CA2219744A1 - Dilatation balloons containing polyesteretheramide copolymer - Google Patents
Dilatation balloons containing polyesteretheramide copolymer Download PDFInfo
- Publication number
- CA2219744A1 CA2219744A1 CA002219744A CA2219744A CA2219744A1 CA 2219744 A1 CA2219744 A1 CA 2219744A1 CA 002219744 A CA002219744 A CA 002219744A CA 2219744 A CA2219744 A CA 2219744A CA 2219744 A1 CA2219744 A1 CA 2219744A1
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- Prior art keywords
- balloon
- copolymer
- polyesteretheramide
- weight percent
- shore
- Prior art date
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Classifications
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- 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
- A61L29/00—Materials for catheters, medical tubing, cannulae, or endoscopes or for coating catheters
- A61L29/04—Macromolecular materials
- A61L29/049—Mixtures of macromolecular compounds
-
- 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
- A61L29/00—Materials for catheters, medical tubing, cannulae, or endoscopes or for coating catheters
- A61L29/04—Macromolecular materials
- A61L29/06—Macromolecular materials obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/13—Hollow or container type article [e.g., tube, vase, etc.]
- Y10T428/1352—Polymer or resin containing [i.e., natural or synthetic]
Abstract
Disclosed is a dilatation balloon having a single layer containing polyesteretheramide copolymer. The dilatation balloon may also contain polyamide and/or additional polymers, and may contain substantially no polyetheramide having substantially no ester linkages.
Description
CA 022l9744 l997-l0-28 W 096/37240 PCT/Lb~'''0~291 DILATATION BALLOONS CONTAINING
POLYESTERETHERAMIDE COPOLYMER
Backgrollnd of the Invention The present invention is generally directed to dilatation balloons containing polyesteretheramide copolymer.
The use of balloon catheters ~or coronary angioplasty is known in the art. In an angioplasty procedure, a partially occluded blood vessel, i.e., one containing a stenosis, is treated by the use o~ an expanding balloon member which presses the stenosis back against the vessel wall. Typically, the expander member or balloon is carried on the distal end o~ a dilatation catheter which is routed through the vascular system to a locaticn within, for example, a coronary artery containing a stenotic lesion. Following placement of the expander member across the lesion as desired, ~luid is introduced into the proximal end o~ the catheter to in~late the expander member to a relatively high pressure, thereby restoring patency to the vessel.
Coronary angioplasty procedures and angioplasty devices are described in detail in Vliestra et al., "Coronary Balloon Angioplasty," Blackwell Scientific Publications (1994).
Medical balloons that are known in the art are disclosed in the ~ollowing documents: U.S. Patent Nos.
4 964 853 and 4 994 032 to Sugiyama et al; U.S. Patents No. 4 906 244, 5 108 415, 5 156 612, 5 236 659, and ~ 5 304 197, to Pinchuk et al; U.S. Patent Nos. 5 226 880 30 and 5 334 148 to Martin; U.S. Patent No. 5 250 069 to CA 022l9744 l997-l0-28 W 096/37240 PCT~Bg<'~8291 Nobuyoshi et al; U.S. Patent No. 5,328,468 to Kaneko et al.; European Patent Application No. 0 566 755; and Japanese laid-open patent application No. 58-188463.
(All documents cited herein, including the foregoing, are incorporated herein in their entireties for all purposes.) It is an object of the present invention to provide a balloon for an angioplasty device which is made, at least in part, of polyesteretheramide copolymer.
Other objects and advantages of the invention will become apparent to those skilled in the art through familiarization with the specification and claims herein.
Sllmm~ry of the Invent;on In sum, the present invention relates to a balloon for an angioplasty device having a single polymeric layer. The layer may have from about 20 to about 100 weight pércent polyesteretheramide copolymer and from about 0 to about 80 wei~ht percent polyamide. The layer contains substantially no polyetheramide having substantially no ester linkages. The polyesteretheramide copolymer may be a block or random copolymer. The polyesteretheramide copolymer may have a hardness of from about 45 Shore D to about 78 Shore D, preferably from about 55 Shore D to about 75 Shore D, and more preferably ~rom about 63 to about 72 Shore D. Even more pre~erably, the polyesteretheramide copolymer may have a hardness selected from about 63 Shore D, about 70 Shore D, and about 72 Shore D. The single polymeric layer may contain at least about 2 weight percent polyamide such as nylon 12, nylon 11, nylon 6, nylon 6/6, nylon -4/6, and W 096/37240 PCTAB9~G291 combinations thereof. The single polymeric layer may further contain at least about Z wei~ht percent polymer such as polyester copolymer, polyurethane copolymer, polyethylene, and combinations thereof. The polymeric layer may have at least about 40 weight percent polyesteretheramide copolymer and more preferably at least about 80 weight percent polyesteretheramide copolymer. The balloon may have from about 20 to about 80 weight percent nylon 12 and about 20 to about 80 weight percent polyesteretheramide copolymer, preferably about 60 weight percent nylon 12 and about 40 weight percent polyesteretheramide copolymer. Alternatively, the balloon may have about 25 to about 80 weight percent nylon 4/6 and about 20 to about 75 weight percent polyesteretheramide copolymer, preferably about 65 weight percent nylon 4/6 and about 35 weight percent polyesteretheramide copolymer.
