WO1999043364A1 - Absorbable copolymers and surgical articles fabricated thefefrom - Google Patents
Absorbable copolymers and surgical articles fabricated thefefrom Download PDFInfo
- Publication number
- WO1999043364A1 WO1999043364A1 PCT/US1999/004242 US9904242W WO9943364A1 WO 1999043364 A1 WO1999043364 A1 WO 1999043364A1 US 9904242 W US9904242 W US 9904242W WO 9943364 A1 WO9943364 A1 WO 9943364A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- suture
- monofilament
- glycolide
- random copolymer
- sutures
- Prior art date
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Classifications
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS 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
- A61L17/00—Materials for surgical sutures or for ligaturing blood vessels ; Materials for prostheses or catheters
- A61L17/06—At least partially resorbable materials
- A61L17/10—At least partially resorbable materials containing macromolecular materials
- A61L17/12—Homopolymers or copolymers of glycolic acid or lactic acid
Definitions
- ⁇ bsorbable copolymers of randomly polymerized glycolide and caprolactone are described. Processes for making the copolymers and surgical articles made totally or in part from such copolymers, including sutures, are also described.
- Bioabsorbable surgical devices made from copolymers derived from glycolide and epsilo -caprolactone are known in the art. Such bioabsorbable surgical devices include surgical sutures .
- a desirable characteristic of a bioabsorbable suture is its ability to exhibit and maintain desired tensile properties for a predetermined time period followed by rapid absorption of the suture mass (hereinafter "mass loss”.)
- Absorbable multifilament sutures such as DEXON sutures (made from glycolide homopoly cr and commercially available from Davis & Geek, Danbury, Connecticut) , VICRY sutures (made from a copolymer of glycolide and lactide and commercially available from Ethicon, Inc., Som erville, New Jersey), and POLYSORB sutures (also made from a copolymer of glycolide and lactide and commercially available from United States Surgical Corporation, Norwalk, Connecticut) are known in the industry as short term absorbable sutures.
- DEXON sutures made from glycolide homopoly cr and commercially available from Davis & Geek, Danbury, Connecticut
- VICRY sutures made from a copolymer of glycolide and lactide and commercially available from Ethicon, Inc., Som erville, New Jersey
- POLYSORB sutures also made from a copolymer of glycolide and lactide and commercially available from United States Surgical Corporation, Norwalk,
- the classification short term absorbable sutures generally refers to surgical sutures which retain at least about 20 percent of their original strength at three weeks after implantation, with the suture rnasr.; being es ⁇ crii- i.il.ly absorbed in the body within about 60 to 90 days post: implantation.
- absorbable sutures are generally classified as sutures capable of retaining at least about 20 percent of their original strength for six or more weeks after implantation, with the suture mass being essentially absorbed in the body within about 180 days post implant ion.
- PDS II sutures commercially available from Ethicon, Tnc . , Sommervi . ' IJ.e , New Jersey
- MAXON suture is another absorbable synthetic monofilament that reportedly generally fits this absorption profile.
- BIOSYN onofilament sutures which exhibit good flexibility, handling characteristics, knot strength and absorption characteristics similar to those of presently available short term absorbable multifilament sutures.
- gut suture refers Co a collagen based suture of any type or origin often fabricated from the mammalian intestines, such as the serosal layer of bovine intestines or the submucosal fibrous layer of layer sheep intestines.
- Gut sutures exhibit the unique combination of two week strength retention and about 75 day mass loss wh ⁇ c maintaining acceptable modulus and tensile strength; and thus are still widely used in gynecological surgery.
- U.S. Patent No. 4,700,704 to Jamiolkowski does teach that sutures can be fabricated from random copolymers of glycolide and epsilon-caprolactone, and more specifically from random copolymers containing from 20 to 35 weight percent epsilon-caprolactone and from 65 to 80 weight percent glycolide.
- Jamiolkowski reports that sutures fabricated from glycolide/epsilon-caprolactone copolymers containing over 35% caprolactone under are not orientable to a dimensionally stable fiber.
