Blends of absorbable polyoxaesters containing amines and/or amido groups

The present invention relates to polyoxaesters containing amines and/or amido groups and blends thereof with other polymers and more particularly to surgical products made from polyoxeasters containing amines and/or amido groups and blends thereof with other polymers.

Background of the Invention

Since Carothers early work in the 1920s and 1930s, aromatic polyester particularly poly(ethylene terephthalate) have become the most commercial important polyesters. The usefulness of these polymers is intimately linked to the stiffening action of the p-phenylene group in the polymer chain. The presence of the p-phenylene group in the backbone of the polymer chain leads to high melting points and good mechanical properties especially for fibers, films and some molded products. In fact poly(ethylene terephthalate) has become the polymer of choice for many common consumer products, such as one and two liter soft drink containers.

Several related polyester resins have been described in U.S. Patents 4,440,922, 4,552,948 and 4,963,641 which seek to improve upon the properties of poly(ethylene terephthalate) by replacing terephthalic acid with other related dicarboxylic acids which contain phenylene groups. These polymers are generally designed to reduce the gas permeability of aromatic polyesters.

Other aromatic polyesters have also been developed for specialty- applications such as radiation stable bioabsorbable materials. U.S. Patents 4,510,295, 4,546,152 and 4,689,424 describe radiation sterilizable aromatic polyesters which can be used to make sutures and the like. These polymers like, poly(ethylene terephthalate), have phenylene groups in the backbone of the polymers.

However, less research has been reported on aliphatic polyesters. After Carothers initial work on polyesters, aliphatic polyesters were generally ignored because it was believed that these materials had low melting points and high solubilities. The only aliphatic polyesters that have been extensively studied are polylactones such as polylactide, polyglycolide, poly(p-dioxanone) and polycaprolactone. These aliphatic polylactones have been used primarily for bioabsorbable surgical sutures and surgical devices such as staples. Although polylactones have proven to be useful in many applications they do not meet all the needs of the medical community. For example films of polylactones do not readily transmit water vapor, therefore, are not ideally suited for use as bandages where the transmission of water vapor would be desired.

Only recently has there been renewed interest in non-lactone aliphatic polyesters. U.S. Patent 5,349,028 describes the formation of very simple aliphatic polyesters based on the reaction of a diol with a dicarboxylic acid to from a prepolymer chains that is then coupled together. These polyesters are being promoted for use in fibers and molded articles because these polyesters are biodegradable after they are buried such as in a landfill. However, these materials are not disclosed as being suitable for use in surgical devices.

Thus it is an object of the present invention to provide a new class of aliphatic polyesters and blends thereof that may be used in surgical devices such as sutures, molded devices, drug delivery matrices, coatings, lubricants and the like.

Summary of the Invention

We have discovered a new class of synthetic polymeric materials and blends thereof that may be used to produce surgical devices such as sutures, sutures with attached needles, molded devices, drug delivery matrices, coatings, lubricants and the like. The invention also contemplates a process for producing the polymers and blends thereof. The aliphatic polyoxaesters of the present invention is a polyester comprising a first divalent repeating unit of formula I:         [O-C(O)-C(R₁)(R₂)-O-(R₃)-O-C(R₁)(R₂)-C(O)-]     I and a second repeating unit selected from the group of formulas consisting of:         [-O-R₁₂-]_U,     XIV and optionally a third repeating unit with a formula selected from the group consisting of:         [-O-R₄-]_A,     II         [-O-R₅-C(O)-]_B,     III         ([-O-R₁₃-C(O)]_P-O-)_LG     XI and combinations thereof, wherein R₁ and R₂ are independently hydrogen or an alkyl group containing 1 to 8 carbon atoms; R₃ is an alkylene unit containing from 2 to 12 carbon atoms or is an oxyalkylene group of the following formula:         -[(CH₂)_C-O-]_D-(CH₂)_E-     IV wherein C is an integer in the range of from 2 to about 5, D is an integer in the range of from about 0 to about 2,000, and E is an integer in the range of from about 2 to about 5, except when D is zero in which case E will be an integer from 2 to 12; R₁₂ is an alkylene unit containing from 2 to 8 carbon atoms and containing an internal amine (-N(R₁₀)-) or amide (-N(R₁₁,)-); R₁₀ and R₁₁ are independently hydrogen or an alkyl group containing 1 to 8 carbon atoms; A and U are independently integers in the range of from 1 to about 2,000 and preferably are indepently in the range of from 1 to about 1,000; R₁₂ is an alkylene unit containing from 2 to 8 carbon atoms; R₅ and R₁₃ are independently selected from the group consisting of-C(R₆) (R₇)-, -(CH₂)₃-O-, -CH₂-CH₂-O-CH₂-, -CR₈H-CH₂-, -(CH₂)₄-, -(CH₂)_F-O-C (O) - and -(CH₂)_k-C(O) -CH₂-; R₆ and R₇ are independently hydrogen or an alkyl containing from 1 to 8 carbon atoms; R₈ is hydrogen or methyl; F and K are integers in the range of from 2 to 6; B is an integer in the range of from 1 to n such that the number average molecular weight of formula III is less than about 200,000; P is an integer in the range of from 1 to m such that the molecular weight of formula XI is less than about 1,000,000; G represents the residue minus from 1 to L hydrogen atoms from the hydroxyl group of an alcohol previously containing from 1 to about 200 hydroxyl groups; and L is an integer from about 1 to about 200.