The present invention also relates to a balloon for an angioplasty device having a single polymeric layer consisting essentially of a polyesteretheramide copolymer. The polyesteretheramide copolymer may be a block or random copolymer. The polyesteretheramide copolymer may have a hardness of from about 45 Shore D to about 78 Shore D, preferably from about 55 Shore D to about 75 Shore D, and more preferably about 63 to about 72 Shore D. Even more pre~erably the polyesteretheramide copolymer may have a hardness selected ~rom 63 Shore D, 70 Shore D, and 72 Shore D. The balloon may consist of polyesteretheramide.
W 096/37240 PCT/lb9G/~291 The present invention also relates to a balloon for an angioplasty device having a single polymeric layer having (a) at least 9l weight percent polyesteretheramide copolymer, (b) from 0 to 9 weight percent polyamide, and S (c) from 0 to 9 weight percent of a polymer other than polyesteretheramide and polyamide. The balloon may have at least about 95 weight percent polyesteretheramide copolymer.
Descr;pt;o~ of the ~raw;ngs FIG. l is a perspective view of an expander member of the present invention joined to the distal end of a catheter;
FIG. 2 is a cross-sectional view of a balloon form used to make expander members of the present invention;
FIG. 3 is a schematic view of a mold apparatus used to make expander members of the present invention;
FIG. 4 shows a response surface that details the effects of processing variables and material selection on balloon wall thickness for PEBAX 6333 balloons;
FIG. 5 shows a response surface that details the effects of processing variables and material selection on balloon burst pressure for PEBAX 6333 balloons;
FIG. 6 shows a response surface that details the effects of processing variables and material selection on balloon K-stat for PEBAX 6333 balloons;
FIG. 7 shows a response sur~ace that details the effects of processing variables and material selection on balloon hoop stress for PEBAX 6333 balloons;
WO 96/37240 PCT~B96/00291 FIG. 8 shows a response surface that details the effects of processing variables and material selection on balloon wall thickness for PEBAX 7033 balloons;
FIG. 9 shows a response surface that details the effects of processing variables and material selection on balloon burst pressure for PEBAX 7033 balloons;
FIG. 10 shows a response surface that details the effects of processing variables and material selection on balloon K-stat 7033 for PEBAX 7033 balloons.;
FIG. 11 shows a response surface that details the effects of processing variables and material selection on balloon hoop stress for PEBAX 7033 balloons;
FIG. 12 shows a response surface that details the effects of processing variables and material selection on balloon wall thickness for PEBAX 7233 balloons;
FIG. 13 shows a response surface that details the effects of processing variables and material selection on balloon burst pressure for PEBAX 7233 balloons;
FIG. 14 shows a response surface that details the effects of processing variables and material selection on balloon K-stat for PEBAX 7233 balloons; and FIG. 15 shows a response surface that details the effects of processing variables and material selection on balloon hoop stress for PEBAX 7233 balloons.
Descript;on of the Preferre~ ~mho~iments With reference to FIG. 1, expander member 2 is attached to the distal end of a catheter shaft 4. The expander member 2, otherwise known as a balloon, has a single polymeric layer 6 which surrounds the catheter shaft 4. The expander member 2 shown is bonded at two WO 96/37240 PcTlLb96~G29l bonding sites 8a,b by thermal bonding, by laser bonding, with adhesives, or by other methods known in the art.
The expander members o~ the present invention contain polyesteretheramide copolymer. The structure o~
these polymers consists o~ regular and linear ch~; n~
rigid polyamide blocks and ~lexible polyether blocks.
Such copolymers may be described by the ~ollowing formula:
O O
HO-~C-PA-C-O-PE-O~iH
where PA is a polyamide block; and where PE is a polyether block.
Polyesteretheramide copolymer materials are sold under the trademark PEBAX by Atochem Inc. o~ Glen Rock, New Jersey. Properties o~ several grades of PEBAX are disclosed in Atochem's brochure entitled ~'PEBAX Polyether Block Amide" (December 1987).
The expander member o~ the present invention may contain polyamide. Polyamide materials include nylon 12, nylon 11, nylon 6, nylon 6/6, and nylon 4/6. Such materials are sold under the trademark ZYTEL by Dupont.
The expander member of the present invention may ~urther contain a polymer other than polyesteretheramide copolymer or polyamide, such as polyester copolymer, polyurethane copolymer, polyethylene, and combinations thereo~.
The single polymeric layer making up the expander member may be a blend o~ suitable materials. Such a blend may be created by mixing the desired resins and CA 022l9744 l997-l0-28 W 096/37240 PCT~B96/00291 then extruding these resins to form a parison. The single layer can also be a graft copolymer. Such a graft copolymer can be ~ormed, ~or example, by reacting polyamide (such as Nylon 12) with polyphenylether graft S maleic anhydride (PPE-graft-MA). So called polymer alloys, and the like, are also included within the purview of this application.
The expander member of the present invention may be formed by first generating a parison in an extruder. The parison will typically have an inside diameter of from about .01 to .031 inches (0.025 to 0.079 cm), and a wall thickness of from about .0035 to .015 inches (.0089 to 0.038 cm).
