|Publication number||US2563897 A|
|Publication date||Aug 14, 1951|
|Filing date||Jul 13, 1945|
|Priority date||Jul 13, 1945|
|Also published as||DE845311C|
|Publication number||US 2563897 A, US 2563897A, US-A-2563897, US2563897 A, US2563897A|
|Inventors||Chester G Landes, Charles S Maxwell, Lucius H Wilson|
|Original Assignee||American Cyanamid Co|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (20), Referenced by (67), Classifications (25)|
|External Links: USPTO, USPTO Assignment, Espacenet|
g- 1951 H. WILSON ET AL 2,563,897
SIZING CELLULOSIC FIBERS WITH CATIONIC MELAMINE RESIN AND HYDROPHOBIC MATERIAL Filed July 13, 1945 5 Sheets-Sheet l Aug. 14, 1951 H. WILSON ET AL 2,
SIZING CELLULOSIC FIBERS WITH CATIONIC MELAMINE RESIN AND HYDROPHOBIC MATERIAL Filed July 13, 1945 5 Sheets-Sheet 5 1 06/06 W/A JO/V,
Z4. madam Patented Aug. 14, 1951 OFFICE SIZING CELLULOSIC FIBERS WITH CAT- IONIC MELAMINE RESIN AND HYDRO- PHOBIC MATERIAL Lucius H. Wilson, Greenwich, Chester G. London,
New Canaan, and Charles S. Maxwell, Old assignors to American Cyanamid Company, New York, N. Y., a corpo- Greenwich, Conn.,
ration of Maine Application July 13, 1945, Serial No. 604,904
This invention relates to the application of coating or impregnating materials to fibrous cellulosic material, to coated or impregnated cellulosic flbers obtained thereby, and to the manufacture of other articles from the coated or impregnated fibers. More particularly, the invention relates to the incorporation of dispersions or emulsions of water-insoluble coating or impregnating materials such as resins, precipitated or insoluble sizes, elastomers, waxes, pitches, bitumens, oils, etc., into fibrous cellulosic material such as paper stock, cotton and the like followed if desired by forming the resulting pretreated cellulosic material into fibrous felted sheets or articles such as paper, paper board, moulded or premoulded cellulosic articles and the like. The invention includes processes for the manufacture of new types of paper, paper board, pulp and pulp preforms as well as a wide variety of novel products obtained therefrom,
either directly or by subsequent treatments such as shredding, impregnating, cold pressing, hot pressing, heating, calendering, hot calendering and the like.
Heretofo-re the principal, methods of incorporating resins, waxes, waterproofing and greaseproofing agents, binding agents and the like into a sheet of pulp or paper have been by impregnation of the formed sheet or object by a water solution, organic solvent solution or dispersion of the material to be incorporated or by addition of the impregnating agent to the pulpwater slurry, called slush stock or paper stock, either as a substantially water-insoluble dry powdered material or as a precipate from a water solution, solvent solution, or dispersion or emulsion of the impregnating material. Thus, for example, it is common practice to add fillers such as clay and sizing materials such as rosin soap. rosin or wax emulsions or dispersions, lactices, asphalt emulsions and the like to slush stock in the beater, stock chest or at any other point in the stock system prior to sheet formation, preceded or followed by the addition of alum. By this procedure the sizing materials are precipitat ed and the resulting flocs are entangled or mixed with the fibrous paper stock and are carried into the finished paper.
'I'hisprocedure works fairly well in those cases where only small amounts of certain materials are added to the paper, such as amounts on the order of 0.5% to 5% on the weight of the fiber. However, serious operating difficulties are frequently encountered when attempts are made to incorporate larger quantities of impregnating agents by these methods. Some or all of the following difficulties are frequently encountered.
1. The resinous material is agglomerated in balls or lumps instead of forming fiocs of small particle sizes. This may cause thesheet to stick to the presses, 'driers, felts and calenders when the impregnated pulp is run out on a papermaking machine.
2. Coverage of the individual fibers may be Poor.
3. Distribution of the resin in the sheet may be non-uniform, resulting in a mottled appearance of the sheet and causing non-uniform ink reception.
4. Sheet formation is often harmed.
5. Precipitation of the resin is frequently incomplete, and much of the resinous impregnating material is lost in the white water.
6. Agglomerates of the resin, together with unprecipitated resin, tend to deposit as sticky aggregates in pipe lines, tanks, and various other portions of the papermaking equipment.
Some of these difficulties, such as the appearance of rosin spots and lumps of agglomerated material are frequently encountered in paper mills even when amounts as small as 0.25 %-3% of certain types of rosin and wax emulsions are added.
The present invention has as a principal object an improved method for the incorporation of impregnating agents into fibrous cellulosic material in such a. manner that many of the difiiculties enumerated above are avoided. In accordance with preferred embodiments of the invention, this is accomplished by obtaining a more uniform and complete coating or impregnation of the cellulosic fibers with the impregnating agent prior to the felting or forming step. A second important object is to provide a process for the incorporation of a wide variety of impregnating agents into or upon fibrous oellulosic material in such a manner that these added materials do not seriously interfere with the normal method of production 01' paper pulp sheets, pulp preforms and the like on standard papermaking equipment, even when large quantities of impregnating materials are used. A further object is to eliminate many of the difliculties ordinarily encountered in the coagulation of resinous dispersions by inorganic precipitating agents such as alum, including difiiculties arising through non-uniform coverage of the pulp fibers, formation of sticky aggregates of the precipitated material, and extremely slow drainage of water from agglomerated resin-fiber masses on the sheet-forming wire or screen.
Further objects of the invention involve the formation, on standard papermaking or pulpforming or preforming equipment, of easily handied sheets, boards and preforms containing new combinations of fibers, or fibers and fillers, with certain special resinous impregnating agents that have not heretofore been incorporated successfully by slush stock treatment. Thus, for example, certain special thermosetting resins or condensates such as urea-formaldehyde resins, phenol-formaldehyde resins, alkyd resins and the like may be incorporated into paper stock in the quantities necessary for premoulding and moulding processes. Similarly, a wide variety of thermoplastic resins, elastomers and the like may be incorporated in the large quantities necessary for laminating and moulding processes.
A wide variety of organic binders, sizing agents, oils, waxes, pitches, gums and natural resins may also be incorporated. Various combinations of any two or more of these resins may likewise be incorporated if desired. By applying the principles of our invention, resin-impregnated paper or paper board having superior properties can be prepared, as well as new types of products made from the treated paper or pulp by such conventional operations as laminating, moulding, pressing, calendaring, extruding and the like. Instead of forming the treated pulps or fibers, they can be shredded, chopped or ground to produce new types of insulating agents, moulding powders, fillers for standard moulding or casting resins, and the like.
Our invention is based on the discovery of an unusual type of flocculation and deposition that is brought about by the action of cationic melamine-aldehyde resins in an aqueous system containing fibrous cellulosic material of the type of aper pulp suspended therein together with an aqueous dispersion of water-insoluble coating or impregnating agents. We have found that in such a system the cationic melamine-aldehyde resin causes a controlled flocculation such that particles of the impregnating agent are uniformly coated upon or impregnated into the cellulose fibers. When dispersed or defiocculated water-insoluble impregnating or coating agents are applied in this manner, we have found that the cellulosic fibers retain their property of felting or forming into shaped or sheeted articles despite the presence of large quantities of the impregnating agent, which in some cases may even be greater than the weight of the cellulosic fibers themselves. Moreover, when the proper quantities of cationic melamine-aldehyde resin are applied in the manner hereinafter described a high degree of retention of the fiocculated material by the cellulosic fibers is obtained, and losses and deposition of organic material in the white water system is avoided.
Figures 1 to 6 are views of photomicrographs. Figures '7 to are graphs illustrating various comparative tests.
Fig. l is an electronmicrograph of emulsionpolymerized polystyrene and Fig. 2 is a similar micrograph of the same dispersion after it has been fiocculated by adding a cationic melam nealdehyde resin colloid.
Fig. 3 is a photomicrograph showing cellulosic fibers pretreated with cationic melamine-aldehyde resin and having polystyrene resin particles distributed thereon, whfle Fig. 4 is a similar photomicrograph in which the resin was coagulated with alum. I
Figs. 5 and 6 are electronmicrographs of cellulosic fibers coated with polystyrene in quantities of 50% and respectively, based on the dry fiber weight.