Detailed Description of the Invention

The aliphatic polyoxaesters of the present invention are the reaction product of an aliphatic polyoxycarboxylic acid and at least one of the following compounds: a diol (or polydiol), a lactone (or lactone oligomer), a coupling agent or combination thereof.

Suitable aliphatic alpha-oxycarboxylic acids for use in the present invention generally have the following formula:         HO-C(O)-C(R₁)(R₂)-O-(R₃)-O-C(R₁) (R₂)-C(O)-OH     V wherein R₁ and R₂ are independently selected from the group consisting of hydrogen or an alkyl group containing from 1 to 8 carbon atoms and R₃ is an alkylene containing from 2 to 12 carbon atoms or is an oxyalkylene group of the following formula:         -[(CH₂)_C-O-]_D-(CH₂)_E-     IV wherein C is an integer in the range of from about 2 to about 5, D is an integer in the range of from about 0 to about 2,000 and preferably from about 0 to about 12, and E is an integer in the range of from about 2 to about 5. These aliphatic alpha-oxycarboxylic acids may be formed by reacting diol or polydiol containing an internal amine or internal amide with an alpha-halocarboxylic acid such bromoacetic acid or chloroacetic acid under suitable conditions.

Suitable amine and amide containing diols or polydiols for use in the present invention are diol or diol repeating units with up to 8 carbon atoms having the formula:         H[-(O-R₁₂-)_U]OH,     XIV wherein R₁₂ is an alkylene unit containing from 2 to 8 methylene units and containing an internal amine (-N(R₁₀)-) or amide (-N(R₁₁)-); R₁₀ and R are independently hydrogen or an alkyl group containing 1 to 8 carbon atoms; U is an integer in the range of from 1 to about 2,000 and preferably from 1 to 1,000. Examples of suitable amine and amide containing diols include diethanol amine and 2-hydroxyl-N-(2-hydroxyethyl) acetamide. The polyoxaester may additionally contain diols or polydiols for use in the present invention are diol or diol repeating units with up to 8 carbon atoms having the formulas:         H[-(O-R₄-)_A]OH,     VI wherein R₄ is an alkylene unit containing from 2 to 8 methylene units; A is an integer in the range of from 1 to about 2,000 and preferably from 1 to about 1,000. Examples of suitable diols include diols selected from the group consisting of 1,2-ethanediol (ethylene glycol), 1,2-propanediol (propylene glycol), 1,3-propanediol, 1,4-butanediol, 1,5-pentanediol, 1, 3-cyclopentanediol, 1,6-hexanediol, 1,4-cyclohexanediol, 1,8-octanediol and combinations thereof. Examples of preferred polydiols include polydiols selected from the group consisting of polyethylene glycol (H[-O-CH₂-CH₂-]_AOH) and polypropylene glycol (H[-O-CH₂-CH(CH₃)-]_AOH).

The polymer produced by reacting the aliphatic dioxycarboxylic acid with the diols discussed above should provide a polymer generally having the formula:         [-O-C(O)-C(R₁)(R₂)-O-(R₃)-O-C(R₁)(R₂)-C(O)-(O-R₁₂)_U-]_N     VII wherein R₁, R₂, R₃, R₁₂ and U are as described above; and N is an integer in the range of from about 1 to about 10,000 and preferably is in the range of from about 10 to about 1,000 and most preferably in the range of from about 50 to about 200.

