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Process for preparing hydrogels as spherical beads of large size    
United States Patent4224427   
Link to this pagehttp://www.wikipatents.com/4224427.html
Inventor(s)Mueller; Karl F. (New York, NY); Heiber; Sonia J. (Bedford Hills, NY); Plankl; Walter L. (Yorktown Heights, NY)
AbstractThe disclosure describes an improved process for the preparation of uniform, spherical beads of up to 5 mm diameter of a crosslinked, water-insoluble hydrogel by suspension polymerization in a concentrated aqueous salt solution of 95-30% by weight of a monoolefinic water-soluble monomer containing at least 5% of a hydroxy substituted hydrophilic vinyl monomer with 5-70% by weight of a terminal diolefinic macromer crosslinking agent in the presence of water-insoluble, gelatinous, strong water-bonding inorganic metal hydroxides as suspending agents in the absence of excess alkali. The hydrogels have a host of pharmaceutical and industrial uses.
   














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Inventor     Mueller; Karl F. (New York, NY); Heiber; Sonia J. (Bedford Hills, NY); Plankl; Walter L. (Yorktown Heights, NY)
Owner/Assignee     Ciba-Geigy Corporation (Ardsley, NY)
Patent assignment
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Publication Date     September 23, 1980
Application Number     05/911,636
PAIR File History     Application Data   Transaction History
Image File Wrapper   Patent Term   Fees
Litigation
Filing Date     June 1, 1978
US Classification     526/93 525/10 525/404 525/424 525/426 525/440 525/445 525/455 525/479 525/920 525/921 525/925 526/172 526/221 526/226 526/227 526/234 526/237 526/259 526/260 526/279 526/318.42 526/320 526/321 526/332 526/909 526/910 526/930
Int'l Classification     C08F 002/18
Examiner     Briggs Sr.; Wilbert J.
Assistant Examiner    
Attorney/Law Firm     Hall; Luther A. R.
Address
Parent Case     This is a continuation-in-part application of copending application, Ser. No. 817,404, filed July 20, 1977, now abandoned.
Priority Data    
USPTO Field of Search     260/29.7 M 260/859 R 260/827 260/873 526/320 526/909 526/910 526/93 525/404 525/440 525/920 525/921 525/925
Patent Tags     preparing hydrogels spherical beads large size
   
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What is claimed is:

1. An improved process for preparing essentially uniform spherical beads of up to 5 mm diameter of a crosslinked, water-insoluble hydrogel by suspension polymerization of (A) 95 to 30% by weight of the hydrogel of a water-soluble monoolefinic monomer or mixture of said water-soluble monomers, and from 0 to 70% by weight based on the total monomer of a water-insoluble monoolefinic monomer or mixture of said water-insoluble monomers, with the proviso that the final hydrogel does not contain over 60% by weight of said water-insoluble monomer components, with (B) 5 to 70% by weight of the hydrogel of a polyolefinic crosslinking macromer of the formula ##STR9## wherein a is 1 or 2, R.sub.1 is a polycondensate chain having a molecular weight from about 200 to about 8,000 which contains hydrocarbon residues connected via ether, ester, amide or urea linkages or is a polysiloxane of molecular weight between 400 and 8,000; R.sub.2 is hydrogen, methyl or --CH.sub.2 COOR.sub.4 ; R.sub.4 is hydrogen or alkyl of 1 to 10 carbon atoms; R.sub.3 is hydrogen or --COOR.sub.4 with the proviso that at least one of R.sub.2 and R.sub.3 is hydrogen; X is an oxygen atom, --COO-- or --CONR.sub.5 ; R.sub.5 is hydrogen or alkyl of 1 to 5 carbon atoms; Y is a direct bond or the radical R.sub.6 --Z.sub.1 --CONH-- R.sub.7 NHCO--Z.sub.2 --; R.sub.6 is linked to X and represents branched or linear alkylene of 1 to 7 carbon atoms; Z.sub.1 is an oxygen atom or --NR.sub.5 --; Z.sub.2 is Z.sub.1 or a sulfur atom; and R.sub.7 is the diradical of an aliphatic, alicyclic or aromatic diisocyanate with the proviso that in case X is oxygen, Y is different from a direct bond and R.sub.2 and R.sub.3 are hydrogen, with a polymerization initiator in a concentrated aqueous inorganic salt solution wherein the improvement comprises

carrying out the suspension polymerization with monoolefinic monomers containing at least 5% by weight of the total monomers of a hydroxy substituted hydrophilic vinyl monomer;

employing as the crosslinking agent a polyolefinic macromer having a molecular weight from about 400 to about 8,000 and

utilizing from 0.01 to 5% by weight, based on the hydrogel, of a suspending agent selected from the water-insoluble, gelatinous, strongly water-bonding, inorganic metal hydroxides and metal hydroxy salts in the absence of excess alkali or free hydroxyl ions.

2. A process according to claim 1 wherein the water-soluble monomer is a monolefinic, monocyclic, azacyclic compound.

3. A process according to claim 1 wherein the water-soluble monomer is a hydroxyalkyl ester of acrylic or methacrylic acid in which alkyl is of 2 to 4 carbon atoms.