Figs. 7 and 8 are graphs showing, respectively, the effect of pH of standing and of time of standing on the pulp freeness.
Figs. 9 and 10 are similar graphs showing the effect of varying quantities of colloidal melamine resin on the retention of polystyrene and wax in dispersed condition.
The process of our invention comprises as an essential feature the flocculation of an aqueous dispersion of an impregnating agent in the presence of fibrous cellulosic material suspended in the aqueous medium by the action of a cationic melamine-aldehyde resin. The distinctive type of flocculation that is obtained when an aqueous solution of cationic melamine-aldehyde resin colloid is added to an aqueous dispersion such, for example, as an emulsion-polymerized polystyrene dispersion is shown in Figs. 1 and 2 of the drawings, and will be described and illustrated hereinafter in greater detail. The invention in its broader aspects includes any process wherein this flocculating action is used for the deposition or incorporation of an impregnating agent into fibrous cellulosic material.
In addition to the foregoing we have also found, as one of the most important features of our invention, that the distinctive flocculating action of the cationic melamine-aldehyde resin colloid continues. and is in many cases actually enhanced, after the cationic melamine resin has been adsorbed on the fibrous cellulosic material. The importance of this discovery resides in the fact that the melamine resin, being distributed uniformly over and through the cellulosic fibers, causes a uniform deposition and retention of the impregnating agent on the fibers after it has been fiocculated. This discovery has enabled us to deposit large quantities of any desired impregnating agent on fibers of cellulosic materials such as paper stock while retaining the felting properties of the fibers, so that after impregnation they can still be felted together and formed into sheeted or moulded products by conventional wet-moulding or papermaking procedures.
The distinctive manner in which the impregnating agent is deposited uniformly along the entire length of cellulosic fibers containing an adsorbed layer of cationic melamine-aldehyde resin is most clearly shown by reference to Fig. 3 of the drawings, which is a photomicrograph at the relatively low magnification of 75 diameters. Fig. 4, which is included for purposes of comparison, is a similar photomicrograph in which the resin was coagulated by the addition of alum, no melamine-aldehyde colloid being used. It will be seen from Fig. 3 that the cationic melamine-aldehyde resin causes the flocculated polystyrene resin particles to be distributed in relatively finely divided condition along the cellulosic fibers, whereas in Fig. 4 the fibers themselves are almost completely devoid of resin.
In an aqueous dispersion of fibrous cellulosic material to which a cationic melamine-aldehyde resin and an aqueous dispersion of an impregnating agent have been added, it will therefore be seen that two types of flocculation are occurring. That portion of the cationic melaminealdehyde resin which has adsorbed on the celluscreen or wire. v flocculations it is possible, by proper control of amass? losic fibers exerts both a flocculating and a clustering action, as described above. Free or unadsorbed melamine-aldehyde resin colloid, if present in the system, causes the distinctive type of flocculation shown in Fig. 2 of the drawings, and the fiocs so produced are largely deposited on or entangled with the impregnated cellulosic fibers, either immediately or duringsubsequent felting or forming steps. The net result of this combined action is to retain large quantities of the impregnating agent on the cellulosic material in a uniform and well-distributed condition after the water has been drained from the sys- Although our invention is not dependent on any particular theory of operation, we offer the following as the most probable explanation of the unusual type of flocculation and retention that is obtained. As is noted above, definite quantities of the cationic melamine resin colloid are adsorbed upon and retained by the cellulosic'fibers when the cationic melamine resin solution is added to an aqueous suspension thereof. We believe. as a result of this treatment, the fiber-resin entity becomes positively charged, as contrasted with the negative charge usually associated with cellulose fibers. The resulting positively charged, resin-treated fibers in aqueous suspension exert an appreciable fiocculating action on emulsions or dispersions of water-insoluble organic materials, and this is particularly evident when the emulsified or dispersed impregnating material carries a negative charge as whenan anionic dispersing agent is employed in its preparation. The result is that after addition of the emulsion or dispersion of the impregnating agent to the aqueous suspension of resin-treated cellulosic pulp, the dispersed particles are attracted to and flocculated on the positively charged fibers forming a layer or coating upon and around the fibers and permitting the formation of a mat of the coated fibers on a screen or paper machine wire, with substantial retentionof both the fibers and the coagulated particles of the non-fibrous dispersion.
When the aqueous suspension of cellulosic material is pretreated with a controlled excess of the cationic melamine-aldehyde resin, over and above that required to impart a positive charge on the cellulosic fibers, the unadsorbed positively charged melamine-resinalso possesses a strong flocculating action. Therefore when an emulsion or dispersion of an organic impregnating agent is added, two simultaneous fiocculating actions occur. Part of the dispersed non-fibrous particles of impregnating agent are attracted to and de posited on the positively charged fibers, forming a substantially uniform coating over the entire fiber surface. Simultaneously, the remainder of the emulsified or dispersed particles are coagulated into small fiocs or agglomerates containing in intimate admixture the melamine-resin colloid and particles of the added emulsion or dispersion. These flocs or aggregates of combined resins, by reason of their finely divided condition, readily coat or entangle with the fibrous portion of the mixture and offer little resistance to the drainage of the water during felting and forming of a sheet or mass of the pulp on a As a result of these combined the amount of added melamine-aldehyde resin colloid and other factors, to obtain complete or nearly complete retention of both the melamine g5 losic material. By coating or impregnating resin and almost any desired proportion of or: ganic impregnating agents. 4
Although the foregoing represents what we regard as the most probable explanation of the phenomena involved, the process of our invention is not necessarily limited thereto. 0n the contrary, it is possible that other factors may play an important part in the flocculation of the dispersed impregnating agents. Thus, for example, both the cellulose fibers and the melamine resin collold particles attached thereto, as well as the excess melamine resin colloid remaining in aqueous suspension, undoubtedly present enormous surfaces upon which the molecules of various emulsifying agents can be adsorbed from water solution. It is therefore quite possible that the melamine resin coated fibers, as well as the melamine resin colloid itself, may adsorb appreciable quantities of emulsifying or emulsion-star bilizing agents associated with a third component added to the system, and thereby contribute to the flocculation of the particles of the third component and their agglomeration on the fibers. This mechanism may explain why materials dispersed by means of non-ionic or in some cases even by cationic dispersing or emulsifying agents are often retained with cellulose fibers by means of the cationic melamine resin colloid solution.
The fiocculating agents which we employ in practicing our invention, and which are designated for convenience as cationic melamine aldehyde resins," are resinous materials containing melamine and ca y n a positive electrical charge when in aqueous solution. These colloidal resin solutions may be prepared. by dissolving ordinary melamine-aldehyde condensation products, such as methylol melamines in acids such as hydrochloric acid to form acidified or acid-type" resin solutions having a glass electrode pH value within the range of about 0.5 to about 3.5 when measured at 15% solids, or pH values up to 4.5 when measured in more dilute solutions, followed by aging to the colloidal condition, as described in U. S. Patent No. 2,345,543. Another class of cationic melamine-aldehyde resins that may be used in practicing the present invention are the resinous copolymers of melamine, urea and aldehydes such as formaldehyde containing at least 0.7 mols of melamine for each 4 mols of urea and about 14 mols of combined formaldehyde for each mol of melamine+urea that are described in U. S. Patent No. 2,485,079. These cationic melamine resin copolymers are obtained by first preparing an acidified aqueous solution of an aldehyde condensation product of melamine and urea containing lmol per cent of urea and 30-99 mol per cent of melamine and about 0.2-1.5 mols of acid per mol of melamine, depending on the strength of the acid, and aging the solution until the colloidal cationic condition is reached. The essential requirement of aminotriazine-aldehyde condensation products used as flocculating agents in the process of our invention is that they be in the waterdispersible or hydrophilic partially polymerized condition and that they carry a positive electrical charge, and any suitable aminotriazine-aldehyde resin possessing these characteristics may be employed.