Suitable lactone monomers that may be used in the present invention generally have the formula: <chemistry id="chem0001" num="0001"><img file="EP0771832A2_D0001.tif" /></chemistry> These lactone monomers (or equivalent acids, if any) may be polymerized to provide polymers of the following general structures:         H[-O-R₅-C(O)-]_BOH     IX         (H[-O-R₁₃-C(O)]_P-O-)_LG     X wherein R₅ and R₁₃ are independently selected from the group consisting of -C(R₆) (R₇)-, -(CH₂)₃-O-, -CH₂-CH₂-O-CH₂-, -CR₈H-CH₂-, - (CH₂)₄-, -(CH₂)_F-O-C(O) - and -(CH₂)_κ-C(O)-CH₂-;R₆ and R₇ are independently hydrogen or an alkyl containing from 1 to 8 carbon atoms; R₈ is hydrogen or methyl; F and K are integers of from 2 to 6; B is an integer in the range of from 1 to n such that the number average molecular weight of formula IX is less than about 200,000, preferably is less than about 100,000, more preferably less than about 40,000 and most preferably less than 20,000. P is an integer in the range of from 1 to m such that the number average molecular weight of formula X is less than about 1,000,000, preferably less than 200,000, more preferably less than 40,000 and most preferably is less than 20,000; G represents the residue minus from 1 to L hydrogen atoms from the hydroxyl groups of an alcohol previously containing from 1 to about 200 hydroxyl groups; and L is an integer from 1 to about 200. Preferably G will be the residue of a dihydroxy alcohol minus both hydroxyl groups. Suitable lactone-derived repeating units may be generated from the following monomers include but are not limited to lactone monomers selected from the group consisting of glycolide, d-lactide, 1-lactide, meso-lactide, ε-caprolactone, p-dioxanone, trimethylene carbonate, 1,4-dioxepan-2-one, 1,5-dioxepan-2-one and combinations thereof.

The polymer formed by reacting the above described amine and amide containing diols (or polydiol) XIV and the aliphatic polyoxycarboxylic acid V may also be copolymerized in a condensation polymerization with the lactone polymers IX and X described above to form a polymer generally of the formula:         [(-C(O)-C(R₁)(R₂)-O-R₃-O-C(R₁)(R₂)-C(O)-(O-R₁₂)_U-O)_S(C(O)-R₅-O)_B]_W     XII or         [(-C(O)-C(R₁)(R₂)-O-R₃-O-C(R₁)(R₂)-C(O)-(O-R₁₂)_U-O)_S([-O-R₁₃-C(O)]_P-O-)_LG]_W     XIII wherein S is an integer in the range of from about 1 to 10,000 and preferably from 1 to 1,000 and W is an integer in the range of from about 1 to about 1,000. These polymers may be made in the form of random copolymers or block copolymers. To the diols, aliphatic polyoxycarboxylic acids and lactone monomers described above there may be added a coupling agent selected from the group consisting of trifunctional or tetrafunctional polyols, oxycarboxylic acids, and polybasic carboxylic acids (or acid anhydrides thereof). The addition of the coupling agents causes the branching of long chains, which can impart desirable properties in the molten state to the polyester prepolymer. Examples of suitable polyfunctional coupling agents include trimethylol propane, glycerin, pentaerythritol, malic acid, citric acid, tartaric acid, trimesic acid, propane tricarboxylic acid, cyclopentane tetracarboxylic anhydride and combinations thereof.

The amount of coupling agent to be added before gelation occurs is a function of the type of coupling agent used and the polymerization conditions of the polyoxaester or molecular weight of the prepolymer to which it is added. Generally in the range of from about 0.1 to about 10 mole percent of a trifunctional or a tetrafunctional coupling agent may be added based on the moles of aliphatic polyoxaester polymers present or anticipated from the synthesis.

The preparation of the aliphatic polyoxaester is preferably a polymerization performed under melt polycondensation conditions in the presence of an organometallic catalyst at elevated temperatures. The organometallic catalyst is preferably a tin-based catalyst e.g. stannous octoate. The catalyst will preferably be present in the mixture at a mole ratio of diol, aliphatic polyoxycarboxylic acid and optionally lactone monomer to catalyst will be in the range of from about 5,000 to about 80,000/1. The reaction is preferably performed at a temperature no less than about 120°C under reduced pressure. Higher polymerization temperatures may lead to further increases in the molecular weight of the copolymer, which may be desirable for numerous applications. The exact reaction conditions chosen will depend on numerous factors, including the properties of the polymer desired, the viscosity of the reaction mixture, and the glass transition temperature and softening temperature of the polymer. The preferred reaction conditions of temperature, time and pressure can be readily determined by assessing these and other factors.

Generally, the reaction mixture will be maintained at about 220°C. The polymerization reaction can be allowed to proceed at this temperature until the desired molecular weight and percent conversion is achieved for the copolymer, which will typically take about 15 minutes to 24 hours. Increasing the reaction temperature generally decreases the reaction time needed to achieve a particular molecular weight, but also may increase the extent of side reactions. We have found that reaction at about 220°C to be generally suitable.