- Jamiolkowski further reports that some sutures fabricated from glyc ⁇ lide/epsilon-caprolactone copolymers containing 15% caprolactone are also not orientable to a dimensionally stable fiber. Furhermore, Jamiolkowski also reports the undesirable combination of low modulus and low tensile strength for the glycolide/ epsilon-caprolactone copolymers which he was able to f bricate into sutures .
- sutures made from random copolymer of glycolide and epsilon-caprolactone would provide the strength retention and mass loss characteristics approximating those of gut sutures while maintaining an acceptable modulus and tensile strength.
- absorbable surgical articles formed from a random copolymer of glycolide and caprolactone exhibit strength retention, mass loss and modulus similar to that of gut sutures.
- the copolymers used in forming surgical articles include between about' 2 r ⁇ ⁇ C. .-.I.oul. 2 weighI*. percent of hydroxy onproi ⁇ ⁇ • .-.rid euter units and between about 75 and 63 weight percent of glycolic acid ester units.
- the random copolymers can be spun into fibers.
- the fibers can be advantageously fabricated into either monofilament or ultifilament sutures having physical properties simi-lnr to those of guc sutures.
- the process for a given size suture, comprises the operations of extruding the random caprolactone/glycolide copolymer at an extrusion temperature of from about 70°C to about 21 I V , C to provide a monofilament fiber, passing the solidified monofilament through water (or other suitable liquid medium) quench bath at a temperature of from about 15° C to about 25° C or through in air (or other suitable gaseous medium) at from about 15°C to about 25°C, stretching the monofilament through a welln air ovenn at an overall sl-.rc- ch ratio of f-r.or..
- the monofilament is stretched through three air ovens by four godet stations.
- the first air oven is maintained at ambient temperature
- the second air oven is heated to a temperature above the crystalization temperature of the glycolide /epsilon caprolactone copolymer at about flO" C to about 110° C
- the third air oven is set at about 85° C to about 120° C.
- the draw ratio between the first and second godet station ranges between about 5:1 to about 8:1.
- the draw ratio between the second and third godet station ranges between about 1.3:1 to about 1.8:1.
- the draw ratio between the third and fourth godet station ranges between about 1.04:1 to about 1.06:1.
- the r.uture then may be annealed with or without relaxation at a temperature of from about 30°C to about 120°C to provide the finished suture.
- FIG. 1 is a schematic illustration of an ap a a us which i:i; suitable for manufacturing of monofilament sutures c " !i..-e.lor.ed herein; .nitf
- Tin* nii l ⁇ copo.l.yiiiei.' C ⁇ U I be pi.'ep. i r.'ed using cuiive L ion ⁇ l technique;.;.
- monomers can be dried, mixed in a reaction v s l with an initiator (ei her a .'jingle or multifunctional initiator) and a suitable polymeriz tion catalyst and heated at temperatures from about 170 'C to about 200' C for a 0 period of: time ranging from about 10 hours to about 30 hours.
- the copolymer has repeating units derived from glycolide randomly combined with repeating units derived from caprolactone. Repeating units derived from glycolide comprise between about 25 5 and about ⁇ ' ⁇ wo.itjliL. percent oC the copolymer and pre erably about 30 weight, percent of caprolactone and about 70 weicjht percent of gylcolide. Copolymers of caprolactone and glycolide havi ncf an inherent, viscosi y of from about 1.0 Co about 1.8 dl/g measured at 30 'C and at: a, concentration of 0.25 g/dl in chloroform or liFIP may 0 generally be used.
- >o. ' l ymers can be formed into surgi c.i ' l -ni if .c:; ii im; -my I; iiii technique, suel) a;.:, Lot; example, c extrusion, molding and/or solvent casting.
- the copolymer:.; cni be used alone, 1-).! ended witih other absorbable composi ion:.;, or in combination with non-absorbable components.
- a wide variety of surgical airt de can be manufactured from the copolymer::;
- Fibers made Ero the copolymers can be knitted, woven or made into non-woven materials with other fibers, either absorbable or nonabsorbable to form fabrics, such as meshes and felts.
