US2487899A - Process of wax sizing papermaking fibers using a cationic surface active agent - Google Patents

Process of wax sizing papermaking fibers using a cationic surface active agent Download PDF

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US2487899A
US2487899A US593102A US59310245A US2487899A US 2487899 A US2487899 A US 2487899A US 593102 A US593102 A US 593102A US 59310245 A US59310245 A US 59310245A US 2487899 A US2487899 A US 2487899A
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wax
fibers
amino
cationic surface
surface active
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US593102A
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Laurence R Sherman
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Nopco Chemical Co
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Nopco Chemical Co
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Priority to BE462915D priority patent/BE462915A/xx
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Priority to GB4366/46A priority patent/GB612326A/en
Priority to FR931212D priority patent/FR931212A/en
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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
    • D21H23/00Processes or apparatus for adding material to the pulp or to the paper
    • 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
    • D21H17/07Nitrogen-containing compounds
    • 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
    • D21H17/60Waxes
    • 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
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/29Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
    • Y10T428/2913Rod, strand, filament or fiber
    • Y10T428/2933Coated or with bond, impregnation or core

Definitions

  • the present invention relates to the sizing of paper. More particularly the present invention relates to the sizing of paper fibers by adding wax thereto.
  • the sizing of paper with wax is well known in the 'artand in general involves the addition of a suitable wax emulsion to the paper stock in a beater with the subsequent addition of alum or the like tobreak the emulsion and fix the wax on the fibers.
  • wax may be deposited directly. upon paper fibers by-the-addition to the fibers and wax of a'cationic surface-active fixing agent. This fixes the wax directly on the fibers and gives a much higher take up of wax than is possible by utilizing a wax emulsion together with alum or the like.
  • a second objectof the present invention is to deposit a high proportion of wax onthe paper fibers by utilizing a cationic surface active agent for fixing the wax on the fibers.
  • a suitable quantity of pulp such as sulfite pulp either in bleached or unbleached condition is charged into a heater or other paper making apparatus capable of disintegrating the same. Thereafter the beater is heated to a temperature sufficient to melt the wax which is subsequently added. In general where ordinary wax having a melting point of approximately 120 F. is used, the beater is brought to a temperature above this point, such as approximately 130160 F., by the use of steam or by other heating means. Thereafter a cationic surface active agent of the type hereinafter to be described is added in the proportion of at least 3% by weight of the wax. The agent apparently fixes the wax on the fibers for no wax is apparent in the apparatus or during the remainder of the process.
  • the cationic surface active agents used in accordance with the present invention include certain amino-amides, glyoxalidines cyclized from those amino-amides, and the solubilized derivatives of either.
  • the amino-amides may best be described by the general formula: e
  • R represents an aliphatic chain containing from 7 to 23 carbon atoms
  • R. denotes a substituent selected from the group consisting of hydrogen and alkylol groups'containing 1 to 3 carbons
  • n is a number selected from the group consisting of 2 and 3 when R stands lfor hydrogen and n is a number selected from the group consisting'of 1, 2 and 3 when R represents an alkylol radical.
  • Glyoxalidines may be formed from amino-amides of the above formula by internal condensation wherein the carboxyl carbon atom of the amido group is linked to the nitrogen atom of the nearest amino group in the molecule.
  • This glyoxalidine ring formation occurs when the oxygen and hydrogen atoms of the amido group combin with a hydrogen atom of the nearest amino group thereby liberating a molecule of water.”
