AU2600497A - Crystalline copolymers and methods of producing such copolymers - Google Patents

Crystalline copolymers and methods of producing such copolymers

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Publication number
AU2600497A
AU2600497A AU26004/97A AU2600497A AU2600497A AU 2600497 A AU2600497 A AU 2600497A AU 26004/97 A AU26004/97 A AU 26004/97A AU 2600497 A AU2600497 A AU 2600497A AU 2600497 A AU2600497 A AU 2600497A
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AU
Australia
Prior art keywords
glycolide
crystalline
copolymer
lactide
added
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
AU26004/97A
Inventor
Hildegard I. Kramer
Andrew M. Lichkus
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Wyeth Holdings LLC
Original Assignee
American Cyanamid Co
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Filing date
Publication date
Application filed by American Cyanamid Co filed Critical American Cyanamid Co
Publication of AU2600497A publication Critical patent/AU2600497A/en
Abandoned legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/78Preparation processes
    • C08G63/82Preparation processes characterised by the catalyst used
    • C08G63/823Preparation processes characterised by the catalyst used for the preparation of polylactones or polylactides
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L17/00Materials for surgical sutures or for ligaturing blood vessels ; Materials for prostheses or catheters
    • A61L17/06At least partially resorbable materials
    • A61L17/10At least partially resorbable materials containing macromolecular materials
    • A61L17/12Homopolymers or copolymers of glycolic acid or lactic acid
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L31/00Materials for other surgical articles, e.g. stents, stent-grafts, shunts, surgical drapes, guide wires, materials for adhesion prevention, occluding devices, surgical gloves, tissue fixation devices
    • A61L31/04Macromolecular materials
    • A61L31/06Macromolecular materials obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/02Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
    • C08G63/06Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from hydroxycarboxylic acids
    • C08G63/08Lactones or lactides

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  • Health & Medical Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Surgery (AREA)
  • Public Health (AREA)
  • Vascular Medicine (AREA)
  • Epidemiology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Animal Behavior & Ethology (AREA)
  • General Health & Medical Sciences (AREA)
  • Organic Chemistry (AREA)
  • Veterinary Medicine (AREA)
  • Polymers & Plastics (AREA)
  • Medicinal Chemistry (AREA)
  • Heart & Thoracic Surgery (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Polyesters Or Polycarbonates (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)

