WO1995016735A1 - Polyethylene therephthalate articles having desirable adhesion and non-blocking characteristics, and a preparative process therefor - Google Patents

Polyethylene therephthalate articles having desirable adhesion and non-blocking characteristics, and a preparative process therefor Download PDF

Info

Publication number
WO1995016735A1
WO1995016735A1 PCT/US1994/013916 US9413916W WO9516735A1 WO 1995016735 A1 WO1995016735 A1 WO 1995016735A1 US 9413916 W US9413916 W US 9413916W WO 9516735 A1 WO9516735 A1 WO 9516735A1
Authority
WO
WIPO (PCT)
Prior art keywords
article
particulate additive
pet
ppm
oriented
Prior art date
Application number
PCT/US1994/013916
Other languages
French (fr)
Inventor
George Joseph Ostapchenko
Original Assignee
E.I. Du Pont De Nemours And Company
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by E.I. Du Pont De Nemours And Company filed Critical E.I. Du Pont De Nemours And Company
Publication of WO1995016735A1 publication Critical patent/WO1995016735A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/34Silicon-containing compounds
    • C08K3/36Silica
    • 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
    • A61L29/00Materials for catheters, medical tubing, cannulae, or endoscopes or for coating catheters
    • A61L29/12Composite materials, i.e. containing one material dispersed in a matrix of the same or different material
    • A61L29/126Composite materials, i.e. containing one material dispersed in a matrix of the same or different material having a macromolecular matrix
    • 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
    • A61L33/00Antithrombogenic treatment of surgical articles, e.g. sutures, catheters, prostheses, or of articles for the manipulation or conditioning of blood; Materials for such treatment
    • A61L33/0094Physical treatment, e.g. plasma treatment
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K9/00Use of pretreated ingredients
    • C08K9/04Ingredients treated with organic substances
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/13Hollow or container type article [e.g., tube, vase, etc.]
    • Y10T428/1334Nonself-supporting tubular film or bag [e.g., pouch, envelope, packet, etc.]
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/13Hollow or container type article [e.g., tube, vase, etc.]
    • Y10T428/1334Nonself-supporting tubular film or bag [e.g., pouch, envelope, packet, etc.]
    • Y10T428/1345Single layer [continuous layer]
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/25Web or sheet containing structurally defined element or component and including a second component containing structurally defined particles
    • Y10T428/259Silicic material
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/31Surface property or characteristic of web, sheet or block
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/31504Composite [nonstructural laminate]
    • Y10T428/31786Of polyester [e.g., alkyd, etc.]

