Search Images Maps Play YouTube News Gmail Drive More »
Sign in
Screen reader users: click this link for accessible mode. Accessible mode has the same essential features but works better with your reader.


  1. Advanced Patent Search
Publication numberUS3189578 A
Publication typeGrant
Publication dateJun 15, 1965
Filing dateApr 23, 1959
Priority dateApr 23, 1959
Also published asDE1419423A1, DE1419518A1, US3061470, US3061472
Publication numberUS 3189578 A, US 3189578A, US-A-3189578, US3189578 A, US3189578A
InventorsHenry R Kuemmerer
Original AssigneeDeering Milliken Res Corp
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Polymers and their production
US 3189578 A
Abstract  available in
Previous page
Next page
Claims  available in
Description  (OCR text may contain errors)

United States Patent 3,189,578 POLYMERS AND THEIR PRODUCTION Henry R. Kuemmerer, Walhalla, S.C., assignor to Deering Milliken Research Corporation, near Pendleton, S.C., a corporation of Delaware No Drawing. Filed Apr. 23, 1959, Ser. No. 808,310 6 Claims. (Cl. 260-775) the basic ingredient of textile yarn sizing formulas. Some advances have been made in the use of synthetic size materials other than modified starch, especially in connection with synthetic yarns. However, these advances have been painfully slow despite the urgent need to conquer the stream pollution problem created by starch being dumped into streams from desizing units. Earlier synthetic sizing materials have met with very limited success because of their high cost and because they are only use ful with a limited number of fibers. Dacron has been a particularly diflicult fiber to size with any prior art materials and spun Dacron yarn sizing has remained a major textile problem prior to this invention.

It is an object of this invention to provide a composition and process by which textile yarns in general and spun Dacron yarn in particular maybe readily sized on conventional equipment to provide excellent weaving ethciency and minimum shedding. Another object of the invention is the provision of a synthetic size which may be easily desized with plain water and dumped into streams without seriously polluting them.

It is one object of this invention to make high molecular weight, water-soluble, tough, flexible, film-forming polymers of polyalkylene ether glycols and aryl diisocyanates. Another object of the invention is the provision of control steps in the polymerization of polyalkylene ether glycols with aryl diisocyanates to control the properties of the polymers thus formed.

Another object of the invention is the provision of an inexpensive method of advantageously sizing and desizing textile yarns while substantially eliminating stream pollution problems. These and other objects of the invention will be more readily apparent from the following detailed description.

The novel polymers of this invention are particularly characterized by their water-solubility and their filmforming properties. They are readily water soluble, making them easy to apply to textile yarns as a size, and they retain their solubility so that desizing may be accomplished by a simple water wash. Thefilms formed from water solutions of these new polymers are very tough and flexible and strong, especially as contrasted with the brittle films of the polyethylene ether glycol polymers alone and the prior art materials produced with water-insoluble reaction products of polyalkylene ether glycols and aryl diisocyanates, which materials are sometimes rubbery and sometimes crumbly.

These water-soluble reaction products of polyalkylene ether glycols and aryl diisocyanates have outstanding advantages over prior art sizing materials in weaving efiiciency and in terms of running efliciency on conventional Patented June 15, 1965 slashers. Good yarn penetration even in the absence of a separate wetting agent is obtained at temperatures of about 120-180 F. Hard size at the squeeze roll is substantially eliminated. There is no sticking on conventional drying cans. Separation of the yarns at the split rods is smooth and even, and broken ends seldom, if ever, appear. At the same time, the size holds the fibers of individual yarns in a very close, tight, unitary relationship for efiicient weaving. These last two seemly contradictory advantages are amply evidenced by the fact that spun Dacron yarns, for example, are so adhesively bound by the size of this invention that their diameter is actually substantially reduced by the sizing operation while the same yarns separate at a greater distance ahead of the split rods than the same yarns sized with conventional materials.

POLYMER PREPARATION In making the polymers according to this invention one molar equivalent of a substantially anhydrous polymer of polyalkylene ether glycol having a molecular weight of from about 6,000 to 7,500 is catalytically reacted with from about 1 to 2 molar equivalents of an aryl diisocyanate (in practice slightly more than 1 mol is required and less than 2 mols is needed to avoid the danger of rapidly forming water-insoluble polymers) to produce polymers of extremely high molecular weight and the reaction is abruptly halted at a point just short of Water insolubility. Preferably the molar ratio is from about 1%:1 to ll zzl of diisocyanate to glycol, respectively. The molar ratio is extremely important as too much diisocyanate rapidly produces water-insoluble products and too little diisocyanate produces brittle polymers which make weak films which are unsuitable for sizing purposes.