In another embodiment, copolymers of aliphatic polyoxaester can be prepared by forming an aliphatic polyoxaester prepolymer polymerized under melt polycondensation conditions, then adding at least one lactone monomer or lactone prepolymer. The mixture would then be subjected to the desired conditions of temperature and time to copolymerize the prepolymer with the lactone monomers in a polycondensation polymerization.

The molecular weight of the prepolymer as well as its composition can be varied depending on the desired characteristic which the prepolymer is to impart to the copolymer. However, it is preferred that the aliphatic polyoxaester prepolymers from which the copolymer is prepared have a molecular weight that provides an inherent viscosity between about 0.2 to about 2.0 deciliters per gram (dl/g) as measured in a 0.1 g/dl solution of hexafluoroisopropanol at 25°C. Those skilled in the art will recognize that the aliphatic polyoxaester prepolymers described herein can also be made from mixtures of more than one diol or dioxycarboxylic acid.

One of the beneficial properties of the aliphatic polyoxaester made by the process of this invention is that the ester linkages are hydrolytically unstable, and therefore the polymer is bioabsorbable because it readily breaks down into small segments when exposed to moist bodily tissue. In this regard, while it is envisioned that co-reactants could be incorporated into the reaction mixture of the aliphatic dioxycarboxylic acid and the diol for the formation of the aliphatic polyoxaester prepolymer, it is preferable that the reaction mixture does not contain a concentration of any co-reactant which would render the subsequently prepared polymer nonabsorbable. Preferably, the reaction mixture is substantially free of any such co-reactants if the resulting polymer is rendered nonabsorbable.

These aliphatic polyoxaesters described herein and those described in Serial No. 08/399,308, filed March 6, 1995 and assigned to Ethicon, now U.S. Patent No. 5,464,929 may be blended together with other homopolymers, copolymers and graft copolymers to impart new properties to the material formed by the blend. The other polymers which the aliphatic polyoxaesters may be blended with include but are not limited to homopolymer and copolymer of lactone type polymers with the repeating units described by Formula VIII, aliphatic polyurethanes, polyether polyurethanes, polyester polyurethanes polyethylene copolymers (such as ethylene-vinyl acetate copolymers and ethylene ethyl acrylate copolymers), polyamides, polyvinyl alcohols, poly(ethylene oxide), polypropylene oxide, polyethylene glycol, polypropylene glycol, polytetramethylene oxide, polyvinyl pyrrolidone, polyacrylamide, poly(hydroxy ethyl acrylate), poly(hydroxyethyl methacrylate). The copolymers (i.e. containing two or more repeating units) including random, block and segmented copolymers. Suitable lactone-derived repeating units may be generated from the following monomers include but are not limited to lactone monomers selected from the group consisting of glycolide, d-lactide, 1-lactide, meso-lactide, ε-caprolactone, p-dioxanone, trimethylene carbonate, 1,4-dioxepan-2-one, 1,5-dioxepan-2-one and combinations thereof. The blends may contain about 1 weight percent to about 99 weight percent of the aliphatic polyoxaesters containing amines and/or amido groups.

For some applications it may be desirable to add additional ingredients such as stabilizers, antioxidants radiopacifiers, fillers or the like.

The aliphatic polyoxaesters and other polymers may be blended using conventional mixing processes known in the art. For example a blend can be prepared using a two-roll mill, an internal mixer (such as a Brabender or Banbury mixer), an extruder (such as a twin screw extruder) or the like.

The polymer blends of this invention can be melt processed by numerous methods to prepare a vast array of useful devices. These polymers can be injection or compression molded to make implantable medical and surgical devices, especially wound closure devices. The preferred wound closure devices are surgical clips, staples and sutures. Alternatively, the polymer blends can be extruded to prepare fibers. The filaments thus produced may be fabricated into sutures or ligatures, attached to surgical needles, packaged, and sterilized by known techniques. The polymer blends of the present invention may be spun as multifilament yarn and woven or knitted to form sponges or gauze, (or non-woven sheets may be prepared) or used in conjunction with other molded compressive structures as prosthetic devices within the body of a human or animal where it is desirable that the structure have high tensile strength and desirable levels of compliance and/or ductility. Useful embodiments include tubes, including branched tubes, for artery, vein or intestinal repair, nerve splicing, tendon splicing, sheets for typing up and supporting damaged surface abrasions, particularly major abrasions, or areas where the skin and underlying tissues are damaged or surgically removed.

Additionally, the polymer blends can be molded to form films which, when sterilized, are useful as adhesion prevention barriers. Another alternative processing technique for the polymer blends of this invention includes solvent casting, particularly for those applications where a drug delivery matrix is desired.