4. A process according to claim 1 wherein the water-soluble monomer is an acrylic or methacrylic acid ester derived from an alcohol of the formula

HO--C.sub.m H.sub.2m --O--(CH.sub.2 CH.sub.2 O).sub.n --R

where R is hydrogen or methyl, m is 2 to 5 and n is 1 to 20.

5. A process according to claim 1 wherein the water-soluble monomer is an N-substituted amide or imide of acrylic or methacrylic acid in which the N-substituent is hydroxyalkyl, wherein alkyl is of 2 to 4 carbon atoms.

6. A process according to claim 1 wherein the water-soluble monomer is a hydroxyalkyl diester of maleic or fumaric acid, wherein alkyl is of 2 to 4 carbon atoms.

7. A process according to claim 1 wherein the water-soluble monomer is a hydroxyalkyl vinyl ether, where the alkyl is of 2 to 4 carbon atoms.

8. A process according to claim 1 wherein the 0 to 15% by weight of the total monomer is selected from the group consisting of acrylic acid, methacrylic acid, 2-vinyl pyridine, 4-vinylpyridine, 2-(dimethylamino)ethyl methacrylate, N-[2-(dimethylamino)ethyl] methacrylamide and sodium styrene sulfonate.

9. A process according to claim 1 wherein the water-soluble monomer is 2-hydroxyethyl acrylate, 2-hydroxyethyl methacrylate, 2-hydroxypropyl acrylate, 2-hydroxypropyl methacrylate, 3-hydroxypropyl acrylate, 3-hydroxypropyl methacrylate, 2,3-dihydroxypropyl acrylate, 2,3-dihydroxypropyl methacrylate, N-vinyl-2-pyrrolidone or N-methylolacrylamide.

10. A process according to claim 9 wherein the water-soluble monomer is 2-hydroxyethyl methacrylate.

11. A process according to claim 9 wherein the water-soluble monomer is N-vinyl-2-pyrrolidone.

12. A process according to claim 1 wherein the water-insoluble monomer is an alkyl acrylate or methacrylate where alkyl is of 1 to 18 carbon atoms.

13. A process according to claim 1 wherein the water-insoluble monomer is a vinyl ester of a carboxylic acid having 2 to 7 carbon atoms.

14. A process according to claim 1 wherein the water-insoluble monomer is a vinyl alkyl ether, wherein alkyl is of 1 to 5 carbon atoms.

15. A process according to claim 1 wherein the insoluble monomer is acrylonitrile or styrene.

16. A process according to claim 1 wherein R.sub.1 is a poly(ethylene oxide), poly(propylene oxide) or poly(tetramethylene oxide) chain with a molecular weight of about 600 to about 4,000.

17. A process according to claim 1 wherein, R.sub.1 is a chain obtained by the condensation reaction of an aliphatic, alicyclic or aromatic dicarboxylic acid or diisocyanate with an aliphatic diol or diamine.

18. A process according to claim 1 wherein R.sub.1 is a polysiloxane chain of the structure ##STR10## wherein R.sub.8 is a branched or linear alkylene of 1 to 7 carbon atoms or ##STR11## n is 1 to 20, R.sub.9 is hydrogen or methyl, x is 3 to 120 and y is 2 to 3.

19. A process according to claim 1 wherein the macromer is a reaction product of a poly(tetramethylene oxide) glycol with a molecular weight of about 600 to about 4,000, first terminated with tolylene-2,4-diisocyanate or isophorone diisocyanate, and then endcapped with a hydroxyalkyl acrylate or methacrylate, where alkyl is of 2 to 4 carbon atoms.

20. A process according to claim 19 wherein the poly(tetramethylene oxide) glycol has a molecular weight of about 1,500 to about 3,000 and the hydroxyalkyl methacrylate is 2-hydroxyethyl methacrylate.

21. A process according to claim 1 wherein the suspending agent is an insoluble, gelatinous metal hydroxide or metal hydroxide salt selected from the group consisting of the hydroxides or hydroxide salts of magnesium, aluminum, zirconium, iron, nickel, chromium, zinc, lead, calcium, cobalt, copper, tin, gallium, manganese, strontium, barium, uranium, titanium, lanthanum, thorium and cerium.

22. A process according to claim 21 wherein the suspending agent is magnesium hydroxide, aluminum hydroxide, magnesium hydroxy salt or aluminum hydroxy salt.

23. A process according to claim 1 wherein the inorganic salt is dissolved in water at a concentration of about 5 to about 25% by weight.

24. A process according to claim 1 wherein the inorganic salt is selected from the chlorides and sulfates of the alkali and alkaline earth metals.

