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Publication numberUS3050437 A
Publication typeGrant
Publication dateAug 21, 1962
Filing dateJun 16, 1959
Priority dateJun 16, 1959
Publication numberUS 3050437 A, US 3050437A, US-A-3050437, US3050437 A, US3050437A
InventorsArlt Jr Herbert G
Original AssigneeAmerican Cyanamid Co
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Manufacture of sized paper
US 3050437 A
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Description  (OCR text may contain errors)

United States Patent 3,050,437 MANUFACTURE OF SIZED PAPER Herbert G. Arlt, In, Pearl River, N.Y., assignor to American Cyanamid Company, New York, N.Y., a corporation of Maine N0 Drawing. Filed June 16, 1959, Ser. No. 820,579 Claims. (Cl. 162-158) The present invention relates to the manufacture of sized paper by use of emulsions of hydrophobic isocyanates. The invention includes the papermaking processes involved and the paper itself.

At the present time the manufacture of paper, paperboard, etc. (hereinafter referred to as paper) of high lactic acid resistance is an important specialty of the papermaking art. Such paper is used for the wrapping of butter, margarine and cheese, and as containers for liquid milk and buttermilk. Customarily the lactic acid resistance of such paper is determined by the penescope method wherein the paper or paperboard is first painted With methyl orange on one side and, after the methyl orange has dried, the paper is contacted with 20% aqueous lactic acid at 100 F. This lactic acid resistance is taken as the time required for the solution to penetrate the paper and produce five red spots. When tested in this manner, first-quality rosin sized paper resists penetration for 300400 seconds.

The discovery has now been made that paper of very satisfactory lactic acid resistance is produced by a process which comprises adding a colloidal emulsion of a hydrophobic organic isocyanate directly to a dilute aqueous suspension of papermaking fibers, sheeting the fibers to form a wet Web, and heating the sheets for 1 to 3 minutes at 200250 F. The sizing is thus in substantial part developed while the paper is on the machine.

I have further discovered that best results are obtained when the isocyanate is added as an anionic emulsion, and particularly when the isocyanate is deposited on the fibers and the fibers are sheeted in the absence of dissolved polyvalent metal ions.

According to the present invention, a beater pulp of papermaking cellulose fibers is prepared at any convenient consistency, for example, between about 0.5% and 5%. To this is added a small amount of the colloidal isocyanate emulsion more particularly described below. The suspension is agitated gently to distribute the emulsion particles uniformly therethrough.

The aqueous suspension of fibers is then sheeted, preferably at a pH between 4.5 and 6, to form a wet waterlaid web containing emulsified isocyanate droplets, and the web is dried on steam-heated rolls, likewise in accordance with conventional practice. The sizing properties of the isocyanate in substantial part are developed during the drying step, the isocyanate droplets reacting chemically with the cellulose of which the fibers are composed.

A simplified flow diagram of the process is as follows:

Form an aqueous suspension of papermaking cellulose fibers Add an emulsion of a hydrophobic organic isocyanate Deposit at least part of the isocyanate on the fibers Sheet the suspension to form a water-laid web Dry the web at a temperature between about 200 F. and 250 F. thereby reacting the deposited isocyanate chemically with the fibers A feature of the invention is that the isocyanate size causes a slight but definite increase in the wet strength of the paper produced. This result is surprising because rosin size, wax size and other sizes commonly used to produce lactic acid resistance impart no such strength and in fact usually have a weakening action.

The paper obtained consists essentially of cellulose fibers having one or more higher alkyl isocyanates uniformly reacted therewith. The paper exhibits very satisfactory resistance to penetration by aqueous lactic acid, ink and water.

