|Publication number||US1773201 A|
|Publication date||Aug 19, 1930|
|Filing date||Dec 18, 1926|
|Priority date||Dec 18, 1926|
|Publication number||US 1773201 A, US 1773201A, US-A-1773201, US1773201 A, US1773201A|
|Inventors||Harold E Cude, Reed P Rose|
|Original Assignee||Gen Rubber Co|
|Export Citation||BiBTeX, EndNote, RefMan|
|Referenced by (3), Classifications (7)|
|External Links: USPTO, USPTO Assignment, Espacenet|
Patented Aug. 19,1930
" UNITED STATES PATENT OFFICE I asap 2. nosn, or uoxson nmen rs, AND HAROLD 2. owns, or 1mm PARK, NEW 1031:, ASSIGZN'OBS 'ro GENERAL RUBBER COMPANY, or raw You, x. Y.,- A com POBA'IION 01' NEW JERSEY P300388 FOR THE PROTJUCTION OF COMBTNATIONS OF RUBBER AND PDEB AND PRODUCTS OBTAINED THEBEBY No Drawing.
This invention relates to processes for the production of combinations of paper and rubber and particularly to such combinations where the rubber is in the form of a dispersion or emulsion; and to the products ob tained thereb The resent invention is also concerne with an-lmproved method for depositing rubber from a natural or artificial dispersion thereof upon paper making fibres of any sort.
The principal object of the inventlon 1s to provide an improved process for depositing rubber from a dispersion such as rubber latex, upon paper-making fibres. Another object of the invention is to make the fibres easier to handle in the beating and paper-making processes. Still another object is to increase the stability of the paper pulp and rubber dispersion with reference to each other in the beater, refining engines, stuff chests, and while running over the paper machine. A further object is to decrease the size of the rubber particles deposited from the dispersion upon the fibres. The invention also aims to furnish a means of obtaining better control of the rate of coagulation of the rubber dispersion. The invention also includes among-its objects means for reducing the co agulation risk when sizing materials such as rosin size and loading materials such as clay, talc, colors, slate, etc., are added in the beater. Still another object is to precipitate or deposit the proteins from natural latex upon the fibres during the paper making operation.
With a preferred embodiment in mind but not desiring to place undue limitation upon the scopeof the invention except what may be required bythe prior art the invention briefly stated consists in mixing a protective colloid with a mass of beaten paper-making pulp, adding a rubber dispersion to the mixture after the latter has been made alkaline, depositing the rubber from the dispersion upon the fibres and coagulating the rubber thereupon, and forming paper from the treated fibres.
Heretofore it has been proposed to make rubber-containing paper y incorporating Application filed December 1a, 1926. man No. 155,104;
rubber latex with paper pulp. One proposed method is as follows:
Paper pulp is beaten in an ordinary paperbeating engine. After this operation is completed the contents of the beater are made alkaline with approximately one half of one percent ammonia, caustic soda, sodium silicate, or other alkali. The beater roll is raised off the bedplate, after which it serves simply as a means of agitating the pulp in the beater. The rubber latex or other emulsion containmg rubber is then added in front of the beater roll to give the desired rcentage of rubber on the paper pulp. A r the latex has become thoroughly mixed with the pulp, the rubber is coagulated by the addition of ZlIlC sulphate, (paper makers alum) aluminum sulphate, or similar chemicals. This co-' agulation takes place in two stages. The 00- agulating solution is added to the material 1n the beater just in front of the beater roll so that it is immediatel mixed with the pulp-latex mixture. This addition is continued until approximately two-thirds of the quantity of solution r uired to neutralize the alkali present in tlie beater .has been added. After this point has been reached .the addition of coagulating solution is stopped for a short time (say ten to twenty mmutes). At the end of this period practicall all of the rubber in the latex has been agg omerated and adheres to the paper fibre. After this stage has been reached the, remainder of the coagulating solution is added, with enough excess to make the entire contents of the beater acid to indicators such as litmus paper.
The theory of adding the coagulantin two stages as above is that the first addition of coagulant causes rubber in the latex to agglomerate but not to coagulate. During the agglomerating stage the rubber is completely adsorbed on the surface of the fibre. After this adsorption has taken lace, the remamder of the coagulating so ution is added so that the agglomerated rubber is completely coagulated and set on the paper fibre.
It has been found that the addition of materials which may be classed as rotective colloids greatly increases the ease 0 handling ill latex the beater and improves the resultper. A large number of these prodlmown, among which are the modified starches, of which the soluble starch esters appear to be the best. Examples of these starch esters are the acetylated starches" known under the trade name of feculoid or tective colloids, the size of the particles in the precipitates or coagula is always very much smaller than would be the case if the protective colloid were not present. In other words the particles can be made to approach more nearly a colloidal condition than where protective agents are not used. This effect may be obtained according to the present invention in connection with the coagulation of rubber latex on to pa r fibre.