Any water-insoluble coating or impregnating agent may be applied by the process of our invention in amounts varying from a few per cent up to more than the weight of the fibrous celluagen we mean, of course, a material which will coat or impregnate the cellulosic ilbers and improve their value for their intended use. The great majority of coating and impregnating materials used in practicing our invention are organic amorphous or micro-crystalline materials of the type of waxes, gums, resins and the like. The following types of materials of this class are illustrative of the wide variety of impregnating agents that may be applied:
paraflin crude scale wax carnauba wax montan wax petrolatum microcrystalline or wax chlorinated waxes Bituminous:
asphalt tars and pitches bitumens Gums, etc.:
gum tragacanth gum ghatti gum elemi starches methyl cellulose Resins:
wood rosin gum rosin heat-treated or disproportionated rosin acid-treated or polymerized rosin hydrogenated rosin limed rosin sulfur-treated rosin Elastomers:
natural latices synthetic latices isoprene polymers neoprene polymers butadiene polymers copolymers of butadiene, isoprene, etc., with acrylonitrile ResinsThermosetting:
thermosetting phenol-aldehyde resins including particularly the phenol and alkylphenol formaldehyde moulding resins urea-aldehyde resins alkyd resins non-cationic melamine-formaldehyde resins alkylated or alcohol-reacted urea-formaldehyde resins alkylated or alcohol-reacted melamineformaldehyde resins Resins-Thermoplastic:
polyvinyl compounds polystyrene polyacrylates polymethacrylates polyvinyl esters such as vinyl chlorides and vinyl acetate polymers and copolymers of the two polyvinyl acetal polyvinyl alcohols copolymers of styrene with vinyl chloride,
acrylic acid esters, acrylonitrile, etc. thermoplastic phenol-formaldehyde resins,
including phenol-acetaldehyde and phenol-furfural resins and corresponding resins obtained from cresols and other alkyl phenols oil-modified phenol-formaldehyde resins amorphous petroleum esters of rosin with polyhydric alcohols such as glycerin, pentaerythritol, dipentaerythritol, polyallyl alcohols, etc.
resins from melamine and higher aldehydes polyindene resins coumarone resins vinylacetylene resins Vinsol" resin; i. e. residue from purifying wood rosin halogenated vinylacetylene resins acetyl gums Any of the above materials, either singly or in admixture, may be applied to fibrous cellulosic materials with the aid of cationic melamineiormaldehyde resins by the process of the present invention. The impregnating agent is added to the aqueous stock suspension containing the cellulose fibers as a dispersion in water or aqueous liquid. Depending on the type of impregnating agent, the dispersions may require no added emulsifying or dispersing agents whatsoever, as in the case of natural latices. However, in many cases dispersions of finer particle size and better impregnating properties are obtained with the aid of dispersing agents, and many types of dispersing agents may be used. In general, any anionic or non-ionic dispersing agent may be employed in emulsifying or suspending the impregnating agents in water or other aqueous liquids, and in certain cases the cationic emulsifying agents may also be used. Typical anionic emulsifying agents which we have employed with success are the soaps of aliphatic and cycle-aliphatic acids such as potassium oleate, potassium naphthenate and the like, amine soaps such as triethanolamine oleate; sulfated aliphatic compounds such as sodium lauryl sulfate and the sulfates of higher secondary alcohols and sulfonated castor oil; sulfonated products such as sodium keryl benzene sulfonate, sodium isopropyl naphthalene sulfonate, esters of sulfocarboxylic acids such as esters of sodium sulfoacetate, dialkyl sulfosuccinamates, disodium monoalkyl sulfosuccinamates; amides of sulfocarboxlic acids such as sodium sulfosuccinamates and the like, sulionated lignin, etc.
Non-ionic emulsifying agents such as polyhydric alcohol esters and ethers may also be used. Typical compounds of this class are polyethylene glycol-substituted maleic acid esters of the formula HO(CH2O)1.CH2.O.CH.(COOR) CH2.COOR; mannitan and sorbitan monoesters of higher fatty acids such as palmitic, stearic and oleic acids and their ethylene oxide condensation products and aryl-alkyl polyether alcohols.
Another class of compounds that may be used either as emulsifying agents or as emulsion stabilizers are the gums and proteins. Thus, for example, gum arabic may be used, as well as soya bean protein, sodium alginate and the like. Ammonium caseinate is another emulsifying agent that has been used with success.
Ammonium or other water-soluble or waterdispersible salts of alkyd resins of high acid number may also be employed, such as the products obtained by adding sodium hydroxide to condensation products of maleic acid and glycerine, modified phthalic anhydride-glycerine-fatty acid condensation products of high acid number, polyhydric alcohol esters of terpene-maleic acid condensation products and the like. In general, therefore, any suitable wetting or emulsifying agent may be used in practicing the invention.
Any fibrous cellulosic material capable of adsorbing cationic melamine-aldehyde resin from stock; rag stock, soda, sulfate, ground-wood, sulfite stock and alpha pulp. Similarly, other forms of fibrous cellulose such as hydrated cotton li'nters, and the like maybe employed. These materials may be used alone or in admixture with fibers from other sources, such as jute, hemp, sisal, strings, chopped canvas, asbestos fibers, glass fibers, and other material, either cellulosic or non-cellulosic, that may improve the impact resistance, mechanical strength or other properties of the formed or moulded impregnated material. Typical products that may be' improved bythe process-pi the invention are waterproof or-moisture-vaporproof paper, paper or board containers or cartons for milk, butter, foods, etc.,
resin-impregnated laminating paper, abrasives composed of resin-impregnated paper coated with abrasive particles, moulded articles, premoulded articles, electrical insulators, filter paper, heatinsulating paper, or loose masses of unfelted and unmoulded impregnated cellulose stock used for air filters, dust filters, heat insulation and the like.
The particular procedure whereby the impregnating agent is flocculated andcoated on the fibrous cellulosic material may vary somewhat with different impregnating agents, but usually follows the same general plan. The cellulosic material is preferably, first suspended in water and may be beaten for shorter or longer periods of time to hydrate the cellulose, after which the stock may be brushed out in a Jordan engine or other refining machine if desired. Any desired ratio of cellulosic material to water may be maintained, but we prefer to operate at a stock consistency of about 0.5% to 6%. The cationic melamine-aldehyde resin is then added, preferably in the form of an aqueous dispersion of about -15% resin solids, after which the stock suspena small sheet-making machine calibrated to permit measurement of the drainage time of the water through the paper-forming wire. The percent resin retention was determined by measuring the increase in weight of the dried sheet and the values on the left-hand scales of Figs. 7 and 8 sion is preferably allowed to stand for anywhere I from 15 minutes up .to 3-4 hours or longer. This period of standing is not a necessary step, since the adsorption of cationic melamine resin by the paper stock is quiterapid, but the subsequent behavior of theimpregnated stock on a paperduring this standing period are illustrated in Fig.
7. The results shown graphically in Fig. '7 were obtained by adding suil'lcient acid or alkali to a 1.5% aqueous suspension of bleached alpha pulp to produce the desired pH upon addition of a cationic melamine-formaldehyde hydrochloric acid colloid, then adding the melamine resin colloid in amounts of 6% resin solids, based on the weight of the paper pulp, stirring thoroughly and allowing the suspension to stand overnight. The
- next morning the pH was adjusted to about 7.0
by adding acid or alkali and a dispersion of emulsion-polymerized polystyrene was added in amounts of 100%, based on the weight of the paper stock, and the freeness was determined on a WilliamsFreeness tester. This instrument is of the drawings represent:
weight of dry sheet-weight of fiber added weight of resin added X It will be noted that maximum resin retention and lowest drainage time come at a pH of about 5, which is also a normal pH for papermaking. It will also be seen, however, that good retention is obtained over a wide range of pH values, which is another advantage of the invention.
The results shown graphically in Fig. 8 were obtained with the same quantities of polystyrene and paper pulp at 1.5% stock consistency, but using 10% of cationic melamine-formaldehyde resin-hydrochloric acid colloid. In this series of tests the melamine resin colloid was added to the paper stock suspension, the resulting pH being about 3.0, after which the stock was allowed to stand for varying periods of time before neutralizing with sodium hydroxide to a pH of 6-7 and adding the polystyrene dispersion. Drainage time was then determined on the Williams Freeness tester and resin retentionwas determined by measuring the'weight of the dry sheet.