Hot water treated molding devices may then be utilized to blow mold the expander members of the present invention. Tubing of the desired material and having a required size and thickness is inserted into a balloon processing mold and heated to a temperature of from about 200-212~F (93-100~C). Weight may be added to the mold as desired. The tubing is subjected to longitll~;n~1 tension and high-pressure nitrogen 380-500 psi is introduced into the tubing in the mold. The mold rem~; n.q in a hot water bath for a predetermined period of time of from about 10-45 seconds, preferably 25 seconds. The mold is then removed and placed in a cooling pot for a predetermined period of time of ~rom about 20-40 seconds, pre~erably 30 seconds, after which the mold may be opened and the balloon removed.
In an alternative process, the balloons are ~ormed in balloon blow molding machines. The tubing is inserted CA 022l9744 l997-l0-28 W 096/37240 PCT~B96/00291 into the mold and the ends of the tubing secured into mold gaskets. The tubing is thereafter heated in the range of 190-220~F (87-104~C) for about 10 to 45 seconds, preferably 25-30 seconds, and the heated tubing is subjected to longitll~;n~l tension and expanded 1-2 times its length in the axial direction. The stretched tubing is pressurized with nitrogen in the range of about 350-500 psi and heat treated in the mold for about 10-20 seconds at about 250-280~F (121-138~C), preferably about 260-270~F (127-132~C). The mold is then cooled to room temperature and allowed to set at room temperature in the mold under pressure for approximately 10 to 15 seconds.
Thereafter, the system can be depressurized and the balloon removed from the mold.
~ples Balloons were made of polyesteretheramide block copolymer and then tested to determine certain characteristics.
~x~m~les 1-180 180 balloons were made according to the following process:
Parisons of 100 weight percent polyesteretheramide block copolymer were extruded. The parisons had inside diameters of about .015 inches to about .023 inches, wall thicknesses of about .006 inches to about .010 inches, and lengths of about 18 inches.
The parisons were placed in the mold apparatus illustrated in FIGS. 2 and 3. As shown in FIG. 2, the balloon form 8 had a void 10 corresponding to the final shape of the expander member. The void was made up by a W 096/37240 PCT~B96iO~291 proximal form 24, a body form 26, and a distal form 28.
With reference to FIG. 3, the distal end of the parison was inserted into the proximal end 14 of the mold apparatus 12, and pushed through the proximal form 24, the body form 26, and the distal form 28 until it exited the distal end 16 of the mold section. Cap 18 was then placed over the distal end 16 of the apparatus 12 thereby clamping and sealing the distal end of the parison. The mold was then placed in a handle 20 such that the proximal end of the parison freely extended from the handle 20. Weights 22 were then placed over the proximal end of the parison and onto the mold.
The open prox; m~ 1 end of the parison was then connected to a pressurized nitrogen source by a Touhy Borst clamp. The nitrogen source was capable of achieving m~;mllm pressures of 1,000 psi. The nitrogen source was then opened to varying degrees of between 350-500 psi and the mold was placed in a bath of hot water (212~F). The hot water bath warmed the parison. The freely extending proximal end of the parison was held by hand such that only about the distal form 28 was under water, until the mold dropped due to longitudinal stretching and the distal end of the parison expanded radially (about 15-30 seconds). Still holding the mold by hand, the mold continued to drop until it was entirely under water and the proximal end o~ the balloon expanded radially (about an additional 1-10 seconds).
The mold was then removed ~rom the hot water bath and placed in a cold water bath of about 60-75~F ~or W O 96/37240 PCT/Lb9~ ~v291 about 30 seconds. The nitrogen was then shut o~, and the balloon was removed ~rom the mold.
The balloons were tested by attaching the balloons to a pressurized nitrogen source in a 37~C water bath, expanding the balloons under several predetermined pressures o~ nitrogen (50 psi, 100 psi, 150 psi, and burst pressure), and then measuring several ~;men~ions and the burst pressure of the balloons. Dimensions were measured with a snap gauge.
Tables 1-18 below list certain parameters o~ the process utilized to make the subject balloons (hot pot temperature, cold pot temperature, weight added to mold, and nitrogen pressure). The tables also show results of the testing o~ the expander members. K stat was calculated as ~ollows: (Burst pressure)-((K Stat)(Burst Pressure Standard Deviation)). Hoop stress was calculated as ~ollows: (Balloon Burst Pressure) (Balloon Diameter)/(2)(Balloon Wall Thickness).
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POLYESTERETHERAMIDE COPOLYMER
Backgrollnd of the Invention The present invention is generally directed to dilatation balloons containing polyesteretheramide copolymer.
The use of balloon catheters ~or coronary angioplasty is known in the art. In an angioplasty procedure, a partially occluded blood vessel, i.e., one containing a stenosis, is treated by the use o~ an expanding balloon member which presses the stenosis back against the vessel wall. Typically, the expander member or balloon is carried on the distal end o~ a dilatation catheter which is routed through the vascular system to a locaticn within, for example, a coronary artery containing a stenotic lesion. Following placement of the expander member across the lesion as desired, ~luid is introduced into the proximal end o~ the catheter to in~late the expander member to a relatively high pressure, thereby restoring patency to the vessel.
Coronary angioplasty procedures and angioplasty devices are described in detail in Vliestra et al., "Coronary Balloon Angioplasty," Blackwell Scientific Publications (1994).
Medical balloons that are known in the art are disclosed in the ~ollowing documents: U.S. Patent Nos.