Description

CRYSTALLINE COPOLYMERS AND METHODS OF
PRODUCING SUCH COPOLYMERS
TECHNICAL FIELD
The present invention relates to glycolide and dl- lactide based copolymer compositions and more particularly to crystalline copolymer compositions comprising less than sixty -two weight percent or less glycolide and methods of producing such compositions which are useful in the
manufacture of absorbable medical devices. BACKGROUND ART
Copolymers of, and surgical devices made from dl-lactide and glycolide are well known. U.S. Patents relating to such copolymers and the like include: 3,620,218; 3,636,956; 3,9102,497; 3,918,455; 3,937,223; 4,137,921; 4,157,437;
4,243,775; 4,443,430; 4,835,139; 5,013,553; 5,198,220;
5,242,910; 5,229,469; 5,317,065; 5,320,624; 5,384,133;
5,395,747; 5,403,713; 5,425,984; 5,431,679; 5,439,884 and 5,470,340. The desirable physical properties of medical grade bioabsorbable copolymers such as those made from dl- lactide and glycolide are strongly influenced by the degree of crystallinity thereof. Prior patents such as U.S. Patent No. 5,320,624 disclose that compositions derived from lactide and glycolide in which the lactide moieties predominate have unexpected desired properties such as a decreased degree of crystallinity. Accordingly, it is well established that such copolymers which contain thirty-eight weight percent or more dl-lactide which is optically inactive are characteristically amorphous or lack crystallinity.
Likewise, U.S. Patent No. 4,157,437 which discloses a crystalline copolymer of lactide and glycolide, requires a major portion thereof to include optically active lactide which is known to be crystalline. No mention is made of absorbable copolymeric medical devices made of optically inactive and characteristically amorphous dl-lactide and glycolide specifically designed to be crystalline to improve the physical properties thereof.
DISCLOSURE OF INVENTION
The present invention provides novel compositions made of approximately sixty-two weight percent or less glycolide and approximately thirty-eight weight percent or more optically inactive dl-lactide having the unexpected
characteristic of being crystalline. According to prior art teachings such compositions are characteristically
amorphous. However, the compositions of the present
invention have a bioabsorbable, segmented molecular
architecture comprising a plurality of dl-lactide and glycolide linkages and mixtures thereof which are
unexpectedly crystalline. The crystallinity of such
compositions is unexpected since dl-lactide linkages are characteristically non-crystalline or amorphous.
The process of manufacturing the compositions of the present invention is a two or more stage ring-opening copolymerization of highly reactive monomer linkages
utilizing an initiator. A catalyst is also employed in the suitable methods used to produce the crystalline
compositions described in detail below. It is important to note that the catalyst type and the level of catalyst employed affect both the polymerization and
transesterification rates of the cyclic esters described in this invention. Tin based catalysts such as stannouε chloride dihydrate and stannous octoate are preferred.
Additionally, the inherent viscosity or molecular weight of the subject composition is strongly influenced by the amount of initiator used during polymerization. Again, the methods of producing the novel compositions of the present invention are described in great detail below.
The crystalline compositions of the present invention are useful in the area of medical devices in that the compositions are readily bioabsorbable and have superior physical and tensile properties over amorphous copolymers of the same composition. Medical devices fabricated from the subject crystalline compositions are dimensionally stable at ambient conditions in contrast to amorphous counterparts.
This superior physical property is a valued improvement from both an economical and a commercial point of view due to the elimination of the need for refrigerated shipping and storage thereof.
Accordingly, it is one object of the present invention to provide novel crystalline copolymer compositions which are dimensionally stable at ambient conditions and thereby eliminate the need for refrigerated shipping and storage thereof.
It is another object of the present invention to provide novel crystalline copolymer compositions useful in the manufacture of medical devices.
It is another object of this invention to provide absorbable medical devices having improved properties manufactured from the novel crystalline copolymer
compositions of the present invention.
It is another object of this invention to provide a novel method of producing the novel crystalline compositions of the present invention.
Other objects of the invention are achieved herein by providing absorbable medical devices derived from the novel crystalline compositions of the present invention.
BEST MODE FOR CARRYING OUT THE INVENTION
In accordance with the present invention, it has now been found that desirable physical properties of medical grade bioabsorbable copolymers such as those made from optically inactive dl-lactide and glycolide are strongly influenced by the degree of crystallinity thereof. However, teachings to date indicate that a decrease in crystallinity improves the physical properties of a synthetic composition to be used in the manufacture of a medical device. The subject invention to the contrary provides for the increased crystallinity of characteristically amorphous compositions to achieve improved physical properties. The novel
unexpectedly crystalline compositions of the present
invention are made up of approximately sixty-two weight percent or less glycolide and approximately thirty-eight weight percent or more optically inactive dl-lactide but preferably approximately fifty weight percent glycolide and approximately fifty weight percent optically inactive dl- lactide. According to prior art teachings and methods of manufacture such compositions were heretofore