This curve shows that a reasonably low drainage time is obtainable with very high quantities of resin, in this case equal to the weight of the paper fstock,.'after a standing time of only 30 minutes, and that even better results are obtained with a'longer standing time up to 3-4 hours. No decrease in resin retention is noted when longer standing times are used.
After pretreatment of cellulosic stock with :the
' cationic melamine resin, the impregnating agent is introduced in the form of an aqueous suspension, preferably of relatively fine particle size. Insofar as we have been able to determine, the flocculating action of the cationicmelamine-al-r 'dehyde resin is not dependent on the particle 7 size of the added impregnating agent, but a much more uniform coating of the cellulose fibers and better performance on the papermaking ma chine is obtained whena dispersion of fine particle size is used. Aqueous dispersions having an average particle size of 1-2 microns or less have given excellent results in practice, and therefore we recommend the addition of the impregnating agent in the form of an aqueous dispersion having at most this particle size. The flocculation of the impregnating agent and its adsorption by the cationic melamine resin-treated cellulose fiber is quite rapid, and the standing time of the mixture after the impregnating agent has been added makes very little difference in the results obtained. The stock can therefore be formed immediately after the addition of the impregnating agent or after a considerable period of time, as desired.
The optimum quantity of the colloidal melamine resin that should be used to obtain the best retention of a dispersed or emulsified resin, wax, or other impregnating agent may vary with the nature and particle size of the dispersion, the nature of the melamine resin colloid, the time of contact between the pulp fibers and the melamine resin colloid, the pH of the stock and other factors. Also, because of the properties of the dispersed material added and the requirements of the finished sheet or article to be made, it may be desirable to modify the proportion of melamine resin colloid in order to obtain increased properties thereof in the finished product. In general, the proper amount of melamine resin colloid required may vary from small amounts on the order of 0.1%, based on the weight of the paper stock, up to several times the weight of the impregnating agent. It is usually desirable to run trials with the specific dispersion to be added. under the desired operating conditions, before deciding finally on the exact proportions to use.
Thus, for example, one series of tests was made by adding increasing quantities of an aqueous dispersion of emulsion-polymerized polystyrene, prepared with the aid of an anionic emulsifying agent and having a particle size of less than 0.5 microndiameter, to suspensions of 3 g. of krait paper pulp in 500 ml. of water to which 0.15 g. of colloida1 melamine-formaldehyde resin had been added. It was found that in neutral solutions (pH=7) about 10 parts by weight of polystyrene were retained in a sheet of paper made from the above mixture for each part of melamine resin. When the pH of the stock prior to addition of the polystyrene dispersion was raised to 10 by the addition of an alkali such as ammonium or sodium hydroxide about 6 parts of the polystyrene were retained in the formed sheet, while stock adjusted to a pH e of 4.0 with acid showed a retention in the finished sheet of about 14 parts of polystyrene for each part of colloidal melamine resin. These results show that although the pH of the stock has an appreciable efiect on the retention of dispersions under some conditions,'it is possible by suitable adjustments to retain large amounts of a resin or other dispersion in paper over a wide pH range of the stock. Additional examples will be presented later in which variations in pH show even less effect on the retention of resinous dispersions.
Another set of experiments was made at three diiferent stock consistencies in which all conditions were held constant except the proportion of melamine resin colloid in the furnish. Two gram portions of moderately beaten alpha pulp were first treated with varying proportions of melamine resin colloid and the suspensions allowed to age at a pH of about 3-4 for about 15 hours. Then the suspensions were adjusted to a pH of 6.5-7.0-and two grams (dry basis) of an aqueous anionic dispersion of polystyrene were added with stirring. After standing for 5 minutes each batch of pulp and resins was filtered on a fill-mesh wire in the Williams Freeness tester noting the time for drainage, the clarity of the white water and the total weight and nitrogen content of the finished dry sheet. The results of these tests are shown graphically in Fig. 9 of the drawings, wherein the solid curves represent total resin retention (i. e. both polystyrene and melamine resin) while the broken lines show drainage time as indicated on the right-hand scale. It will be noted that the retention of resins increases rapidly up to a maximum of more than 80% when about 2-10% of melamine resin colloid, on the weight of the polystyrene, is used, the exact amount varying with the stock consisten y. With increasing proportions of melamine resin colloid, the overall resin retention decreased to some extent. It also will be noted that the drainage time increases as the proportion of melamine resin colloid is increased. Since in most commercial operations it would be desirable to run with the highest possible resin retention and the lowest possible drainage time, it is apparent that the optimum 12 proportion of melamine resin colloid to obtain such results would be about 3-8% on the weight of polystyrene to be added. At the same time, a higher proportion of melamine resin can be incorporated in the finished sheet, if desired, without too much sacrifice in resin retention and stock freeness. 0
Fig. 10 shows the effect of varying the ratio of impregnating agent to paper stock. The procedure described in obtaining the values shown on Fig. 9 was followed, but varying quantities of emulsified wax were used. Equal quantities of a 1.5% water suspension of moderately beaten alpha pulp was treated with the indicated quantity of colloidal melamine-formaldehyde-hydrochloric acid colloid, allowed to stand overnight, neutralized with sodium hydroxide to a pH of 6-7 and the wax added as an aqueous emulsion of 50% solids, prepared with a lignin sulfonate emulsifying agent. The stock was then made up to constant volume, formed into paper on a handsheet machine, and the amount of wax was determined by solvent extraction.
These curves illustrate the fact that larger quantities oi the cationic-melamine-aldehyde resin are needed to obtain the maximum retention' with decreasing quantities of impregnating agent, but that good retention can be obtained at any desired ratio of impregnating agent to fiber by observing the proper operating conditions. When using relatively large quantities of impregnatin agent. on the ord r of 50-100% or more of the we ght of the cellulosic fibers, the optimum quantity oi cationic resin is within the ran e of about 9,15%. with Smaller tm of impregnating a ent, such as 5-50% on the weight of the cellulose. larger quantities oi. the cationic resin on the order of 5-30% should be used. Larger duantities of the melamine resin colloid u to or more on the wei ht of the impregnating agent may be added to modify the properties of the finished product if desired, but in such cases there is a definite falling off in the retention and also an increase in the drainage time of the stock.
Although a h gh degree of flocculation and retention oi. the addedlimpregnating agent is obtained by the use of cationic melamine-aldehyde resins alone, it is sometime advantageous to add an additional precipitating agent during the stock preparation. Thus, for example,-better drainage of water from the stock on the papermaking wire or screen is frequently obtained when small quantitles of alum on the order of 0.5-3%, based on the weight of the cellulosic material, are added. The alum or other precipitating agent is almost always added after the other ingredients have been mixed, since it would tend to coagulate and precipitate the colloidal cationic melamine resin in solution if it were added first, but in special cases where a preliminary coagulation of excess melamine resin may be desirable the alum or other electrolyte may of course be introduced ahead of the impregnating agent if desired.
The principles of our invention may be applied in a wide variety of fields of papermaking, moulding, laminating, extruding, prei'orming and the like and in general wherever a fibrous cellulosic material intimately associated with thermoplastic, thermosetting, waxy, bituminous or other type of bonding, impregnating or coating material is desired. The following are illustrative of some of the fields in which the invention may be employed.
As is noted above, the principles of the present invention may be applied to a more uniiorm incorporation of larger quantities of waxes, bituminous material and the like into paper stock before the sheet-making procedure. When the object is to obtain ink resistance, waterproofing and the like these sizes are applied in relatively small amounts on the order of 1-5% or, in the case of asphalt, up to 10%, based on the dry weight of the paper stock. The cationic melamine-aldehyde resin solution is first mixed with the aqueous stock suspension at any desired consistency, such as an 0.5-% stock suspension in the beater chest and allowed to stand for 0.5-3 hours, after which the size is added in the form of an aqueous dispersion. Flocculation of the dispersed sizing material by the cationic melamine resin takes place rapidly, and particles thereof, intimately mixed with the particles of colloidal melamine resin are retained uniformly by the paper stock. The impregnated stock is then run out on the papermaking wire or cylin-' der and the resulting paper passed through heated drying rolls in the usual manner. Wall board, insulating board, and heavy stock for paper containers may be made by this method.