- Compor.i ions including the e random copolymers can also be used as an absorbable coating for surgical devices.
- the copolymers are spun into fibers to be used in making sutures.
- Multifila ent sutures of the present invention may be made by methods known in the art. Braid constructions such as those disclosed and claimed in U.S. Patent No.'s 5,059,213 and 5,019,093 are suitable for the multi ilament suture of the present invention.
- Fig. 1 substantially illustrates the extruding, quenching and stretching operations of the monofilament manufacturing operation herein.
- Extruder unit 10 is of a known or conventional type and is equipped with controls for regulating the temperature of barrel 11 in various zones thereof, e.g., progressively higher temperatures in three consecutive zones A, B and C along the length of the barrel.
- Pellets or powder of resins of the present invention are introduced to the extruder through hopper 12. Any of the above described copolymers which are useful for the formation of fibers can be used herein.
- Motor-driven metering pump 13 delivers melt extruded resin at a constant rate to spin pack 14 and thereafter through spinneret 1.5 possessing one or more orifices of desired diameter to provide a molten monofilament 16 which then enters quench bath 17, e.g., containing water, where the monofilament solidifies.
- the distance monofilament 16 travels after emerging from spinneret 113 to the point where it enters quench bath 17, i.e., the air gap, can vary and can advantageously be from about
- barrel ⁇ one A of the extruder can be maintained at a temperature of from about 170°C to 215°C, 2one B at from about 170°C to 215°C and zone C at from about 170"C to about 15"--.
- Additional temperature param ters include: metering pump block 13 at from about 170 V C to about 215°C, spinneret 15 at from about 170°C to about 225"C and quench bath at from about 15°C to about 40°C.
- Monofilament 16 is passed through quench bath 17 around driven roller 18 and over idle roller 19.
- a wiper may remove excess water from the monofilament as it is removed from quench bath .1,7.
- first godet station 1 which is equiped with five individual godets, i.e. godets 101, 102, 103, 104 and 105.
- monofilament 16 Upon entering godet station 1, monofilament 16 is wrapped around a first godet 101 provided with nip roll 22 to prevent slippage which might otherwise result from the subsequent stretching operation; and subsequently passed over godet 101, under godet 102, over godet 103, under godet 104, and over godet 105 to godet station 2, containing godets 106, 107, 108, 109, and HO, where it is wrapped over godet 106, under godet 107, over godet 108, under godet 109, and over godet 110..
- Monofilament 16 passing from godet station 1 to godet station 2 is drawn through air oven 23 at a temperature ranging form about 20°C to about 30"C by the godets of godet station 2 which rotate at speeds faster than the speed of the godet station 1 to provide the desired draw ratio, which is from about 5:1 to about 10:1 and preferably from about 6:1 to about 8:1, to effect the molecular orientation of the copolymer from which it is fabricated and thereby increase its tensile strength.
- monofilament .16 is then subjected to a second and a third
- Monofilament 16 is subsequently drawn from godet 105 through air oven 24, which is maintained nt from about 80"C to about 110°C, t.o godot station 3 eout.ii niiuj yodot-s 113, 112, 113, 114, and 115 where it is wrapped over godet 111, under godet 112, over godet 113, under godet 114, and over godet 115.
- Godet station . ' ? spinw faster than godet: station 2 to provide the desired draw ratio, which is from about 1.3:1 to about 1.8:1.
- Godet station 4 spins faster than godet station 3 to provide the desired draw ratio, which is from about 1.05:1 to about 1.06:1. It should be understood that the godet arrangements in each of godet stations 1, 2, 3, and 4, respectively should not be limited to the above described arrangement and that each godet station may have any suitable godet arrangement.
- monofilament 16 is only passed through godet stations 1 and 2 and not subjected to any further stetching operations .
- Annealing of the suture also may be accomplished with or without shrinkage of the suture.