25. A process according to claim 24 wherein the inorganic salt is sodium chloride or sodium sulfate.

26. A process according to claim 1 wherein from 0.01 to 1% by weight based on monomer of a polymerization catalyst selected from the organic peroxides and azo initiators is used.
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BACKGROUND OF THE INVENTION

This invention pertains to an improved process for the preparation of uniform, spherical beads of up to 5 mm diameter of a crosslinked, water-insoluble hydrogel by suspension polymerization in a concentrated aqueous salt solution of 95-30% by weight of a monoolefinic monomer containing at least 5% of a hydroxy substituted hydrophilic vinyl monomer with 5-70% by weight of a terminal polyolefinic macromer crosslinking agent in the presence of water-insoluble, gelatinous, strong water-bonding inorganic metal hydroxides as suspending agents in the absence of excess alkali. The hydrogels have a host of pharmaceutical and industrial uses. The spherical beads exhibit a degree of swelling in water of from 5 to 200%.

Hydrogels have been described since 1956 (U.S. Pat. No. 2,976,576) and subsequently a large number of patents have been issued describing the synthesis and use of hydrogels based primarily on 2-hydroxyethyl methacrylate and, to a lesser extent, on N-vinylpyrrolidone. Typically, these hydrogels are crosslinked, water-swellable polymers made by copolymerization of 2-hydroxyethyl methacrylate with a small amount of ethylene or butylene dimethacrylate. They are used as polymeric, inert carriers for active substances, which are slowly and controllably released from these carriers; such active substances may be drugs (U.S. Pat. Nos. 3,574,826; 3,577,512; 3,551,556; 3,520,949; 3,576,760; 3,641,237; 3,660,563); agricultural chemicals (U.S. Pat. No. 3,576,760); or fragrances (U.S. Pat. Nos. 3,567,118; 3,697,643).

Their uses as antifogging coatings (U.S. Pat. No. 3,488,215), body implants and bandages have also been described in U.S. Pat. Nos. 3,577,516; 3,695,921, 3,512,183; 3,674,901. The widely used soft contact lens consists of this material (U.S. Pat. Nos. 3,488,111; 3,660,545).

In the pharmaceutical field the main interest lies in the slow and controllable release of drugs from such hydrogels. Drug-containing hydrogel preparations have been described as being in the form of bandages; subcutaneous implants; buccal devices, intrauterine devices, eye inserts. They are made by complicated fabrication procedures which usually involves casting the monomer solution into a suitable mold and polymerizing in the presence of a free radical generating initiator.

The use of drug loaded hydrogel granules as an oral dose form has also been suggested (U.S. Pat. No. 3,551,556). It is indeed one of the most useful applications of this concept in medicine since it allows the delivery into the bloodstream of an orally taken drug to be spread out over several hours in a reproducible manner. This eliminates wasteful and potentially dangerous peak drug concentrations in the blood, while prolonging the time during which preferred and effective drug levels in the blood are maintained.

There are two methods, by which hydrogel granules can be prepared. (1) One method consists of dicing or granulating a hydrogel sheet cast in the conventional manner and screening out the proper particle size. This method has several disadvantages: (a) It involves time consuming bulk polymerization of large amounts of materials in the form of relatively thin sheets; (b) the final product consists of jagged, rough particles with large surface area and sharp edges which are not only objectional from the aesthetic standpoint, but also are ill-suited for the controlled release of a drug, which depends on a uniform diffusion rate and therefore on uniform particles with well-defined surface and volume.

(2) The second method of making hydrogel granules, and by far the superior one, is suspension polymerization. Suspension polymerization consists of suspending a liquid monomer phase in a nonsolvent medium by stirring and with the aid of a protective colloid as a stabilizer, and polymerizing the stirred suspension by conventional means. Polymerization is heat induced or catalyzed by decomposition of a free radical chemical initiator. This method yield uniformly spherical beads in a one-step process and is widely used in the production of polystyrene, poly(vinyl chloride) and polyacryaltes, and poly(vinyl acetate). A good summary of the present state of the art is given by E. Farber in the Encyclopedia of Polymer Science and Technology, Vol. 13, pp 552-571, (1970), Interscience, N.Y. The relevant teachings therein are incorporated herein by reference. In case of water-soluble monomers used in the production of hydrogels, such as 2-hydroxyethyl methacrylate and N-vinylpyrrolidone, the nonsolvent medium is usually an organic liquid or an aqueous salt solution.

In U.S. Pat. No. 3,390,050 suspension polymerization of water-soluble monomers in the presence of large amounts of active ingredients is described. This process is, however, not suitable for the preparation of hydrogel beads for an orally administered drug since it is impossible to purify the polymer without leaching out the drug.

Most references to suspension polymerization of a 2-hydroxyethyl methacrylate refer to silicone oil or organic media such as mineral oil or xylene as the insoluble suspending phase (U.S. Pat. Nos. 3,567,118; 3,574,826; 3,575,123; 3,577,518; 3,583,957). These processes give generally particles with very irregular, imperfect and porous surfaces, unsuited for uses where diffusion rather than adsorption and desorption is the working mechanism. Besides these factors, the workup of the polymer on a technical scale would pose a problem.

