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 : wherein r 1 and r 2 are independently selected from the group consisting of hydrogen or an alkyl group containing from 1 to 8 carbon atoms and r 3 is an alkylene containing from 2 to 12 carbon atoms or is an oxyalkylene group of the following formula : 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 : wherein r 12 is an alkylene unit containing from 2 to 8 methylene units and containing an internal amine (-- n ( r 10 )--) or amide (-- n ( r 11 )--); r 10 and r 11 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 : wherein r 4 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 -- ch 2 -- ch 2 --! a oh ) and polypropylene glycol ( h -- o -- ch 2 -- ch ( ch 3 )--! a oh ). the polymer produced by reacting the aliphatic dioxycarboxylic acid with the diols discussed above should provide a polymer generally having the formula : wherein r 1 , r 2 , r 3 , r 12 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 : ## str1 ## these lactone monomers ( or equivalent acids , if any ) may be polymerized to provide polymers of the following general structures : wherein r 5 and r 13 are independently selected from the group consisting of -- c ( r 6 )( r 7 )--, --( ch 2 ) 3 -- o --, -- ch 2 -- ch 2 -- o -- ch 2 --, -- cr 8 h -- ch 2 --, --( ch 2 ) 5 --, --( ch 2 ) f -- o -- c ( o )-- and --( ch 2 ) k -- c ( o )-- ch 2 --; r 6 and r 7 are independently hydrogen or an alkyl containing from 1 to 8 carbon atoms ; r 8 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 , l - lactide , mesolactide , 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 : 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 ser . no . 08 / 399 , 308 , filed mar . 6 , 1995 and assigned to ethicon , now u . s . pat . 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 ), absorbable polyoxalates , absorbable polyanhydrides and combinations thereof . 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 , l - 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 polymers and blends of this invention can be melt processed by numerous methods to prepare a vast array of useful devices . these polymers and blends 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 polymers 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 and 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 polymers and blends can be molded to form films which , when sterilized , are useful as adhesion prevention barriers . another alternative processing technique for the polymer and 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 : v . catheters ( including , but not limited to , the catheters described in u . s . pat . no . 4 , 883 , 699 which is hereby incorporated by reference ) in another embodiment , the polymers and blends ( including prepolymers and suitable crosslinked polymers ), 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 polymers and 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 ( this is the initial iv for crosslinkable polymers ), 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 ( which would be the final iv of a crosslinked polymer ) 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 ( this is the initial iv of the crosslinkable polymer ), 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 polymers and 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 polymers and 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 yet another embodiment of the present invention , the polymers and blends can be used as a pharmaceutical carrier in a drug delivery matrix . to form this matrix the polymers and blends 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 polymers and 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 polymers and blends 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 polymers and 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 polymer or blend may be tested in appropriate in vitro and in vivo models to achieve the desired drug release profiles . for example , a drug could be formulated with a polymer or blend 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 and blends of the present invention can be crosslinked to affect mechanical properties . crosslinking may either be chemically or physical . chemically crosslinked polymer chains are connected by covalent bonds , which can be formed by reactive groups contained on the polymers , the addition of crosslinking enhancers and / or irradiation ( such as gamma - irradiation ). physical crosslinked on the other hand connects the polymer chains through non - covalent bonds such as van der waals interactions , hydrogen bonding or hydrophobic interactions . in particular , crosslinking can be used to control the water swellability of said invention . for example , formulas vii a and vii b may be endcapped with one or more crosslinkable regions . similarly , formula xii and xiii may be crosslinked by attaching one or more polymerizable regions to an amine group . the polymerizable regions are preferably polymerizable by photoinitiation by free radical generation , most preferably in the visible or long wavelength ultraviolet radiation . the preferred