The abrupt halting of the reaction may be accomplished by the addition of an aliphatic monohydroxy alcohol as a stopping agent which reacts with isocyanate radicals to block further reaction with the glycol. Aliphatic mono-- hydroxy alcohols are preferred, as polymers so stopped have been found to maintain better weaving efliciency over a period of time when used as a size. Methanol and isopropanol, being both inexpensive and efficient, are excellent stopping agents tor -abruptly halting the polymerization reaction at the right point. The minimum amount of stopping agent to be added will vary according to the excess of diisocyanate used. While a theoretical minimum may be readily calculated, it is preferred to add at least a molar equivalent for the isocyanate used, as a safe excess. Additional quantities are ordinarily not harmful.

The reaction should proceed as far as reasonably possible short of the point of water-insolubility to obtain polymers having the most desirable film strength. For example, if the reaction is carried out under standardized conditions and water insolubil-ity is first found to occur after a certain time X, products made in accordance with this invention may be made by duplicating the conditions except that reaction is halted at a time less than time X and greater than of X.

Many methods may be used to determine the end point at which the reaction should be stopped to obtain a polymer that will provide tough flexible films which are readily water-soluble. In commercial production where everything is standardized, an empirical time-temperature relationship may be established by trial and error. After a little experience with given materials, a skilled chemist can tell the end point by visual inspect-ion of the reaction massi.e. its viscosity, reaction to stirring, stringiness, etc. Also with any given reactants, empirical viscosity determinations may be used.

The polymerization time and temperature may be varied over a considerable range so long as the react-ion is stopped at the critical point. The reaction must be carried out at a temperature above the melting point of the polyalkylene ether glycol. However, the reaction proceeds slowly unless the temperature -is elevated above about 70 C. but the temperature should not exceed 150 C. because higher temperatures tend to decompose the polyoxyalkylene chains. The preferred range is from about 100 C. to 150 C. The time of the reaction is a function of the temperature, the reactants, the catalyst and other factors. Suitable times have varied from 8 minutes to about an hour.

The term polyalkylene ether glycols as used throughout the specification and claims refers to polyethers which are derived from alkylene oxides or glycols or from other heterocylic ethers such as dioxolane, and which may be represented by the formula HO(RO) H, in which R stands for a lower alkylene radical and n is an integer greater than 1. Not all the alkylene radicals present need be the same, and polyethers containing a mixture of radicals can be used, although the choice of radicals should be such that the resulting polymer is water soluble. These polyalkylene ether glycols are waxy solids. The preferred glycols are polyethylene ether glycols.

A wide variety of aryl diisocyanates may be used in this invention, .but monophenyl diisocyanate: are preferred. Suitable compounds include 2,4-toluene diisocyanate, mphenylene diisocyanate, 4-chloro'1,3-phenylene diisocyanate, met-hyl'ene-bis-(t-phenyl isocyanate), naphthalene- 1,5-d-iisocyanate and the like.

Any catalyst known to be useful in the reaction of polyalkylene ether glycols with aryl diisocyanates may be used in the present invention including the tertiary organic bases of US. Patent No. 2,692,874 such as triethylamine, pyridine, tri-n-butylphosphine, their acid salts and the like.

However, it has been found that particularly good results are obtained by using organo-metal salts, such as cobalt naphthenate and similar salts of lead, zinc, copper and manganese. The organic radicals may be either aliphatic or aromatic residues.

The term substantially anhydrous polymer is used to define a polymer containing less than about 0.5% moisture. It has been found that some commercial polyalkylene ether glycols containing as much as 0.5% moisture react improperly to provide films of poor strength, making them unsuitable for textilesizes. In practice, the moisture content of the polyalkylene ether glycols will be kept as low as possible.

SIZING PROCEDURE weaving efiiciency. The amount of silicone used will be from about 0.01% to 1% and preferably about 0.25%. Somewhat larger quantities may be used in some instances but such uses are merely wasteful. Furthermore, it has been found that raising the addition of ammonia to raise the pH of the solution to about pH 8.5-9.5 also provides a definite improvement in weave room performance, apparently by reduction of any tendency of the polymers to pick-up moisture. The amount of size to be applied will vary somewhat according to the nature of the fibrous materials, the type of yarn, the denier or count and the like but in general 2.5% to 5% polymer solids on the weight of the yarn provides a suitable size. The concentration of the sizing solution may vary over a fairly wide range of from about 2% to 15% but a 4% to 8% solution of the p y is P eferred.