Suspension polymerization of 2-hydroxyethyl methacrylate (HEMA) in the presence of 0.5 to 2% of shortchain cross-linking agents (a composition conventionally named "Hydron") and using an aqueous salt solution as medium has been described in U.S. Pat. No. 3,689,634, but there is no mention of a suspending agent as being a necessary ingredient of the recipe. However, it can be demonstrated that without such a suspending agent no useful particles or beads are obtained, only large agglomerations of polymer.

It is, however, well-known in the prior art that certain water-soluble polymers, such as polyvinylpyrrolidone and hydroxyethyl cellulose are excellent suspending agents for suspension polymerization. It is also known that certain highly insoluble inorganic compounds such as calcium sulfate, barium sulfate, calcium phosphate, magnesium phosphate, calcium carbonate and magnesium hydroxide are also useful.

The use of magnesium hydroxide as the suspension stabilizer in the suspension polymerization of vinyl monomers is disclosed in U.S. Pat. No. 2,801,992, but with the explicit teaching that excess alkali or free hydroxyl ions must be present. The magnesium hydroxide in the absence of excess alkali is ineffective as a suspension stabilizer. Indeed, even a stoichiometric amount of alkali to form magnesium hydroxide is insufficient to produce an effective stabilizer.

While the presence of excess alkali and free hydroxyl ions (high pH values) would cause no deleterious side effects with some suspension polymerization systems, there are many vinyl monomers, such as the acrylic esters, vinyl acetate and the like, which could undergo undesired base catalyzed hydrolysis in such systems at high pH values. It is certainly preferred to polymerize such vinyl monomers under essentially neutral conditions not within the purview of the teachings of U.S. Pat. No. 2,801,992.

It was found when water-soluble polymers were used as suspending agents that the hydrogel granules were of irregular shape and with very porous surfaces. If uniform beads were formed, they were of such small size (e.g., <0.3 mm diameter) as to be of no practical value for the slow release of active ingredients. The same was true for the inorganic suspending agents, except that even more agglomeration occurred. Of all inorganic compounds only the insoluble gelatinous metal hydroxides gave smooth beads. In the case of poly(2-hydroxyethyl methacrylate) or "Hydron" these beads were of unusable small sizes and not uniformly spherical. But in the presence of macromeric crosslinking agents as described in this invention, regular, uniformly smooth spherical beads of up to 5 mm diameter could be obtained.

In the course of these investigations it was now unexpectedly discovered that it is the simultaneous presence of at least 5% by weight of 2-hydroxyethyl methacrylate (HEMA) or another hydroxy substituted vinyl monomer and at least 5% by weight of a polyolefinic macromeric crosslinking agent in the polymerizing mixture, and insoluble gelatinous metal hydroxides in the absence of excess alkali or free hydroxyl ions in the suspending aqueous medium which allows the manufacture of uniform sperical beads with up to 5 mm diameter. The suspending medium is an aqueous salt solution dissolving HEMA to not over 10%. The particle size is easily controlled by stirring, slow stirring speeds resulting in large beads and higher speeds in small beads.

Although the instant process can be modified to make small beads (<0.3 mm) by high speed stirring, no other known process is known to make uniform beads of over 0.3 mm other than the present invention. The preferred bead size for the controlled delivery of oral medications is from 0.6 mm to about 1.5 mm.

Some of the hydrogel compositions of this invention are the subject of U.S. Pat. No. 4,192,827.

SUMMARY AND OBJECT OF THE INVENTION

It is an object of the present invention to provide an improved process for the preparation of uniform, spherical hydrogel beads of up to 5 mm diameter having a host of pharmaceutical and industrial uses.

It is a further objective of the present invention to provide uniform, spherical hydrogel beads comprising a crosslinked polymer prepared by suspension polymerization in an aqueous salt solution of 95 to 30% by weight of a hydrophilic monomer (A) which consists of 5-100% of a hydroxy substituted vinyl monomer; and 5 to 70% by weight of a terminally substituted polyolefinic macromer crosslinking agent (B) in the presence of a suspending agent selected from the water-insoluble, gelatinous, strongly water-bonding, inorganic metal hydroxides and metal hydroxy salts in the absence of excess alkali.

The instant process involves the combined use of the particular gelatinous inorganic hydroxides, the monomer crosslinking compound and hydroxy substituted monomer in order to produce the uniform sperical hydrogel beads with up to 5 mm diameter. Each of the three ingredients was found, unexpectedly, to be necessary for the preparation of up to 5 mm large beads.

DETAILED DESCRIPTION

The instant invention pertains to an improved process for preparing essentially uniform sperical beads of up to 5 mm diameter of a crosslinked, water-insoluble hydrogel by suspension polymerization of (A) 95 to 30% by weight of the hydrogel of a water-soluble monoolefinic monomer or mixture of said water-soluble monomers, and from 0-70 by weight based on the total monomer of a water-insoluble monoolefinic monomer or mixture of said water-insoluble monomers, with the proviso that the final hydrogel does not contain over 60% by weight of said water-insoluble monomer components, with (B) 5 to 70% by weight of the hydrogel of a polyolefinic crosslinking agent, with a polymerization initiator in a concentrated aqueous inorganic salt solution wherein the improvement comprises

carrying out the suspension polymerization with monoolefinic monomers containing at least 5% by weight of the total monomers of a hydroxy substituted hydrophilic vinyl monomer;

employing as the crosslinking agent a polyolefinic macromer having a molecular weight from about 400 to about 8,000, and

utilizing from 0.01 to 5% by weight, based on the hydrogel, of a suspending agent selected from the water-insoluble, gelatinous strongly water-bonding, inorganic metal hydroxides and metal hydroxy salts in the absence of excess alkali or free hydroxy ions.