- the desired length of suture may be wound around ⁇ creel and the creel placed in ⁇ heating cabinet, under nitrogen flow maintained at the desired temperature, e.g. about 70 " C to about 120 'C, as described in U.S. Patent No. 3,630,205. After a suitable period of residency in the heating cabinet, e.g., for up to about 18 hours or so, the suture will have undergone essentially no shrinkage. ⁇ shown in U.S. Patent No.
- the creel may be rotated within the heating cabinet in order to .insure uniform heating of the mono ilament- or the cabinet may be ⁇ f the circulating hot air type in which case un orm heating of the mono ilament w ll bo achieved without the
- the creel with s annealed suture is removed from the heating cabinet and when returned to room temperature, the suture is removed from the creel, conveniently by cutting the wound monofilament at opposite ends of the creel.
- the annealed sutures, optionally attached to surgical needles, are then ready to be packaged and sterilized.
- the suture may be annealed on line with or without relaxation.
- the fourth godet station rotates at a slower speed than the third godet station thus relieving tension on the filament.
- suture 101 may be attached to a surgical needle 100 as shown in Fig. 2 by methods well known in the art. Wounds may be sutured by passing the needled suture through tissue to create wound closure. The needle preferably is then removed from the suture and the suture tied.
- the suture can carry a therapeutic agent which will be deposited at the repair site.
- the therapeutic agent can be chosen for its antimicrobial properties, capability for promoting repair or reconstruction and/or new tissue growth.
- Antimicrobial agents such as broad spectrum antibiotic (gentamycin sulf te. erythromycin or derivatized glycopeptides) which are slowly released into the tissue can be applied in this manner to aid in combating clinical and sub-clinical infections in ⁇ tissue repair site.
- one or several growth promoting factors can be introduced into the sutures, e.g., fibroblast growth factor, bone growth factor, epidermal growth factor, platelet derived growth factor, macrophage derived growth factor, alveolar derived growth
- Some therapeutic indications are: glycerol with tissue or kidney plasminogen activator to cause thrombosis, superoxide dimuta ⁇ e to scavenge tissue damaging free radicals, tumor necrosis factor for cancer therapy or colony stimulating factor and interferon, interleukin-2 or other lymphokine to enhance the immune system.
- sutures of the present invention may be desirable to dye the sutures of the present invention in order to increase visibility of the suture in the surgical field.
- Dyes known to be suitable for incorporation in sutures can be used. Such dyes include but are not limited to carbon black, bone black, D&C Green No. 6, and D&C Violet No. 2 as described in the handbook of U.S. Colorants for Food, Drugs and Cosmetics by Daniel M. Marrion (1979).
- sutures in accordance with the invention are dyed by adding up to about a few percent and preferably about 0.2% dye, such as D&C Violet No. 2 to the resin prior to extrusion .
- EXAMPLE 1 Dry glycolide (4200 grams) and undistilled epsilon- caprolactone were added to a reactor along with 0.35 grams of distil.! od stannour, octoate and 3 grams of 1,6 hexancdiol . The mixture was dried for about 48 hours with agitation under flow of nitrogen. The reactor temperature was then set at 100 ' C. When the temperature of the reactants reached 100 "C the
- Table I sets forth typical conditions for extruding, stretching of size 3/0 sutures in accordance with this invention. All of the monofilament sutures were fabricated from the resin of Example 1.
- Si are Size 3/0
- Table III sets forth the physical properties of the size 3/0 suture of the present invention.
- the suture made of the copolymer provided herein shows a desired physical properties, such as modulus and tensile strength.
- Example 2 TNVITI.0 STRENGTH RETENTION Monofilament sutures manufactured in accordance with the above described process using the copolymer of Example 1 were tested for in vitro strength retention. In vitro loop-pull strength retention is indicative of in vivo strength retention. The in vitro strength retention of the suture was tested as follows:
- the suture r-ample ⁇ were stored in a container filled with Sorenson's buffer solution at 37 "C. After various periods of time, the suture samples were then removed from the container to test their loop-pull strength as follows. A knotted loop was formed. in a test suture in three steps as shown in FIGS. 3A - 3C. As shown in step 1 of of I'-'IG 3A , each suture was given a double throw (left over right ) around a 2 c diameter cylinder. In Step 2, the free ends of the suture were set in a single throw throw (right over left) onto the initial throw of r:i-r » p .1. Finally, in ytep J, another double throw ( loft over right) was set onto the single throw of Step 2 to complete the knot.