L ght-weight papers having improved tearing strength, water resistance and other desirable properties may be obtained by incorporating dispersions of rubbers, polyacrylates, elastomers, and various copolymers by means of the process described. Properties of the sheet may be modifled by heating, wet or dry pressing, calendering, hot calendering, friction calendering. plating and the like. Likewise the paper may be dried on a polished metal cylinder such as is used on a Yankee paper machine. By the use of our process cheaper and weaker pulps, such as ground wood, waste fibers, and short-flbered materials, may often be used while still obtaining good sheet properties.
MANUFACTURE OF PAPER HAVING A HIGH RESIN CONTENT Paper impregnated with large quantities of thermoplastic or thermosetting resins such as polystyrene, polyethylacrylate, modified or unmodified phenol-formaldehyde resins and the like may be used for a wide variety of purposes, such as for laminating by heat and pressure, in the manufacture of electrical insulators and condensers, in board moulding processes and the like. Quantities of resinous binders ranging from 5% up to considerably more-than the weight of the fibrous cellulosic material can be incorporated by the following procedure:
A fibrous cellulosic material such as kraft paper stock is hydrated by'heating in the usual manner, preferably somewhat less than in the ordinary papermaking procedure. The stock is then diluted with water to a consistency oi about 1-6% solids and a colloidal solution of cationic 14 the stock solution after the cationic melamine resin solution has been added but before introducing the resinous emulsion. Likewise alum may be added to assist in controlling the pH, eliminating foam or stickiness, and modifying the drainage characteristics of the stock.
Paper or paper board containing 5-75% on the basis of the finished sheet weight of resins,
pitches, waxes and the like can be used for various purposes for which paper is ordinarily used but having improved strength resistance, weight resistance, water resistance, water vapor resistance, grease resistance, reduced expansion and contraction under varying humidity conditions, etc. In many instances full development of these desirable properties will depend upon mechanical treatments such as high temperature drying, cold or hot calendering and the like. Boards treated by our process provide paper cartons and containers having improved protective properties, and costs can be held at a reasonable point by using dispersions or emulsions of cheap resinous materials. Wall boards, structural boards and papers, insulating boards, floor covering, shingles and the like may also be made by the same process.
Waxed or oiled papers can be made by incorporating high proportions of amorphous or crystalline waxes or mineral or vegetable oils in the form of emulsions or dispersions. Heating or hot calendering generally is required to develop maximum transparency and water resistance. Strong and flexible papers having the properties of leather or cloth can be manufactured by incorporating synthetic or natural rubber latices, elastomers, and resins in suitable proportion. Heating, calendering, and other mechanical processing can be used to enhance the desired properties. Fire or flame resistance may be imsetting resins. Mineral fibers and fillers also may be incorporated at the same time to assist in obtaining maximum fire resistance.
PREFORIVIING AND MOU'LDING cellulosic fibrous materials such as paper stock impregnated with resinous binders by the process 01' our invention constitute an important article of commerce, for they can be dewatered and sold as such or lightly pressed into a cohesive mass. This mass may be preformed by suitable moulding procedures into shaped pieces for subsequent hot moulding processes or may be chopped, shredded, or ground (either in the dry or wet state) and used subsequently for impression, transfer, or injection moulding either alone or mixed with other types of moulding powders. When rubber latex or other forms of natural or synthetic rubber are coated on the fibers in the manner described above, the product can be worked on heated rolls wherein other fillers such as finely divided carbon black or zinc oxide may be incorporated together with curing accelerators such as mercaptobenzothiazole and antioxidants if desired after which the product can be cured by heating moulds in the usual manner.
In the manufacture of large articles of irregular shape from moulding compositions containing a resinous binder together with a cellulosic filler considerable difllculty has been experienced in obtaining adequate draw or flow in all parts of the mould.- To overcome this difficulty a technique of preforming or premoulding has been deacter of the filler is retained and therefore the preforming can be done by wet moulding processes. Moreover, there is much less loss of resin fibrous material is shredded or chopped to obtain better flow in the mould. Mouldings of high mechanical strength and impact resistance are obtained by this procedure.
The invention will be further illustrated by the following specific examples, which show preferred embodiments thereof. It should be understood, however, that the invention in its broader aspects is not limited to these examples, but
in the white water when operating in accordthat other modifications and variations in maance with the principles of the present invention. terials, quantities and procedures may be resorted Preforms prepared with the aid of cationic to within the scope of the appended claims. melamine-aldehyde resin solutions have greatly Example 1 e man mo ldin roblems and have in- She types of fille rs and resins that may 61511801 Samples of bleached Kraft pulp be moulded Wood flour. cotton flocks, kraft were diluted to 1% consistency and 1,200 cc. porpaper Stock and other standard materials may be tions were used to make handsheets treated as used as well as macerated cellulosic fabrics such follows: as canvas, cords and other fillers that impart in No addltlonscreased toughness and impact Strength to the 30 B. 10% of colloidal melamine-formaldehyde resin moulded piece. Any of these fillers, or any deadded, based on the y Weight f t sired mixture thereof can be suspended in water, P ptreated with cationic melamine-aldehyde resin 100% of o yme ized poly ty e was solution and then impregnated uniform y with added, based on e d y Weight of the 9 1 thermosetting or thermoplastic resinous binders 1075 of the colloidal melamine-formaldehyde in the manner described above, after which they resin was added With Stirring and the can be preformed into the desired shape by 0f the p ystyrene dispersion. straining or forming on a screen or other perme- Handsheets were made by filtering 1,000 cc. able surface having the desired shape. Losses portions of each pulp slurry through a 150-mesh due to resins dissolved or suspended in the water copper screen in a Buchner funnel. The filtrate passing through the screen are usually less than was returned through the residue two times. The 25%, and even these small quantities of resin can volume of filtrate was then measured and the be readily recovered by reuse of the water. total solids determined. The sheet was dried. Phenol-formaldehyde and cresol-formaldehyde weighed and analyzed for total nitrogen. resins are advantageously applied by this method The results are shown in the following table in in amounts of 10-l00%, based on the dry weight which all the figures are by weight and are exof the cellulosic fibers. Other resins, such as pressed in grams.
Materials Added Materials Found Pmess White Melamine Fiber 1101 13 Total 2% Total lggSltizn 1 Approximate. I Determined by Kieldahl nitrogen analysis.
those described in the following examples, can also be applied.
LAMINATING AND MOULDING Sheets and boards impregnated with large quantities of thermoplastic or thermosetting resins by the process of the invention are particularly well suited for laminating and moulding processes, by reason of the uniform distribution of the resinous material. Laminating paper is referably made on an ordinary Fourdrinier machine or a cylinder machine. Heavier board for moulding purposes is often made on a so-called wet machine; i. e. a papermaking cylinder feeding a. drum on which the wet sheet may be wound until board of the desired thickness is obtained. When thermosetting resins are used a curing catalyst such as phthalic acid, oxalic acid and the like may be sprayed on the wet paper before it is dried or, in the case of phenol-formaldehyde resins, hexamethylene tetramine may be applied as a spray to the dried paper or board. Laminating is accomplished by pressing a stack of the impregnated sheets between hot platens. Moulding is accomplished either directly from the paper or board, used as a preform, or after the felted These results show clearly the increase in retention both of polystyrene and of cationic melamine-formaldehyde resin that is obtained when the two are used together. The untreated paper pulp failed to retain any appreciable amount of polystyrene, despite the fact that the white water was filtered twice. It retained only about 40% of the added melamine resin colloid when no polystyrene was used. However, substantially all the polystyrene (at least 95%) and approximately of the melamine resin were retained in Process D wherein both ingredients were added.
The polystyrene used in this and other examples was prepared as follows: 1.2 parts by weight of Duponol C were dissolved in 58.8 parts of water heated to 94 C. and 0.05 part of 40% hydrogen peroxide were added. 40 parts of styrene were then introduced uniformly over 1.5 hours. The exothermic polymerization reaction proceeded smoothly and was complete after 3.5 hours. Steam was blown through the batch to remove unpolymerized material and the dispersion was adjustedto 25% solids. Duponol C is a higher alkyl sulfate (molecular weight 350) containing 10.8% NazSO; and 3.4% moisture.