4 964 853 and 4 994 032 to Sugiyama et al; U.S. Patents No. 4 906 244, 5 108 415, 5 156 612, 5 236 659, and ~ 5 304 197, to Pinchuk et al; U.S. Patent Nos. 5 226 880 30 and 5 334 148 to Martin; U.S. Patent No. 5 250 069 to CA 022l9744 l997-l0-28 W 096/37240 PCT~Bg<'~8291 Nobuyoshi et al; U.S. Patent No. 5,328,468 to Kaneko et al.; European Patent Application No. 0 566 755; and Japanese laid-open patent application No. 58-188463.
(All documents cited herein, including the foregoing, are incorporated herein in their entireties for all purposes.) It is an object of the present invention to provide a balloon for an angioplasty device which is made, at least in part, of polyesteretheramide copolymer.
Other objects and advantages of the invention will become apparent to those skilled in the art through familiarization with the specification and claims herein.
Sllmm~ry of the Invent;on In sum, the present invention relates to a balloon for an angioplasty device having a single polymeric layer. The layer may have from about 20 to about 100 weight pércent polyesteretheramide copolymer and from about 0 to about 80 wei~ht percent polyamide. The layer contains substantially no polyetheramide having substantially no ester linkages. The polyesteretheramide copolymer may be a block or random copolymer. The polyesteretheramide copolymer may have a hardness of from about 45 Shore D to about 78 Shore D, preferably from about 55 Shore D to about 75 Shore D, and more preferably ~rom about 63 to about 72 Shore D. Even more pre~erably, the polyesteretheramide copolymer may have a hardness selected from about 63 Shore D, about 70 Shore D, and about 72 Shore D. The single polymeric layer may contain at least about 2 weight percent polyamide such as nylon 12, nylon 11, nylon 6, nylon 6/6, nylon -4/6, and W 096/37240 PCTAB9~G291 combinations thereof. The single polymeric layer may further contain at least about Z wei~ht percent polymer such as polyester copolymer, polyurethane copolymer, polyethylene, and combinations thereof. The polymeric layer may have at least about 40 weight percent polyesteretheramide copolymer and more preferably at least about 80 weight percent polyesteretheramide copolymer. The balloon may have from about 20 to about 80 weight percent nylon 12 and about 20 to about 80 weight percent polyesteretheramide copolymer, preferably about 60 weight percent nylon 12 and about 40 weight percent polyesteretheramide copolymer. Alternatively, the balloon may have about 25 to about 80 weight percent nylon 4/6 and about 20 to about 75 weight percent polyesteretheramide copolymer, preferably about 65 weight percent nylon 4/6 and about 35 weight percent polyesteretheramide copolymer.
The present invention also relates to a balloon for an angioplasty device having a single polymeric layer consisting essentially of a polyesteretheramide copolymer. The polyesteretheramide copolymer may be a block or random copolymer. The polyesteretheramide copolymer may have a hardness of from about 45 Shore D to about 78 Shore D, preferably from about 55 Shore D to about 75 Shore D, and more preferably about 63 to about 72 Shore D. Even more pre~erably the polyesteretheramide copolymer may have a hardness selected ~rom 63 Shore D, 70 Shore D, and 72 Shore D. The balloon may consist of polyesteretheramide.
W 096/37240 PCT/lb9G/~291 The present invention also relates to a balloon for an angioplasty device having a single polymeric layer having (a) at least 9l weight percent polyesteretheramide copolymer, (b) from 0 to 9 weight percent polyamide, and S (c) from 0 to 9 weight percent of a polymer other than polyesteretheramide and polyamide. The balloon may have at least about 95 weight percent polyesteretheramide copolymer.
Descr;pt;o~ of the ~raw;ngs FIG. l is a perspective view of an expander member of the present invention joined to the distal end of a catheter;
FIG. 2 is a cross-sectional view of a balloon form used to make expander members of the present invention;
FIG. 3 is a schematic view of a mold apparatus used to make expander members of the present invention;
FIG. 4 shows a response surface that details the effects of processing variables and material selection on balloon wall thickness for PEBAX 6333 balloons;
FIG. 5 shows a response surface that details the effects of processing variables and material selection on balloon burst pressure for PEBAX 6333 balloons;
FIG. 6 shows a response surface that details the effects of processing variables and material selection on balloon K-stat for PEBAX 6333 balloons;
FIG. 7 shows a response sur~ace that details the effects of processing variables and material selection on balloon hoop stress for PEBAX 6333 balloons;
WO 96/37240 PCT~B96/00291 FIG. 8 shows a response surface that details the effects of processing variables and material selection on balloon wall thickness for PEBAX 7033 balloons;
FIG. 9 shows a response surface that details the effects of processing variables and material selection on balloon burst pressure for PEBAX 7033 balloons;
FIG. 10 shows a response surface that details the effects of processing variables and material selection on balloon K-stat 7033 for PEBAX 7033 balloons.;
FIG. 11 shows a response surface that details the effects of processing variables and material selection on balloon hoop stress for PEBAX 7033 balloons;
FIG. 12 shows a response surface that details the effects of processing variables and material selection on balloon wall thickness for PEBAX 7233 balloons;
FIG. 13 shows a response surface that details the effects of processing variables and material selection on balloon burst pressure for PEBAX 7233 balloons;
FIG. 14 shows a response surface that details the effects of processing variables and material selection on balloon K-stat for PEBAX 7233 balloons; and FIG. 15 shows a response surface that details the effects of processing variables and material selection on balloon hoop stress for PEBAX 7233 balloons.