- T n represents the time elapsed in weeks since the sample was placed in the solution, with n representing the number of weeks .
- the suture samples were stored in ⁇ container filled with Sorenson' ⁇ buffer solution at 80 "C. After various periods of time, the suture samples were then removed from the container filterred, rinsed with distiioled water and dried for about 6 hours at about 40 * C under vaccum and subsequently weighed.
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- Vascular Medicine (AREA)
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- Life Sciences & Earth Sciences (AREA)
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Abstract
Description
Claims
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE69942930T DE69942930D1 (en) | 1998-02-25 | 1999-02-25 | Surgical suture made of resorbable copolymers |
CA002320728A CA2320728C (en) | 1998-02-25 | 1999-02-25 | Absorbable copolymers and surgical articles fabricated therefrom |
AU28808/99A AU2880899A (en) | 1998-02-25 | 1999-02-25 | Absorbable copolymers and surgical articles fabricated thefefrom |
EP99909646A EP1071480B1 (en) | 1998-02-25 | 1999-02-25 | Sutures made from absorbable copolymers |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US3019198A | 1998-02-25 | 1998-02-25 | |
US09/030,191 | 1998-02-25 | ||
US09/161,606 | 1998-09-26 | ||
US16160699A | 1999-02-24 | 1999-02-24 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1999043364A1 true WO1999043364A1 (en) | 1999-09-02 |
Family
ID=26705767
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1999/004242 WO1999043364A1 (en) | 1998-02-25 | 1999-02-25 | Absorbable copolymers and surgical articles fabricated thefefrom |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP1071480B1 (en) |
AU (1) | AU2880899A (en) |
WO (1) | WO1999043364A1 (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4700704A (en) | 1982-10-01 | 1987-10-20 | Ethicon, Inc. | Surgical articles of copolymers of glycolide and ε-caprolactone and methods of producing the same |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE581211A (en) * | 1958-08-01 | |||
US5133739A (en) * | 1990-02-06 | 1992-07-28 | Ethicon, Inc. | Segmented copolymers of ε-caprolactone and glycolide |
US5403347A (en) * | 1993-05-27 | 1995-04-04 | United States Surgical Corporation | Absorbable block copolymers and surgical articles fabricated therefrom |
CA2127636C (en) * | 1993-07-21 | 2009-10-20 | Cheng-Kung Liu | Plasticizers for fibers used to form surgical devices |
US5431679A (en) * | 1994-03-10 | 1995-07-11 | United States Surgical Corporation | Absorbable block copolymers and surgical articles fabricated therefrom |
US5747637A (en) * | 1995-09-07 | 1998-05-05 | Mitsui Toatsu Chemicals, Inc. | Bioabsorbable polymer and process for preparing the same |
US5718716A (en) * | 1996-09-20 | 1998-02-17 | Ethicon, Inc. | Process for manufacturing sutures from copolymers of glycolide and E-caprolactone |
-
1999
- 1999-02-25 AU AU28808/99A patent/AU2880899A/en not_active Abandoned
- 1999-02-25 WO PCT/US1999/004242 patent/WO1999043364A1/en active Application Filing
- 1999-02-25 EP EP99909646A patent/EP1071480B1/en not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4700704A (en) | 1982-10-01 | 1987-10-20 | Ethicon, Inc. | Surgical articles of copolymers of glycolide and ε-caprolactone and methods of producing the same |
Non-Patent Citations (1)
Title |
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See also references of EP1071480A4 * |
Also Published As
Publication number | Publication date |
---|---|
EP1071480A1 (en) | 2001-01-31 |
AU2880899A (en) | 1999-09-15 |
EP1071480A4 (en) | 2004-07-14 |
EP1071480B1 (en) | 2010-11-10 |
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