In more detail, the surgical and medical uses of the filaments, films, and molded articles of the present invention include, but are not necessarily limited to:

Knitted products, woven or non-woven, and molded products including: <dl id="dl0001" compact="compact"><dt>a.</dt><dd>burn dressings</dd><dt>b.</dt><dd>hernia patches</dd><dt>c.</dt><dd>medicated dressings</dd><dt>d.</dt><dd>fascial substitutes</dd><dt>e.</dt><dd>gauze, fabric, sheet, felt or sponge for liver hemostasis</dd><dt>f.</dt><dd>gauze bandages</dd><dt>g.</dt><dd>arterial graft or substitutes</dd><dt>h.</dt><dd>bandages for skin surfaces</dd><dt>i.</dt><dd>suture knot clip</dd><dt>j.</dt><dd>orthopedic pins, clamps, screws, and plates</dd><dt>k.</dt><dd>clips (e.g.,for vena cava)</dd><dt>l.</dt><dd>staples</dd><dt>m.</dt><dd>hooks, buttons, and snaps</dd><dt>n.</dt><dd>bone substitutes (e.g., mandible prosthesis)</dd><dt>o.</dt><dd>intrauterine devices (e.g.,spermicidal devices)</dd><dt>p.</dt><dd>draining or testing tubes or capillaries</dd><dt>q.</dt><dd>surgical instruments</dd><dt>r.</dt><dd>vascular implants or supports</dd><dt>s.</dt><dd>vertebral discs</dd><dt>t.</dt><dd>extracorporeal tubing for kidney and heart-lung machines</dd><dt>u.</dt><dd>artificial skin and others</dd><dt>v.</dt><dd>catheters (including, but not limited to, the catheters described in U.S. Patent No. 4,883,699 which is hereby incorporated by reference)</dd><dt>w.</dt><dd>scaffoldings for tissue engineering applications.</dd></dl>

In another embodiment, the polymer blends can be used to coat a surface of a surgical article to enhance the lubricity of the coated surface. The polymer blends may be applied as a coating using conventional techniques. For example, the polymer blends may be solubilized in a dilute solution of a volatile organic solvent, e.g. acetone, methanol, ethyl acetate or toluene, and then the article can be immersed in the solution to coat its surface. Once the surface is coated, the surgical article can be removed from the solution where it can be dried at room or elevated temperatures until the solvent and any residual reactants are removed.

For use in coating applications the polymer blends should exhibit an inherent viscosity, as measured in a 0.1 gram per deciliter (g/dl) of hexafluoroisopropanol (HFIP), between about 0.05 to about 2.0 dl/g, preferably about 0.10 to about 0.80 dl/g. If the inherent viscosity were less than about 0.05 dl/g, then the polymer blends may not have the integrity necessary for the preparation of films or coatings for the surfaces of various surgical and medical articles. On the other hand, although it is possible to use polymer blends with an inherent viscosity greater than about 2.0 dl/g, it may be exceedingly difficult to do so.

Although it is contemplated that numerous surgical articles (including but not limited to endoscopic instruments) can be coated with the polymer blends of this invention to improve the surface properties of the article, the preferred surgical articles are surgical sutures and needles. The most preferred surgical article is a suture, most preferably attached to a needle. Preferably, the suture is a synthetic absorbable suture. These sutures are derived, for example, from homopolymers and copolymers of lactone monomers such as glycolide, lactide, ε-caprolactone, 1,4-dioxanone, and trimethylene carbonate. The preferred suture is a braided multifilament suture composed of polyglycolide or poly(glycolide-co-lactide).

The amount of coating to be applied on the surface of a braided suture can be readily determined empirically, and will depend on the particular copolymer and suture chosen. Ideally, the amount of coating applied to the surface of the suture may range from about 0.5 to about 30 percent of the weight of the coated suture, more preferably from about 1.0 to about 20 weight percent, most preferably from 1 to about 5 weight percent. If the amount of coating on the suture were greater than about 30 weight percent, then it may increase the risk that the coating may flake off when the suture is passed through tissue.

Sutures coated with the polymer blends of this invention are desirable because they have a more slippery feel, thus making it easier for the surgeon to slide a knot down the suture to the site of surgical trauma. In addition, the suture can be passed through body tissue more easily, thereby reducing tissue trauma. These advantages are exhibited in comparison to sutures which do not have their surfaces coated with the polymer blends of this invention.

In another embodiment of the present invention when the article is a surgical needle, the amount of coating applied to the surface of the article is an amount which creates a layer with a thickness ranging preferably between about 2 to about 20 microns on the needle, more preferably about 4 to about 8 microns. If the amount of coating on the needle were such that the thickness of the coating layer was greater than about 20 microns, or if the thickness was less than about 2 microns, then the desired performance of the needle as it is passed through tissue may not be achieved.