characteristically amorphous.
The novel processes of manufacturing the novel
crystalline compositions of the present invention are two or more stage ring-opening copolymerizations but preferably a two stage sequential addition copolymerization to increase crystallinity. The copolymerization is achieved by using one or more initiators and one or more catalysts. Suitable initiators for the manufacture of the crystalline copolymers of the present invention include but are not limited to alcohols. Suitable alcohol initiators include but are not limited to 1-docecanol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 1,10-decanediol, inositol, pentacrythritol, mannitol, sorbitol, erythritol, ethylene glycol and 1,3- propane diol. Preferably, lauryl alcohol, i.e., 1-docecanol is used as the initiator of choice to increase the polymer block characteristics, i.e., to increase sequence length and thereby increase the degree of crystallinity, of the
copolymer.
The inherent viscosity or molecular weight of a
copolymer is directly influenced by the initiator and the amount of initiator used during the polymerization. For the novel crystalline copolymers of the present invention, an inherent viscosity of greater than 0.5 dl/g at a
concentration of 0.5g/dl in a solvent such as
hexafluoroisopropanol at 30°C is preferred. However, an inherent viscosity within the range of 0.3 to 0.8 dl/g but preferably 0.5 or 0.6 dl/g is preferred for controlled release devices where a strength value is not necessary. For articles of manufacture of formable devices which do not require high strength, an inherent viscosity within the range of 0.05 to 0.3 dl/g but preferably .05 to 0.1 dl/g is required for adequate formability. A suitable inherent viscosity for fiber applications would be within the range of 0.8 dl/g or higher such as 2.0 dl/g but most preferably approximately 1.0dl/g for adequate tensile properties. In order to achieve these desired inherent viscosities the initiator/dl-lactide ratio should be greater than
approximately 1:60 but preferably approximately 1:100. A suitable melting point for the crystalline compositions of the present invention is at least 140°C but preferably 160°C or greater.
The polymerization and transesterification rates of the cyclic esters of the present invention are directly
influenced by the one or more catalysts employed. Suitable catalysts include but not limited to stannous chloride, dibutyl tin dilaurate, dibutyl tin diacetate, dibutyl tin dichloride, stannic chloride pentahydrate, aluminum
isopropoxide, antimony trioxide, stannic fluoride, stannous citrate, stannous acetate, antimony trifluoride, tin
teteraisopropoxide, lead oxide, tetraisopropyl titanate, titanium acetyl acetonate, tetraoctylene glycol titanate, boron trifluoride etherate, aluminum trichloride, stannous chloride dihydrate and stannous octoate. Stannous chloride dihydrate and/or stannous actoate are preferred catalysts for the production of the present compositions due to their superior properties when utilized in a biological system. Most preferably stannous chloride dihydrate is used as the catalyst of choice in the present invention in order to control the required polymerization time. However, other catalysts would be suitable to produce the subject
compositions although the tin based catalysts have been found to have superior bioabsorbable characteristics in vivo.
Suitable reaction conditions for the present invention include polymerizations carried out at a temperature of approximately 160°C to 240°C but most preferably at a
temperature of approximately 180°C to 200°C. The
polymerizations are carried out within this temperature range over a period of approximately 1 hour to 4 hours but preferably approximately 2 to 3 hours to achieve the desired degree of crystallinity within the range of 2 to 30 percent, but preferably approximately 10 percent. The reaction conditions set forth herein likewise allows the subject compositions to be prepared in an economically and
commercially desirable amount of time.
A wide variety of absorbable, implantable medical devices can be manufactured in whole or in part from the novel copolymers of the present invention. Such devices include plugs, fasteners, pins, bone screws and other implantable devices. As expressed above, the novel
copolymers of the present invention provide dimensional stability at ambient temperatures thereby eliminating the need for refrigerated shipping and storage of such medical implant devices. The elimination of the need for
refrigeration makes the copolymers of the present invention economically and commercially desirable.
The examples below are used to further describe and further illustrate a few of the novel crystalline copolymers of the present invention. The following examples are in no way intended to limit the scope of the novel crystalline compositions covered herein. Examples:
I. Single State Reactions:
Examples 1 through 6: 50/50 to 75/25 Copolymers of dl- lactide/glycolide
Six copolymers were prepared from glycolide and
optically inactive dl-lactide. Ring opening polymerization of glycolide and dl-lactide were conducted using 0.40 mole percent with respect to the total monomer concentration of 1-dodecanol as the initiator and 0.001 to 0.005 mole percent with respect to total monomer concentration of stannous chloride dihydrate as catalyst. The polymerizations were carried out in a 2CV reactor. When combined, the molten mixture of monomers, initiator and catalyst was charged to a stirred reactor at 180°C, under nitrogen atmosphere, at 28 to 35 rpm. The reaction temperature was raised from 180°C to 200°C over a 15 minute time period. Stirring and heating was continued for an additional 45 minutes, for a total reaction time of two and one half hours. The reaction time was extended for some polymers. The resulting copolymers were ground and dried under vacuum at 110°C, 0.2 mm Hg, for 16 hours. Analytical results are summarized in Table 1.