The hydrophilic portion of the hydrogel composition is prepared by the polymerization of a water-soluble monoolefinic monomer or a mixture of said monomers containing at least 5% of a hydroxy substituted vinyl monomer and which can contain from 0 to 70%, and preferably at most 50%, by weight of the total amount of the monomers, of a water-insoluble monoolefinic monomer or mixture of said water-insoluble monomers.

The process employs as water-soluble, hydroxy substituted monomers water-soluble derivatives of acrylic and/or methacrylic acid, such as hydroxyalkyl esters where alkyl is of 2 to 4 carbon atoms, e.g., 2-hydroxyethyl, 3-hydroxypropyl, 2-hydroxypropyl or 2,3-dihydroxypropyl esters.

Still another group of water soluble hydroxy substituted esters of acrylic or methacrylic acid are the ethoxylated and poly-ethoxylated hydroxyalkyl esters, such as esters of alcohols of the formula

HO--C.sub.m H.sub.2m --O--(CH.sub.2 CH.sub.2 --O).sub.n --H

where

m represents 2 to 5 and

n represents 1 to 20

or esters of analogous alcohols, wherein a part of the ethylene oxide units is replaced by propylene oxide units. Further suitable esters are 3-(dimethylamino)-2-hydroxypropyl esters.

Another class of suitable derivatives of acrylic or methacrylic acid are their water-soluble amides or imides substituted by lower hydroxyalkyl groups where alkyl is of 2 to 4 carbon atoms such as N-(hydroxymethyl)-acrylamide and -methacrylamide, N-3-(hydroxypropyl)-acrylamide, N-(2-hydroxymethyl)-methacrylamide and N-[1,1-dimethyl-2-(hydroxymethyl)-3-oxabutyl]-acrylamide; water-soluble hydrazine derivatives, such as dimethyl-(2-hydroxypropyl)amine methacrylimide and the corresponding derivatives of acrylic acid.

Also useful, in combination with comonomers, are for instance, the hydroxyalkyl esters of maleic and fumaric acids with alkyl of 2 to 4 carbon atoms, such as di-(2-hydroxyethyl) maleate, and ethoxylated hydroxyalkyl maleates, hydroxyalkyl monomaleates, such as 2-hydroxyethyl monomaleate and alkoxylated hydroxyalkyl monomaleate with vinyl ethers, vinyl esters, styrene or generally any monomer which will easily copolymerize with maleates or fumarates.

Still other preferred water-soluble monomers are hydroxyalkyl vinyl ethers with alkyls of 2 to 4 carbon atoms, such as 2-hydroxyethyl vinyl ether, 4-hydroxybutyl vinyl ether, in combination with maleates, fumarates, or generally all monomers which will easily copolymerize with vinyl ethers.

Especially valuable as hydroxy-substituted, water-soluble monomers are hydroxyalkyl acrylates and methacrylates, such as 2-hydroxyethyl acrylate, 2-hydroxyethyl methacrylate, 2-hydroxypropyl acrylate, 3-hydroxypropyl methacrylate and 2,3-dihydroxypropyl methacrylate. Especially preferred hydroxy substituted vinyl monomers are 2-hydroxyethyl methacrylate and 2- or 3-hydroxypropyl methacrylate.

Most preferred is 2-hydroxyethyl methacrylate.

Water-soluble comonomers, which do not contain hydroxy groups are: acrylic and methacrylic acid and alkyl ethers of polyethoxylated hydroxy alkyl esters thereof, such as esters of alcohols of the formula

HO--C.sub.m H.sub.2m O--(CH.sub.2 CH.sub.2 --O).sub.n CH.sub.3,

where

m=2 to 5 and

n=4 to 20

Dialkyl amino alkyl esters and amides, such as 2-(dimethylamino)ethyl,- or 2-(diethylamino)ethyl acrylate and methacrylate, as well as the corresponding amides; amides substituted by lower oxa-alkyl or lower dialkylamino alkyl groups, such as N-(1,1-dimethyl-3-oxa-butyl) acrylamide; water-soluble hydrazine derivatives, such as trialkylamine methacrylamide, e.g., triethylamine-methacrylimide and the corresponding derivatives of acrylic acid. Monoolefinic sulfonic acids and their salts, such as sodium ethylene sulfonate, sodium styrene sulfonate and 2-acrylamido-2-methylpropanesulfonic acid; N-[2-(dimethylamino)-ethyl]-acrylamide and -methacrylamide, N-[3-(dimethylamino)-2-hydroxypropyl]-methacrylamide.