Definitions

  • PET Polyethylene terephthalate
  • Polyethylene terephthalate are derived from the film form. Films are prepared by many techniques well known to the practitioner, including extrusion.
  • polyethylene terephthalate film is molecularly oriented, certain physical properties such as tensile strength, impact strength, flex life, and permeability to water and organic vapors are enhanced.
  • Oriented polyethylene terephthalate is widely used in a variety of industries including electronics (as dielectrics, coverings, and the like), the wire and cable industry (as, for example, filaments and protective sheaths) , fibers, and polymeric articles of manufacture (such as beverage containers) , to name a few. It finds particular application in the medical device field, including medical dilatation products where strength is a critical property.
  • U.S. Re 33,561 relates to medical dilation balloons (balloon catheters) especially useful in medical dilatation procedures.
  • oriented polyethylene terephthalate film is that it is difficult to adhesively bond to other polymeric substrates. Such adhesion is desirable as with Re 33,561 inasmuch as the polymeric balloon must be suitably attached to other medical instruments for insertion into a vessel and surgical manipulation.
  • the surface adhesion properties of oriented polyethylene terephthalate film are improved when it is subjected to surface treatment with, for example, any of the following energy sources: electrical stress accompanied by corona discharge; a flame; a gaseous plasma (such as oxygen, chlorine, etc.); short wave ultraviolet light; and oxidizing chemicals (sulfuric acid dichromate, potassium permanganate, etc.) .
  • the treated surface is generally characterized by measuring the contact angle between a drop of liquid (usually water) and the treated surface, according to conventional techniques.
  • a drop of liquid usually water
  • the Sessile drop technique as reviewed by R. E. Johnson, Jr. and R. H. Dettre, "Surface and Colloid Science", Volume 2, Interscience, New York, NY, 1969 measures advancing and receding contact angles for two chemicals at a given temperature.
  • High contact angle values indicate a low concentration of polar groups (or less adhesion) and low values indicate a high concentration of polar groups (or more adhesion) .
  • Blocking is also known to occur in oriented polyethylene terephthalate articles that have not been surface treated, but only under extremes of temperature and pressure. Any treatment that enhances adhesion to other materials may also contribute sharply to blocking. Blocking can be so severe that when the surfaces are pulled apart, damage is sufficient to render the article unusable.
  • Japanese Application 59 206456 (11/1984); CA 102 (16) :133192k discloses block-resistant oriented polyester films having excellent adhesion to vapor- deposited metals, prepared by polymerizing ethylene glycol and terephthalic acid in the presence of 10-10,000 ppm of powdered kaolinite having a particle size of 0.1-3 micrometers. The resultant polymer was then mixed with 50-20,000 ppm of a fatty amide, melt extruded, cast and biaxially stretched into film.
  • Japanese Application 53 125479 (11/1978); CA 90 (12) :88476b discloses biaxially oriented polyester films containing 80 ppm silica having an average particle diameter of 0.3 micrometer and 20 ppm of kaolin having an average particle diameter of 0.8 micrometer, said films having a peak-to-valley surface roughness of 0.05-0.3 micrometer and excellent block resistance.
  • the present invention provides a surface-treated article of oriented polyethylene terephthalate (PET) exhibiting low self-adhesion and high bondability to other surfaces, consisting essentially of oriented PET and about 100 to about 5000 parts per million (ppm) of a particulate additive uniformly dispersed therein, the additive being chemically inert to PET and having an average particle size in the range of about 0.03 to about 0.6 micrometers.
  • PET polyethylene terephthalate
  • step (b) polymerizing the mixture of step (a) and subsequently isolating a PET/particulate additive product therefrom;
  • step (c) forming an oriented article of the product of step (b) ;
  • the surface-treated, oriented PET article of the invention has increased surface polarity relative to untreated oriented PET and exhibits high bondability to other surfaces.
  • the article nevertheless exhibits low self-adhesion or blocking relative to a surface-treated, oriented PET article containing no particlulate additive.
  • Films and tubes may be prepared by this process, of various sizes and shapes as required by the practioner.
  • medical dilation balloons are advantageously prepared according to Re 33,561, previously referenced, using surface- treated, oriented polyethylene terephthalate film of the present invention.
  • Polyethylene terephthalate is prepared by numerous methods; one such method is according to U.S. 2,465,319 which is incorporated by reference herein. In general, this preparation involves the condensation of ethylene glycol and terphthalic acid. The resulting product in the from of a film is next stretched in longitudinal and atranssverse directions in a manner such as is described in U.S. 2,823,421 (incorporated by reference herein) to provide a biaxially oriented polyethylene terephthalate film. U.S. 2,823,421 is directed to the stretching of polyethylene terephthalate film to produce an oriented product having an outstanding combination of physical, chemical and electrical properties.
  • An extruded, molten amorphous film of polyethylene terephthalate is continuously longitudinally stretched at a rate of at least 400 percent per minute for not more than 3.25 times at a temperature of 80-90°C.
  • the longitudinally stretched film is then preheated at 90-95°C and continuously transversely stretched substantially the same amount and at the same rate at a temperature of 90-110°C, to produce a balanced, biaxially oriented film.
  • the film is finally heat-set at 150-250°C.
  • "surface" is any of the surfaces of the article for which enhanced properties according to this invention is desired. It may be one side of the article or, for example, the inside and outside of a dilation balloon.
  • the "energy source” employed in the surface treatment step (d) may be selected from a wide variety of conventional energy sources used for surface treatment techniques, including, without limitation, electrical stress accompanied by corona discharge; plasma; flame; ultraaaaviolet light; and chemical treatment.
  • Treatment with corona discharge or ultraviolet light can be conducted according to the procedures set forth in Owens, D. K., "The Mechanism of Corona and Ultraviolet Light Induced Self-Adhesion of Poly(ethylene terephthalate) Film", J. Applied Poly. Sci., 2 ⁇ , 3315-3326 (1975) .
  • Corona treatment is also described in Owens, D. K., “The Mechanism of Corona and Ultraviolet Light Induced Self-Adhesion of Poly(ethylene terephthalate) Film", J. Applied Poly. Sci. , ⁇ ), 265-271 (1975) .
  • said additive must be uniformly dispersed within the PET, must be chemically inert towards PET, and have an average particle size in the range of about 0.03 to about 0.6 micrometer, preferably 0.06 to 0.3 micrometer.
  • the particles are preferably but not essentially spherical in shape.
  • the particulate additive should be present in the PET of the invention at a concentration in the range of about 100 to about 5000 parts per million (ppm) , preferably 500 to 2000 ppm.
  • the amount, particle size and particle shape of the particulate additive used in the present process is important not only for the control of self-adhesion in the matrix PET but also for retaining the strength of films and other articles prepared by the process.
  • a preferred particulate additive is silica.
  • Other particulate compounds may be used, however, provided they are of the required particle size and are chemically inert to PET, both under in-use conditions and under conditions of preparation of the PET articles of the invention.
  • the particulate additive is uniformly dispersed within the PET by admixing a dispersion of said additive in ethylene glycol with a polymerization solution of ethylene glycol and an alkyl ester of terephthalic acid, preferably the methyl ester, and then polymerizing said solution in the presence of the additive according to known condensation polymerization methods, such as those described in the references described hereinabove. Appropriate additives will be stable and inert under said polymerization conditions.