11 Example 2 A colloidal solution of cationic melamine-tormaldehyde resin was prepared as described in U. S. Patent No. 2,345,543 by dissolving to a 12% solution a spray-dried condensation product of about 3 mols 01' aqueous formaldehyde solution with one mol of melamine in warm water containing 0.8 moi of HCl for each mol oi melamine and aging about 16 hours. I
Bleached kraft pulp was soaked in water for /2 hour, circulated in a five pound laboratory beater for hour, beaten V2 hour under full load (31 lbs.), refined ior 2 minutes in a laboratory Jordan and adjusted to 1.2% consistency.
A polyethylacrylate dispersion having a resin solids content of and an average particle size less than 1 micron was prepared, by the emulsion polymerization procedure described in Example 1, using the same emulsifying agent.
The paper stock suspension was first treated with 3% of colloidal melamine-formaldehyde resin, based on the dry weight of the fibers; by adding the resin solution and stirring for minutes. The pH was then adjusted to about 6-7 by adding sodium or ammonium hydroxide and the polyethylacrylate emulsion was added. The mixture was then stirred 30 minutes and formed into sheets on a Valley handsheet machine having a -mesh forming wire. The sheets were couched from the wire with blotters and dried without pressing on a drum drier at roe-120 C. for approximately 10 minutes.
The retention of the acrylate emulsion was determined by examination of the white water. It was found that the melamine resin colloid was very effective in producing a uniform deposition and retention of the polyethylacrylate emulsion;
in fact, the retention was practically complete in 18' grains resin colloid not adsorbed by the pulp The impregnated pulp was again suspended in water to 1% consistency, the suspension having a pH of 6.3, and one portion was made into handsheets, which were found on analysis to contain 1.1% of melamine resin. Another portion was treated with of emulsion-polymerized polystyrene, based on the dry weight of the paper pulp, and handsheets were made. The same quantity Of polystyrene emulsion was also added to another 1% slurry of the same paper pulp which had not been pretreated with the melamine resin and the same sheetmaking procedure was followed.
More than 80% or the polystyrene was retained by the melamine resin-treated pulp and was impregnated uniformly throughout the finished sheets. The sheets prepared from the untreated pulp contained little or none or the added polystyrene.
This example shows that the fiocculating action of the colloidal melamine-aldehyde resins persists even after the resin has been adsorbed by fibrous materials. Cellulosic paper stock and other fibrous material pretreated with the resin colloid can therefore be used as a fiocculating agent for emulsions or suspensions of waxes, gums, resins and other similar materials.
Example 4 A 12% solution of colloidal melamine-formaldehyde resin contining 5 grams of resin was diluted with water to 2 litersand 200 grams of an aqueous emulsion containing 50 grams of polystyrene were added with stirring. The polystyrene was immediately fiocculated, and the resulting precipitate was filtered oil. The filtrate was clear, showing that complete precipitation had been obtained.
The precipitated resin was dried, ground, and a portion was moulded at C. and 3,600 pounds per square inch. A clear moulded piece was obtained.
These results show that good retention of the polyethylacrylate by the cellulosic paper stock is obtained even when large quantities are applied.
Example 3 Bleached kraft paper pulp was soaked in water for A: hour, circulated in a laboratory heater for hour, and then beaten l hour with full load on the beater roll. The beaten pulp was refined for 2 minutes and diluted with water to 1.2% consistency. A quantity of colloidal melamineformaldehyde resin equal to the dry weightof the paper pulp was added as a 12% solution acidifled with 0.8 mol of hydrochloric acid per mol of melamine and the mixture was stirred 30 minutes. The pulp was then filtered and washed with a large quantity of water to remove all mel- A' sample of the resin was analyzed for nitrogen and found to contain 6.75% of melamine-formaldehyde resin.
The above-described procedure was repeated using 25 grams of the melamine resin and 25 grams of polystyrene and neutralizing with emmonia prior to the filtration. A clear filtrate was again obtained. The precipitate contained 46% or melamine-formaldehyde resin.
This example shows the fiocculating action of the colloidal, cationic melamine-aldehyde resin solutions in the absence of fibrous cellulose material and illustrates the importance of the presence of excess melamine resin colloid in the system over and above that which hasbeen adsorbed on the cellulosic fibers. However, the coagulation ll of resinous dispersions in aqueous dispersions The Per Cent Resin Retention I Ave. Sheet, Wt. (Grams) The mixture was The solids content pic at 105 C. to
mmmm moan momm mmmm mama mmmw mmmm mmwm 0 0 0 0 pH of Cali Slurry (inches) 0000 0000 0000 000 0 0000 .0000 0000 0000 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 AI LA 5 5 5 5 6 6 6 6 7 7 7 7 Example 6 Mela- 1111118 5556 wmmm hmmw mmmm wmmm mmwm mmmm F. with 440 grams of water containing on Dry Fiber Resin. Per Cent Phenol A solution of 200 grams of a tertiary butyl Bleached kraft paper stock was impregnated Various quantities of phenol-formaldehyde res- Fiber the shape of the mold without any apparent tearing, and a well-moulded piece of good appearance was obtained.
300 grams of methyl cyclohexanone was mixed at 200 melamine-formaldehyde resin (20% on the dry 10 2.5 grams of sodium dioctyl sulfosuccinate and 10 grams of a sorbitan monopalmitate-ethylene oxide condensation product. homogenized to an emulsion having an average particle size of 1-2 microns.
0.5 micron were added and the mixture stirred as determined by heating a sam for an additional 10 minutes, after which it was diluted to 0.6% paper pulp and made into handwith the phenol-formaldehyderesin solution by the following procedure: The stock was diluted with water to 1% fiber consistency and colloidal melamine-aldehyde resin solution was added, the mixture stirred for 5 minutes, and the pH adjusted to the desired figure by the addition of sodium hydroxide or hydrochloric acid.
phenol-formaldehyde resin emulsion was then added, followed by an additional 5 minute stirring, whereupon the impregnated fibers were made into handsheets on a laboratory sheetmaking machine. These sheets were pressed between blotters and dried at 100-120 C. on a drum drier after which they were heated at 260 C. for one hour.
11 and melamine-formaldehyde colloid were applied to the stock in this manner and the resin retention was determined. The quantities used and the results obtained are given in the following table.
phenol-formaldehyde condensation product in constant weight, was 23.8%.
. 19 containing no fibrous cellulosic material is not claimed as such in the present application, since this is claimed in our copending application Serial No. 604,967 filed concurrently herewith.
Example 5 parts by weight of dry bleached kraft pulp were mixed with water to a 1% suspension and 168 parts of a 12% colloidal cationic solution of paper stock) were added and sth'red for 10 minutes. The pH of the slurry was adjusted to 4.0 and 160 parts of an emulsion-polymerized polystyrene dispersion having a particle size of about sheets on a Valley machine. The white water was clear, indicating that substantially all the polystyrene was retained by the paper stock.
The handsheets were shredded mechanically, filled into a mold at 155 C. and pressed at that temperature for 5 minutes. A well-moulded piece of good mechanical strength and appearance was obtained.
A second batch of kraft pulp was impregnated with 20% of melamine-formaldehyde resin and 200% of polystyrene resin by the procedure described above, except the pH of the pulp slurry containing the cationic melamine-aldehyde resin 30 was raised to 7.0 prior to adding the polystyrene dispersion. The impregnated pulp was formed into a sheet 0.25 inch thick on a Buchner funnel and dried at 200 F.
A disk was out from the center of this sheet 3 and placed in a disk mold at 155 C. After a few minutes for the preform to become heated the mold was closed and a pressure of 3600 lbs/sq. in. was applied for 5 minutes. The preform took Blank......
1 Grams of dry fiber in the suspension from which the sheet was made. Sheet weight-Fiber x Weight of resin added amass? These results show that a high degree of retention of thermosetting resins of the type of phenol-formaldehyde condensation products is obtained by the use of colloidal melamine-aldehyde resin solutions. Other phenol-formaldehyde condensation products, such as those prepared from phenol itself, mixtures of phenol and cresols, and mixtures of phenol, cresols and xylenols may also be used.