Molecular weight was characterized by a determination of the inherent viscosity in HFIP (Hexafluorisopropanol) at 30°C and a concentration of 0.5 g/dl as referenced in Table 1.
Although all six copolymers were prepared by a single stage reaction, differences in their physical properties were influenced by composition. Crystalline polymers were obtained with glycolide-rich compositions (Ex. 5 and Ex. 6). A shift from polymers with crystalline to those with
amorphous properties is observed with the increase of noncrystalline optically inactive dl-lactide linkages
(Ex. 1, Ex. 2, Ex. 3 Ex. 4) which are unsuitable for the present invention. II. Sequential Addition Copolymers:
Examples 7 through 14: 50/50 to 25/75 copolymers of dl- latide/glycolide
Eight polymers of glycolide and optically inactive dl- lactide were prepared using sequential addition
polymerization.
Ring opening polymerization of dl-lactide and glycolide were conducted using 0.40 mole percent with respect to total monomer concentration of 1-dodencanol, i.e., lauryl alcohol as initiator and 0.005 mole percent with respect to total monomer concentration of stannous chloride dihydrate as catalyst. Copolymers were prepared by first synthesizing a prepolymer of glycolide and optically inactive dl-lactide with the desired monomer proportions, followed by a
subsequent glycolide addition and continuation of the reaction for a specific length of time. The block length of the crystalizable linkages affecting the crystallinity of the final copolymer, was controlled through the glycolide proportions in the second stage.
Polymerization was carried out in a 2 CV reactor. The molten mixture of monomers, initiator and catalyst was charged to the reactor at 180°C, under nitrogen atmosphere, and stirred at approximately 28 to 35 revolutions per minute (rpm). The reaction temperature was raised from 180°C to 200°C over a 15 minute time period. Stirring and heating was continued for an additional 60 to 145 minutes, for a total reaction time of 2 to 2.5 hours. After the prepolymer was converted, molten glycolide was added with continued
stirring to provide a homogeneous distribution of the glycolide in the prepolymer. The reaction was allowed to continue for 15 to 45 minutes. The resulting polymers were ground and dried under vacuum for 19 hours at 110°C/0.2 Hg. Compositions and polymer properties are listed in Table 2. The molecular weight was characterized by determination of inherent viscosity in HFIP (Hexaflurorisopropanol) at 30°C and a concentration of 0.5 g/dl.
Although the overall composition of glycolide to dl- lactide was kept the same for examples 7-11 and for examples 12-14, respectively, it is clear, that the use of a two stage polymerization process produces copolymers with different levels of crystallinity. It was also observed that the melting temperature and crystallinity of the final copolymer increased proportionally with the increase of the glycolide fraction in the second stage addition.
A. Example 7
Stage 1:
Time: 2.25 hrs
Temperature: 180°C then increased to 200°C over 15 min . and continued for 120 mins at 200°C.
Charge: glycolide: 97.53 g, dl-lactide: 151.35 g
SnCl22H2O: 23.69 mg
1-dodecanol: 1.574 g
Stage 2:
Time: 15 min (and 30 min time cuts
Temperature 200°C
Charge: Glycolide: 24.34 g
B. Example 8
Stage 1:
Time: 2.25 hrs
Temperature 180°C then increased to 200°C over 15 min. and continued for 120 mins at 200°C.
Charge: glycolide: 97353 g, dl-lactide: 151.35 g
SnCl22H2O: 23.69 mg
1-dodecanol: 1.574 g
Stage 2:
Time: 65 min
Temperature: 210°C
Charge: Glycolide: 24.334 g C. Example 9
Stage 1:
Time: 2.25 hrs
Temperature: 180°C then increased to 200°C over 20 min and continued for 115 mins at 200°C.
Charge: glycolide: 85.53 g, dl-lactide: 151.35 g
SnCl22H2O: 23.69 mg
1-dodecanol: 1.574 g
Stage 2:
Time: 15 min (and 30 min) time cuts
Temperature: 200°C
Charge: Glycolide: 36.51 g
D. Example 10
Stage 1:
Time: 2.25 hrs
Temperature: 180°C then increased to 200°C over 20 min. and continued for 115 mins at 200°C.
Charge: glycolide: 73.20 g, dl-lactide: 151.35 g
SnCl22H2O: 23.69 mg
1-dodecanol: 1.574 g
Stage 2:
Time: 15 min (and 30 min) time cuts
Temperature 200°C
Charge: Glycolide: 48.68 g E. Example 11
Stage 1:
Time: 2.25 hrs
Temperature: 180°C then increased to 200°C over 20 min. and continued for 115 mins at 200°C.
Charge: glycolide: 21.92 g, dl-lactide: 136.27 g
SnCl22H2O: 21.32 mg
1-dodencanol: 1.409 g
Stage 2:
Time: 15 min (and 30 min) time cuts
Temperature: 200°C
Charge: Glycolide: 87.78 g F. Example 12
Stage 1:
Time: 2.25 hrs
Temperature: 180°C then increased to 200°C over 15 min and continued for 120 mins at 200°C.
Charge: glycolide: 6.09 g, dl-lactide: 227.02 g
SnCl22H2OL 22.69 mg
1-dodecanol: 1 5 -7-4 g
Stage 2:
Time: 15 min (and 30 min time cuts
Temperature : 200°C
Charge: Glycolide: 63.85 g
G. Example 13
Stage 1:
Time: 2.25 hrs
Temperature: 180°C then increased to 200°C over 20 min and continued for 115 mins at 200°C.
Charge: glycolide: 13.99 g, dl-lactide: 113.51 g
SnCl22H2OL 11.85 mg
1-dodecanol: 0.787 g
Stage 2:
Time: 15 min (and 30 min) time cuts
Temperature: 200°C
Charge: Glycolide: 10.49 g
Each of the eight copolymers produced in Examples seven through fourteen set forth above are unexpectedly
crystalline. Heretofore, copolymers of optically inactive dl-lactide and glycolide in such proportions were known to be characteristically amorphous. However, the novel
crystalline copolymers produced as disclosed herein have desirable physical properties for absorbable medical
devices.
Additionally, while the preceding examples have been directed to the preparation of specific copolymers of optically inactive dl-lactide and glycolide, these examples are for purposes of illustration only and are not limiting of the invention.
Many different embodiments of this invention will be apparent to those skilled in the art and may be made without departing from the spirit and scope thereof. It is
accordingly understood that this invention is not limited to the specific embodiments set forth herein except as defined in the appended claims.