In sizing operations, as distinguished from fruit and vegetable coating and the like, hygroscopic properties of the polymer must be minimized because Weaving is normally done under very high humidity conditions. The use of polyurethanes end-blocked with alkoxy groups, i.e., alcohol stopped reaction products of the invention, has been found to be particularly valuable interms of lowered hygroscopic tendencies. Silicones are very eifective in reducing any stickiness which may tend to occur as a result of moisture pick-up of hygroscopic polymers.

Surprisingly, the silicone rises through the polymers of aryl diisocyanate and polyalkylene ether glycol when mixtures of the two are cast into films from an aqueous medium. This provides a sort of two layer effect permitting the hydrophobic properties of the silicone to 'be eifectively utilized.

Thus, in the preferred manner of sizing, one will use an aqueous medium containing an alcohol stopped watersoluble polymer of the invention and a silicone with the medium having a controlled pH of from about 8.5-9.5. Yarns sized in accordance with this preferred procedure have a coating of polymer topped by a coating of silicone.

The stability of-the polymer in solution is excellent so that it may be stored in any-of its liquid or solid forms and its good water solubility permits mixing at any point in the mill whereby a separate mixing operation and operator, as required for starch sizing, may be eliminated.

The invention is described both in the specification. and

claims in terms of sizing textile yarns and it will be understood that the term yarn" includes both spun fiber yarns and filament yarns. The invention is particularly applicable to spun Dacron, spun mixtures" of cotton and Dacron, cotton, viscose and acetate and the like.

In some instances a permanent size is desirable to provide a loom finished fabric. In such instances, the polymers of this invention may be further reacted in situ on yarn to provide the desired products. In these reactions, formaldehyde, acetaldehyde, acrolein, other aldehydes, and/or aldehyde donors such as methylol melamines, methylol ureas, methylol ethylene ureas, copolymers of acetone and formaldehydes, methylol acetylene diureas and the like may be added to the sizing solution preferably in the presence of an acidic catalyst so that they will react with the polymer on the slasher dry cans to produce water-insoluble cross-linked films on the yarn.

The invention will be better understood by reference to the following typical examples:

Example 1 92 pounds of substantially anhydrous polyethylene ether glycol in a molecular weight range of 6000-7500 (Carbowax 6000) was melted in a 50 gallon reactor equipped with a reflux condenser and a stirrer. When the temperature reached 70 C.,4 pounds and 3 ounces of 2,4-toluene diisocyanate (Nacconate was added: with stirring.

183 grams of a 6% solution of cobalt naphthenate' was added forthwith to catalyze the reaction. At the end of the addition, the temperature had risen to 88 C. as heating was continued throughout the reaction. In about 20 minutes the reaction temperature reached C. This temperature was maintained for 15 minutes while stirring continued. At the end of the 15 minute period, 9 pounds of isopropanol were added and stirred into the mixture to halt the reaction and heating was stopped. Water was then added in a quantity suflicient to make a 25% solution of the polymer which was then ready for further dilution and use as a size.

After addition of the diisocyanate and catalyst, the reacting mass became more viscous as the reaction proceeded. Towards the end of the reaction period, the reaction mass was stiffening and would string out several inches behind a stirring rod. There was little change in physical appearance on addition of the methnnolexccpt Example 2 To 35 grams of molten (120 C.) polyethylene ether glycol of a molecular weight range of 6000-7500, there was added 1 gram of 2,4-toluene diisocyanate and 5 drops of cobalt naphthenate solution (6%). The temperature was maintained for 5 minutes after which water was added in a quantity suflicient to make a solution. The reaction proceeded as in Example 1, except that the smaller quantity required less time for reaction to the same point and reaction was topped with water rather than methanol. The appearance of the two solution products was not distinguishable to the naked eye. The product of this example had a viscosity of 333 centipoises.

Repeating this example using m-phenylene diisocyanate or methylene-bis-(4-phenyl isocyanate) (in 50% benzene solution) instead of 2,4-toluene diisocyanate produced products of similar appearance and utility as a size.

