein R, R and R are organic radicals generally having from 1 to about 12 carbon atoms; R, is an alkyl radical having from about 5 to about 24 carbon atoms; X is halogen; a, b and c are numbers having a value of from zero to 3; x is a number having a value of from about 1 to about 10 and y is a number having a value of from about 0.8 to about 4.
The fibers which may be treated in according with the process of the present invention include textile and paper fibers, and the process is particularly useful in treating paper pulp and paper products.
According to the process of the present invention,
the fibrous materials are treated by applying thereto the resins hereinbefore as aqueous dispersions, generally the dispersions containing from about 0.1 to about 10 percent by weight resin, preferably from about 1 to about 5 weight percent. The dispersions may contain the resins in greater amounts; however, it has been found that subjecting the fibrous materials to treatment with aqueous dispersions of resin containing from about 1 to about 5 percent by weight resin, for a time sufficient to provide an addon of resin from about 0.2 to about 2 percent by weight, preferably from about 0.2 to about 1.5 percent by weight, based on the dry weight of the fibrous material treated.
The dispersion may be added to the material to be treated by any method known to the art. The dispersions are particularly suited to the treatment of paper pulp. In treating pulp, the dispersion is added to the pulp slurry, with stirring, in amounts to obtain the desired addon, the pulp is sheeted out by conventional methods and dried.
The resins utilized in treating the fibrous materials, as stated, are those of the formula:
wherein R, R and R are organic radicals generally having from 1 to about 12 carbon atoms; R is an alkyl radical having from about 5 to about 24 carbon atoms; X is halogen; a, b and c are numbers having a value of from zero to 3; x is a number having a value of from about 1 to about and y is a number having a value of from about 0.8 to about 4.
The molecular weight of the resins may vary from about 500 to'about 2,500, or higher.
The resins used in the present process are prepared by:
a. N-methyl aniline, or a substituted N-methyl anilines, or mixtures thereof are condensed with formaldehyde and a non-N-substituted aniline or mixtures thereof;
b. the resin obtained from (a) is reacted with a carbonic dihalide to convert the N-methyl amino groups to carbamoyl halide groups and the amino groups to isocyanate groups;
c. the resin of (b) is reacted with a C C alcohol at the isocyanate sites; and
d. the resin of (c) is reacted with pyridine N-oxide, substituted pyridine N-oxides, or suitable mixtures thereof to obtain the resins.
Suitable carbonic dihalides are phosgene, carbonic dibromide, and the like. Preferably, phosgene is the carbonic dihalide utilized.
Suitable N-methyl anilines for use in formulating the resinous compositions of the present invention include N-methyl aniline; 3,5-dimethyl N-methyl aniline; 4- dodecyl N-methyl aniline; 4-phenyl N-methyl aniline; 4-naphthyl N-methyl aniline; 3-(2-chloro) propyl N- methyl aniline; 3,4,5-trimethyl N-methyl aniline, and the like, as well as a mixtures thereof. The most preferred N-methyl aniline is the unsubstituted N-methyl anilines.
Suitable pyridine N-oxides for formulating the resinous compositions of the present invention include 3,5- dimethyl pyridine N-oxide; 3,5-dipropyl pyridine N- oxide; 3-methyl pyridine N-oxide; 4-naphthyl pyridine N-oxide; 4-phenyl pyridine N-oxide; 3-hexyl pyridine N-oxide; 4-(3-chloropropyl) pyridine N-oxide and the like, or mixtures thereof. The most preferred reactant is unsubstituted pyridine N-oxide.
The formaldehyde employed may be obtained from such sources as aqueous solutions of formaldehyde, trioxane, paraformaldehyde, and the like. Preferably, the formaldehyde is used as an aqueous solution, about 37 percent by weight formaldehyde. v
Suitable non-N-substituted anilines useful in preparing the resins of the present invention include 3,5- dimethyl aniline; 3,5-dipropyl aniline; 4-phenyl aniline; 4-naphthyl aniline; 4-(4-chloro phenyl) aniline; 3-hexyl aniline; 4-dodecylaniline and the like, or mixtures thereof. The most preferred reactant is unsubstituted aniline.
The reaction of the aniline compound, the N-methyl aniline compound and formaldehyde is conducted by adding the fomaldehyde on a continuous basis to the aniline compounds in a system acidified to a low pH of a suitable mineral acid such as hydrochloric acid, the formaldehyde added in sufficient amounts to effect condensation of the anilines present. Following the addition of the formaldehyde, the reaction mixture is made alkaline by the addition thereto of a suitable alkaline agent, as for example, aqueous sodium hydroxide,
a solid product separating. The liquid phase is removed by decantation, and the residue heated to remove any remaining water. The pH of the reaction system, during the addition of the formaldehyde, is generally maintained at l or less.
The temperature during the step (a) reaction is generally maintained at from about to about 160C, preferably from about 130 to about 160C, with the time required to effect the condensation being on the order of from about 60 to about 90 minutes.
The reaction product of step (a) is then reacted with the selected carbonic dihalide, preferably phosgene, by adding a suitable solvent to the resin, heating to temperatures sufficient to remove any water present, cooling to less than about 35C, and adding the carbonic dihalide continuously, in about stoichiometric amounts to react with the N-methyl amino groups, converting the groups to carbamoyl chloride groups, and the amino groups to isocyanate groups.
Heat is applied to move the temperature gradually up to about 150C, evolving hydrochloric acid. The temperature is generally moved through a range of from about 35 to about 150C over a period of about 90 minutes. The solvent is removed by distillation, generally at about C under reduced pressures.
Suitable solvents include the halogenated hydrocarbons, such as chlorobenzene, dichlorobenzene and the like.
Generally the reaction is completed within a period of from about 90 to 120 minutes.
The product of step (b) is then reacted with the fatty alcohol by adding the alcohol, with stirring, to the resin in amounts sufficient to convert the isocyanate groups to carbamoyl ester groups, generally at a temperature of about 90C, the reaction being essentially completed within a period of about 30 minutes.
The reaction product from step (c) is then reacted with the selected pyridine N-oxide by adding the pyridine N-oxide in about stoichiometric amounts, based on the carbamoyl halide groups present, stirring and allowing the reaction mixture to stand for about 2-8 hours, maintaining the temperature at ambient temperatures; however, the reaction may be conducted at elevated temperatures, on the order of about 90C.
EXAMPLE 1 N-methyl aniline (257 parts by weight) is condensed with aniline (149 parts by weight) and formaldehyde at a pH of about 1 and at a temperature of about C. The reaction product is added to dichlorobenzene and heated to remove water-present. Phosgene is added to the reaction system, after cooling, and the temperature gradually increased to about 150C over a period of about 90 minutes. Following the removal of the solvent, 48.6 grams of the product'and 32.5 grams of stearyl alcohol is heated at 90C for 120 minutes. The reaction mixture is dissolved in chloroform and added to a solution of pyridine'N-oxide in chloroform (17 grams pyridine N-oxide in 102 grams chloroform). The reaction mixture is stirred for 60 minutes and on solvent evaporation, a water dispersible product is obtained.
In the following examples, kraft pulp of 450 ml freeness, and 0.30 consistancy, is admixed with a 5 percent aqueous dispersion of a resin prepared in accordance with the procedure of Example 1, and the concentration is adjusted to the indicated level. After stirring for 30 minutes, hand sheets are prepared and cured for 30 minutes, at 105C and conditioned overnight at about 25C and 50 percent relative humidity. The results are set forth in the following table.
and c are numbers having a value of from zero to 3; x is a number having a value of from 1 to 10 and y is a number having a value of from 0.8 to 4.
TREAT- MENT EXAMPLE LEVEL Add on pH TENSILE STRENGTH (Kg/mm) Dry Wet Control 0 O 8.0 7.0 0.3 4 l 1.0 0.2 8.0 5.7 0.6 16 2 2.5 0.6 7.4 5.0 1.0 20 3 2.5 0.7 7.4 4.0 1.2 4 5.0 1.4 7.4 3.8 [.6 42 5 5.0 1.5 7.3 4.6 1.2 30
The samples of l-5, when subjected to a standard water-methanol water repellency test, are unwetted by 10, 40, 60, 60 and 80 percent methanol-water solutions, respectively.
What is claimed is:
l. A process for rendering fibrous materials wetstrengthened and water repellent which comprises treating said fibrous material with a wet-strengthening and 0.1 to 10 percent of water repelling amount of an aqueous dispersion comprising water and a resinous composition of the formula CH O wherein R, R and R are alkyl or aryl organic radicals 45 addon is from 0.2 to 1.5 percent by weight.
having from 1 to 12 carbon atoms; R, is an alkyl radical having from 5 to 24 carbon atoms; X is halogen; a, b
8. The paper produced by the process as defined by claim 7.