In another embodiment of the present invention, the polymer blends can be used as a pharmaceutical carrier in a drug delivery matrix. To form this matrix the blend would be mixed with a therapeutic agent to form the matrix. The variety of different therapeutic agents which can be used in conjunction with the polymer blends of the present invention is vast. In general, therapeutic agents which may be administered via the pharmaceutical compositions of the invention include, without limitation: antiinfectives such as antibiotics and antiviral agents; analgesics and analgesic combinations; anorexics; antihelmintics; antiarthritics; antiasthmatic agents; anticonvulsants; antidepressants; antidiuretic agents; antidiarrheals; antihistamines; antiinflammatory agents; antimigraine preparations; antinauseants; antineoplastics; antiparkinsonism drugs; antipruritics; antipsychotics; antipyretics, antispasmodics; anticholinergics; sympathomimetics; xanthine derivatives; cardiovascular preparations including calcium channel blockers and beta-blockers such as pindolol and antiarrhythmics; antihypertensives; diuretics; vasodilators including general coronary, peripheral and cerebral; central nervous system stimulants; cough and cold preparations, including decongestants; hormones such as estradiol and other steroids, including corticosteroids; hypnotics; immunosuppressives; muscle relaxants; parasympatholytics; psychostimulants; sedatives; and tranquilizers; and naturally derived or genetically engineered proteins, polysaccharides, glycoproteins, or lipoproteins.

The drug delivery matrix may be administered in any suitable dosage form such as oral, parenteral, a subcutaneously as an implant, vaginally or as a suppository. Matrix formulations containing the polymer blends may be formulated by mixing one or more therapeutic agents with the polyoxaester. The therapeutic agent, may be present as a liquid, a finely divided solid, or any other appropriate physical form. Typically, but optionally, the matrix will include one or more additives, e.g., nontoxic auxiliary substances such as diluents, carriers, excipients, stabilizers or the like. Other suitable additives may be formulated with the polymer blend and pharmaceutically active agent or compound, however, if water is to be used it should be added immediately before administration.

The amount of therapeutic agent will be dependent upon the particular drug employed and medical condition being treated. Typically, the amount of drug represents about 0.001% to about 70%, more typically about 0.001% to about 50%, most typically about 0.001% to about 20% by weight of the matrix.

The quantity and type of polyoxaester incorporated into the parenteral will vary depending on the release profile desired and the amount of drug employed. The product may contain blends of polymers having different molecular weights to provide the desired release profile or consistency to a given formulation.

The polymer blends, upon contact with body fluids including blood or the like, undergoes gradual degradation (mainly through hydrolysis) with concomitant release of the dispersed drug for a sustained or extended period (as compared to the release from an isotonic saline solution). This can result in prolonged delivery (over, say 1 to 2,000 hours, preferably 2 to 800 hours) of effective amounts (say, 0.0001 mg/kg/hour to 10 mg/kg/hour) of the drug. This dosage form can be administered as is necessary depending on the subject being treated, the severity of the affliction, the judgment of the prescribing physician, and the like.

Individual formulations of drugs and polyoxaester may be tested in appropriate <i>in vitro</i> and <i>in vivo</i> models to achieve the desired drug release profiles. For example, a drug could be formulated with a polyoxaester and orally administered to an animal. The drug release profile could then be monitored by appropriate means such as, by taking blood samples at specific times and assaying the samples for drug concentration. Following this or similar procedures, those skilled in the art will be able to formulate a variety of formulations.

The polymers, copolymers and blends of the present invention can be crosslinked to affect mechanical properties. Crosslinking can be accomplished by the addition of crosslinking enhancers and/or irradiation (such as gamma-irradiation). In particular, crosslinking can be used to control the water swellablity of said invention.

In a further embodiment of the present invention the polyoxaestes containing amines and/or amido groups and polymer blends of the present invention can be used in tissue engineering applications as supports for cells. Appropriate tissue scaffolding structures are known in the art such as the prosthetic articular cartilage described in U.S. Patent 5,306,311, the porous biodegradable scaffolding described in WO 94/25079, and the prevascularized implants described in WO 93/08850 (all hereby incorporated by reference herein). Methods of seeding and/or culturing cells in tissue scaffoldings are also known in the art such as those methods disclosed in EPO 422 209 B1, WO 88/03785, WO 90/12604 and WO 95/33821 (all hereby incorporated by reference herein).

The Examples set forth below are for illustration purposes only, and are not intended to limit the scope of the claimed invention in any way. Numerous additional embodiments within the scope and spirit of the invention will become readily apparent to those skilled in the art.