Modified phenolic resins may also be applied to fibers of cellulose and the like by the use of colloidal melamine-formaldehyde resin solutions as illustrated in this example. Thus, for example, resins obtained by the condensation of mixtures of phenols and aminotriazines such as melamine with formaldehyde or other reactive aldehydes may be applied in this manner. Typical aminotriazine-phenol-formaldehyde resin syrups that may be used are described in detail in U. S. Patent No. 2,229,291. Any of these resins may be emulsifled and applied to aqueous suspensions of a filler such as paper stock by the procedure described above, and the resulting impregnated filler is well suited for use in pulp moulding processes.
Example 7 Sheets impregnated with phenol-formaldehyde resin by the process described in the preceding example were moulded into laminated board. A water suspension of bleached kraft stock of 1% consistency was treated with 20% of melamine-formaldehyde resin colloid and then with 200% of the phenolic resin, based on the dry weight of the paper fibers, and the resulting impregnated stock was made into 6 x 6-inch sheets i on a Valley handsheet machine. The wet sheets Kraft paper stock was impregnated with finely divided polystyrene and made into paper on a Fourdrinier papermaking machine. The stock was beaten at 6% consistency for 1.25 hours and then diluted with water to 2%. Colloidal cationic melamine-formaldehyde resin, acidified with 0.8
mol of hydrochloric acid 'per mol of melamine and aged 16-20 hours at 12% resin solids was added to the diluted stock in the beater chest with thorough agitation. After about minutes suflicient sodium hydroxide solution was added to raise the pH to 6.7 and the polystyrene was then stirred in. An emulsion-polymerized polystyrene was used which was prepared by introducing styrene with agitation into a 2 water solution of Duponol C, a sodium alkyl sulfate emulsifying agent, heated to C, adding 5-8% hydrogen peroxide, refluxing to complete the polymerization, diluting to 30% solids and steaming to remove unreacted monomer, and diluting to 24.3% solids.
After all the resin was. added the stock consistency was 2.57%. On the dry basis the furnish contained 62.8% pulp, 33.7% polystyrene and 3.5% melamine-formaldehyde resin. The stock was not further refined after its original beating. .The purpose of the run was to make 10-point (0.010-inch) laminating paper, and it was found that this caliper was obtained at a consistency in the head box of 0.91% solids and a wire speed of 27 feet per minute. At first the stock was run out on the machine at 20 C., but at this temperature it was quite slow on the wire. Much better performance was obtained by heating the stock to 35 C. With this change, and with a few adjustments to the suction at the boxes and couch roll to prevent sticking on ,the first press roll the machine was operated successfully.
During the last part of the run alum in amounts of 1-2% on the weight of the fiber was added at the beater chest and in the closed white water system. This made the stock slighly more free on the pa ermaking wire.
The machine was equipped with 17 drying rolls which were operated at temperatures increasing from F. at the first drier to 188 F. at the last. There was no deposit on or sticking to the drier felts, and no deposit on the driers. The finished sheet contained 74.6% paper fibers, 22.6% polystyrene and 2.8% melamine-formaldehyde resin. The resinretentions were therefore 57% and 68%, respectively. Only 0.06% of chloride ion was present, thus showing thatall the hydrochloric acid was released from the cationic melamine resin during the process.
A sample of the resin-impregnated paper made in this'run was broken up by continued beating in water, dried, and an electron photomicrograph made of a representative sample of the fibers at 14,000 diameters. This photomicro. graph is reproduced as Fig. 5 of the drawings. Reference to this figure shows the adhesion of the fiocculated resin to the individual cellulosic fibers.
Example 9 Two additional mill trials were made on the papermaking machine referred to in the preceding example using the same polystyrene emulsion and cationic melamine-formaldehyde resin in larger quantities.
In the first of these runs the furnish contained, on the dry basis, 48.1% of bleached kraft paper pulp, 47.1% polystyrene and 4.8% of the melamine-formaldehyde resin. The stock was prepared as described in the preceding example, no alum being added, at a consistency in the stuff box of 3.63% and a pH of 4.5. At the head box the consistency was 0.81%, the stock temperature was 34-47 0., and the pH was 6.2. (The water supply was slightly alkaline, having a pH of 8.2.) Paper having a caliper of 12-16 point (0.012-0.016 inch) was made without difficulty at a wire speed of 28.5 feet per minute using drying roll temperatures of from to F. The paper analyzed 55.5% cellulose pulp, 40.3% polystyrene and 4.2% melamineformaldehyde resin and the retentions were therefore 74% of the polystyrene and 75% of the melamine resin. Even larger quantities of resins were incorporated into the paper during the second run. The furnish contained on the dry basis 35.4% kraft pulp, 58.9% polystyrene and 5.7% cationic melamine-formaldehyde resin. The machine speed was 28.3 feet per minute, as before, and the paper was 0.012 inch in thickness and contained 50.6% pulp, 44.5% polystyrene and 4.9% melamine resin. The paper from both runs had a very low chlorine content (0.05%).
Fig. 6 of the drawings is a photomicrograph of fibers of the paper containing 44.5% polystyrene and 4.9% melamine resin. This figure shows clearly that at high resin-pulp ratios the individual fibers are completely coated with resin, yet retain their identity as fibers and thus their sheet-forming characteristics. The location of the resin along the individual fibers in Figs. and 6 demonstrates clearly the unusual fiocculating properties of the cationic melamine aldeyhyde resins.
What we claim is:
1. In a method of making a formed cellulosic product by the steps of preparing an aqueous suspension of fibrous cellulosic material, impregnating the cellulosic material with a waterinsoluble hydrophobic organic impregnating agent and forming the impregnated cellulosio material into a felted product, the improvement which consists in first adding a colloidal solution of hydrophilic cationic melamine-aldehyde resin to the aqueous fiber suspension, then adding an aqueous dispersion containing the impregnating agent in defiocculated condition and fiocculating the impregnating agent in admixture with the suspended fibers by the action of the cationic melamine-aldehyde resin, and thereby depositing a substantial proportion of the impregnating agent uniformly on the fibers along with melamine-aldehyde resin.
2. A method according to claim 1 in which the quantity of water-insoluble hydrophobic organic impregnating agent is more than 5% but not more than about 200% of the dry weight of the fibrous cellulosic material.
3. A method according to claim 1 in which the water-insoluble hydrophobic organic impregnating agent comprises polystyrene.
4. A method according to claim 1 in which the aqueous dispersion of defiocculated impregnating agent contains a member of the group consisting of anionic and nonionic emulsifying agents.
5. A method of impregnating fibrous cellulosic material with a hydrophobic organic impregnating agent while preserving the freeness and felting properties thereof which consists in preparing a water suspension of the fibrous cellulosic material at 0.5-6% consistency, adding to said suspension a hydrophilic cationic melamine-aldehyde resin in amounts of 2-30% of the weight of the organic impregnating agent to be added, allowing the suspension to stand at a pH in the range of about 2.5 to about 7.0 for at least 30 minutes, then adding an aqueous dispersion containing the hydrophobic organic impregnating agent in deflocculated condition, fiocculating the impregnating agent in admixture with the suspended cellulosic fibers by the action of the cationic melamine-aldehyde resin, and thereby depositing a substantial proportion of the impregnating agent uniformly on the fibers along with melamine-aldehyde resin.
6. A method according to claim 5 in which the quantity of water-insoluble hydrophobic organic impregnating agent is more than 5% but not more than about 200% of the dry weight of the fibrous cellulosic material.
7. A method according to claim 5 in which the water-insoluble hydrophobic organic impregnating agent comprises polystyrene.
8. A method for the production of felted fibrous cellulosic material having a uniform content of a water-insoluble hydrophobic organic impregnating agent which consists in preparing a water suspension of the fibrous cellulosic material, adding to said suspension a colloidal solution of hydrophilic cationic melamine-aldehyde resin, allowing the resulting suspension to stand at a pH of about 3-6 for at least 30 minutes, neutralizing the suspension by the addition of alkali. and then adding an aqueous dispersion containing the water-insoluble hydrophobic organic impregnating agent in a defiocculated condition, fiocculating the impregnating agent in admixture with the suspended fibers by the action of the cationic melamine-aldehyde resin and thereby depositing a substantial proportion of the impregnating agent uniformly on the fibers along with melamine-aldehyde resin, and forming the impregnated fibers into a felted product while draining the suspending water therefrom.