polymerizable regions are acrylates , diacrylates , oligoacrylates , methacrylates , dimethacrylates , oligomethoacrylates , or other biologically acceptable photopolymerizable groups . other initiation chemistries may be used besides photoinitiation . these include , for example , water and amine initiation schemes with isocyanate or isothiocyanate containing macromers used as the polymerizable regions . useful photoinitiaors are those which can be used to initiate by free radical generation polymerization of the macromers without cytotoxicity and within a short time frame , minutes at most and most preferably seconds . preferred dyes as initiators of choice for long wave length ultraviolet ( lwuv ) or visible light initiation are ethyl eosin , 2 , 2 - dimethoxy - 2 - phenyl acetophenone , other acetophenone derivatives , and camphorquinone . crosslinking and polymerization may be initiated among macromers by a light activated free - radical polymerization initiator such as 2 , 2 - dimethoxy - 2 - phenyl acetophenone , other acetophenone derivatives , and camphorquinone . in other cases , crosslinking and polymerization are initiated among macromers by a light - activated free - radical polymerization initiator such as 2 , 2 - dimethoxy - 2 - phenylacetophenone or a combination of ethyl eosin ( 10 - 4 to 10 - 2 m ) and triethanol amine ( 0 . 001 to 0 . 1m ), for example . the choice of the photoinitiator is largely dependent on the photopolymerizable regions . although we do no wish to be limited by scientific theory , it is believed that the macromer includes at least one carbon - carbon double bond , light absorption by the dye can cause the dye to assume a triplet state , the triplet state subsequently reacting with the amine to form a free radical which initiates polymerization . preferred dyes for use with these materials include eosin dye and initiators such as 2 , 2 - dimethyl - 2 - phenylacetophenone , 2 - methoxy - 2 - phenylacetophenone , and camphorquinone . using such initiators , copolymers may be polymerized in situ by lwuv light or by laser light of about 514 nm , for example . initiation of polymerization ( crosslinking ) is accomplished by irradiation with light at a wavelength of between about 200 - 700 nm , most preferably in the long wavelength ultraviolet range or visible range , 320 nm or higher , most preferably about 514 nm or 365 nm . there are several photooxidizable and photoreductible dyes that may be used to initiate polymerization ( crosslinking ). these include acridine dyes , for example , acriblarine ; thiazine dyes , for example , thionine ; xanthine dyes , for example , rose bengal ; and phenazine dyes , for example , methylene blue . these are used with cocatalysis such as amines , for example , triethanolamine ; sulphur compounds , for example , rso 2 r 1 ; heterocycles , for example , imidazole ; enolates ; organometallics ; and other compounds , such as n - phenyl glycine . other initiators include camphorquinones and acetophenone derivatives . thermal polymerization ( crosslinking ) initiator systems may also be used . thermal initiators may be selected to allow polymerization to be initiated at a desired temperature . at times it may be desired to use a high temperature to initiate polymerization such as during a molding process . for many medical uses it will be desired to use systems that will initiate free radical polymerization at physiological temperatures include , for example , potassium persulfate , with or without tetramethyl ethylenediamine ; benzoylperoxide , with or without triethanolamine ; and ammonium persulfate with sodium bisulfite . the crosslinked polymers ( including copolymers ) and blends ( hereinafter polymers ) can be prepared and used for many of the same uses as described heretofor . in addition , crosslinked polymers can be used for the prevention of surgical adhesions , tissue adhesions , tissue coatings and in tissue engineering . a preferred application is a method of reducing formation of adhesions after a surgical procedure in a patient . the method includes coating damaged tissue surfaces in a patient with an aqueous solution of a light - sensitive free - radical polymerization initiator and a macromer solution as described above . the coated tissue surfaces are exposed to light sufficient to polymerize the macromer . the light - sensitive free - radical polymerization initiator may be a single compound ( e . g ., 2 , 2 - dimethoxy - 2 - phenyl acetophenone ) or a combination of a dye and a cocatalyst ( e . g ., ethyl eosin and triethanol amine ). additionally , the crosslinked polymers can also be used to form hydrogels which are a three dimensional network of hydrophilic polymers in which a large amount of water is present . in general the amount of water present in a hydrogel is at least 20 weight percent of the total weight of the dry polymer . the most characteristic property of these hydrogels is that it swells in the presence of water and shrinks in the absence of water . the extent of swelling ( equilibrium water content ) is determined by the nature ( mainly the hydrophilicity ) of the polymer