Claims (8)

1. A PROCESS FOR RENDERING FIBROUS MATERIALS WETSTRENGTHENED AND WATER REPELLENT WHICH COMPRISES TREATING SAID FIBROUS MATERIAL WITH A WET-STRENGTHENING AND 0.1 TO 10 PERCENT OF WATER REPELLING AMOUNT OF AN AQUEOUS COMPRISING WATER AND A RESINOUS COMPOSITION OF THE FORMULA
2. A process as defined by claim 1 wherein the resin is present in the trlating solution in an amount of from 1 to 5 percent.
3. A process as defined by claim 2 wherein a, b and c are zero.
4. A process as defined by claim 3 wherein X is chlorine.
5. A process as defined by claim 4 wherein the ratio of x to y is 1:1.
6. A process as defined by claim 5 wherein the fibrous material treated is paper pulp.
7. A process as defined by claim 6 wherein the resin addon is from 0.2 to 1.5 percent by weight.
8. The paper produced by the process as defined by claim 7.
US323177A 1973-01-12 1973-01-12 Process for fiber treatment Expired - Lifetime US3880710A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US323177A US3880710A (en) 1973-01-12 1973-01-12 Process for fiber treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US323177A US3880710A (en) 1973-01-12 1973-01-12 Process for fiber treatment

