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US5098625A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for forming an expanded porous tetrafluoroethylene polymer

Assignee: Yeu Ming Tai Chemical Industrial Co Ltd
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Filing: 1990-12-17
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Granted: 1992-03-24
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Expires: 2010-12-17
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Abstract

Abstract A process for preparing an improved expanded porous polytetrafluorethylene product having a higher density and improved cold flow properties and prepared from a paste formed from a polytetrafluoroethylene resin and a lubricant. The method includes extruding the paste through an extrusion die at a reduction ratio of less than 100, calendering the extrudate, removing the lubricant, and heating the extrudate to a temperature greater than the crystalline melting point of polytetrafluoroethylene but generally below the temperature at which thermal decomposition becomes appreciable while concurrently expanding the extrudate to at least twice its original length.

Inventors

  • 👤 James Huang
  • 👤 William Chou
  • 👤 David Chou

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 14:51
CPC Classifications
B; B29; B29C; B29C55/00; B29C55/02; B29C55/18; B29C48/00; B29C48/022; B29C48/25; B29C48/36; B29C48/475; B29C55/04; B29C55/06; B29C67/00; B29C67/24; B29C48/03; B29C48/07; B29C48/08; B29K; B29K2027/00; B29K2027/12; B29K2027/18; B29K2105/00; B29K2105/04; Y; Y10; Y10S; Y10S425/00; Y10S425/055