chains and the crosslinking density . the kinetics of hydrogel swelling is limited by the diffusion of water through the outer layers of the dried hydrogel . therefore , while hydrogels swell to a large extent in water , the time it takes to reach equilibrium swelling may be significant , depending on the size and shape of the hydrogel . to reduce the amount of time it takes for a hydrogel to reach equilibrium , hydrogel foams may be used . hydrogels foams may be made by crosslinking polymers in the presence of gas bubbles . the hydrogels foams prepared with macroscopic gas cells will have an open celled structure similar to sponges except that the pore size will generally be an order of magnitude larger . hydrogels may be used for many of same uses that have been described for polyoxaesters such as wound dressings materials , since the crosslinked hydrogels are durable , non - antigenic , and permeable to water vapor and metabolites , while securely covering the wound to prevent bacterial infection . hydrogels may also be used for coatings in general and medial coatings in particular . hydrogel coatings may provide a smooth slippery surface and prevent bacterial colonization on the surface of the medical instrument . for example hydrogels may be used as coatings on urinary catheter surfaces to improve its biocompatability . hydrogels may also be used in a variety of applications where the mechanical swelling of the hydrogel is useful such as in catheters as a blend component with a biocompatable elastomer ( such as the elastomer described in u . s . pat . no . 5 , 468 , 253 hereby incorporated by reference ). additionally , hydrogels could be used for drug delivery or immobilization of enzyme substrates or cell encapsulization . other uses for hydrogels have been described in the literature many of which are discussed in chapter one of hydrogels and biodegradable polymers for bioapplications , published by the amercian chemical society ( which is hereby incorporated by reference herein ). crosslinking to form crosslinked structures can be performed in a variety of ways . for example the polymers may be crosslinked while being synthesized such as by utilizing multifunctional monomers or oligomers . however , crosslinking at other times is also advantageous . for example , crosslinking may be performed during the manufacture of a device such by adding a thermal initiator to the polymer prior to injection molding a device . additionally , crosslinking of a polymerizable region with a photoinitiator may be performed during stereolithography to form devices . european patent application 93305586 . 5 describes the process for performing stereolithography ( with photopolymerizable materials ). as previously discussed photoinitiation may be used in vivo to crosslink the polymers of the present invention for various wound treatments such as adhesion prevention and wound sealing . coating may also be applied to devices and crosslinked in situ to form films that will conform to the surface of the device . 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 . pat . no . 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 . 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 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 . preparation of polyoxaester from the methyl esters of 3 , 6 - dioxaoctanedioic acid and ethylene glycol ## str3 ## 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 . a flame dried , mechanically stirred , 250 - milliliter glass reactor , suitable for polycondensation reaction , was charged with 44 . 44 g ( 0 . 2 mole ) of 3 , 6 , 9 - trioxaundecanedioic acid , 62 . 07 g ( 1 . 0 mole ) of distilled ## str4 ## 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 . 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 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 . 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 . 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 . the polyoxaester of example 3 was tested for in vitro 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 . 2m 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 . polyoxaester of example 2 was tested for in vitro 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 .
the present invention describes a crosslinked aliphatic polyoxaesters containing amines and / or amido groups and blends thereof with other polymers that may be used to produce surgical devices such as sutures , sutures with attached needles , molded devices , and the like . the crosslinked aliphatic polyoxaesters of the present invention is formed from an aliphatic polyoxaester having a first divalent repeating unit of formula i : o -- c -- c -- o ---- o -- c -- c -- ! i and a second repeating unit of the formula : -- o -- r . sub . 12 --!. sub . u , xvi and optionally a third repeating unit with a formula selected from the group consisting of : -- o -- r . sub . 4 --!. sub . a , ii -- o -- r . sub . 5 -- c --!. sub . b , iii !. sub . p -- o --). sub . l g xi and combinations thereof wherein r 12 contains an internal amine or internal amide group wherein the aliphatic polyoxaester has been crosslinked .