  • Sufficient additive dispersion is admixed with the glycol and diester monomers to provide a particulate additive content in the final polymerization product in the range of about 100 ppm to about 5000 ppm, preferably 500 to 2000 ppm.
  • sequential steps (a) and (b) are essential for obtaining a uniform dispersion of particulate additive in the polymer.
  • Post-polymerization addition of particulates to polymer does not provide adequately uniform distribution of particles within the polymer for purposes of this invention.
  • the present process is also believed to result in the complete encapsulation of the additive particles within the polymer, so that no free additive is present in the surface of the final polymeric article.
  • U.S. Re 33,561 which is incorporated by reference herein provides for balloon catheters useful for the relief of arterial stenosis and other ailments requiring a surgical procedure involving insertion of an instrument into blood vessels or body cavities. These balloons are effective in that they have thin walls which are flexible, readily collapsible and easily transportable within the body. Other physical properties include minimal radial expansion on inflation, and high burst strength (with any rupture confined to the axial direction to ensure against traumatic removal) , among other attributes making these balloons effective for a number of medical procedures .
  • the flexible balloon be made of a high molecular weight, biaxially oriented polymer having a burst pressure of at least 200 psi (1.4 MPa) and a radial expansion of less than 5 percent at 200 psi (1.4 MPa) .
  • balloon failure is the desired mode of failure.
  • protective coatings such as, for example, silicone coatings, applied to the outer surface of dilation balloons for improved abrasion resistance, adhere adequately to the surface treated, oriented polyethylene terephthalate balloons of this invention but not to untreated, oriented polyethylene terephthalate balloons .
  • particulate additive in the articles of the present invention provides anti-blocking properties without in any way impairing bondability of said articles to other surfaces.
  • PET resin having an intrinsic viscosity of about 1, a density of 1.41 g/cm 3 , and a diethylene glycol content of about 2 weight percent, was dried to less than 0.005 weight percent water at 177°C and then processed into single lumen tubing having an outside diameter of 0.34 mm and a wall thickness of 0.064 mm, using conventional tubing extrusion technique.
  • Biaxially oriented balloons having an outside diameter of 3 mm, a single wall thickness of 0.0076 mm and a cylindrical length of 2 cm were fabricated from the extruded tubing using the process of U.S. Patent No. Re 33,561, and then plasma treated in an oxygen atmosphere maintained at a pressure between 13 and 130 Pa in a Gasonics/IPC Model 7102 Plasma Treater for 8 minutes at 300 watts and 13.56 MHz.
  • Ten plasma-treated balloons were tested for blocking by connecting the proximal end of a balloon to a Tuohy-Borst adapter and then heat sealing the distal end with an electrical heating element.
  • the Tuohy-Borst adapter with the sealed balloon attached was then connected to a commercial "PRESTO" inflation device (C. R. Bard, Inc. USC Division), that had been de- aerated as much as possible and contained 4 cm 3 of distilled water.
  • the plunger was pulled to its limit to remove air from the balloon; the balloon was evacuated to a pressure of about 16 KPa.
  • the screw plunger was pushed and rotated to achieve a pressure of 1300 KPa.
  • This pressure was held for one minute while the balloon was checked for leaks. If no leaks were found, the plunger was pulled to its limit, again with the pressure device pointing down, to achieve a balloon pressure of about 16 KPa. While ensuring that the balloon had been completely deflated, this pressure was held for 20 minutes.
  • the balloon was then reinflated to a pressure of 1200 KPa as quickly as possible and maintained at that pressure for one minute while the balloon was checked for leaks.
  • the balloon pressure was returned to atmospheric and the Tuohy-Borst adapter and balloon were disconnected from the inflation device.
  • the inside surface of the balloon was then examined for delamination caused by blocking, using a stereo polarizing microscope. Changes in balloon wall thickness as a result of delamination were evident as localized differences in retardation colors when viewed between crossed Polaroid's (step A) . If blocking was not observed, the Tuohy-Borst adapter with balloon was reattached to the inflation device and the vacuum-pressure-vacuum cycle was repeated except that the final vacuum was held for 40 minutes.
  • the balloon was again checked for leaks at 1200 KPa and re-inspected for delamination using the stereo polarizing microscope (step B) . If blocking was not observed, the vacuum-pressure-vacuum cycle was again repeated except that the final vacuum was held for 140 minutes. The balloons were again checked for leaks and delamination (step C) .
  • a Blocking Tendency value was obtained by assigning a value of 10 (100 divided by the number of balloons tested) to balloons that failed at step A, 5 (50 divided by the number of balloons tested) to balloons that failed at step B and 1 (10 divided by the number of balloons tested) to balloons that failed at step C.
  • a Blocking Tendency value of 100 indicates all balloons failed at step A, and a value of 0 indicates that all balloons survived all three steps .
  • EXAMPLE 1 Balloons were fabricated using a PET resin having essentially the same properties as in the results of the Procedure section, except the resin contained 1230 ppm of spherical silica particles having an average particle size of 0.3 micrometer.
  • the silica particles were added as a slurry in ethylene glycol (Nippon Shokubai "Seahostar” KE-E30) to the mixture of ethylene glycol and dimethyl terephthalate monomers before polymerization.
  • the average burst strength of 20 balloons was 2014 KPa with a standard deviation of 88 KPa.
  • the Blocking Tendency value for 10 plasma- treated balloons was 0.
  • EXAMPLE 2 Balloons were fabricated using a PET resin having essentially the same properties as in the results of the Procedure section, except that the resin contained 825 ppm of spherical silica particles having an average particle size of 0.3 micrometer. The silica particles were added as a slurry in ethylene glycol (Nippon
  • spherical silica particles having an average particle size of 0.2 micrometer.
  • the silica particles were added as a slurry in ethylene glycol (Nippon Shokubai "Seahostar” KE-E20) to the mixture of ethylene glycol and dimethyl terephthalate monomers before polymerization.
  • the average burst strength of 20 balloons was 2093 KPa with a standard deviation of 79 KPa.
  • the Blocking Tendency value for 10 plasma treated balloons was 1.
  • Balloons were fabricated using a PET resin having essentially the same properties as in the results of the Procedure section, except that the resin contained 920 ppm of spherical silica particles having an average particle size of 0.2 micrometer.
  • the silica particles were added as a slurry in ethylene glycol (Nippon Shokubai "Seahostar” KE-E20) to the mixture of ethylene glycol and dimethyl terephthalate monomers before polymerization.
  • the average burst strength of 20 balloons was 1937 KPa with a standard deviation of 71 KPa.
  • the Blocking Tendency value for 10 plasma treated balloons was 4.
  • Balloons were fabricated using a PET resin having essentially the same properties as in the results of the Procedure section, except that the resin contained 1554 ppm of spherical silica particles having an average particle size of 0.06 micrometers.
  • the silica particles were added as a slurry in ethylene glycol (Philadelphia Quartz Co.'s Silica Dispersion DP5480) to the mixture of ethylene glycol and dimethyl terephthalate monomers before polymerization.
  • the average burst strength of 20 balloons was 1937 KPa with a standard deviation of 71 KPa.
  • the Blocking Tendency value for 10 plasma treated balloons was .