Claims Analysis

Total Claims: 20
Claim 1
Independent Claim 203 words
A process for preparing an expanded porous polytetrafluoroethylene product having a higher density, greater flexibility, and a lower matrix tensile strength than conventionally extruded, stretched, and sintered polytetrafluoroethylene products, and for which the resulting properties can be varied while maintaining a constant rate of expansion during the process, the method comprising: extruding a paste formed from a polytetrafluoroethylene resin and a lubricant at a reduction ratio of less than 100 to thereby produce an extruded paste at a relatively low extrusion pressure; calendering the extrudate; removing the lubricant from the calendered extrudate; concurrently heating and expanding the calendered extrudate, and wherein the heating step further comprises, heating the thus calendered extrudate to a temperature greater than the crystalline melting point of polytetrafluoroethylene but below its thermal decomposition temperature for a time period sufficient to substantially equilibrate the temperature of the extrudate while expanding the extrudate, but short enough to prevent substantial decomposition of the polytetrafluoroethylene, and wherein the expanding step further comprises, concurrently expanding the extrudate during heating at a fixed rate of expansion and to at least twice its original length; and varying the heating temperature at a constant rate of expansion to control the porosity and deformability of the resulting polytetrafluoroethylene.
Claim 2
Dependent Claim 203 words
A process for preparing an expanded porous polytetrafluoroethylene product having a higher density, greater flexibility, and a lower matrix tensile strength than conventionally extruded, stretched, and sintered polytetrafluoroethylene products, and for which the resulting properties can be varied while maintaining a constant rate of expansion during the process, the method comprising: extruding a paste formed from a polytetrafluoroethylene resin and a lubricant at a reduction ratio of less than 100 to thereby produce an extruded paste at a relatively low extrusion pressure; calendering the extrudate; removing the lubricant from the calendered extrudate; concurrently heating and expanding the calendered extrudate, and wherein the heating step further comprises, heating the thus calendered extrudate to a temperature greater than the crystalline melting point of polytetrafluoroethylene but below its thermal decomposition temperature for a time period sufficient to substantially equilibrate the temperature of the extrudate while expanding the extrudate, but short enough to prevent substantial decomposition of the polytetrafluoroethylene, and wherein the expanding step further comprises, concurrently expanding the extrudate during heating at a fixed rate of expansion and to at least twice its original length; and varying the heating temperature at a constant rate of expansion to control the porosity and deformability of the resulting polytetrafluoroethylene.
Claim 3
Dependent Claim 35 words
A process according to claim 1 wherein the step of heating the extrudate to a temperature above the crystalline melting point of polytetrafluoroethylene comprises heating the extrudate to a temperature greater than about 320° C.
Claim 4
Dependent Claim 46 words
A process according to claim 1 wherein the step of heating the extrudate to a temperature below its thermal decomposition temperature comprises heating the extrudate to a temperature at which the extrudate shows substantially no weight loss for a period of at least about one hour.
Claim 5
Dependent Claim 34 words
A process according to claim 1 wherein the step of heating the extrudate to a temperature below its thermal decomposition temperature comprises heating the extrudate to a temperature no greater than about 430° C.
Claim 6
Dependent Claim 34 words
A process according to claim 1 wherein the step of heating the extrudate to a temperature below its thermal decomposition temperature comprises heating the extrudate to a temperature no greater than about 400° C.
Claim 7
Dependent Claim 29 words
A process according to claim 1 further comprising the step of shaping the extrudate following the step of calendering the extrudate and preceding the step of removing the lubricant.
Claim 8
Dependent Claim 21 words
A process according to claim 1 wherein the step of removing the lubricant comprises heating the extrudate to remove the lubricant.
Claim 9
Dependent Claim 53 words
A process according to claim 1 and further comprising the steps of: preparing a paste from a polytetrafluoroethylene resin and a lubricant prior to the step of extruding the paste through an extrusion die; and cooling the resulting product after the step of varying the heating temperature at a constant rate of expansion.
Claim 10
Dependent Claim 43 words
A process according to claim 8 wherein the step of heating the calendered extrudate to remove the lubricant comprises heating the extrudate to a temperature of about 300° C. for a time period sufficient for the lubricant to substantially evaporate from the extrudate.
Claim 11
Dependent Claim 41 words
A process according to claim 8 wherein the step of heating the extrudate to a temperature above the crystalline melting point of polytetrafluoroethylene comprises heating the extrudate to a temperature of about 360° C. for a period of about 10 minutes.
Claim 12
Dependent Claim 35 words
A process according to claim 8 wherein the step of heating the extrudate to a temperature above the crystalline melting point of polytetrafluoroethylene comprises heating the extrudate to a temperature greater than about 327° C.
Claim 13
Dependent Claim 37 words
A process according to claim 8 wherein the step of heating the extrudate to a temperature above the crystalline melting point of polytetrafluoroethylene comprises heating the extrudate to a temperature of between about 350° and 400° C.
Claim 14
Dependent Claim 82 words
A process according to claim 8 wherein the step of heating the extrudate to a temperature greater than the crystalline melting point of polytetrafluoroethylene but below its thermal decomposition temperature while concurrently expanding the heating extrudate to at least twice its original length comprises heating the extrudate while concurrently expanding to produce a product having a matrix tensile strength of between about 4000 and 6800 pounds per square inch and a density of between about 0.45 and 0.55 grams per cubic centimeter.
Claim 15
Dependent Claim 34 words
A process according to claim 8 wherein the step of concurrently expanding the heated extrudate to at least twice its original length comprises transferring a portion of the heated extrudate between two rotating drums.
Claim 16
Dependent Claim 59 words
A process according to claim 8 wherein the step of concurrently expanding the heated extrudate to at least twice its original length comprises transferring a portion of the heated extrudate from the circumference of a first rotating drum to the circumference of a second rotating drum that has a circumference larger than the circumference of the first rotating drum.
Claim 17
Dependent Claim 23 words
A process according to claim 15 wherein the diameter of the second rotating drum is twice the diameter of the first rotating drum.
Claim 18
Dependent Claim 51 words
A process according to claim 8 wherein the step of concurrently expanding the heated extrudate to at least twice its original length comprises transferring a portion of the heated extrudate from a first rotating drum to a second rotating drum while the second drum is rotating faster than the first drum.
Claim 19
Dependent Claim 35 words
A process according to claim 8 wherein the step of concurrently expanding the heated extrudate to at least twice its original length comprises expanding the heated extrudate to at least four times its original length.
Claim 20
Dependent Claim 60 words
A process according to claim 8 wherein the step of heating the extrudate while concurrently expanding the heated extrudate comprises passing the extrudate through an expansion oven in a substantially continuous fashion while heating the extrudate to a temperature at which the temperature of the extrudate substantially equilibrates in the period during which the extrudate passes through the expansion oven.

References Cited (Backward Citations)

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US3260774A Cited
US3389201A Cited
US3664915A Cited
US3953566A Cited
US4187390A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1995-03-24 1995-09-23 1996-03-24 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1999-03-24 1999-09-23 2000-03-24 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2003-03-24 2003-09-23 2004-03-24 $7700.00 Window Closed / Lapsed

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