<b>Example 1</b>

Preparation of 3,6-Dioxaoctanedioic acid dimethylester

The diacid, 3,6-dioxaoctanedioic acid, was synthesized by oxidation of triethylene glycol. The oxidation was carried out in a 500 milliliter, three-neck round bottom flask equipped with a thermometer, an additional funnel, a gas absorption tube and a magnetic spinbar. The reaction flask was lowered into an oil bath resting upon a magnetic stirrer. To the reaction flask was added 157.3 ml of a 60% nitric acid solution; 37.0 g of triethylene glycol was added to the additional funnel. The <chemistry id="chem0002" num="0002"><img file="EP0771832A2_D0002.tif" /></chemistry> contents of the flask were heated to 78-80°C. A test tube containing 0.5 g of glycol and one milliliter of concentrated nitric acid was warmed in a water bath until brown fumes started appearing. The contents were then added to the reaction flask. The mixture was stirred for a few minutes; the glycol was then carefully added. The rate of addition had to be monitored extremely carefully to keep the reaction under control. The addition rate was slow enough so that the temperature of the exothermic reaction mixture was maintained at 78-82°C. After the addition was completed (80 minutes), the temperature of the reaction mixture was maintained at 78-80° C for an additional hour. While continuing to maintain this temperature range, the excess nitric acid and water was then distilled off under reduced pressure (water suction). The syrupy residue was cooled; some solids appeared. The reaction product had the IR and NMR spectra expected for the dicarboxylic acid; the crude product was used as such for esterification.

Esterification of the crude 3,6-dioxaoctanedioic acid was accomplished as follows: To the reaction flask containing 36 g of the crude diacid, was added 110 ml of methanol. This was stirred for 3 days at room temperature after which 15 g of sodium bicarbonate was added and stirred overnight. The mixture was filtered to remove solids. To the liquor was added an additional 10 g of sodium bicarbonate; this mixture was stirred overnight. The mixture was again filtered; the liquor was fractionally distilled.

NMR analysis of the esterified product showed a mixture of dimethyl triglycolate (78.4 mole%) and monomethyltriglycolate (21.6 mole%) . No significant condensation of diacid was observed.

<b>Example 2</b>

Preparation of polyoxaester from the methyl esters of 3,6-dioxaoctanedioic acid and ethylene glycol

<chemistry id="chem0003" num="0003"><img file="EP0771832A2_D0003.tif" /></chemistry>

A flame dried, mechanically stirred, 50-milliliter glass reactor suitable for polycondensation reaction, was charged with 20.62 g (approximately 0.1 mole) of the methyl esters of 3,6-dioxaoctanedioic acid from Example 1, 18.62 g (0.3 mole) of distilled ethylene glycol, and 0.0606 ml of a solution of 0.33M stannous octoate in toluene. After purging the reactor and venting with nitrogen, the temperature was gradually raised over the course of 26 hours to 180°C. A temperature of 180°C was then maintained for another 20 hours; all during these heating periods under nitrogen at one atmosphere, the methanol formed was collected. The reaction flask was allowed to cool to room temperature; it was then slowly heated under reduced pressure (0.015-1.0 mm) over the course of about 32 hours to 160°C, during which time additional distillates were collected. A temperature of 160°C was maintained for 4 hours after which a sample, a few grams in size, of the polymer formed was taken. The sample was found to have an inherent viscosity (I.V.) of 0.28 dl/g, as determined in hexaflouroisopropanol (HFIP) at 25°C at a concentration of 0.1 g/dl. The polymerization was continued under reduced pressure while raising the temperature, in the course of about 16 hours, from 160°C to 180°C; a temperature of 180°C was maintained at for an additional 8 hours, at which time a polymer sample was taken and found to have an I.V. of 0.34 dl/g. The reaction was continued under reduced pressure for another 8 hours at 180°C. The resulting polymer has an inherent viscosity of 0.40 dl/g, as determined in HFIP at 25°C and at a concentration of 0.1 g/dl.

<b>Example 3</b>

Preparation of polyoxaester with 3,6,9-trioxaundecanedioic acid and ethylene glycol

A flame dried, mechanically stirred, 250-milliliter glass reactor, suitable for polycondensation reaction, was <chemistry id="chem0004" num="0004"><img file="EP0771832A2_D0004.tif" /></chemistry> charged with 44.44 g (0.2 mole) of 3,6,9-trioxaundecanedioic acid, 62.07 g (1.0 mole) of distilled ethylene glycol, and 9.96 milligrams of dibutyltin oxide. After purging the reactor and venting with nitrogen, the contents of the reaction flask were gradually heated under nitrogen at one atmosphere, in the course of about 32 hours, to 180°C, during which time the water formed was collected. The reaction mass was allowed to cool to room temperature. The reaction mass was then heated under reduced pressure (0.015-1.0 mm), gradually increasing the temperature to 180°C in about 40 hours; during this time additional distillates were collected. The polymerization was continued under reduced pressure while maintaining 180°C for an additional 16 hours. The resulting polymer has an inherent viscosity of 0.63 dl/g as determined in HFIP at 25°C and at a concentration of 0.1 g/dl.