Claims (31)

1. A crystalline copolymer composition comprising approximately 38 weight percent or greater optically inactive dl-lactide and approximately 62 weight percent or less glycolide.
2. The crystalline composition of claim 1 having a melting point of approximately 140°C or greater.
3. The crystalline composition of claim 1 having an inherent viscosity of 0.3 dl/g to 2.0 dl/g.
4. The crystalline composition of claim 1 extruded to form an absorbable medical device.
5. The crystalline composition of claim 1 molded to form an absorbable medical device.
6. The crystalline composition of claim 1 drawn to form an absorbable medical device.
7. The crystalline composition of claim 1 having crystallinity within the range of 2 to 30 percent.
8. A method of preparing a crystalline copolymer of optically inactive dl-lactide and glycolide containing approximately 62 weight percent or less glycolide
comprising:
a. preparing a monomer mixture of optically inactive monomer dl-lactide and the monomer glycolide;
b. polymerizing in a two stage sequential
polymerization process said monomer mixture to obtain a crystalline copolymer of dl-lactide and glycolide.
9. The method of claim 8 wherein said crystalline copolymer has a melting point of at least 140°C.
10. The method of claim 8 wherein said crystalline copolymer has an inherent viscosity of 0.3 dl/g to 2.0 dl/g
11. The method of claim 8 wherein said crystalline copolymer has a crystallinity within the range of 2 to 30 percent.
12. The method of claim 8 wherein one or more
initiators are added to said monomer mixture.
13. The method of claim 8 wherein a 1-dodecanol initiator is added to said monomer mixture.
14. The method of claim 8 wherein an ethylene glycol initiator is added to said monomer mixture.
15. The method of claim 8 wherein one or more catalyst is added to said monomer mixture.
16. The method of claim 8 wherein a tin based catalyst is added to said monomer mixture.
17. The method of claim 8 wherein stannous chloride dihydrate is added to said monomer mixture as a catalyst.
18. The method of claim 8 wherein stannous octoate is added to said monomer mixture as a catalyst.
19. A method of preparing a crystalline copolymer of optically inactive dl-lactide and glycolide containing approximately 62 weight percent or less glycolide
comprising: a. preparing a block copolymer comprising optically inactive dl-lactide and glycolide; and
b. admixing with said block copolymer additional
glycolide monomer to provide an approximate total 62 weight percent or less glycolide in the
copolymer-monomer mixture; and
c. polymerizing said copolymer-monomer mixture to
obtain said crystalline copolymer of optically inactive dl-lactide and glycolide.
20. The method of claim 19 wherein said crystalline copolymer has an inherent viscosity of 0.3 dl/g to 2.0 dl/g.
21. The method of claim 19 wherein said crystalline copolymer has a crystallinity within the range of 2 to 30 percent.
22. The method of claim 19 wherein one or more
initiators are added to prepare said block copolymer.
23. The method of claim 19 wherein a 1-dodecanol initiator is added to prepare said block copolymer.
24. The method of claim 19 wherein a ethylene glycol initiator is added to prepare said block copolymer.
25. The method of claim 19 wherein a catalyst is added to prepare said block copolymer.
26. The method of claim 19 wherein a tin based catalyst is added to prepare said block copolymer.
27. The method of claim 19 wherein stannous chloride dihydrate is added as a catalyst to prepare said block polymer.
28. The method of claim 19 wherein stannous chloride is added as a catalyst to prepare said block polymer.
29. The method of claim 19 wherein said crystalline copolymer has a melting point of at least 140°C.
30. An implantable medical device comprised of a crystalline copolymer approximately 38 weight percent or greater optically inactive dl-lactide and approximately 62 weight percent or less glycolide.
31. An implantable medical device, at least a portion of which is fabricated from a crystalline copolymer of optically inactive dl-lactide and glycolide containing approximately 62 weight percent or less glycolide.
AU26004/97A 1996-04-01 1997-03-31 Crystalline copolymers and methods of producing such copolymers Abandoned AU2600497A (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US1468196P 1996-04-01 1996-04-01
US60014681 1996-04-01
PCT/US1997/005294 WO1997036553A1 (en) 1996-04-01 1997-03-31 Crystalline copolymers and methods of producing such copolymers