The preferred met d of carrying out the invention is as follows: The paper making fibre is beaten until it'has nearly-reached the condition required to form a satisfactory sheet on any standardtype of paper machine such as a Fourdrinier, cylinder, and wet machines. Before the beating is finished the protective colloid is added in amounts varying from 1 to 5%. Acetylated starches, glue or casein, or other protective colloid, may be employed, being added in solution or in a fine suspension depending upon the nature of the colloid. After the solution of protective colloid has been added, the mixturein the beater is then made alkaline with ammonium hydroxide, caustic soda, sodium silicate, or other alkali, until the mixture reacts decided- I alkaline to an indicator'such as litmus. 'I he heating is then continued until the fibre is in a suit-able condition for paper making, by which time the rotective colloid will have become thorough y mixed with the fibre. The beater roll is then raised oil the bedplate, so that it serves only as a means 'for agitation. A rubber dispersion, such as rub- 3 her latex containing either its normal quantit of rubber or diluted to, to of dry ru her, is then added tothe pulp in the heater,
and preferably just in front of the beater roll. The rubber dispersion or the rubber latex is preferably strained through a fine screen or cloth at the time of addition. The beater roll continues to revolve and thoroughly mixes the latex or dispersion with the pulp and protective colloid. The protective colloid here serves to keep the rubber particles Also the comixing operation in a very fine state of subdivision. After the rubber dispersion has becomethorou hly mixed with the ulp the rubber is ag Fom- .e'rated upon the fi res by the addition 0 some coagulating solution, preferably a solution of paper makers alum. About two-thirds of the amount necessary to cause complete coagulation is added to the beater at this time, and the m1xmg is continued for a short period durm which the rubber articles become deposite upon the fibres. of' the coagulating solution is added, the amount being suflicient to impart a strong acid reaction to litmus paper.
adding the coagulant slowly and continuous.
ly and in a sufiicient dilution to prevent local coagulation during the early part of the rocess. When the coagulant is added s owly and continuously, agglomeration will take place first in precisely the same manner as when the rubber is deposited upon the fibre in two steps as described above.
When glue or other protein is used as the protective colloid it will be found that a much stronger paper can be obtained if the glue is set or coagulated by protein precipitants such as the heavy metal salts, organic color bases, the so-called alkaloidal reagents, the polyhydric phenols, for example tannic acid and the various so-called tannic extracts. Similarly a strong paper can be obtained if such protein reclpitants are added to the paper pulp be ore the formation of the sheet upon the paper-making machine, when the pulp contains no additional protective colloid but only the protein derived from rubber latex. Undoubtedly in this latter case the increase of strength thus observed is due to the action of the precipitating agent upon the natural proteins which are present in the latex and at the same time upon the protective function of these proteins. After-the coagulation operation has been completed a solution of a olyhydric phenol such as tannic acid or the li e, may be added for the purpose of precipitating the protein, which is present when rubber latex is used as the rubber dispersion, upon the aper fibres. After the as been completed the paper fibre is then handled in the standard way for making paper.
The amount of protective agent which is used for the above process depends to a lar e extent upon the particular pulp used and t e results which are sought in the finished paper. Ordinarily the amount of feculoid, glue or casein 'which is required varies between one] hen the remainder addition of approximately three percent of .1
the weight of the paper fibres used.
It is standard practice in the manufacture of practically all paper to use commercial rosin size in order to give the necessary fin ish to the sheet. This material may be added to the beater at any desired stage in the process after the addition of the protective agent and alkali. It has been found in many cases that the addition of commercial rosin size to paper pulp containing latex prior to coagulation of the rubber causes some premature coagulation of the rubber .in the latex on account of the presence of soda ash in the commercial size, with the formation of spots of rubber on the-finished paper. This difficulty may be completely overcome by use of some one of the above protective a ents.
It has been shown in this work t lat when approximately three percent of a soluble starch such as feculoid on the basis of the paper pulp contained in the beater is used, the strength of the finished paper is materially increased over that which can be obtained if rubber alone were used. The stateent invention reveal the rubber particles in a' very much smaller size than in ordinary latex paper, and in many instances the fibres have the general appearance of being coated with a continuous film of rubber.,
Having thus described our invention, what we claim and desire to protect by Letters Patent is:
1. A process for the manufacture of paper and rubber and similar combinations which comprises beating paper-making fibre, successively incorporating a protective colloid and a rubber dispersion with the fibre, depositing the rubber from said dispersion upon the fibre, and making the treated fibre into a sheet.