Still another class of water-soluble monomers are the monoolefinic, monocyclic, azacyclic compounds such as N-vinylpyrrole, N-vinylsuccinimide, N-vinyl-2-pyrrolidone, 1-vinylimidazole, 1-vinylindole, 2-vinylimidazole, 4(5)-vinylimodazole, 2-vinyl-1-methylimidazole, 5-vinylpyrazoline, 3-methyl-5-isopropenylpyrazole, 5-methylenehydantoin, 3-vinyl-2-oxazolidone, 3-methacrylyl-2-oxazolidone, 3-methacrylyl-5-methyl-2-oxazolidone, 3-vinyl-5-methyl-2-oxazolidone, 2- and 4-vinylpyridine, 5-vinyl-2-methylpyridine, 2-vinyl-pyridine-1-oxide, 3-isopropenylpyridine, 2- and 4-vinylpiperidine, 2- and 4-vinylquinoline, 2,4-dimethyl-6-vinyl-s-triazine and 4-acrylylmorpholine.

The preferred monomer is N-vinyl-2-pyrrolidone.

Preferred among these monomers which can be used at a level of from 0 to about 15% by weight of the total monomers are acrylic acid, methacrylic acid, 2-vinyl pyridine, 4-vinylpyridine, 2-(dimethylamino)ethyl methacrylate, N-[2-dimethylamino)ethyl] methacrylamide and sodium styrene sulfonate.

Preferred water-soluble monomers are 2-hydroxyethyl acrylate, 2-hydroxyethyl methacrylate, 2-hydroxypropyl acrylate, 2-hydroxypropyl methacrylate, 3-hydroxypropyl acrylate, 3-hydroxypropyl methacrylate, 2,3-dihydroxypropyl acrylate, 2,3-dihydroxypropyl mathacrylate, N-vinyl-2-pyrrolidone and N-methylolacrylamide. It is noted that, when N-vinyl-2-pyrrolidone or any other non-hydroxy bearing water-soluble monomer is used, a second monomer containing hydroxyl groups must also be used concomitantly in the instant process.

Suitable hydrophobic comonomers, which may be incorporated into the reaction mixture, are for example, water-insoluble olefinic monomers, such as alkyl acrylates or methacrylates in which alkyl has 1 to 18 carbon atoms, e.g., methyl and ethyl methacrylate or acrylate; vinyl esters derived from alkane-carboxylic acids having 2 to 7 carbon atoms, e.g., vinyl acetate and vinyl propionate, or vinyl benzoate; acrylonitrile; styrene; and vinyl alkyl ethers in which the alkyl portion of the ether chain has 1 to 5 carbon atoms, e.g., methyl, ethyl, propyl, butyl or amyl vinyl ether.

Preferred embodiments are the alkyl acrylates or metacrylates where alkyl is 1 to 18 carbon atoms.

Other preferred embodiments are the vinyl alkyl ethers wherein alkyl is from 1 to 5 carbon atoms.

Still other preferred water-insoluble monomers are acrylonitrile and styrene.

The terminal polyolefinic macromer crosslinking agent (B) olefinic moieties are preferably provided by acyl groups of lower .alpha.,.beta.-mono-unsaturated aliphatic monocarboxylic or dicarboxylic acids or by vinyloxy moieties. These vinyl moieties are linked by a macromolecular chain containing repeating ester, amide or urethane, but particularly ether linkages. The molecular weight of the chain may vary from about 400 to about 8,000, preferable between about 600 and 5,000 and, especially, between about 1,500 and 3,000. Thus, the macromer preferably corresponds to the formula ##STR1## wherein a is 1 or 2; R.sub.1 is a polycondensate chain having a molecular weight from about 200 to about 8,000 which contains hydrocarbon residues connected via ether, ester, amide or urea linkages or is a polysiloxane of molecular weight between 400 and 8,000; R.sub.2 is hydrogen, methyl or --CH.sub.2 COOR.sub.4 ;

R.sub.4 is hydrogen or alkyl of 1 to 10 carbon atoms; R.sub.3 is hydrogen or --COOR.sub.4 with the proviso that at least one of R.sub.2 and R.sub.3 is hydrogen; X is an oxygen atom, --COO-- or --CONR.sub.5 --;

R.sub.5 is hydrogen or alkyl of 1 to 5 carbon atoms; Y is a direct bond or the radical --R.sub.6 --Z.sub.1 --CONH--R.sub.7 --NHCO--Z.sub.2 ;

R.sub.6 is linked to X and represents branched or linear alkylene of 1 to 7 carbon atoms; Z.sub.1 is an oxygen atom or --NR.sub.5 --; Z.sub.2 is Z.sub.1 or a sulfur atom; and R.sub.7 is the diradical of an aliphatic, alicyclic or aromatic diisocyanate with the proviso that in case X is oxygen, Y is different from a direct bond and R.sub.2 and R.sub.3 are hydrogen.

Preferably a is 1.