Abstract

Surface treated articles of polyethylene terephthalate (PET) are disclosed having low self-adhesion and high bondability to other surfaces. The articles comprise oriented PET and about 100-5000 ppm of a particulate additive uniformly dispersed therein. The additive is chemically inert to PET and has an average particle size of about 0.03 to 0.6 micrometers. A process for the preparation of such articles is also disclosed.

Description

TITLE
POLYETHYLENE TEREPHTHALATE ARTICLES HAVING
DESIRABLE ADHESION AND NON-BLOCKING CHARACTERISTICS,
AND A PREPARATIVE PROCESS THEREFOR BACKGROUND OF THE INVENTION
Polyethylene terephthalate (PET) has been demonstrated as an effective polymer for a wide variety of products. Its properties of strength, durability and the like make it suitable for any number of applications, from filaments and fibers to beverage containers .
Many uses of polyethylene terephthalate are derived from the film form. Films are prepared by many techniques well known to the practitioner, including extrusion.
Moreover, if the polyethylene terephthalate film is molecularly oriented, certain physical properties such as tensile strength, impact strength, flex life, and permeability to water and organic vapors are enhanced. Oriented polyethylene terephthalate is widely used in a variety of industries including electronics (as dielectrics, coverings, and the like), the wire and cable industry (as, for example, filaments and protective sheaths) , fibers, and polymeric articles of manufacture (such as beverage containers) , to name a few. It finds particular application in the medical device field, including medical dilatation products where strength is a critical property. For example, U.S. Re 33,561 relates to medical dilation balloons (balloon catheters) especially useful in medical dilatation procedures.
One limitation to oriented polyethylene terephthalate film is that it is difficult to adhesively bond to other polymeric substrates. Such adhesion is desirable as with Re 33,561 inasmuch as the polymeric balloon must be suitably attached to other medical instruments for insertion into a vessel and surgical manipulation. The surface adhesion properties of oriented polyethylene terephthalate film are improved when it is subjected to surface treatment with, for example, any of the following energy sources: electrical stress accompanied by corona discharge; a flame; a gaseous plasma (such as oxygen, chlorine, etc.); short wave ultraviolet light; and oxidizing chemicals (sulfuric acid dichromate, potassium permanganate, etc.) . The treated surface is generally characterized by measuring the contact angle between a drop of liquid (usually water) and the treated surface, according to conventional techniques. For example, the Sessile drop technique as reviewed by R. E. Johnson, Jr. and R. H. Dettre, "Surface and Colloid Science", Volume 2, Interscience, New York, NY, 1969 measures advancing and receding contact angles for two chemicals at a given temperature. High contact angle values indicate a low concentration of polar groups (or less adhesion) and low values indicate a high concentration of polar groups (or more adhesion) .
However, a consequence of such surface treatment procedures is that while adhesion of the oriented polyethylene terephthalate film to other materials improves, the film undesirably adheres to itself when two such treated surfaces contact one another. This self-adhesion phenomenon, known as blocking, can occur, for example, when films are stacked for storage, when folds of dilation balloons are tightly wrapped together, or when filaments are pinched together. Blocking tendency is enhanced under high humidity conditions and moderate pressure during storage.
Blocking is also known to occur in oriented polyethylene terephthalate articles that have not been surface treated, but only under extremes of temperature and pressure. Any treatment that enhances adhesion to other materials may also contribute sharply to blocking. Blocking can be so severe that when the surfaces are pulled apart, damage is sufficient to render the article unusable.
D. K. Owens, J. Applied Polymer Sci., 19, 3315 (1975) showed that oriented polyethylene terephthalate film after corona or untraviolet radiation treatment exhibits strong self-adhesion under bonding conditions where no adhesion occurs with untreated film. Self- adhesion was shown to be reversibly reduced by the application of hydrogen-bonding liquids to the film surface, or by chemical reaction of the polar groups present on the radiation-treated surface.
R. K. Her, in "The Chemistry of Silica", John Wiley & Sons, Inc., 1979, pp. 428, 429, 578, 587, discloses that coloidal silica, silica gels or silica powders incorporated with polymers can reduce self- adhesion or blocking of the polymer. Small particles of silica on the surface of a polyester film are said to act as spacers, preventing sticking and blocking. Antiblocking in polymer films can be attained by adding fine particulate silica to the mixed monomers before polymerization; 0.5% silica, based on polymer, allegedly reduces self-adhesion by 50% .
Japanese Application 59 206456 (11/1984); CA 102 (16) :133192k discloses block-resistant oriented polyester films having excellent adhesion to vapor- deposited metals, prepared by polymerizing ethylene glycol and terephthalic acid in the presence of 10-10,000 ppm of powdered kaolinite having a particle size of 0.1-3 micrometers. The resultant polymer was then mixed with 50-20,000 ppm of a fatty amide, melt extruded, cast and biaxially stretched into film. Japanese Application 53 125479 (11/1978); CA 90 (12) :88476b discloses biaxially oriented polyester films containing 80 ppm silica having an average particle diameter of 0.3 micrometer and 20 ppm of kaolin having an average particle diameter of 0.8 micrometer, said films having a peak-to-valley surface roughness of 0.05-0.3 micrometer and excellent block resistance.
G. J. L. Griffin, Appl. Polym. Symp. , No. 16, 1971 67-86; C.A. 75, 130413w discloses that the incorporation of particulate silica antiblocking additive into low density polyethylene extruded film produces numerous small protuberances in the film surface and that the polymer has lower solubility in the regions of the protuberances. It remains a desirable goal to provide an oriented polyester film that not only exhibits strong antiblocking characteristics, but can also be strongly bonded to the surfaces of other materials .
SUMMARY OF THE INVENTION The present invention provides a surface-treated article of oriented polyethylene terephthalate (PET) exhibiting low self-adhesion and high bondability to other surfaces, consisting essentially of oriented PET and about 100 to about 5000 parts per million (ppm) of a particulate additive uniformly dispersed therein, the additive being chemically inert to PET and having an average particle size in the range of about 0.03 to about 0.6 micrometers.
Also provided is a process for preparing an article of oriented polyethylene terephthalate exhibiting low self-adhesion and high bondability to other surfaces, comprising:
(a) admixing with a polymerization solution comprising an alkyl ester of terephthalic acid and ethylene glycol a particulate additive uniformly dispersed in ethylene glycol, the additive being chemically inert under polymerization conditions and having an average particle size in the range of about 0.03 to about 0.6 micrometers, in an amount sufficient to provide a particulate additive content in the polymerization product in the range of about 100 ppm to about 5000 ppm;
(b) polymerizing the mixture of step (a) and subsequently isolating a PET/particulate additive product therefrom;
(c) forming an oriented article of the product of step (b) ; and
(d) treating a surface of the oriented article with an energy source to increase the polarity of the surface.
The surface-treated, oriented PET article of the invention has increased surface polarity relative to untreated oriented PET and exhibits high bondability to other surfaces. The article nevertheless exhibits low self-adhesion or blocking relative to a surface-treated, oriented PET article containing no particlulate additive.