  • compounds corresponding to soluble acid salts or alkylated derivatives of the above type of compound may be used. These may be produced by treating a glyoxalidine or amide compound of the general formula above described with an aliphatic monocarboxylic acid of from 1 to 3 carbon atoms such as acetic, formic, glycolic, etc. or with a suitable ester of a mineral acid, as, for example, diethyl sulfate, triethyl phosphate, ethyl iodide, etc.
  • the resultant solubilized compounds may then be illustrated by the general formula:
  • R denotes a substituent selected from the group consisting respectively of hydrogen, when R Z is a 1 to 3 carbon aliphatic monocarboxylic acid, and an aliphatic alkyl group of from 1 to 3 carbon atoms, when Hz is an ester of a mineral acid with a 1 to 3 carbon aliphatic alcohol, and Z is selected fromthe group consisting of the respective residues of said acid and said ester; and where the formula also, encompasses the same derivatives of glyoxalidines produced from the amino-amides prior to addition of the R and Z radicals by linking the carboxyl carbon atom with the nitrogen atom of the near-- est amino group accompanied by liberation of a molecular proportion of water.
  • a suitable fat or fatty acid is;
  • the amino-amide may be heated to a relatively high temperature to drive off water in order to form a cyclic compound.
  • the cyclic compound equivalent to the amino-amide may then be-treated with an agent rendering the compound water soluble such as a suitable ester of a mineral acid, for example diethyl sulfate, triethyl phosphate, ethyl iodide, or an aliphatic monocarboxylic acid of from 1 to 3 carbon atoms such as acetic, formic, glycolic, etc., or the aminoamide may be added to the paper fibers and wax and thereafter the acid.
  • an agent rendering the compound water soluble such as a suitable ester of a mineral acid, for example diethyl sulfate, triethyl phosphate, ethyl iodide, or an aliphatic monocarboxylic acid of from 1 to 3 carbon atoms such as acetic, formic, glycolic, etc.
  • temperatures in the neighborhood of 200 C. or from 180 to 210 C. are utilized for the amidiflcation, and in the event the cyclic compound is desired, temperatures in the neighborhood of 300 C. are used.
  • Various polyalkylene polyamine, alkylene alkylol polyamine or polyalkylene alkylol polyamine compounds having from 2 to 4 amino groups may be used as, for
  • fatty acid portion of the compound may be utilized as the fatty acid portion of the compound.
  • oieic acid, ricinoleic acid, lauric acid, stearic acid, palmitic acid, etc. are examples of the fatty acids which may be utilized in preparing the amino-amide compound.
  • Example I 47.8 parts by weight of hydrogenated soybean oil and 25.2 parts of ethanol ethylenediamine were heated in a closed. vessel at 150 C. for approximately 6 to 8 hours in order to condense the same.
  • the resultant product is believed to consist largely of an amino-amide having the following formula:
  • a process for wax-sizing paper fibers consisting of suspending the fibers in water, heating the suspension to a temperature sufficiently high to melt wax, adding wax to the aqueous suspension, heating the suspension until the wax has completely melted and mixed with the fibers, and fixing the wax on the fibers by adding a cationic surface active substance to the fiber and wax suspension, said cationic substance being selected from the group consisting of amino-amides having the general formula:
  • R represents an aliphatic chain containing from 7 to 23 carbon atoms
  • R. denotes a substituent selected from the group consisting of hydrogen and alkylol groups containingl to 3 carbons
  • n is a number selected from the group consisting of 2 and 3 when R stands for hydrogen and n is a number selected from the group of 1, 2 and 3 when R represents an alkylol radical
  • R denotes a substituent selected from the group consisting respectively of hydrogen, when R z is a 1 to 3 carbon aliphatic monocarboxylic acid, and an aliphatic alkyl group of from 1 to 3 carbon atoms
  • R 2 is an ester of a mineral acid with a 1 to 3 carbon aliphatic alcohol
  • z is selected from the group consisting of the respective residues of said acid and said ester.
  • a process for wax-sizing paper fibers consisting of suspending the fiber in water and heating the water suspension to a temperature sufficiently high to melt wax, adding wax thereto, heating the wax and fiber until the wax has completely melted and mixed with the fiber and adding ethanol amino ethylene stearamide to fix the wax on the fibers.