<b>Example 4</b>

Preparation of polyoxaester with polyglycol diacid and ethylene glycol

A flame dried, mechanically stirred, 500-milliliter glass reactor (suitable for polycondensation reaction) was charged with 123.8 g (0.2 mole) polyglycol diacid (molecular weight about 619), 62.07 g (1.0 mole) of distilled ethylene glycol, and 9.96 milligrams of dibutyltin oxide. After purging the reactor and venting with nitrogen, the contents of the reaction flask was heated under nitrogen at one atmosphere, gradually increasing the temperature to 200°C in about 32 hours; during this time the water formed was collected. The reaction flask was heated gradually under reduced pressure (0.015-1.0 mm) from room temperature to 140°C in about 24 <chemistry id="chem0005" num="0005"><img file="EP0771832A2_D0005.tif" /></chemistry> hours, during which time additional distillates were collected. A polymer sample of about ten grams was taken at this stage, and found to have an I.V. of 0.14 dl/g in HFIP at 25°C, 0.1 g/dl. The polymerization was continued under reduced pressure while heating from 140°C to 180°C in about 8 hours, and then maintained at 180°C for an additional 8 hours. A polymer sample was again taken and found to have an I.V. of 0.17 dl/g. The reaction temperature was then increased to 190°C and maintained there under reduced pressure for an additional 8 hours. The resulting polymer has an inherent viscosity of 0.70 dl/g as determined in HFIP at 25°C and at a concentration of 0.1 g/dl.

<b>Example 5</b>

Copolymer of polyoxaester/caprolactone/trimethylene carbonate at 5/5/5 by weight

A flame dried, 50-milliliter, round bottom single-neck flask was charged with 5 grams of the aliquot of the polyoxaester of Example 4 having an I.V. of 0.14 dl/g, 5.0 grams (0.0438 mole) of ε-caprolactone, 5.0 grams (0.0490 mole) of trimethylene carbonate, and 0.0094 milliliters of a 0.33 molar solution of stannous octoate in toluene.

The flask was fitted with a magnetic stirrer bar. The reactor was purged with nitrogen three times before venting with nitrogen. The reaction mixture was heated to 160°C and maintained at this temperature for about 6 hours. The copolymer was dried under vacuum (0.1 mm Hg) at 80°C for about 16 hours to remove any unreacted monomer. The copolymer has an inherent viscosity of 0.34 dl/g, as determined in HFIP at 25°C and at a concentration of 0.1 g/dl. The copolymer is a viscous liquid at room temperature. The mole ratio of polyoxaester/PCL/PTMC was found by NMR analysis to be 47.83/23.73/28.45.

<b>Example 6</b>

Copolymer of polyoxaester/caprolactone/glycolide at 6/8.1/0.9 by weight

A flame dried, 25-milliliter, round bottom, single-neck flask was charged with 6 grams of the polyoxaester of Example 4 having an I.V. of 0.17 dl/g., 8.1 grams (0.0731 mole) of ε-caprolactone, 0.9 grams (0.008) mole of glycolide and 0.0080 milliliters of a 0.33 molar stannous octoate solution in toluene. The flask was fitted with a magnetic stirrer bar. The reactor was purged with nitrogen three times before venting with nitrogen. The reaction mixture was heated to 160°C and maintained at this temperature for about 18 hours. The copolymer has an inherent viscosity of 0.26 dl/g in HFIP at 25°C and at a concentration of 0.1 g/dl. The copolymer is solid at room temperature. The mole ratio of polyoxaester/PCL/PGA/caprolactone was found by NMR analysis to be 56.54/37.73/3.79/1.94.

<b>Example 7</b>

<b>In Vitro</b>

Hydrolysis

The polyoxaester of Example 3 was tested for <i>in vitro</i> hydrolysis at both 50°C and at reflux temperature. A 100 mg sample of the polyoxaester, placed in 100 ml of a phosphate buffer solution (0.2 M in phosphate, pH 7.27), was completely hydrolyzed in about 7 days at 50°C, whereas at reflux it was completely hydrolyzed in about 16 hours.

<b>Example 5</b>

<b>In Vitro</b>

Hydrolysis

Polyoxaester of Example 2 was tested for <i>in vitro</i> hydrolysis at 50°C and at reflux temperature. A 100 mg sample of the polyoxaester, placed in a 100 ml buffer solution (pH 7.27), was completely hydrolyzed in about 25 days at 50°C, whereas at reflux it was completely hydrolyzed in about 16 hours.