Descript;on of the Preferre~ ~mho~iments With reference to FIG. 1, expander member 2 is attached to the distal end of a catheter shaft 4. The expander member 2, otherwise known as a balloon, has a single polymeric layer 6 which surrounds the catheter shaft 4. The expander member 2 shown is bonded at two WO 96/37240 PcTlLb96~G29l bonding sites 8a,b by thermal bonding, by laser bonding, with adhesives, or by other methods known in the art.
The expander members o~ the present invention contain polyesteretheramide copolymer. The structure o~
these polymers consists o~ regular and linear ch~; n~
rigid polyamide blocks and ~lexible polyether blocks.
Such copolymers may be described by the ~ollowing formula:
O O
HO-~C-PA-C-O-PE-O~iH
where PA is a polyamide block; and where PE is a polyether block.
Polyesteretheramide copolymer materials are sold under the trademark PEBAX by Atochem Inc. o~ Glen Rock, New Jersey. Properties o~ several grades of PEBAX are disclosed in Atochem's brochure entitled ~'PEBAX Polyether Block Amide" (December 1987).
The expander member o~ the present invention may contain polyamide. Polyamide materials include nylon 12, nylon 11, nylon 6, nylon 6/6, and nylon 4/6. Such materials are sold under the trademark ZYTEL by Dupont.
The expander member of the present invention may ~urther contain a polymer other than polyesteretheramide copolymer or polyamide, such as polyester copolymer, polyurethane copolymer, polyethylene, and combinations thereo~.
The single polymeric layer making up the expander member may be a blend o~ suitable materials. Such a blend may be created by mixing the desired resins and CA 022l9744 l997-l0-28 W 096/37240 PCT~B96/00291 then extruding these resins to form a parison. The single layer can also be a graft copolymer. Such a graft copolymer can be ~ormed, ~or example, by reacting polyamide (such as Nylon 12) with polyphenylether graft S maleic anhydride (PPE-graft-MA). So called polymer alloys, and the like, are also included within the purview of this application.
The expander member of the present invention may be formed by first generating a parison in an extruder. The parison will typically have an inside diameter of from about .01 to .031 inches (0.025 to 0.079 cm), and a wall thickness of from about .0035 to .015 inches (.0089 to 0.038 cm).
Hot water treated molding devices may then be utilized to blow mold the expander members of the present invention. Tubing of the desired material and having a required size and thickness is inserted into a balloon processing mold and heated to a temperature of from about 200-212~F (93-100~C). Weight may be added to the mold as desired. The tubing is subjected to longitll~;n~1 tension and high-pressure nitrogen 380-500 psi is introduced into the tubing in the mold. The mold rem~; n.q in a hot water bath for a predetermined period of time of from about 10-45 seconds, preferably 25 seconds. The mold is then removed and placed in a cooling pot for a predetermined period of time of ~rom about 20-40 seconds, pre~erably 30 seconds, after which the mold may be opened and the balloon removed.
In an alternative process, the balloons are ~ormed in balloon blow molding machines. The tubing is inserted CA 022l9744 l997-l0-28 W 096/37240 PCT~B96/00291 into the mold and the ends of the tubing secured into mold gaskets. The tubing is thereafter heated in the range of 190-220~F (87-104~C) for about 10 to 45 seconds, preferably 25-30 seconds, and the heated tubing is subjected to longitll~;n~l tension and expanded 1-2 times its length in the axial direction. The stretched tubing is pressurized with nitrogen in the range of about 350-500 psi and heat treated in the mold for about 10-20 seconds at about 250-280~F (121-138~C), preferably about 260-270~F (127-132~C). The mold is then cooled to room temperature and allowed to set at room temperature in the mold under pressure for approximately 10 to 15 seconds.
Thereafter, the system can be depressurized and the balloon removed from the mold.
~ples Balloons were made of polyesteretheramide block copolymer and then tested to determine certain characteristics.
~x~m~les 1-180 180 balloons were made according to the following process:
Parisons of 100 weight percent polyesteretheramide block copolymer were extruded. The parisons had inside diameters of about .015 inches to about .023 inches, wall thicknesses of about .006 inches to about .010 inches, and lengths of about 18 inches.
The parisons were placed in the mold apparatus illustrated in FIGS. 2 and 3. As shown in FIG. 2, the balloon form 8 had a void 10 corresponding to the final shape of the expander member. The void was made up by a W 096/37240 PCT~B96iO~291 proximal form 24, a body form 26, and a distal form 28.
With reference to FIG. 3, the distal end of the parison was inserted into the proximal end 14 of the mold apparatus 12, and pushed through the proximal form 24, the body form 26, and the distal form 28 until it exited the distal end 16 of the mold section. Cap 18 was then placed over the distal end 16 of the apparatus 12 thereby clamping and sealing the distal end of the parison. The mold was then placed in a handle 20 such that the proximal end of the parison freely extended from the handle 20. Weights 22 were then placed over the proximal end of the parison and onto the mold.
The open prox; m~ 1 end of the parison was then connected to a pressurized nitrogen source by a Touhy Borst clamp. The nitrogen source was capable of achieving m~;mllm pressures of 1,000 psi. The nitrogen source was then opened to varying degrees of between 350-500 psi and the mold was placed in a bath of hot water (212~F). The hot water bath warmed the parison. The freely extending proximal end of the parison was held by hand such that only about the distal form 28 was under water, until the mold dropped due to longitudinal stretching and the distal end of the parison expanded radially (about 15-30 seconds). Still holding the mold by hand, the mold continued to drop until it was entirely under water and the proximal end o~ the balloon expanded radially (about an additional 1-10 seconds).