Many different articles of manufacture are contemplated for preparation according to the process of the invention. Films and tubes may be prepared by this process, of various sizes and shapes as required by the practioner. In the field of medical devices, medical dilation balloons are advantageously prepared according to Re 33,561, previously referenced, using surface- treated, oriented polyethylene terephthalate film of the present invention.
DETAILED DESCRIPTION OF THE INVENTION
Polyethylene terephthalate is prepared by numerous methods; one such method is according to U.S. 2,465,319 which is incorporated by reference herein. In general, this preparation involves the condensation of ethylene glycol and terphthalic acid. The resulting product in the from of a film is next stretched in longitudinal and atranssverse directions in a manner such as is described in U.S. 2,823,421 (incorporated by reference herein) to provide a biaxially oriented polyethylene terephthalate film. U.S. 2,823,421 is directed to the stretching of polyethylene terephthalate film to produce an oriented product having an outstanding combination of physical, chemical and electrical properties. An extruded, molten amorphous film of polyethylene terephthalate is continuously longitudinally stretched at a rate of at least 400 percent per minute for not more than 3.25 times at a temperature of 80-90°C. The longitudinally stretched film is then preheated at 90-95°C and continuously transversely stretched substantially the same amount and at the same rate at a temperature of 90-110°C, to produce a balanced, biaxially oriented film. The film is finally heat-set at 150-250°C. In the surface treatment step (d) , "surface" is any of the surfaces of the article for which enhanced properties according to this invention is desired. It may be one side of the article or, for example, the inside and outside of a dilation balloon. The "energy source" employed in the surface treatment step (d) may be selected from a wide variety of conventional energy sources used for surface treatment techniques, including, without limitation, electrical stress accompanied by corona discharge; plasma; flame; ultraaaaviolet light; and chemical treatment.
Treatment with corona discharge or ultraviolet light can be conducted according to the procedures set forth in Owens, D. K., "The Mechanism of Corona and Ultraviolet Light Induced Self-Adhesion of Poly(ethylene terephthalate) Film", J. Applied Poly. Sci., 2Λ, 3315-3326 (1975) . Corona treatment is also described in Owens, D. K., "The Mechanism of Corona and Ultraviolet Light Induced Self-Adhesion of Poly(ethylene terephthalate) Film", J. Applied Poly. Sci. , ϋ), 265-271 (1975) .
A discussion of surface treatment using plasma appears in Rose, P. W. and Kaplon, S. L. "Plasma Treatment", Plastics Finishing and Decoration,. Van Nostrand Reinhold Company, 1986. Preferably, surface treatment using plasma is conducted for less than about 16 minutes and at less than 300 watts. U.S. 3,431,135 and U.S. 3,153,683 review the fundamentals of flame treatment . Any of a variety of chemicals may be used for their surface treating properties. Such chemicals are selected according to the desired result, as will be readily appreciated by those skilled in the art.
With respect to the particulate additive present in the PET of the invention, said additive must be uniformly dispersed within the PET, must be chemically inert towards PET, and have an average particle size in the range of about 0.03 to about 0.6 micrometer, preferably 0.06 to 0.3 micrometer. The particles are preferably but not essentially spherical in shape.
The particulate additive should be present in the PET of the invention at a concentration in the range of about 100 to about 5000 parts per million (ppm) , preferably 500 to 2000 ppm.
The amount, particle size and particle shape of the particulate additive used in the present process is important not only for the control of self-adhesion in the matrix PET but also for retaining the strength of films and other articles prepared by the process. Of particular interest herein is the preparation of medical dilation balloons wherein balloon burst strength as well as adhesive properties is particularly important. A preferred particulate additive is silica. Other particulate compounds may be used, however, provided they are of the required particle size and are chemically inert to PET, both under in-use conditions and under conditions of preparation of the PET articles of the invention.
In step (a) of the present process for preparing articles of the invention, the particulate additive is uniformly dispersed within the PET by admixing a dispersion of said additive in ethylene glycol with a polymerization solution of ethylene glycol and an alkyl ester of terephthalic acid, preferably the methyl ester, and then polymerizing said solution in the presence of the additive according to known condensation polymerization methods, such as those described in the references described hereinabove. Appropriate additives will be stable and inert under said polymerization conditions. Sufficient additive dispersion is admixed with the glycol and diester monomers to provide a particulate additive content in the final polymerization product in the range of about 100 ppm to about 5000 ppm, preferably 500 to 2000 ppm.
In the process of the invention, sequential steps (a) and (b) are essential for obtaining a uniform dispersion of particulate additive in the polymer.
Post-polymerization addition of particulates to polymer does not provide adequately uniform distribution of particles within the polymer for purposes of this invention. The present process is also believed to result in the complete encapsulation of the additive particles within the polymer, so that no free additive is present in the surface of the final polymeric article.
U.S. Re 33,561 which is incorporated by reference herein provides for balloon catheters useful for the relief of arterial stenosis and other ailments requiring a surgical procedure involving insertion of an instrument into blood vessels or body cavities. These balloons are effective in that they have thin walls which are flexible, readily collapsible and easily transportable within the body. Other physical properties include minimal radial expansion on inflation, and high burst strength (with any rupture confined to the axial direction to ensure against traumatic removal) , among other attributes making these balloons effective for a number of medical procedures . The patent requires that the flexible balloon be made of a high molecular weight, biaxially oriented polymer having a burst pressure of at least 200 psi (1.4 MPa) and a radial expansion of less than 5 percent at 200 psi (1.4 MPa) .
In experiments with medical dilation balloon catheters, it has been found that adequate adhesion of the surface treated, oriented polyethylene terephthalate articles of the invention to other surfaces, particularly polymeric surfaces such as polyethylene, requires use of an adhesive. Suitable adhesives are commercially available products such as, for example, ultraviolet light-curable acrylic adhesives. Such adhesives are well known to those skilled in the art. Destructive testing of dilation balloon catheters has shown that adhesive bonding of surface treated, oriented polyethylene terephthalate directly to polyethylene without use of an adhesive, or adhesive bonding of untreated, oriented polyethylene terephthalate to polyethylene with an adhesive, each results in bond failure rather than balloon failure. Use of an adhesive in bonding surface treated balloons of the present invention to polyethylene results in balloon failure rather than bond failure in destructive testing; balloon failure is the desired mode of failure. It has also been observed that protective coatings, such as, for example, silicone coatings, applied to the outer surface of dilation balloons for improved abrasion resistance, adhere adequately to the surface treated, oriented polyethylene terephthalate balloons of this invention but not to untreated, oriented polyethylene terephthalate balloons .