Description

Patented Nov. 15, 1949 2,487,899 WAX SIZING PAPERMAKING raoc'nss or FIBERS USING A CATIONIC SURFACE AC- TIVE AGENT Laurence R. Sherman, Glens Falls, N. Y., assignor to Nopco Chemical Company, Harrison,
corporation of New Jersey No Drawing. Application May 10,1945,
1 Serial No. 593,102
" 4 Claims. (01. 92+21) The present invention relates to the sizing of paper. More particularly the present invention relates to the sizing of paper fibers by adding wax thereto.
The sizing of paper with wax is well known in the 'artand in general involves the addition of a suitable wax emulsion to the paper stock in a beater with the subsequent addition of alum or the like tobreak the emulsion and fix the wax on the fibers.
It has now been discovered in accordance with the present invention that wax may be deposited directly. upon paper fibers by-the-addition to the fibers and wax of a'cationic surface-active fixing agent. This fixes the wax directly on the fibers and gives a much higher take up of wax than is possible by utilizing a wax emulsion together with alum or the like. a
' It is one of the objects of the present inven-' tion, therefore, to provide a novel process for sizing paper, fibers with wax by depositing the wax, directly on the fibers from a molten con-.
dition.
A second objectof the present invention is to deposit a high proportion of wax onthe paper fibers by utilizing a cationic surface active agent for fixing the wax on the fibers. I
Other objects and advantages of the present invention will become apparent from the present description and claims.
In practicing the present process a suitable quantity of pulp such as sulfite pulp either in bleached or unbleached condition is charged into a heater or other paper making apparatus capable of disintegrating the same. Thereafter the beater is heated to a temperature sufficient to melt the wax which is subsequently added. In general where ordinary wax having a melting point of approximately 120 F. is used, the beater is brought to a temperature above this point, such as approximately 130160 F., by the use of steam or by other heating means. Thereafter a cationic surface active agent of the type hereinafter to be described is added in the proportion of at least 3% by weight of the wax. The agent apparently fixes the wax on the fibers for no wax is apparent in the apparatus or during the remainder of the process. Almost all of the wax introduced becomes fixed onto the pulp fibers, for when paper formed from this wax-sized pulp is extracted with a suitable solvent to determine its wax content the total quantity of wax in the paper is found to be nearly 100% of the weight of wax which was added to the pulp. The finished sheets thus prepared are smooth and show no evidence of wax Y spots and appear in every way to be suitably sized.
The cationic surface active agents used in accordance with the present invention include certain amino-amides, glyoxalidines cyclized from those amino-amides, and the solubilized derivatives of either. The amino-amidesmay best be described by the general formula: e
H RFC-(NHCH:CHI)1|, 'N
' I R where R represents an aliphatic chain containing from 7 to 23 carbon atoms; R. denotes a substituent selected from the group consisting of hydrogen and alkylol groups'containing 1 to 3 carbons, and n is a number selected from the group consisting of 2 and 3 when R stands lfor hydrogen and n is a number selected from the group consisting'of 1, 2 and 3 when R represents an alkylol radical. Glyoxalidines may be formed from amino-amides of the above formula by internal condensation wherein the carboxyl carbon atom of the amido group is linked to the nitrogen atom of the nearest amino group in the molecule. This glyoxalidine ring formation occurs when the oxygen and hydrogen atoms of the amido group combin with a hydrogen atom of the nearest amino group thereby liberating a molecule of water." Further, compounds corresponding to soluble acid salts or alkylated derivatives of the above type of compound may be used. These may be produced by treating a glyoxalidine or amide compound of the general formula above described with an aliphatic monocarboxylic acid of from 1 to 3 carbon atoms such as acetic, formic, glycolic, etc. or with a suitable ester of a mineral acid, as, for example, diethyl sulfate, triethyl phosphate, ethyl iodide, etc. The resultant solubilized compounds may then be illustrated by the general formula:
. o H r [R -t l(NHCHzCH,),N R z a where R R and n have thevalues assigned previously, R. denotes a substituent selected from the group consisting respectively of hydrogen, when R Z is a 1 to 3 carbon aliphatic monocarboxylic acid, and an aliphatic alkyl group of from 1 to 3 carbon atoms, when Hz is an ester of a mineral acid with a 1 to 3 carbon aliphatic alcohol, and Z is selected fromthe group consisting of the respective residues of said acid and said ester; and where the formula also, encompasses the same derivatives of glyoxalidines produced from the amino-amides prior to addition of the R and Z radicals by linking the carboxyl carbon atom with the nitrogen atom of the near-- est amino group accompanied by liberation of a molecular proportion of water.
In preparing the cationic compound which fixes the wax on. the fibers in accordance with the present invention, a suitable fat or fatty acid is;