Example 3 A warp of several thousand ends of 100% spun Dacron yarns was sized on conventional synthetic slasher equipment having a heated size-box, standard squeeze rolls and Teflon-coated dry cans. The yarns were impregnated by passing them through the size box containing a water solution of the product of Example 1 diluted to 6% solids and brought to pH 9 with ammonia. The size box temperature was kept at 150 F. and the squeeze rolls were set to leave 3.5% solids on the yarn. Drying was completely conventional with dry can temperatures of about 200 F. The slasher operated smoothly without hard size problem, with no sticking on the cans and excellent action was noted at the split rods. It appears as though splitting might be a smooth tear for no jagged edges were noted at the split lines and the split ran back from the rods a greater distance than normal.

A beam of the sized yarns was placed on a loom and readily woven into an all Dacron fabric of standard plainweave construction. Good weaving etficiency was noted immediately and shedding was minimized.

Complete desizing was eflected by washing the woven fabric for 30 minutes in lukewarm water, even without a surface active agent.

Example 4 In a suitable reaction vessel there is placed 50 parts by weight of dimethyl silicone oil (5000 centipoises), 20 parts by weight of perchlorethylene, 25 parts toluene, and 5 parts oleic acid. The resulting mixture agitated until solution was complete.

A size mixture was prepared as in Example 3 except there was dispersed in the aqueous mixture 2% by weight of the above silicone solution. The size mixture was then applied according to the procedure of Example 3 to a warp of several thousand ends of 100% spun polyethylene terephthalate (Dacron) yarns. The sized yarns appeared to have more lubricity than those from the preceding example, and this may account for the even greater weaving efficiency noted.

This example was repeated using methyl hydrogen silicone, chain stopped with trimethyl silicone, in the place of the dimethyl silicone oil and the results were substantially duplicated. Other silicones useful in the treatment of textiles may be substituted for those listed above or the coated yarns may be top coated with chlorosilane vapors if desired.

Example 5 To prepare a loom finished fabric, an all cotton warp was sized with a 5% solution of a product prepared in accordance with Example 3 to deposit 5% solids (weight basis) thereon. At the time of mixing the sizing solution (just prior to use), 0.1% of formaldehyde was added. A conventional cotton slasher was used with the size box heated to a temperature of F. Excellent running conditions were noted as in Example 4. The sized warp was woven into an all cotton fabric. Weaving efiiciency was good and shedding was minimized.

Because of the formaldehyde, the size film had become insoluble and could not be washed out, thus providing a high-quality loom finished cotton fabric.

Those skilled in the art will find that certain changes may be made in the precise conditions, proportions and procedures set forth above without departing from the invention as defined in the claims.


1. A water-soluble polyurethane which forms tough, flexible and strong films from water solutions thereof and which is a reaction product of an arylene diisocyanate and a polyethylene ether glycol of the formula HO(CH CH O) H wherein n is an integer sufficient to provide a molecular weight of from 6,000 to 7,500, said arylene diisocyanate being present in a molar ratio of 1%:1 to 1% :1 moles of arylene diisocyanate per mole of polyethylene ether glycol, said reaction having been terminated with at least one molar equivalent of an aliphatic monohydroxy alcohol per molar equivalent of said arylene diisocyanate when the reaction product had approached but not;

References Cited by the Examiner UNITED STATES PATENTS 2,284,637 6/42 Catlin 26077.5v 2,871,226 1/59 McShane 26077.5 2,871,227 1/59 Walter 26077.5 2,946,767 7/60 Gassmann 260- 77.5 2,948,691 8/60 Windemuth et al. 26077.5 2,952,665 9/60 Bunge 260453 2,977,330 3/61 Brower 26025 3,021,307 2/62 Csendes 26077.5

FOREIGN PATENTS 208,983 7/57 Australia.

LEON J. BERCOVITZ, Primary Examiner.



Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2284637 *Sep 29, 1938Jun 2, 1942Du PontPolymeric carbamates and their preparation
US2871226 *Mar 24, 1955Jan 27, 1959Du PontElastomeric condensation products prepared from polyether glycols
US2871227 *Mar 24, 1955Jan 27, 1959Du PontElastomeric condensation products prepared from polyether glycols
US2946767 *Aug 9, 1956Jul 26, 1960Ciba LtdManufacture of reaction products of polyisocyanates with ethylene oxide addition products
US2948691 *May 6, 1952Aug 9, 1960Mobay Chemical CorpHigh molecular weight polyether urethane polymers
US2952665 *Dec 6, 1956Sep 13, 1960Bayer AgHigh molecular weight cyclic trimers containing blocked isocyanate groups
US2977330 *Dec 5, 1957Mar 28, 1961Dow Chemical CoCellular polyalkylene-etherglycolorganic diisocyanate reaction product and method of preparing same
US3021307 *Jun 30, 1958Feb 13, 1962Du PontPolyurethane elastomers cured with paraformaldehyde
AU208983B * Title not available
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3321819 *Dec 24, 1964May 30, 1967Union Carbide CorpProcess for sizing and desizing textile fibers
US3350361 *Jul 26, 1963Oct 31, 1967Lankro Chem LtdUrethane polymers and methods of applying compositions containing the polymers
US3384623 *Dec 31, 1964May 21, 1968Toyo Spinning Co LtdProduction of polyurethane elastomers
US3402149 *Dec 4, 1964Sep 17, 1968Thiokol Chemical CorpProcess for preparing polyureapolyurethane molding powders
US3427192 *May 20, 1964Feb 11, 1969Deering Milliken Res CorpTextile sizing composition
US3427272 *Mar 22, 1968Feb 11, 1969Deering Milliken Res CorpWater-soluble polyurethane produced by reacting an aldehyde and the reaction product of an organic diisocyanate and an anhydrous polyalkylene ether glycol
US3472802 *Nov 23, 1966Oct 14, 1969Inter Chem CorpNovel nitrocellulose flexographic printing inks
US3864195 *May 7, 1973Feb 4, 1975Patterson Henry GStable synthetic carpet backing material
US3982986 *May 1, 1975Sep 28, 1976Inmont CorporationLaminates and method of making them
US3990839 *Aug 14, 1974Nov 9, 1976Hoechst AktiengesellschaftProcess for obtaining irregular shadow dyeings on polyester fibers and mixtures thereof
US4079028 *May 17, 1976Mar 14, 1978Rohm And Haas CompanyPolyurethane thickeners in latex compositions
US4082703 *Apr 5, 1976Apr 4, 1978Union Carbide CorporationPolyurethane prepolymers, rebonded polyurethane foam and methods of forming the same
US4150946 *Nov 8, 1977Apr 24, 1979Rhone-Poulenc IndustriesWater-soluble polyurethanes and compositions and application thereof to substrates
US4155892 *Oct 3, 1977May 22, 1979Rohm And Haas CompanyPolyurethane thickeners for aqueous compositions
US4524036 *Apr 9, 1984Jun 18, 1985University Of LiverpoolProcess for the manufacture of polyurethane resin for electrostatic spinning
US4530876 *Aug 12, 1983Jul 23, 1985Ppg Industries, Inc.Warp sizing composition, sized warp strands and process
US4762750 *Feb 26, 1987Aug 9, 1988Ppg Industries, Inc.Flexible, chemically treated bundles of fibers and process
US4762751 *May 22, 1986Aug 9, 1988Ppg Industries, Inc.Flexible, chemically treated bundles of fibers, woven and nonwoven fabrics and coated bundles and fabrics thereof
US4863994 *Jun 24, 1988Sep 5, 1989The Dow Chemical CompanyUse of monohydric alcohols in molded polyurethane resins
US7994213 *May 28, 2008Aug 9, 2011Taewoong Medical Co., Ltd.Coating agent for drug releasing stent, preparation method thereof and drug releasing stent coated therewith
USB497473 *Aug 14, 1974Feb 3, 1976 Title not available
U.S. Classification528/49, 528/74, 528/76, 8/DIG.400, 8/115.6, 28/178
International ClassificationD06M15/11, C08G18/48, C08F251/00, C08G18/10, C08L71/02, D06M15/564, C08L3/02, C08G18/84, C09J133/08, C09J103/02, D06M15/267
Cooperative ClassificationC08G18/10, Y10S8/04, C09J103/02, C08L3/02, D06M15/564, C08G18/84, D06M15/11, C09J133/08, C08L71/02, C08F251/00, Y10S8/18, D06M15/267, C08G18/4833
European ClassificationC08F251/00, C08L3/02, C08G18/10, C09J103/02, C09J133/08, D06M15/11, D06M15/564, D06M15/267, C08G18/84, C08G18/48F