The presence of particulate additive in the articles of the present invention provides anti-blocking properties without in any way impairing bondability of said articles to other surfaces.
Although numerous applications are envisaged for PET oriented, surface-treated articles of the invention that are at once relatively non-blocking yet adherable to other surfaces, the following specific embodiments relate to medical dilation balloons. However, it will be clear to those of ordinary skill in the art that the non-blocking and adhesive properties demonstrated for the dilation balloons can be achieved with oriented PET articles prepared for different uses by the process of the invention.
EXAMPLES PROCEDURE
The following illustrates the general procedure used in the examples of the invention, except that no particulate additive was present. The results of this procedure section provide a basis of comparison for the examples wherein particulate additive is present.
Polyethylene terephthalate (PET) resin having an intrinsic viscosity of about 1, a density of 1.41 g/cm3, and a diethylene glycol content of about 2 weight percent, was dried to less than 0.005 weight percent water at 177°C and then processed into single lumen tubing having an outside diameter of 0.34 mm and a wall thickness of 0.064 mm, using conventional tubing extrusion technique. Biaxially oriented balloons having an outside diameter of 3 mm, a single wall thickness of 0.0076 mm and a cylindrical length of 2 cm were fabricated from the extruded tubing using the process of U.S. Patent No. Re 33,561, and then plasma treated in an oxygen atmosphere maintained at a pressure between 13 and 130 Pa in a Gasonics/IPC Model 7102 Plasma Treater for 8 minutes at 300 watts and 13.56 MHz.
Twenty balloons were tested for burst pressure by measuring the balloon pressure at which failure occurred, resulting in an average value of 1937 KPa with a standard deviation of 71 KPa.
Ten plasma-treated balloons were tested for blocking by connecting the proximal end of a balloon to a Tuohy-Borst adapter and then heat sealing the distal end with an electrical heating element. The Tuohy-Borst adapter with the sealed balloon attached was then connected to a commercial "PRESTO" inflation device (C. R. Bard, Inc. USC Division), that had been de- aerated as much as possible and contained 4 cm3 of distilled water. With the inflation device pointed down, the plunger was pulled to its limit to remove air from the balloon; the balloon was evacuated to a pressure of about 16 KPa. With the balloon evacuated, the screw plunger was pushed and rotated to achieve a pressure of 1300 KPa. This pressure was held for one minute while the balloon was checked for leaks. If no leaks were found, the plunger was pulled to its limit, again with the pressure device pointing down, to achieve a balloon pressure of about 16 KPa. While ensuring that the balloon had been completely deflated, this pressure was held for 20 minutes.
The balloon was then reinflated to a pressure of 1200 KPa as quickly as possible and maintained at that pressure for one minute while the balloon was checked for leaks. The balloon pressure was returned to atmospheric and the Tuohy-Borst adapter and balloon were disconnected from the inflation device. The inside surface of the balloon was then examined for delamination caused by blocking, using a stereo polarizing microscope. Changes in balloon wall thickness as a result of delamination were evident as localized differences in retardation colors when viewed between crossed Polaroid's (step A) . If blocking was not observed, the Tuohy-Borst adapter with balloon was reattached to the inflation device and the vacuum-pressure-vacuum cycle was repeated except that the final vacuum was held for 40 minutes. The balloon was again checked for leaks at 1200 KPa and re-inspected for delamination using the stereo polarizing microscope (step B) . If blocking was not observed, the vacuum-pressure-vacuum cycle was again repeated except that the final vacuum was held for 140 minutes. The balloons were again checked for leaks and delamination (step C) .
All ten balloons passed step A. Six balloons failed at step B, and the remaining four balloons failed at step C.
A Blocking Tendency value was obtained by assigning a value of 10 (100 divided by the number of balloons tested) to balloons that failed at step A, 5 (50 divided by the number of balloons tested) to balloons that failed at step B and 1 (10 divided by the number of balloons tested) to balloons that failed at step C. A Blocking Tendency value of 100 indicates all balloons failed at step A, and a value of 0 indicates that all balloons survived all three steps . A Blocking Tendency value of 34 (6 balloons x 5 plus 4 balloons x 1 = 34) was obtained. EXAMPLE 1 Balloons were fabricated using a PET resin having essentially the same properties as in the results of the Procedure section, except the resin contained 1230 ppm of spherical silica particles having an average particle size of 0.3 micrometer. The silica particles were added as a slurry in ethylene glycol (Nippon Shokubai "Seahostar" KE-E30) to the mixture of ethylene glycol and dimethyl terephthalate monomers before polymerization. The average burst strength of 20 balloons was 2014 KPa with a standard deviation of 88 KPa. The Blocking Tendency value for 10 plasma- treated balloons was 0.
EXAMPLE 2 Balloons were fabricated using a PET resin having essentially the same properties as in the results of the Procedure section, except that the resin contained 825 ppm of spherical silica particles having an average particle size of 0.3 micrometer. The silica particles were added as a slurry in ethylene glycol (Nippon
Shokubai "Seahostar" KE-E30) to the mixture of ethylene glycol and dimethyl terephthalate monomers before polymerization. The average burst strength of 20 balloons was 2068 KPa with a standard deviation of 73 KPa. The Blocking Tendency value for 10 plasma treated balloons was 1.
EXAMPLE 3
Balloons were fabricated using a PET resin having essentially the same properties as in the results of the Procedure section, except that the resin contained
545 ppm of spherical silica particles having an average particle size of 0.2 micrometer. The silica particles were added as a slurry in ethylene glycol (Nippon Shokubai "Seahostar" KE-E20) to the mixture of ethylene glycol and dimethyl terephthalate monomers before polymerization. The average burst strength of 20 balloons was 2093 KPa with a standard deviation of 79 KPa. The Blocking Tendency value for 10 plasma treated balloons was 1. EXAMPLE 4
Balloons were fabricated using a PET resin having essentially the same properties as in the results of the Procedure section, except that the resin contained 920 ppm of spherical silica particles having an average particle size of 0.2 micrometer. The silica particles were added as a slurry in ethylene glycol (Nippon Shokubai "Seahostar" KE-E20) to the mixture of ethylene glycol and dimethyl terephthalate monomers before polymerization. The average burst strength of 20 balloons was 1937 KPa with a standard deviation of 71 KPa. The Blocking Tendency value for 10 plasma treated balloons was 4.
EXAMPLE 5
Balloons were fabricated using a PET resin having essentially the same properties as in the results of the Procedure section, except that the resin contained 1554 ppm of spherical silica particles having an average particle size of 0.06 micrometers. The silica particles were added as a slurry in ethylene glycol (Philadelphia Quartz Co.'s Silica Dispersion DP5480) to the mixture of ethylene glycol and dimethyl terephthalate monomers before polymerization. The average burst strength of 20 balloons was 1937 KPa with a standard deviation of 71 KPa. The Blocking Tendency value for 10 plasma treated balloons was .