reacted with a polyalkylene polyamine compound in; order to form an amino-amide, or in the alternative, the fatty acid or fat is reacted with enace an alkylene alkylol polyamine or a polyalkylene alkylol polyamine compound. Thereafter. the amino-amide may be heated to a relatively high temperature to drive off water in order to form a cyclic compound. The amino-amide. or the cyclic compound equivalent to the amino-amide, may then be-treated with an agent rendering the compound water soluble such as a suitable ester of a mineral acid, for example diethyl sulfate, triethyl phosphate, ethyl iodide, or an aliphatic monocarboxylic acid of from 1 to 3 carbon atoms such as acetic, formic, glycolic, etc., or the aminoamide may be added to the paper fibers and wax and thereafter the acid.
In general, temperatures in the neighborhood of 200 C. or from 180 to 210 C. are utilized for the amidiflcation, and in the event the cyclic compound is desired, temperatures in the neighborhood of 300 C. are used. Various polyalkylene polyamine, alkylene alkylol polyamine or polyalkylene alkylol polyamine compounds having from 2 to 4 amino groups may be used as, for
- example, diethylene triamine, ethanol ethylene diamine, ethanol diethylene triamine, triethylene tetramine, etc. Almost any fatty acid or fatty acid glyceride having from 8 to 24 carbon atoms in the chain may be utilized as the fatty acid portion of the compound. Thus, oieic acid, ricinoleic acid, lauric acid, stearic acid, palmitic acid, etc. are examples of the fatty acids which may be utilized in preparing the amino-amide compound.
The following specific example serves to illustrate but is not intended to limit the present invention.
Example I 47.8 parts by weight of hydrogenated soybean oil and 25.2 parts of ethanol ethylenediamine were heated in a closed. vessel at 150 C. for approximately 6 to 8 hours in order to condense the same. The resultant product is believed to consist largely of an amino-amide having the following formula:
Approximately 1500 grams of unbleached sulfite pulp and 1000 grams of bleached sulfite pulp were disintegrated in a laboratory beater with 50 l. of water and heated to 160 F. 50 grams of scale wax were added to the beater followed by grams of the amino-amide prepared as above set forth. Beating was then continued for 30 minutes. Hand sheets made from the stock had a good appearance and feel. Samples of these sheets were extracted with petroleum ether to determine the wax content and the wax content thereof was approximately 1.98% which was evidence of excellent take up of the wax.
Having described my invention, what I claim as new and desire to secure by Letters Patent is:
1. A process for wax-sizing paper fibers, the steps consisting of suspending the fibers in water, heating the suspension to a temperature sufficiently high to melt wax, adding wax to the aqueous suspension, heating the suspension until the wax has completely melted and mixed with the fibers, and fixing the wax on the fibers by adding a cationic surface active substance to the fiber and wax suspension, said cationic substance being selected from the group consisting of amino-amides having the general formula:
and salts oi said amino-amides having the general formula:
where R represents an aliphatic chain containing from 7 to 23 carbon atoms, R. denotes a substituent selected from the group consisting of hydrogen and alkylol groups containingl to 3 carbons, and n is a number selected from the group consisting of 2 and 3 when R stands for hydrogen and n is a number selected from the group of 1, 2 and 3 when R represents an alkylol radical, R denotes a substituent selected from the group consisting respectively of hydrogen, when R z is a 1 to 3 carbon aliphatic monocarboxylic acid, and an aliphatic alkyl group of from 1 to 3 carbon atoms, when R 2 is an ester of a mineral acid with a 1 to 3 carbon aliphatic alcohol, and z is selected from the group consisting of the respective residues of said acid and said ester.
2. A process according to claim 1 in which the quantity of said cationic surface active substance added is at least 3% of the weight of wax present in the suspension.
3. A process for wax-sizing paper fibers, the steps consisting of suspending the fiber in water and heating the water suspension to a temperature sufficiently high to melt wax, adding wax thereto, heating the wax and fiber until the wax has completely melted and mixed with the fiber and adding ethanol amino ethylene stearamide to fix the wax on the fibers.
4. A process according to claim 3 in which the quantity of ethanol amino ethylene stearamide added is at least 3% of the weight of wax present in the suspension.
LAURENCE R. SHERMAN.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 1,992,589 Tucker Feb. 26, 1935 2,096,129 Neitzke Oct. 19, 1937 2,186,609 Kress Jan. 9, 1940 2,206,090 Haggenmacher July 2, 1940 2,268,273 Wilkes -Q Dec. 30, 1941 2,277,788 Shipp Mar. 31, 1942 2,343,090 Smith Feb. 29, 1944 2,343,095 Smith Feb. 29, 1944 2,401,027 Tausch May 28, 1946 2,442,972 Edelstein June 8, 1948 FOREIGN PATENTS Number Country Date 319,745 Great Britain Dec. 29, 1930 OTHER REFERENCES TAPPI, Technical Association Papers, Series 22, pp. 264-267 (1939).
Paper Trade Journal. Aug. 22, 1940, pp. 30 and 31.
Rayon Textile Monthly, March 1944, p. 79.
Journal of Society Chemical Industries, April 1938, p. 117.
Industrial and Engineering Chemistry, January 1941, PP. 16-22.
US593102A 1945-05-10 1945-05-10 Process of wax sizing papermaking fibers using a cationic surface active agent Expired - Lifetime US2487899A (en)