Publications (1)

Publication Number Publication Date
US3880710A true US3880710A (en) 1975-04-29

Family

ID=23258046

Family Applications (1)

Application Number Title Priority Date Filing Date
US323177A Expired - Lifetime US3880710A (en) 1973-01-12 1973-01-12 Process for fiber treatment

Country Status (1)

Country Link
US (1) US3880710A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5833807A (en) * 1997-04-17 1998-11-10 E. I. Du Pont De Nemours And Company Aramid dispersions and aramid sheets of increased uniformity
EP1277880A1 (en) * 2001-07-21 2003-01-22 Teijin Twaron GmbH Process for preparing p-Aramide paper, p-Aramide paper, p-Aramide pulp, and the use of the paper and the pulp

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2518266A (en) * 1946-08-14 1950-08-08 Ici Ltd Quaternary ammonium textile treatment agents and method of application thereof
US2518267A (en) * 1947-10-07 1950-08-08 Ici Ltd Quaternary compounds and manufacture and use thereof as textile treating agents

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2518266A (en) * 1946-08-14 1950-08-08 Ici Ltd Quaternary ammonium textile treatment agents and method of application thereof
US2518267A (en) * 1947-10-07 1950-08-08 Ici Ltd Quaternary compounds and manufacture and use thereof as textile treating agents

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5833807A (en) * 1997-04-17 1998-11-10 E. I. Du Pont De Nemours And Company Aramid dispersions and aramid sheets of increased uniformity
EP1277880A1 (en) * 2001-07-21 2003-01-22 Teijin Twaron GmbH Process for preparing p-Aramide paper, p-Aramide paper, p-Aramide pulp, and the use of the paper and the pulp

Similar Documents

Publication Publication Date Title
US2595935A (en) Wet strength paper and process for the production thereof
US4450045A (en) Preparation of water-soluble, nitrogen-containing condensates and their use in papermaking
US3239491A (en) Resin for wet strength paper
US4371674A (en) Water soluble crosslinked ethyleneimine grafted polyamidoamine
CA1144691A (en) Sizing accelerator
US4328142A (en) Preparation of water-soluble condensates and their use as crosslinking agents for the preparation of papermaking aids
US4075177A (en) Thermally hardenable cationic resin from dicarboxylic acid, dialkanolamine and polyamine copolymer condensed with epichlorohydrin
US3922243A (en) Ketene dimer modified water-dispersible thermosettable cationic resins
US3622528A (en) Polyethylenimine fatty acid epichlorohydrin product
US3728214A (en) Polyamine-acrylamide-polyaldehyde resins having utility as wet and dry strengthening agents in papermaking
CA1045735A (en) Stable rosin dispersions
US5714552A (en) Process for making epichlorohydrin resins
US3923745A (en) Water-dispersible thermosettable cationic resins and paper sized therewith
DE19728789A1 (en) Preparation of poly:amine epichlorohydrin polycondensate solution with low di:chloro-propan-ol content
US3880710A (en) Process for fiber treatment
US2694630A (en) Sized waterlaid glass fiber products and process of preparing the same
DE2928878A1 (en) AQUEOUS SOLUTION OF A HEAT-CURING OR FIXABLE RESIN, PROCESS FOR ITS PREPARATION AND ITS USE IN A PAPER COAT
US3692092A (en) Paper containing a polyethylenimine-fatty acid epichlorohydrin product
DE69132043T2 (en) Process for the preparation of epichlorohydrin resins
US2890978A (en) Paper of high dry strength and low wet strength
US3880707A (en) Process for fiber treatment
AU654847B2 (en) Epihalohydrin/polyamine polymers containing low levels of dihalopropanols, process for making the same and paper sizes made therefrom
US2758026A (en) Sized waterlaid glass fiber products and process of preparing the same
US3635842A (en) Short life paper size from modified polyalkylene-imines
US4520159A (en) Process for producing polyaminopolyamides containing halohydrin functionality

Legal Events

Date Code Title Description
AS Assignment

Owner name: OCCIDENTAL CHEMICAL CORPORATION

Free format text: CHANGE OF NAME;ASSIGNOR:HOOKER CHEMICALS & PLASTICS CORP.;REEL/FRAME:004109/0487

Effective date: 19820330