As sizing agents good results are obtained with alkyl isocyanates containing at least 10 carbon atoms. The isocyanate grouping is mono-valent and the invention includes the use of dior poly-isocyanates. Thus the invention includes such isocyanates as 2-ethyldecyl isocyanate, 9-phenylhexadecyl isocyanate, and 6-cyclohexyldodecyl isocyanate. There maybe also used poly-isocyanates such as 1,18-octadecyl diisocyanate and 1,12-dodecyl diisocyanate, wherein one long chain alkyl grouping connects two isocyanate radicals and imparts hydrophobic properties to the molecule as a whole. Considerably better results are obtained where the alkyl radicals are straight chain. Accordingly, I prefer to use isocyanates such as decyl isocyanate, hexadecyl isocyanate and octadecyl isocyanate.

The isocyanates used in the process of the present invention are liquid or solids having low melting points and are thus readily emulsified. A suitable procedure comprises slowly pouring the isocyanate into a rapidly agitated volume of water containing an anionic dispersing agent to form a crude or primary emulsion which can then be converted to a colloidal emulsion by known means, for example, by passage through a homogenizer until the dispersed isocyanate particles or droplets (hereinafter for convenience generically referred to as droplets have been reduced to substantially colloidal dimensions, so that the emulsion shows substantially no tendency to cream on standing. As non-ionic emulsifying agents there may be used, for example, the condensation products of ethylene oxide with long chain alkyl phenols, the higher fatty amides, or the fatty acid polyhydric alcohol esters; as anionic emulsifying agents there may be used the soaps of fatty acids with alkali hydroxides, the higher alkyl sulfates and sulfonates, and the aryl and alkaryl sulfonates as such or after reaction with formaldehyde. In practice, the non-ionic agents and the polyalkaryl naphthalene sulfonate dispersing agents are preferred as these agents are at a basis weight of about 50 lbs. and 200 lbs. per x /500 ream. The light sheets are dried for one minute at 240 F. and the heavy sheets for 3 minutes at 240 F.

The handsheets are conditioned for 24 hours at 73 F. and relative humidity. The thick sheets are tested for their Water absorption and resistance to penetration by hot 20% aqueous lactic acid solution (penescope method) and the thin sheets for their wet strength and their resistance to penetration by ink. Results are as stable both at acid and alkaline pH values eliminating lo follows:

1 On dry weight of fibers. 2 Before sheeting.

1 By penescope.

4 Optical.

5 Increase in weight after 15 minutes of total immersion.

need for precise pH control. However, the invention does not depend on the particular emulsifying agent selected.

The emulsion is uniformly added to the fibrous suspension at any convenient solids content. I prefer, however, to add the emulsion in dilute free-fiowing form, i.e., at a solids content of 5% to 15% by weight, so as to facilitate uniform distribution of the colloidal droplets throughout the suspension.

The invention will be described more particularly by the examples which follow. These examples represent specific embodiments of the invention and are not to be construed as limitations thereon.

Examples 1-7 The following illustrates the results obtained by the process of the present invention of a pulp which is normally very difiicult to size. The results are shown in comparison with those obtained in control experiments.

An aqueous suspension of well-beaten bleached hardwood kraft pulp is prepared at 0.6% consistency and is adjusted to a neutral pH. The sizing agent is prepared by rapidly agitating 10 gm. of octadecyl isocyanate with ml. of water and 0.2 gm. of a mixture of sodium diisopropyl naphthalene sulfonate and sodium triisopropyl naphthalene sulfonate to form an anionic emulsion which is homogenized three times in a laboratory homogenizer. A stable colloidal suspension is obtained.

A non-ionic emulsion is prepared in the same manner using a p-nonylphenol-ethylene oxide emulsifying agent in place of the anionic agents shown above.

Aliquots of pulp are Withdrawn and treated as shown in the table below, after which the aliquots are gently stirred to distribute the colloidal sizing agent uniformly therethrough. The aliquots are then adjusted to pH 4.5 with hydrochloric acid, sheeted on a Nash handsheet machine, and formed into handsheets in accordance with usual laboratory practice. The handsheets are prepared The results show that good sizing can be obtained with alum present, but that best results are obtained when the papermaking process is performed by use of an anionic emulsion in the absence of any polyvalent metal salt.