Publications (1)

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JP (1) JP2000508017A (en)
AU (1) AU2600497A (en)
BR (1) BR9710651A (en)
CA (1) CA2250760A1 (en)
WO (1) WO1997036553A1 (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6007565A (en) * 1997-09-05 1999-12-28 United States Surgical Absorbable block copolymers and surgical articles fabricated therefrom
US6206883B1 (en) 1999-03-05 2001-03-27 Stryker Technologies Corporation Bioabsorbable materials and medical devices made therefrom
US7700819B2 (en) 2001-02-16 2010-04-20 Kci Licensing, Inc. Biocompatible wound dressing
US7763769B2 (en) 2001-02-16 2010-07-27 Kci Licensing, Inc. Biocompatible wound dressing
US6747121B2 (en) 2001-09-05 2004-06-08 Synthes (Usa) Poly(L-lactide-co-glycolide) copolymers, methods for making and using same, and devices containing same
US7494950B2 (en) 2003-09-05 2009-02-24 Synthes (U.S.A.) Bone cement compositions having fiber-reinforcement and/or increased flowability
US8012501B2 (en) 2004-06-10 2011-09-06 Synthes Usa, Llc Flexible bone composite
DE102007036101A1 (en) 2007-08-01 2009-02-05 Boehringer Ingelheim Pharma Gmbh & Co. Kg New glycolide-rich copolymers
US20100216948A1 (en) * 2009-01-23 2010-08-26 Tipton Arthur J Polymer mixtures comprising polymers having different non-repeating units and methods for making and using same
CN113788938B (en) * 2021-09-15 2023-04-11 杭州锐健马斯汀医疗器材有限公司 Medical lactide polymer and preparation method thereof

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4243775A (en) * 1978-11-13 1981-01-06 American Cyanamid Company Synthetic polyester surgical articles
US4137921A (en) * 1977-06-24 1979-02-06 Ethicon, Inc. Addition copolymers of lactide and glycolide and method of preparation
CA1123984A (en) * 1977-11-16 1982-05-18 Yuzi Okuzumi Block copolymers of lactide and glycolide and surgical prosthesis therefrom
US4443430A (en) * 1982-11-16 1984-04-17 Ethicon, Inc. Synthetic absorbable hemostatic agent
JPH0613602B2 (en) * 1987-07-14 1994-02-23 三井東圧化学株式会社 Method for producing d-l-lactic acid-glycolic acid copolymer
US5320624A (en) * 1991-02-12 1994-06-14 United States Surgical Corporation Blends of glycolide and/or lactide polymers and caprolactone and/or trimethylene carbonate polymers and absorbable surgical devices made therefrom

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EP0907338A4 (en) 1999-09-01
WO1997036553A1 (en) 1997-10-09
CA2250760A1 (en) 1997-10-09
EP0907338A1 (en) 1999-04-14
BR9710651A (en) 1999-08-17
JP2000508017A (en) 2000-06-27

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