The mold was then removed ~rom the hot water bath and placed in a cold water bath of about 60-75~F ~or W O 96/37240 PCT/Lb9~ ~v291 about 30 seconds. The nitrogen was then shut o~, and the balloon was removed ~rom the mold.
The balloons were tested by attaching the balloons to a pressurized nitrogen source in a 37~C water bath, expanding the balloons under several predetermined pressures o~ nitrogen (50 psi, 100 psi, 150 psi, and burst pressure), and then measuring several ~;men~ions and the burst pressure of the balloons. Dimensions were measured with a snap gauge.
Tables 1-18 below list certain parameters o~ the process utilized to make the subject balloons (hot pot temperature, cold pot temperature, weight added to mold, and nitrogen pressure). The tables also show results of the testing o~ the expander members. K stat was calculated as ~ollows: (Burst pressure)-((K Stat)(Burst Pressure Standard Deviation)). Hoop stress was calculated as ~ollows: (Balloon Burst Pressure) (Balloon Diameter)/(2)(Balloon Wall Thickness).
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W096/37240 PCT~B96100291 Examples 181-206 26 balloons were made according to the process described for Examples 1-180, except that the mold apparatus did not utilize weights 22 separately, but S rather incorporated a preselected weight into handle 20.
The balloons were tested to measure distension and balloon burst strength. Distension is defined as the ratio of two balloon diameters. In this test, a balloon was inflated to a series of pressures. The diameter was measured at each pressure. The distension is the ratio of the diameter at the lowest pressure to the diameter at the highest pressure. Inflation was performed at 1 bar increments up to burst pressure.
To test the balloons, the balloons were first placed in temperature controlled water bath, and warmed for a m; n, mllm of 1 minute in water. The balloons were then attached to a pneumatic inflation/deflation device. A
vacuum was created. Starting with a 4 bar pressure for 20 seconds, the balloon diameter and length were measured. The balloons were deflated, and the measurements were recorded. Increasing the pressure by 1 bar, the balloon diameters and lengths were measured.
This procedure was repeated until the balloons bursted.
The burst pressure and the type of burst profile were recorded.
Tables 19-21 below show the results of the testing of the expander members.
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W O 96/37240 PCT~B96/00291 ~xamples 207-236 30 balloons were made according to the procedure described above ~or Examples 1-180, except that parisons had inside diameters o~ about .025 inches and wall S thicknesses o~ about .0065 inches.
The balloons were tested according to the procedure described above ~or Examples 1-180, except that outside diameters were measured at 1 atm increments from 4-16 atms, and then the balloons were burst.
Tables 22-28 below list certain parameters (PEBAX
grade, dimensions, cone angle, rated burst, and hold time representing the total amount o~ time that the mold was held in the water). The tables also show results o~ the testing o~ the expander members.
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W096/37240 PCT~B96100291 Examples 181-206 26 balloons were made according to the process described for Examples 1-180, except that the mold apparatus did not utilize weights 22 separately, but S rather incorporated a preselected weight into handle 20.
The balloons were tested to measure distension and balloon burst strength. Distension is defined as the ratio of two balloon diameters. In this test, a balloon was inflated to a series of pressures. The diameter was measured at each pressure. The distension is the ratio of the diameter at the lowest pressure to the diameter at the highest pressure. Inflation was performed at 1 bar increments up to burst pressure.
To test the balloons, the balloons were first placed in temperature controlled water bath, and warmed for a m; n, mllm of 1 minute in water. The balloons were then attached to a pneumatic inflation/deflation device. A
vacuum was created. Starting with a 4 bar pressure for 20 seconds, the balloon diameter and length were measured. The balloons were deflated, and the measurements were recorded. Increasing the pressure by 1 bar, the balloon diameters and lengths were measured.
This procedure was repeated until the balloons bursted.
The burst pressure and the type of burst profile were recorded.
Tables 19-21 below show the results of the testing of the expander members.
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W O 96/37240 PCT~B96/00291 ~xamples 207-236 30 balloons were made according to the procedure described above ~or Examples 1-180, except that parisons had inside diameters o~ about .025 inches and wall S thicknesses o~ about .0065 inches.
The balloons were tested according to the procedure described above ~or Examples 1-180, except that outside diameters were measured at 1 atm increments from 4-16 atms, and then the balloons were burst.
Tables 22-28 below list certain parameters (PEBAX
grade, dimensions, cone angle, rated burst, and hold time representing the total amount o~ time that the mold was held in the water). The tables also show results o~ the testing o~ the expander members.
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W 096/37240 PCTAB9~0~291 ~ 4 les 237-266 30 balloons were made according to the procedure described above for Examples 1-180.
The balloons were tested according to the procedure described above for Examples 1-180, except that balloons were tested at 1 atm increments ~rom 4-16 atm and then burst.
Tables 29-35 below list certain parameters (PEBAX
grade, dimensions, cone angle, rated burst, and hold time representing the total amount of time that the mold was held in the water). The tables also show results of the testing of the expander members.