I claim:

1. A method of manufacturing sized paper which comprises forming an aqueous suspension of papermaking cellulose fibers, adding thereto an emulsion of a hydrophobic organic isocyanate, depositing at least part of said isocyanate on said fibers, sheeting the suspension to form a waterlaid web, and drying said Web at a temperature between about 200 F.250 F. whereby said deposited isocyanate chemically reacts with the fibers.

2. A method according to claim 1 wherein the isocyanate is octadecyl isocyanate.

3. A method according to claim 1 wherein the emulsion is anionic and the isocyanate is deposited on the fibers by the action of alum.

4. A method according to claim 1 wherein the emulsion is anionic and the isocyanate is deposited on the fibers and the fibers are sheeted in the absence of dissolved polyvalent metal ions.

5. A method according to claim 1 wherein the fibers are sheeted at a pH between about 4.5 and 6.

References Cited in the file of this patent UNITED STATES PATENTS 2,284,895 Hanford et al June 2, 1942, 2,303,364 Schirm Dec. 1, 1942 2,806,190 Robinson Sept. 10, 1957 2,835,652 Haven May 20, 1958 2,893,898 Evans et a1 July 7, 1959 2,930,106 Wrotnowski Mar. 29, 1960 FOREIGN PATENTS 1,013,946 France May 14, 1952 804,504 Great Britain Nov. 19, 1958

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2284895 *Oct 8, 1937Jun 2, 1942Du PontTreatment of textiles to impart water-repellence
US2303364 *Nov 5, 1938Dec 1, 1942Heberlein Patent CorpProcess and product for making textile and other material water repellent
US2806190 *Nov 6, 1952Sep 10, 1957Sprague Electric CoLow power factor capacitor
US2835652 *Apr 16, 1954May 20, 1958Du PontOrganic phosphorus containing isocyanates and polymers
US2893898 *Apr 30, 1956Jul 7, 1959Bradford Dyers Ass LtdMethod of rendering materials water-repellent
US2930106 *Mar 14, 1957Mar 29, 1960American Felt CompanyGaskets
FR1013946A * Title not available
GB804504A * Title not available
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3212961 *Oct 23, 1961Oct 19, 1965Hercules Powder Co LtdPretreatment of paper pulp with ketene dimer in improving sizeability
US3214325 *May 7, 1962Oct 26, 1965Monsanto CoProcess of sizing paper with a halo-sym-triazine
US3223543 *May 26, 1961Dec 14, 1965American Cyanamid CoPaper sizing emulsion
US3223544 *Mar 19, 1963Dec 14, 1965American Cyanamid CoManufacture of cationic paper sizing ketene dimer emulsions
US3278560 *Jul 25, 1962Oct 11, 1966Monsanto CoPolyglycidylpolyamine compounds
US3499824 *Feb 27, 1967Mar 10, 1970American Cyanamid CoAqueous cationic emulsions of papersizing isocyanates and manufacture of paper therewith
US4240935 *Dec 22, 1978Dec 23, 1980Hercules IncorporatedKetene dimer paper sizing compositions
US4623428 *Oct 22, 1984Nov 18, 1986Ciba-Geigy CorporationProcess for sizing paper with anionic hydrophobic sizing agents and cationic retention aids
US4627889 *May 23, 1983Dec 9, 1986Ciba-Geigy CorporationProcess for sizing paper with anionic hydrophobic sizing agents and cationic retention aids
US5961783 *Jun 6, 1997Oct 5, 1999Vinings Industries, Inc.Process for enhancing the strength and sizing properties of cellulosic fiber using a self-emulsifiable isocyanate and a coupling agent
Classifications
U.S. Classification162/158, 8/192
International ClassificationD21H17/08, D21H17/00
Cooperative ClassificationD21H17/08
European ClassificationD21H17/08