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BE462915D BE462915A (en) 1945-05-10
US593102A US2487899A (en) 1945-05-10 1945-05-10 Process of wax sizing papermaking fibers using a cationic surface active agent
GB4366/46A GB612326A (en) 1945-05-10 1946-02-12 Improvements relating to the sizing of paper fibres and the like
FR931212D FR931212A (en) 1945-05-10 1946-03-28 Paper sizing process

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Cited By (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2563897A (en) * 1945-07-13 1951-08-14 American Cyanamid Co Sizing cellulosic fibers with cationic melamine resin and hydrophobic material
US2601598A (en) * 1947-12-26 1952-06-24 American Cyanamid Co Application of dispersed materials to cellulosic fibers
US2601597A (en) * 1946-09-06 1952-06-24 American Cyanamid Co Application of dispersed coating materials to cellulosic fibers
US2680995A (en) * 1950-12-01 1954-06-15 Stimson Lumber Company Method of making hardboard
US2683089A (en) * 1952-06-10 1954-07-06 American Cyanamid Co Bibulous sheet
US2683088A (en) * 1952-06-10 1954-07-06 American Cyanamid Co Soft bibulous sheet
US2683087A (en) * 1948-02-10 1954-07-06 American Cyanamid Co Absorbent cellulosic products
US2686121A (en) * 1948-07-07 1954-08-10 Morton Chemical Co Process of loading cellulosic fibers
US2694633A (en) * 1950-02-23 1954-11-16 Talbott Dev Associates Affixing organic and inorganic additaments to cellulosic materials
US2739058A (en) * 1952-07-17 1956-03-20 Du Pont Process for sizing paper with polyethylene
US2758025A (en) * 1952-05-23 1956-08-07 Armco Steel Corp High temperature stainless steel
US2764483A (en) * 1951-11-06 1956-09-25 Du Pont Process for sizing paper
US2767089A (en) * 1951-05-21 1956-10-16 Gen Mills Inc Paper containing polyamide resins and process of producing same
US2767088A (en) * 1952-06-24 1956-10-16 Mosinee Paper Mills Company Method of impregnating fibrous materials
US2772969A (en) * 1951-04-18 1956-12-04 American Cyanamid Co Sizing of paper with fatty acid polyalkylenepolyamine compositions
US2794737A (en) * 1954-06-10 1957-06-04 American Cyanamid Co Paper sized with a condensation product of a fatty amine and hexahydro-1, 3, 5-triacrylyl-s-triazine
DE1012165B (en) * 1951-04-18 1957-07-11 American Cyanamid Co Method for gluing paper
US2803171A (en) * 1953-08-26 1957-08-20 Patent & Licensing Corp Process for producing a water vapor impermeable board
US2924397A (en) * 1957-03-18 1960-02-09 Heppner Sales Co Permanent magnet tension device
US2974339A (en) * 1958-04-25 1961-03-14 Key Products Company Dust mop
DE1237423B (en) * 1958-02-11 1967-03-23 Shell Int Research Process for felling waxy substances onto fiber material
US4935096A (en) * 1988-12-06 1990-06-19 Garden State Paper Company, Inc. Process for the deinking of cellulosic materials
WO2006134597A2 (en) * 2005-06-16 2006-12-21 Ha Industrial Technologies Ltd. Paper product and method therefor using molten wax suspension

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DE1030671B (en) * 1954-05-26 1958-05-22 Zschimmer & Schwarz Chem Fab Method for gluing paper
DE2818880C3 (en) * 1978-04-28 1982-05-13 Mobil Oil Ag In Deutschland, 2000 Hamburg Process for sizing paper and cardboard using wax dispersions