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~x~les 267-276 10 balloons were made according to the procedure described above for Examples 1-180, except that parisons had inside diameters of about .025 inches and wall thicknesses of about .0065 inches.
The balloons were tested according to the procedure described above for Examples 1-180, except that outside diameters were measured at 1 atm increments from 4-16 atms, and then the balloons were burst.
Tables 36-38 below list certain parameters (PEBAX
grade, dimensions, cone angle, rated burst, and hold time representing the total amount of time that the mold was held in the water). The tables also show results of the testing of the expander members.
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~mrles 277-306 30 balloons were made according to the procedure described above for Examples 1-180, except that cone angles were 267 and the parison inside diameter was .025 S inches with a wall thickness of .0065.
The balloons were tested according to the procedure described above for Examples 1-180, except that outside diameters were measured at 1 atm increments from 4-16 atms, and then the balloons were burst.
Tables 39-41 below list certain parameters (PEBAX
grade, dimensions, cone angle, rated burst, and hold time representing the total amount of time that the mold was held in the water). The tables also show results of the testing of the expander members.
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CA 022l9744 l997-l0-28 W 096137240 PCT~B96/00291 F.xi~ es 307-366 60 balloons were made according to the following procedure: Tubing was placed into a mold and preheated for 15-30 seconds to a preselected balloon blowing temperature. The tubing was stretched and inflated to make a balloon. The balloon was allowed to remain at the balloon blowing temperature for 15-30 seconds, and then elevated to at least the crystallization temperature for 10-20 seconds. The balloon was then cooled to room temperature and removed from the mold.
The balloons were tested according to the procedure described above for Examples 1-180.
Tables 42-47 below list certain parameters (PEBAX
grade, dimensions, crystallization temperature, mold temperature, left and right stretch dimensions, nitrogen pressure, and air flow). The tables also show results of the testing of the expander members.
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W 096/37240 PCT~B~G/00291 Figures 4-15 were prepared by collecting data according to material type, and reducing the data to a series of quadratic equations that include stretch, crystallization temperature, and balloon blowing S temperature as dependant variables. The equations were then plotted using a statistical design of experiments program called ECHIP . Response variables of interest were then plotted.
With regard to Figures 4-15, the balloons were expanded to two times their original length in the axial direction.
The foregoing specification and figures are presented for the purpose of illustrating, and not limiting, the present invention.
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W 096/37240 PCTAB9~0~291 ~ 4 les 237-266 30 balloons were made according to the procedure described above for Examples 1-180.
The balloons were tested according to the procedure described above for Examples 1-180, except that balloons were tested at 1 atm increments ~rom 4-16 atm and then burst.
Tables 29-35 below list certain parameters (PEBAX
grade, dimensions, cone angle, rated burst, and hold time representing the total amount of time that the mold was held in the water). The tables also show results of the testing of the expander members.
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~x~les 267-276 10 balloons were made according to the procedure described above for Examples 1-180, except that parisons had inside diameters of about .025 inches and wall thicknesses of about .0065 inches.
The balloons were tested according to the procedure described above for Examples 1-180, except that outside diameters were measured at 1 atm increments from 4-16 atms, and then the balloons were burst.
Tables 36-38 below list certain parameters (PEBAX
grade, dimensions, cone angle, rated burst, and hold time representing the total amount of time that the mold was held in the water). The tables also show results of the testing of the expander members.
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~mrles 277-306 30 balloons were made according to the procedure described above for Examples 1-180, except that cone angles were 267 and the parison inside diameter was .025 S inches with a wall thickness of .0065.
The balloons were tested according to the procedure described above for Examples 1-180, except that outside diameters were measured at 1 atm increments from 4-16 atms, and then the balloons were burst.
Tables 39-41 below list certain parameters (PEBAX
grade, dimensions, cone angle, rated burst, and hold time representing the total amount of time that the mold was held in the water). The tables also show results of the testing of the expander members.
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CA 022l9744 l997-l0-28 W 096137240 PCT~B96/00291 F.xi~ es 307-366 60 balloons were made according to the following procedure: Tubing was placed into a mold and preheated for 15-30 seconds to a preselected balloon blowing temperature. The tubing was stretched and inflated to make a balloon. The balloon was allowed to remain at the balloon blowing temperature for 15-30 seconds, and then elevated to at least the crystallization temperature for 10-20 seconds. The balloon was then cooled to room temperature and removed from the mold.
The balloons were tested according to the procedure described above for Examples 1-180.
Tables 42-47 below list certain parameters (PEBAX
grade, dimensions, crystallization temperature, mold temperature, left and right stretch dimensions, nitrogen pressure, and air flow). The tables also show results of the testing of the expander members.
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W 096/37240 PCT~B~G/00291 Figures 4-15 were prepared by collecting data according to material type, and reducing the data to a series of quadratic equations that include stretch, crystallization temperature, and balloon blowing S temperature as dependant variables. The equations were then plotted using a statistical design of experiments program called ECHIP . Response variables of interest were then plotted.
With regard to Figures 4-15, the balloons were expanded to two times their original length in the axial direction.
The foregoing specification and figures are presented for the purpose of illustrating, and not limiting, the present invention.
Claims (25)
1. A balloon for an angioplasty device having a single polymeric layer comprising (a) from about 20 to about 100 weight percent polyesteretheramide copolymer, and (b) from about 0 to about 80 weight percent polyamide; wherein the polymeric layer contains substantially no polyetheramide having substantially no ester linkages.