Claims

£ MM£ 1. A surface-treated article of polyethylene terephthalate (PET) exhibiting low self-adhesion and high bondability to other surfaces, consisting essentially of oriented PET and about 100 to about
5000 parts per million (ppm) of a particulate additive uniformly dispersed therein, said additive being chemically inert to PET and having an average particle size in the range of about 0.03 to about 0.6 micrometer.
2. The article according to Claim 1 wherein the particulate additive is present in the range of 500 to 2000 ppm.
3. The article according to Claim 1 wherein the particulate additive has an average particle size in the range of 0.06 to 0.3 micrometer.
4. The article according to Claim 1 wherein the particulate additive consists of particles which are essentially spherical.
5. The article according to Claim 1 wherein the particulate additive is silica.
6. The article according to Claim 1 in the form of a film.
7. The article according to Claim 1 wherein the PET is biaxially oriented.
8. The article according to Claim 1 in the form of a tube.
9. The article according to Claim 1 in the form of a medical dilation balloon.
10. The article according to Claim 9 having a Blocking Tendency Value (BTV) of less than 10.
11. The article according to Claim 10 having a BTV of less than 5.
12. A process for preparing an article of oriented polyethylene terephthalate (PET) exhibiting low self- adhesion and high bondability to other surfaces, comprising:
(a) admixing with a polymerization solution comprising an alkyl ester of terephthalic acid and ethylene glycol, a particulate additive uniformly dispersed in ethylene glycol, said additive being chemically inert under polymerization conditions and having an average particle size in the range of about 0.03 to about 0.6 micrometers, in an amount sufficient to provide a particulate additive content in the polymerization product in the range of about 100 ppm to about 5000 ppm;
(b) polymerizing the mixture of step (a) and subsequently isolating a PET/particulate additive product therefrom;
(c) forming an oriented article of the product of step (b) ; and
(d) treating a surface of the oriented article with an energy source to increase the polarity of said surface.
13. The process according to Claim 12 wherein, in step (c) , the article is biaxially oriented.
14. The process according to Claim 12 wherein the particulate additive is present in the range of 500 to 2000 ppm.
15. The process according to Claim 12 wherein the average particle size of the particulate additive is in the range of 0.06 to 0.3 micrometers.
16. The process according to Claim 12 wherein the particulate additive consists of particles which are essentially spherical.
17. The process according to Claim 12 wherein the particulate additive is silica.
18. The process according to Claim 12 wherein the energy source of step (d) is selected from the group consisting of electrical stress accompanied by corona discharge, plasma, flame, ultraviolet light and chemical reaction.
19. The process according to Claim 18 wherein the energy source is plasma.
20. The process according to Claim 19 wherein, in step (d) , the surface is treated with plasma for less than about 16 minutes and at less than about 300 watts.
21. A film prepared according to the process of Claim 12.
22. A tube prepared according to the process of Claim 12.
23. A medical dilation balloon prepared according to the process of Claim 12.
24. The medical dilation balloon according to
Claim 23 having a Blocking Tendency Value (BTV) of less than 10.
25. The medical dilation balloon according to Claim 24 having a BTV of less than 5.
PCT/US1994/013916 1993-12-17 1994-12-14 Polyethylene therephthalate articles having desirable adhesion and non-blocking characteristics, and a preparative process therefor WO1995016735A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US16944893A 1993-12-17 1993-12-17
US08/169,448 1993-12-17

Publications (1)

Publication Number Publication Date
WO1995016735A1 true WO1995016735A1 (en) 1995-06-22

Family

ID=22615748

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US1994/013916 WO1995016735A1 (en) 1993-12-17 1994-12-14 Polyethylene therephthalate articles having desirable adhesion and non-blocking characteristics, and a preparative process therefor

Country Status (2)

Country Link
US (1) US5721023A (en)
WO (1) WO1995016735A1 (en)

Families Citing this family (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE60036113T2 (en) * 1999-07-22 2007-12-06 JohnsonDiversey, Inc., Sturtevant LUBRICANT COMPOSITION FOR LUBRICATING A TRANSPORT SYSTEM
ES2378848T3 (en) 1999-08-16 2012-04-18 Ecolab Inc. Method for lubricating the passage of a container along a conveyor system
US6427826B1 (en) 1999-11-17 2002-08-06 Ecolab Inc. Container, such as a food or beverage container, lubrication method
US6495494B1 (en) * 2000-06-16 2002-12-17 Ecolab Inc. Conveyor lubricant and method for transporting articles on a conveyor system
US7384895B2 (en) * 1999-08-16 2008-06-10 Ecolab Inc. Conveyor lubricant, passivation of a thermoplastic container to stress cracking and thermoplastic stress crack inhibitor
DE19942534A1 (en) 1999-09-07 2001-03-08 Henkel Ecolab Gmbh & Co Ohg Lubricants containing fluorine
US7364033B2 (en) * 1999-11-17 2008-04-29 Ecolab Inc. Container, such as a food or beverage container, lubrication method
US6806240B1 (en) 2000-08-14 2004-10-19 Ecolab Inc. Conveyor lubricant, passivation of a thermoplastic container to stress cracking, and thermoplastics stress crack inhibitor
US6576298B2 (en) 2000-09-07 2003-06-10 Ecolab Inc. Lubricant qualified for contact with a composition suitable for human consumption including a food, a conveyor lubrication method and an apparatus using droplets or a spray of liquid lubricant
US6509302B2 (en) 2000-12-20 2003-01-21 Ecolab Inc. Stable dispersion of liquid hydrophilic and oleophilic phases in a conveyor lubricant
US20030114831A1 (en) * 2001-12-14 2003-06-19 Scimed Life Systems, Inc. Catheter having improved curve retention and method of manufacture
US6790213B2 (en) 2002-01-07 2004-09-14 C.R. Bard, Inc. Implantable prosthesis
US8048093B2 (en) * 2003-12-19 2011-11-01 Boston Scientific Scimed, Inc. Textured balloons
US7745381B2 (en) 2005-03-15 2010-06-29 Ecolab Inc. Lubricant for conveying containers
US7741257B2 (en) 2005-03-15 2010-06-22 Ecolab Inc. Dry lubricant for conveying containers
US7727941B2 (en) * 2005-09-22 2010-06-01 Ecolab Inc. Silicone conveyor lubricant with stoichiometric amount of an acid
US7915206B2 (en) * 2005-09-22 2011-03-29 Ecolab Silicone lubricant with good wetting on PET surfaces
US20070073328A1 (en) * 2005-09-26 2007-03-29 Wilson-Cook Medical Inc., Incrementally expandable balloon
US7741255B2 (en) * 2006-06-23 2010-06-22 Ecolab Inc. Aqueous compositions useful in filling and conveying of beverage bottles wherein the compositions comprise hardness ions and have improved compatibility with pet
KR101500019B1 (en) * 2007-02-07 2015-03-09 키모토 컴파니 리미티드 Material for electroless plating, coating liquid for catalyst adhesion, electroless plating method, and plating method
ES2859624T3 (en) 2008-10-03 2021-10-04 Bard Inc C R Implantable prosthesis
SI23021A (en) * 2009-04-20 2010-10-29 Institut "Jožef Stefan" Method of treatment of biomedical polymeric prostheses for improvement of their antithrombogenous properties
CN104987944A (en) 2010-09-24 2015-10-21 艺康美国股份有限公司 Conveyor lubricants including emulsions and methods employing them
WO2014164468A1 (en) 2013-03-11 2014-10-09 Ecolab Usa Inc. Lubrication of transfer plates using an oil or oil in water emulsions
WO2015072364A1 (en) * 2013-11-12 2015-05-21 株式会社シンク・ラボラトリー Non-conductive antibacterial sheet, process for manufacturing same and method for inhibiting the growth of bacteria