In the compounds of formula B.sub.1 and B.sub.2, R.sub.1 is in particular a polyethylene oxide chain, a polypropylene oxide chain or a polytetramethylene oxide chain, or a chain consisting of a polyethylene oxide-polypropylene oxide block copolymer, but it can also represent a chain derived from dicarboxylic acids, diols, diamines or diisocyanates etc., by well known methods of poly-condensation. R.sub.1 can also be a polysiloxane containing chain. The terminal radicals of the compounds of formula B.sub.1 are according to the definitions of R.sub.2 and R.sub.3 and if X represents --COO-- or CONR.sub.5 --, the acyl radicals of acrylic or methacrylic acid or the monoacyl radicals of maleic, fumaric or itaconic acid, or of monoalkyl esters of these acids with straight or branched chain alkanols of 1 to 10 carbon atoms, such as methanol, ethanol, butanol, diisobutyl alcohol or decanol, or if X represents oxygen, the vinyloxy radical of vinyl ethers. Compounds of the formula B.sub.1 with Y being a direct bond are diesters of macromolecular diols, wherein two hydroxy groups are attached to the polycondensate chain R.sub.1 in opposite terminal or almost terminal positions, with .alpha.,.beta.-unsaturated acids. Such diesters can be prepared from said macromolecular diol by well-known acylation methods using reactive functional derivatives or suitable acids, e.g., acid chlorides of acrylic or methacrylic acid, or of monoalkyl esters of maleic, fumaric or itaconic acid, or the anhydride of maleic or itaconic acid. Compounds of formula B.sub.1 with amide group X are diamides obtained from macromolecular diamines by well-known acylation reactions using, e.g., the acid chlorides or anhydrides mentioned above. The macromolecular diamines are prepared, e.g., by reacting corresponding macromolecular diols with twice the molar amount of an alkylenimine, e.g., propylenimine.

The macromolecular bis-maleamic acids obtained by the above reaction when maleic acid anhydride is used as the acylating agent for macromolecular diamines can be further heated or reacted with dehydrating agents to yield the macromolecular bis maleimido compounds of formula B.sub.2. In these compounds, R.sub.1 thus may be, e.g., one of the macromolecular polycondensate chains named as moieties of compounds of the formula B.sub.1.

According to the definition of formula B.sub.1, y can further be a divalent radical --R.sub.6 --Z.sub.1 --CONH--R.sub.7 --NH--CO--Z.sub.1 --. Therein R.sub.6 is, e.g., methylene, propylene, trimethylene, tetramethylene, pentamethylene, neopentylene (2,2-dimethyltrimethylene), 2-hydroxytrimethylene, 1,1-dimethyl-2-(1-oxo-ethyl)trimethylene or 1-(di-methylaminomethyl)ethylene and particular ethylene. The divalent radical R.sub.7 is derived from an organic diisocyanate and is an aliphatic radical such as alkylene, e.g., ethylene, tetramethylene, hexamethylene, 2,2,4-trimethylhexamethylene, 2,4,4-trimethylhexamethylene; fumaroyldiethylene or 1-carboxypentamethylene; a cycloaliphatic radical, e.g., 1,4-cyclohexylene or 2-methyl-1,4-cyclohexylene; and aromatic radical, such as m-phenylene, p-phenylene, 2-methyl-m-phenylene, 1,2-, 1,3-, 1,5-, 1,6-, 1,7-, 1,8-, 2,3- and 2,7-naphthylene, 4-chloro-1,2- and 4-chloro-1,8-naphthylene, 1-methyl-2,4-, 1-methyl-2,7-, 4-methyl-1,2-, 6-methyl-1,3-, and 7-methyl-1,3-naphthylene, 1,8-dinitro-2,7-naphthylene, 4,4'-biphenylene, 3,3'-dichloro-4,4' -biphenylene, 3,3'-dimethoxy-4,4'-biphenylylene, 2,2'-dimethyl- and 3,3'-dimethyl-4,4'-biphenylylene, 2,2'-dichloro-5,5'-dimethoxy-4,4'-biphenylene, methylenedi-p-phenylene, methylenebis-(3-chlorophenylene), ethylenedi-p-phenylene or oxydi-p-phenylene. If in structure B.sub.1, Y is no direct bond, R.sub.6 is always connected to X.

Thus, compounds of the formula B.sub.1, in which Y is said divalent radical, are, if X represents oxygen, bis-vinyl ethers or, if X represents --COO-- or ##STR2## bis-acrylates, bis-methacrylates, bis-maleates, bis fumarates and bis-itaconates.

R.sub.1 is in particular derived from macromeric diols and diamines of 200 to 8000 molecular weight (MW).

Useful macromeric diols are polyethylene oxide diols of 500 to 3000 MW, polypropylene oxide diols of 500 to 300 MW, poly-n-butylene oxide diols of 500 to 3000 MW; poly(-block-ethylene oxide-co-propylene oxide) diols of 500 to 3000 MW, wherein the percentage of ethylene oxide units can vary from 10 to 90%; polyester diols of 500 to 3000 MW obtained by the known methods of polycondensation from diols and diacids, for instance, from propylene glycol, ethylene glycol, butanediol or 3-thia-pentane diol and adipic acid, terephthalic acid, phthalic acid or maleic acid, and which may also contain macromeric diols of the polyether type mentioned above.