2. Aprocess for the manufacture of paper and rubber and similar combinations which comprises beating paper-making fibre, adding a protective colloid before completion of the beating, incorporating a rubber dispersion in the presence of an alkaline material with the fibre, depositing the rubber from said dispersion upon the fibre, and making the treated fibre into a sheet.
3. A process for the manufacture of paper and rubber and similar combinations which comprises beating paper-making fibre, add-- ing a protective colloid thereto, incorporating a rubber dispersion with the ifibre, depositing the rubber from said dispersion upon the fibre, and making the treated fibre into a sheet.
4. A process for the manufacture of paper and rubber and similar combinations which comprises beating paper-making. fibre, mixing a protective colloid therewith, rendering the mixture alkaline, incorporating rubber latex with the beaten fibre, depositing the rubber from said latex upon the colloid coated fibre, and making the treated fibre into a sheet.
5. A process for the manufacture of paper and rubber and similar combinations which comprises beating aper-making fibre, mixing a protective col oid therewith, rendering the mixture definitely alkaline, continuing the beating operation, distributing rubber latex throughout the mixture, agglomerating the rubber from said latex upon the fibres, continuing the mixing, coagulating the rubber upon the fibres, and making the treated fibres into a sheet.
6. A process for the manufacture of paper and rubber and similar combinations which comprises beating paper-making fibre, adding a soluble starch therto, incorporating a ru ber dispersion with the fibre, depositing the rubber from said dispersion upon the fibre, and making the treated fibre into a sheet.
7 A process for the manufacture of paper and rubber and similar combinations which comprises beating paper-making fibre, mixing a soluble starch therewith, rendering the mixture alkaline, incorporating rubber latex with the beatenfibre, depositing the rubber from said dispersion upon the fibre, and making the treated fibre into a sheet.
8. A process for the manufacture of paper and rubber and similar combinations which and rubber and similar combinations which comprises beating paper-making fibre, adding a starch ester thereto, incorporating a rubber dispersion with the fibre, depositingv the rubber from said dispersion upon the fibre, and making thetreated fibre into a sheet.
10. A process for the manufacture of paper and rubber and similar combinations which comprises beating paper-making fibre, mixing a starch ester therewith, renderin the mixture alkaline, incor orating rubber atex with the beaten fibre, epositing the rubber from said latex upon the fibre, and making the treated fibre into a sheet.
11. A- process for the manufacture of paper .and similar combinations which comprises beating aper-making fibre, mixing acetylated starc therewith, renderin the mixture 5 definitely alkaline, continuing't ebeatin operation, distributing rubber latex throng out the mixture, ag lomerating the rubber from said latex upon t e fibres, continuin the mixing, coagulating the rubber upon t e fibres, m and making the treated fibres into a sheet.
1212A process for the manufacture of pa-' per and rubber and similar combinations which comprises beating aper-making fibre to which has been added from 1 to 5% of feculoid, said mixture being definitel alkaline, incorporating rubber latex with the beaten pulp and agitating the pulp, agglomcrating the rubber from said latex upon the pulp by the addition of a portion of a coaguating mixture, continuin the mixing, a
ing a further uantity o coa lating mixture to render-t e beaten pulp lstmctly acid, and making the treated pulp'into a sheet.
13. A process for the manufacture of paper and rubber and similar combinations which comprises beating paper-makin fibre, adding, a roteinous protective co loid thereto, rendering the mixture alkaline, inoorporating rubber latex with tHe mixture, 80 distributing said rubber latex throughout the beaten fibre, precipitating said proteinous protective col oid alon with said rubber upon the beaten fibre, an making the treated fibre-into a sheet. 85 14. A .process for the nanufacture of paper and rubber and similar combinations which comprises adding a' roteinous protective colloid to a mass of beaten papermaking fibre, rendering the beaten mass al- A 40 kaline, mixing rubber latex therewith, de-
ipositing said protein and rubber upon the\ bre byadding a protein precipitated to the beaten mixture, and making the treated fibre into a sheet.
1 5. As a new product, a paper containing rubber and a starch ester deposited upon its fibres.
16. As a new product, a a r containing rubber and acetylated stare db posited upon 60 its fibres.
Signed atNew York, New York, this 16th day of December, 1926. 1
REED P. ROSE. HAROLD E. CUDE.
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US2635045 *||Apr 21, 1948||Apr 14, 1953||Riegel Paper Corp||Making elastomer containing paper|
|US3113065 *||Jun 12, 1961||Dec 3, 1963||Building Products Ltd||Resin bonded fibreboard and the process of making the same|
|US5869168 *||Jan 10, 1997||Feb 9, 1999||Mahn, Jr.; John||Reflective heat activated transfer|
|U.S. Classification||162/170, 162/174, 162/175|
|International Classification||D21H17/00, D21H17/35|