2. The balloon of claim 1 wherein the polyesteretheramide copolymer comprises a block copolymer.
3. The balloon of claim 1 wherein the polyesteretheramide copolymer comprises a random copolymer.
4. The balloon of claim 1 wherein the polyesteretheramide copolymer has a hardness of from about 45 Shore D to about 78 Shore D.
5. The balloon of claim 4 wherein the polyesteretheramide copolymer has a hardness of from about 55 Shore D to about 75 Shore D.
6. The balloon of claim 5 wherein the polyesteretheramide copolymer has a hardness of from about 63 to about 72 Shore D.
7. The balloon of claim 6 wherein the polyesteretheramide copolymer has a hardness selected from about 63 Shore D, about 70 Shore D, and about 72 Shore D.
8. The balloon of claim 1 wherein the single polymeric layer comprises at least about 2 weight percent polyamide.
9. The balloon of claim 8 wherein the polyamide is selected from the group consisting of nylon 12, nylon 11, nylon 6, nylon 6/6, nylon 4/6, and combinations thereof.
10. The balloon of claim 9 comprising from about 20 to about 80 weight percent nylon 12 and about 20 to about 80 weight percent polyesteretheramide copolymer.
11. The balloon of claim 10 comprising about 60 weight percent nylon 12 and about 40 weight percent polyesteretheramide copolymer.
12. The balloon of claim 9 comprising from about 25 to about 80 weight percent nylon 4/6 and about 20 to about 75 weight percent polyesteretheramide copolymer.
13. The balloon of claim 12 comprising about 65 weight percent nylon 4/6 and about 35 weight percent polyesteretheramide copolymer.
14. The balloon of claim 1 wherein the single polymeric layer further comprises at least about 2 weight percent of a polymer selected from polyester copolymer, polyurethane copolymer, polyethylene, and combinations thereof.
15. The balloon of claim 1 wherein the polymeric layer comprises at least about 40 weight percent polyesteretheramide copolymer.
16. The balloon of claim 15 wherein the polymeric layer comprises at least about 80 weight percent polyesteretheramide copolymer.
17. A balloon for an angioplasty device having a single polymeric layer consisting essentially of a polyesteretheramide copolymer.
18. The balloon of claim 17 wherein the polyesteretheramide copolymer comprises a block copolymer.
19. The balloon of claim 17 wherein the polyesteretheramide copolymer has a hardness of from about 45 Shore D to about 78 Shore D.
20. The balloon of claim 19 wherein the polyesteretheramide copolymer has a hardness of from about 55 Shore D to about 75 Shore D.
21. The balloon of claim 20 wherein the polyesteretheramide copolymer has a hardness of from about 63 to about 72 Shore D.
22. The balloon of claim 21 wherein the polyesteretheramide copolymer has a hardness selected from about 63 Shore D, about 70 Shore D, and about 72 Shore D.
23. The balloon of claim 17 consisting of a polyesteretheramide copolymer.
24. A balloon for an angioplasty device having a single polymeric layer comprising (a) at least 91 weight percent polyesteretheramide copolymer, (b) from 0 to 9 weight percent polyamide, and (c) from 0 to 9 weight percent of a polymer other than polyesteretheramide and polyamide.
25. The balloon of claim 24 comprising at least about 95 weight percent polyesteretheramide copolymer.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US44904895A | 1995-05-24 | 1995-05-24 | |
US08/449,048 | 1995-05-24 |
Publications (1)
Publication Number | Publication Date |
---|---|
CA2219744A1 true CA2219744A1 (en) | 1996-11-28 |
Family
ID=23782669
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA002219744A Abandoned CA2219744A1 (en) | 1995-05-24 | 1996-04-09 | Dilatation balloons containing polyesteretheramide copolymer |
Country Status (6)
Country | Link |
---|---|
US (1) | US6200290B1 (en) |
EP (1) | EP0828525B1 (en) |
JP (1) | JP3594971B2 (en) |
CA (1) | CA2219744A1 (en) |
DE (1) | DE69633011T2 (en) |
WO (1) | WO1996037240A1 (en) |
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-
1996
- 1996-04-09 DE DE69633011T patent/DE69633011T2/en not_active Expired - Lifetime
- 1996-04-09 WO PCT/IB1996/000291 patent/WO1996037240A1/en active IP Right Grant
- 1996-04-09 JP JP53552196A patent/JP3594971B2/en not_active Expired - Lifetime
- 1996-04-09 EP EP96907611A patent/EP0828525B1/en not_active Expired - Lifetime
- 1996-04-09 CA CA002219744A patent/CA2219744A1/en not_active Abandoned
-
1998
- 1998-03-12 US US09/041,176 patent/US6200290B1/en not_active Expired - Lifetime
Also Published As
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DE69633011T2 (en) | 2004-12-09 |
WO1996037240A1 (en) | 1996-11-28 |
DE69633011D1 (en) | 2004-09-02 |
EP0828525A1 (en) | 1998-03-18 |
JPH10506562A (en) | 1998-06-30 |
US6200290B1 (en) | 2001-03-13 |
MX9709023A (en) | 1998-03-31 |
JP3594971B2 (en) | 2004-12-02 |
EP0828525B1 (en) | 2004-07-28 |
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EEER | Examination request | ||
FZDE | Discontinued |