More generally, any diol of MW 500 to 3000 is useful, which can be obtained by polycondensation of diols, diamines, diisocyanates, or diacids and thus contain ester, urea, urethane or amide linkage groups.

Similarly useful are diamines of 500 to 4000 MW, especially the bis-aminopropyl ethers of the above-mentioned diols, especially the bis-3-aminopropyl ethers of polyethylene oxide and polypropylene oxide diols.

A preferred embodiment of the instant process employs a macromer (B) wherein R.sub.1 is a poly(ethylene oxide), poly(propylene oxide) or poly(tetramethylene oxide) chain with a molecular weight of about 600 to about 4,000.

Another preferred embodiment of the process employs a macromer (B) wherein R.sub.1 is a chain obtained by the condensation reaction of an aliphatic, alicyclic or aromatic dicarboxylic acid or diisocyanate with an aliphatic diol or diamine.

A particularly preferred embodiment of the instant process uses as the macromer (B) a reaction product of a polyalkylene ether glycol, particularly poly(tetramethylene oxide) glycol with a molecular weight of about 600 to about 4,000, first terminated with tolylene-2,4-diisocyanate or isophorone diisocyanate, and then endcapped with a hydroxyalkyl acrylate or methacrylate where alkyl is of 2 to 4 carbon atoms.

Especially useful are the macromers (B) where the poly(tetramethylene oxide) glycol has a molecular weight of about 1,500 to about 3,000 and the hydroxyalkyl methacrylate is 2-hydroxyethyl methacrylate.

Other preferred macromers (B.sub.1) are those wherein R.sub.1 can also be derived from a polysiloxane containing diol, triol, or dithiol, with a molecular weight of 400 to 8,000. These di- or polyfunctional polysiloxanes can be of two different structures: ##STR3## wherein R.sub.8 is a branched or linear alkylene of 1 to 7 carbon atoms or ##STR4## n is 1 to 20, R.sub.9 is hydrogen or methyl, x is 3 to 120 and y is 2 to 3.

These polysiloxane macromers are preferably endcapped with isophorone diisocyanate or tolylene-2,4-diisocyanate followed by reaction with excess 2-hydroxyethyl methacrylate, 2-hydroxyethyl acrylate or 2-hydroxypropyl acrylate and are described in greater detail in U.S. Pat. No. 4,136,250.

Compounds of the formula B.sub.1, wherein Y is --R.sub.6 Z.sub.1 CONHR.sub.7 --NH--CO--Z.sub.2 -- are obtained in a 2-step reaction by first reacting macromolecular diols or diamines, i.e., compounds which contain two hydroxy or amino groups attached to the polycondensate chain, R.sub.1, in opposite terminal or almost terminal positions, with at least twice the molar amount of an aliphatic, cycloaliphatic or aromatic diisocyanate consisting of two isocyanate groups attached to the radical R.sub.7, and, second, reacting the macromolecular diisocyanates so obtained with a compound of the formula ##STR5## wherein R.sub.2, R.sub.3, X, R.sub.6 and Z.sub.1 have the meaning defined for (B.sub.1) above.

If X represents oxygen, (C) is vinyl ether containing the active hydrogen, for instance an hydroxyalkyl vinyl ether or an aminoalkyl vinyl ether; if X represents --COO-- or ##STR6## (C) is an acrylate, methacrylate, maleate, fumarate, itaconate or the corresponding amide, containing an active hydrogen in the alkyl group. The macromolecular diol or diamine is preferably used in a small excess, i.e., the ratio of isocyano groups to hydroxy or amino groups during the first step of the macromer synthesis should be at least 1:1, but is preferably at least 1:1.05. If the compound of formula C used during the second step of the macromer synthesis, is identical with the hydrophilic monomer comprising (A), then a large excess of this compound can be used, so that the resulting solution of macromer B.sub.1 dissolved or dispersed in Compound C can be used directly for the preparation of the final hydrogel.

The synthesis of the macromer, B, is suitably carried out at a temperature in the range of from about room temperature to approximately 100.degree. C. Preferably, the temperature employed is within the range of about 30.degree.-60.degree. C. The conversion of the isocyanato group is followed by infrared spectroscopy or by titration.

Preferred diisocyanates for preparing the macromer are tolylene-2,4-diisocyanate and isophorone diisocyanate.

Poly(tetramethylene oxide) glycol chain terminated with tolylene-2,4-diisocyanate is commercially available as "Adiprene" from DuPont.

Tolylene-2,4-diisocyanate and isophorone diisocyanate are available commercially.

Another method for preparing the macromer is by reacting a hydroxyl-terminated prepolymer, e.g., polybutylene or polypropylene oxide, with acryloyl chloride, methacryloyl chloride or maleic anhydride and thus forming a macromer without connecting urethane linkages as, for example, a macromer of the formula B.sub