9. A method according to claim 8 in which the quantity of water-insoluble hydrophobic organic impregnating agent is more than 5% but not more than about 200% of the dry weight of the fibrous oellulosic material.
10. A method according to claim 8 in whichthe quantity of water-insoluble hydrophobic organic impregnating agent is about 50-100% of the dry weight of the fibrous cellulosic material and the quantity of hydrophilic cationic melamine-aldehyde resin is about 2-15% of the weight of said hydrophobic organic impregnating agent.
LUCIUS H. WILSON.
CHESTER G. LANDES.
CHARLES S. MAXWELL.
REFERENCES CITED The following references are of record in the file of this patent:
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Paper Trade Journal, August 22, 1940, page 30.
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|US2683087 *||Feb 10, 1948||Jul 6, 1954||American Cyanamid Co||Absorbent cellulosic products|
|US2683089 *||Jun 10, 1952||Jul 6, 1954||American Cyanamid Co||Bibulous sheet|
|US2686744 *||Oct 11, 1951||Aug 17, 1954||American Viscose Corp||Heat sealable wrapping material|
|US2694633 *||Feb 23, 1950||Nov 16, 1954||Talbott Dev Associates||Affixing organic and inorganic additaments to cellulosic materials|
|US2708544 *||Apr 19, 1952||May 17, 1955||Globe Envelopes Ltd||Coated paper receptacles|
|US2708645 *||Jun 22, 1953||May 17, 1955||Globe Envelopes Ltd||Method of making coated paper receptacles|
|US2737464 *||Jun 23, 1953||Mar 6, 1956||Jacques Wolf & Co||Treatment of fibrous materials|
|US2739058 *||Jul 17, 1952||Mar 20, 1956||Du Pont||Process for sizing paper with polyethylene|
|US2745744 *||Feb 9, 1951||May 15, 1956||Permacel Tape Corp||Treating agents incorporation|
|US2754730 *||Jan 28, 1954||Jul 17, 1956||Keyes Fibre Co||Molded fiber-resin article and method of making|
|US2767089 *||May 21, 1951||Oct 16, 1956||Gen Mills Inc||Paper containing polyamide resins and process of producing same|
|US2767090 *||Jun 4, 1954||Oct 16, 1956||Dow Chemical Co||Chemical process and product|
|US2768754 *||Aug 12, 1948||Oct 30, 1956||Southwick W Briggs||Bonded sawdust filter medium|
|US2772970 *||Apr 4, 1952||Dec 4, 1956||Armstrong Cork Co||Method of making fibrous sheet material containing a synthetic rubber binder|
|US2774687 *||Sep 1, 1953||Dec 18, 1956||Ludwig Nottebohm Carl||Process for the manufacture of porous flexible sheet material|
|US2780148 *||Nov 26, 1954||Feb 5, 1957||Weremiczyk Benny||Machine for setting up collapsed cardboard cartons|
|US2785975 *||Oct 30, 1953||Mar 19, 1957||American Marietta Co||Cellulose fiber product containing latex solids and a conjointly precipitated high molecular weight phenol-aldehyde resin-reaction product, and method of producing said product|
|US2789903 *||Sep 2, 1954||Apr 23, 1957||Celanese Corp||Process for production of shaped articles comprising fibrous particles and a copolymer of vinyl acetate and an ethylenically unsaturated acid|
|US2795567 *||Apr 14, 1953||Jun 11, 1957||Monsanto Chemicals||Chemical product|
|US2797163 *||Nov 22, 1952||Jun 25, 1957||James Raymond W||Method of making filter media|
|US2798850 *||Jan 2, 1952||Jul 9, 1957||Kimberly Clark Co||Ion exchange resinous product|
|US2803171 *||Aug 26, 1953||Aug 20, 1957||Patent & Licensing Corp||Process for producing a water vapor impermeable board|
|US2810646 *||Sep 17, 1953||Oct 22, 1957||American Cyanamid Co||Water-laid webs comprising water-fibrillated, wet-spun filaments of an acrylonitrile polymer and method of producing them|
|US2822298 *||Aug 29, 1955||Feb 4, 1958||Armstrong Cork Co||Fibrous products|
|US2898293 *||Dec 28, 1953||Aug 4, 1959||Gulf Research Development Co||Wax sized paper|
|US2924550 *||Jun 25, 1956||Feb 9, 1960||Friedman Alex||Method of molding resin and fiber compositions|
|US2943013 *||Jul 27, 1956||Jun 28, 1960||Hurlbut Paper Company||High ash content absorbent paper for the decorative laminating industry and a process for preparing the same|
|US2980609 *||Jun 22, 1953||Apr 18, 1961||American Cyanamid Co||Clarification of industrial waters|
|US2987421 *||Sep 19, 1955||Jun 6, 1961||Goodrich Co B F||Composition for treating textile materials, method, and article produced thereby|
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|US2998344 *||Jul 11, 1957||Aug 29, 1961||St Regis Paper Co||Wet web binding process and product|
|US3006806 *||Feb 15, 1957||Oct 31, 1961||Olin Mathieson||Sized paper and process therefor|
|US3016325 *||Nov 1, 1955||Jan 9, 1962||Electro Chem Fiber Seal Corp||Process of combining water-insoluble additament with organic fibrous material|
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|US3418237 *||Dec 22, 1963||Dec 24, 1968||American Cyanamid Co||Settling of non-argillaceous ore pulps and mineral suspensions by use of water-soluble acrylic polymers|
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|US3715172 *||Jan 12, 1971||Feb 6, 1973||Nalco Chemical Co||Urea- and melamine- formaldehyde bridging agents|
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|US4125645 *||Sep 29, 1975||Nov 14, 1978||Northern Telecom Limited||Latex modified pulp insulated conductors|
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|US4187142 *||Aug 17, 1977||Feb 5, 1980||The Dow Chemical Company||Method for forming high strength composites|
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|US4234378 *||Apr 27, 1979||Nov 18, 1980||Sakai Chemical Industry Co., Ltd.||Magnet paper sheet and a method for manufacturing the same|
|US4256807 *||Aug 23, 1979||Mar 17, 1981||Northern Telecom Limited||Synthetic latex modified pulp insulated conductors|
|US4510019 *||Nov 17, 1982||Apr 9, 1985||Papeteries De Jeand'heurs||Latex containing papers|
|US4523995 *||Oct 19, 1981||Jun 18, 1985||Pall Corporation||Charge-modified microfiber filter sheets|
|US4608173 *||Jun 7, 1985||Aug 26, 1986||Toa Nenryo Kogyo Kabushiki Kaisha||Filter|
|US4865691 *||Nov 5, 1987||Sep 12, 1989||Colloids, Inc.||Process for internally strengthening paper and board products and products resulting therefrom|
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|US5501804 *||Jul 14, 1994||Mar 26, 1996||Amoco Corporation||Apparatus and process for blending elastomer particles and solution into a uniform mixture|
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|DE1254009B *||Oct 2, 1963||Nov 9, 1967||Dynamit Nobel Ag||Verfahren zum gleichmaessigen Beladen von fuer die Herstellung von Papier, Vliesen od. dgl. geeigneten Fasern mit Kunststoffen|
|EP0067076A1 *||Apr 9, 1982||Dec 15, 1982||Papeteries De Jeand'heurs||Process for the continuous manufacture in an aqueous environment of fibrous webs containing latex or a similar composition and/or a phenoplastic or aminoplastic, webs so obtained and their optional reuse|
|EP0109900A1 *||Nov 16, 1983||May 30, 1984||Papeteries De Jeand'heurs||Process for the production of latex-containing papers, and paper sheets thus obtained|
|WO2014152960A1 *||Mar 14, 2014||Sep 25, 2014||Auburn University||Functionalized cellulose for dewatering and efficiency improvements|
|U.S. Classification||162/166, 162/182, 162/165, 210/508, 210/510.1, 427/391, 210/735, 162/148, 162/138, 162/168.6|
|International Classification||D21H17/51, D21H23/00, D21J1/08, D21H23/76, D21H17/35|
|Cooperative Classification||D21H17/35, D21J1/08, D21H17/51, D21H23/765, D21H23/00|
|European Classification||D21J1/08, D21H23/76B, D21H17/35, D21H23/00, D21H17/51|