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0261430A2 (en) * 1986-08-27 1988-03-30 Teijin Limited Biaxially oriented polyester film
USRE33561E (en) * 1983-07-05 1991-03-26 E. I. Du Pont De Nemours And Company Balloon and manufacture thereof
EP0506033A1 (en) * 1991-03-28 1992-09-30 Diafoil Hoechst Co., Ltd. Polyester film

Family Cites Families (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE288162C (en) *
US2465319A (en) * 1941-07-29 1949-03-22 Du Pont Polymeric linear terephthalic esters
US2823421A (en) * 1952-05-12 1958-02-18 Du Pont Stretching of polyethylene terephthalate film
US3153683A (en) * 1961-10-04 1964-10-20 Du Pont Flame treatment of polyvinyl fluoride film
US3431135A (en) * 1965-07-02 1969-03-04 Du Pont Reducing flame treatment of polyethylene terephthalate film prior to aluminizing
JPS6025255B2 (en) * 1977-04-11 1985-06-17 帝人株式会社 polyester film
JPS6021673B2 (en) * 1978-05-18 1985-05-29 富士写真フイルム株式会社 thermal adhesive polyester film
US4325850A (en) * 1979-05-21 1982-04-20 W. R. Grace & Co. Processing and product enhancement additives for polyolefin film
JPS59111849A (en) * 1982-12-17 1984-06-28 帝人株式会社 Easily slidable polyester film
JPS59206456A (en) * 1983-05-11 1984-11-22 Toray Ind Inc Polyester composition
US4590119A (en) * 1983-07-15 1986-05-20 Toray Industries, Inc. Polyester film and magnetic recording medium therefrom
DE3632094A1 (en) * 1986-09-20 1988-03-24 Mtu Muenchen Gmbh TURBO MACHINE WITH TRANSITIONAL FLOWED STEPS
JPH02127022A (en) * 1988-11-07 1990-05-15 Mitsui Toatsu Chem Inc Film for twist wrapping
JPH02203422A (en) * 1989-01-31 1990-08-13 Toray Ind Inc Video tape
JP2817302B2 (en) * 1990-01-10 1998-10-30 東レ株式会社 Biaxially oriented polyester film
GB9012303D0 (en) * 1990-06-01 1990-07-18 Ici Plc Receiver sheet
US5137939A (en) * 1990-12-19 1992-08-11 Ici Americas Inc. Polyester film containing minute glass spheres and fumed silica useful for microfilm
US5215825A (en) * 1990-12-21 1993-06-01 Toray Industries, Inc. Polyester film and photosensitive material
US5330428A (en) * 1991-05-14 1994-07-19 Scimed Life Systems, Inc. Dilatation catheter having a random copolymer balloon
GB9110590D0 (en) * 1991-05-16 1991-07-03 Ici Plc Polymeric film
JP2661403B2 (en) * 1991-05-20 1997-10-08 東レ株式会社 Biaxially oriented thermoplastic resin film
JP2697360B2 (en) * 1991-05-20 1998-01-14 東レ株式会社 Biaxially oriented laminated polyester film
US5264260A (en) * 1991-06-20 1993-11-23 Saab Mark A Dilatation balloon fabricated from low molecular weight polymers
JPH05124100A (en) * 1991-10-31 1993-05-21 Toray Ind Inc Biaxial oriented polyester film

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
USRE33561E (en) * 1983-07-05 1991-03-26 E. I. Du Pont De Nemours And Company Balloon and manufacture thereof
EP0261430A2 (en) * 1986-08-27 1988-03-30 Teijin Limited Biaxially oriented polyester film
EP0506033A1 (en) * 1991-03-28 1992-09-30 Diafoil Hoechst Co., Ltd. Polyester film

Also Published As

Publication number Publication date
US5721023A (en) 1998-02-24

Similar Documents

Publication Publication Date Title
US5721023A (en) Polyethylene terephthalate articles having desirable adhesion and non-blocking characteristics, and a preparative process therefor
US5951941A (en) Block copolymer elastomer catheter balloons
EP0748232B8 (en) Block copolymer elastomer catheter balloons
US5830182A (en) Block copolymer elastomer catheter balloons
EP0974370B1 (en) Balloon for medical catheter
US4797235A (en) Process for enhanced orientation of polymeric films
JPS60240451A (en) Heat-sealable multilayer film
JP3045873B2 (en) Polymer film
US20020132072A1 (en) Block copolymer elastomer catheter balloons
EP0569263A2 (en) Balloon catheter
EP0361865A2 (en) Metallized breathable films prepared from melt embossed polyolefin/filler precursor films
KR100332729B1 (en) Composite polyester film with barrier properties
WO1994004601A1 (en) Process for surface treatment of polyethylene terephthalate article
JP3585056B2 (en) Polyester shrink film
KR20150129775A (en) Polyamide-based resin film
JPS62119265A (en) Polyester film for packaging
JPH09501893A (en) Multilayer film with self-regulating heat sealability
JP2004051959A (en) Aliphatic polyester film and laminated product
JP2692270B2 (en) Polyester film for fluorescent light shrink packaging
AU671218B2 (en) Polyester films containing glass spheres and calcined china clay
KR100814751B1 (en) Polyester film with good transmissivity of light
JPS62179535A (en) Production of packaging material
KR100330818B1 (en) Polyester films containing precipitated silica particles and calcined china clay
KR100839111B1 (en) Polyester film for artificial marble molding and their preparation method
JPS5816825A (en) Manufacture of biaxial-oriented hollow body made of thermoplastic resin with gas impermeable waterproof coating and hollow body obtained through said method

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): JP

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): AT BE CH DE DK ES FR GB GR IE IT LU MC NL PT SE

DFPE Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101)
121 Ep: the epo has been informed by wipo that ep was designated in this application
122 Ep: pct application non-entry in european phase