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GB319745A (en) * 1928-09-27 1930-12-29 Albert Lewis Clapp Manufacture of waterproof fibrous products
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US2096129A (en) * 1936-02-24 1937-10-19 Bennett Inc Manufacture of sized papers
US2186609A (en) * 1937-05-05 1940-01-09 Paper Chemistry Inst Method of removing wax from waxed paper stock
US2206090A (en) * 1937-05-17 1940-07-02 Warwick Chemical Co Waterproofing composition and similar emulsion
US2268273A (en) * 1939-05-27 1941-12-30 Carbide & Carbon Chem Corp Textile finishing
US2277788A (en) * 1940-08-03 1942-03-31 Du Pont Treatment of textiles and composition useful therefor
US2343090A (en) * 1940-08-03 1944-02-29 Du Pont Treatment of textiles and composition useful therefor
US2343095A (en) * 1940-08-03 1944-02-29 Du Pont Resin dispersion useful in the textile and paper industries
US2401027A (en) * 1942-10-21 1946-05-28 American Anode Inc Deposition of rubber from aqueous dispersions of rubber
US2442972A (en) * 1941-01-23 1948-06-08 Sidney M Edelstein Aqueous dispersions of electropositive materials

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GB319745A (en) * 1928-09-27 1930-12-29 Albert Lewis Clapp Manufacture of waterproof fibrous products
US1992589A (en) * 1931-04-17 1935-02-26 Dewey And Almy Chem Comp Organic fiber and method of preparing same
US2096129A (en) * 1936-02-24 1937-10-19 Bennett Inc Manufacture of sized papers
US2186609A (en) * 1937-05-05 1940-01-09 Paper Chemistry Inst Method of removing wax from waxed paper stock
US2206090A (en) * 1937-05-17 1940-07-02 Warwick Chemical Co Waterproofing composition and similar emulsion
US2268273A (en) * 1939-05-27 1941-12-30 Carbide & Carbon Chem Corp Textile finishing
US2277788A (en) * 1940-08-03 1942-03-31 Du Pont Treatment of textiles and composition useful therefor
US2343090A (en) * 1940-08-03 1944-02-29 Du Pont Treatment of textiles and composition useful therefor
US2343095A (en) * 1940-08-03 1944-02-29 Du Pont Resin dispersion useful in the textile and paper industries
US2442972A (en) * 1941-01-23 1948-06-08 Sidney M Edelstein Aqueous dispersions of electropositive materials
US2401027A (en) * 1942-10-21 1946-05-28 American Anode Inc Deposition of rubber from aqueous dispersions of rubber

Cited By (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2563897A (en) * 1945-07-13 1951-08-14 American Cyanamid Co Sizing cellulosic fibers with cationic melamine resin and hydrophobic material
US2601597A (en) * 1946-09-06 1952-06-24 American Cyanamid Co Application of dispersed coating materials to cellulosic fibers
US2601598A (en) * 1947-12-26 1952-06-24 American Cyanamid Co Application of dispersed materials to cellulosic fibers
US2683087A (en) * 1948-02-10 1954-07-06 American Cyanamid Co Absorbent cellulosic products
US2686121A (en) * 1948-07-07 1954-08-10 Morton Chemical Co Process of loading cellulosic fibers
US2694633A (en) * 1950-02-23 1954-11-16 Talbott Dev Associates Affixing organic and inorganic additaments to cellulosic materials
US2680995A (en) * 1950-12-01 1954-06-15 Stimson Lumber Company Method of making hardboard
DE1012165B (en) * 1951-04-18 1957-07-11 American Cyanamid Co Method for gluing paper
US2772969A (en) * 1951-04-18 1956-12-04 American Cyanamid Co Sizing of paper with fatty acid polyalkylenepolyamine compositions
US2767089A (en) * 1951-05-21 1956-10-16 Gen Mills Inc Paper containing polyamide resins and process of producing same
US2764483A (en) * 1951-11-06 1956-09-25 Du Pont Process for sizing paper
US2758025A (en) * 1952-05-23 1956-08-07 Armco Steel Corp High temperature stainless steel
US2683088A (en) * 1952-06-10 1954-07-06 American Cyanamid Co Soft bibulous sheet
US2683089A (en) * 1952-06-10 1954-07-06 American Cyanamid Co Bibulous sheet
US2767088A (en) * 1952-06-24 1956-10-16 Mosinee Paper Mills Company Method of impregnating fibrous materials
US2739058A (en) * 1952-07-17 1956-03-20 Du Pont Process for sizing paper with polyethylene
US2803171A (en) * 1953-08-26 1957-08-20 Patent & Licensing Corp Process for producing a water vapor impermeable board
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GB612326A (en) 1948-11-11
FR931212A (en) 1948-02-17
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