US3933773A
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US
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Thermoplastic elastomeric copolymers and terpolymers of tetrafluoroethylene and propylene and method of making the same
Assignee: ATK Launch Systems LLC
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Filing: 1973-12-06
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Granted: 1976-01-20
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Expires: 1993-12-06
Abstract
Abstract Thermoplastic elastomeric copolymers of tetrafluoroethylene and propylene and terpolymers of tetrafluoroethylene, propylene and a cure site monomer are disclosed which have a substantially uniform composition, i.e., a substantially uniform molar ratio of monomeric units and a relatively high molar ratio of tetrafluoroethylene units to propylene units within the range 1.0:0.11 to 1.0:0.54. The combination of high molar ratio of tetrafluoroethylene/propylene units, substantially uniform composition and good elastomeric properties is achieved by using a hybrid batch/continuous process wherein a reactor is initially charged with a mixture of tetrafluoroethylene, propylene and, optionally, a cure site monomer having a TFE/propylene molar ratio substantially higher than that of the polymer to be produced, i.e., in the range 1.0:0.01 to 1.0:0.087. The polymerization reaction is then initiated and a mixture of the same monomers is fed to the reactor at such a rate and in such proportions as to maintain the molar ratio of the unreacted monomers substantially the same as that in the initial charge to the reactor.
Inventors
- 👤 Rolf F. Foerster
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-24 04:38
CPC Classifications
C; C08; C08F; C08F214/00; C08F214/18; C08F214/26; C08F214/265
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
188 words
In a process for copolymerizing tetrafluoroethylene and propylene in an emulsion polymerization reaction mixture in a reactor at a temperature of 5° to 120°C. and at a pressure of 100 to 1,000 p.s.i.g., the improvement which consists in initially charging said reactor with an emulsion polymerization reaction mixture consisting essentially of tetrafluoroethylene and propylene in a molar ratio of 1.0:0.01 to 1.0:0.087, adding an initiator to said mixture to cause said tetrafluoroethylene and propylene to form an initial copolymer having a molar ratio of tetrafluoroethylene units to propylene units of at least 1.0:0.54 and thereafter continually feeding to said reactor a monomer mixture having a molar ratio of tetrafluoroethylene to propylene that is substantially the same as the ratio of tetrafluoroethylene units to propylene units in the initially formed copolymer within the reactor and at a feed rate to maintain the reactor pressure substantially constant to cause the monomers within the reactor to be replenished at approximately the same rate as they are consumed in the polymerization reactor and thereby produce a copolymer having a molar ratio of tetrafluoroethylene units to propylene units of from 1.0:0.11 to 1.0:0.54.
Claim 2
Dependent Claim
188 words
In a process for copolymerizing tetrafluoroethylene and propylene in an emulsion polymerization reaction mixture in a reactor at a temperature of 5° to 120°C. and at a pressure of 100 to 1,000 p.s.i.g., the improvement which consists in initially charging said reactor with an emulsion polymerization reaction mixture consisting essentially of tetrafluoroethylene and propylene in a molar ratio of 1.0:0.01 to 1.0:0.087, adding an initiator to said mixture to cause said tetrafluoroethylene and propylene to form an initial copolymer having a molar ratio of tetrafluoroethylene units to propylene units of at least 1.0:0.54 and thereafter continually feeding to said reactor a monomer mixture having a molar ratio of tetrafluoroethylene to propylene that is substantially the same as the ratio of tetrafluoroethylene units to propylene units in the initially formed copolymer within the reactor and at a feed rate to maintain the reactor pressure substantially constant to cause the monomers within the reactor to be replenished at approximately the same rate as they are consumed in the polymerization reactor and thereby produce a copolymer having a molar ratio of tetrafluoroethylene units to propylene units of from 1.0:0.11 to 1.0:0.54.
Claim 3
Dependent Claim
213 words
In a process for preparing a terpolymer of tetrafluoroethylene, propylene and a cure site monomer in an emulsion polymerization reaction mixture in a reactor at a temperature of 5° to 120°C. and a pressure of 100 to 1,000 p.s.i.g., the improvement which consists in initially charging said reactor with an emulsion polymerization reaction mixture consisting essentially of tetrafluoroethylene and propylene in a molar ratio of 1.0:0.01 to 1.0:0.087 and up to 10 mole percent of a cure site monomer, adding an initiator to said mixture to cause said tetrafluoroethylene, propylene and cure site monomer to form an initial terpolymer having a molar ratio of tetrafluoroethylene units to propylene units of at least 1.0:0.54, thereafter continually feeding to said reactor a monomer mixture of tetrafluoroethylene, propylene and cure site units in a molar ratio that is substantially the same as the ratio of tetrafluoroethylene units, propylene units and cure site units in the initially formed copolymer within the reactor and at a feed rate to maintain the reactor pressure substantially constant to cause the monomers within the reactor to be replenished at approximately the same rate as they are consumed in the polymerization reaction and thereby produce a copolymer having a molar ratio of tetrafluoroethylene units to propylene units of from 1.0:0.11 to 1.0:0.54.
Claim 4
Dependent Claim
213 words
In a process for preparing a terpolymer of tetrafluoroethylene, propylene and a cure site monomer in an emulsion polymerization reaction mixture in a reactor at a temperature of 5° to 120°C. and a pressure of 100 to 1,000 p.s.i.g., the improvement which consists in initially charging said reactor with an emulsion polymerization reaction mixture consisting essentially of tetrafluoroethylene and propylene in a molar ratio of 1.0:0.01 to 1.0:0.087 and up to 10 mole percent of a cure site monomer, adding an initiator to said mixture to cause said tetrafluoroethylene, propylene and cure site monomer to form an initial terpolymer having a molar ratio of tetrafluoroethylene units to propylene units of at least 1.0:0.54, thereafter continually feeding to said reactor a monomer mixture of tetrafluoroethylene, propylene and cure site units in a molar ratio that is substantially the same as the ratio of tetrafluoroethylene units, propylene units and cure site units in the initially formed copolymer within the reactor and at a feed rate to maintain the reactor pressure substantially constant to cause the monomers within the reactor to be replenished at approximately the same rate as they are consumed in the polymerization reaction and thereby produce a copolymer having a molar ratio of tetrafluoroethylene units to propylene units of from 1.0:0.11 to 1.0:0.54.
Claim 5
Dependent Claim
38 words
An elastomer consisting essentially of a copolymer of tetrafluoroethylene and propylene having a molar ratio of tetrafluoroethylene units to propylene units of from 1.0 : 0.11 to 1.0 : 0.54 and made by the process of claim 1.
Claim 6
Dependent Claim
42 words
An elastomer consisting essentially of a terpolymer of tetrafluoroethylene, propylene and a cure sits monomer having a molar ratio of tetrafluoroethylene units to propylene units of from 1.0 : 0.11 to 1.0 : 0.54 and made by the process of claim 2.
Claim 7
Dependent Claim
16 words
The process as claimed in claim 1 wherein the reaction temperature is from 40°C. to 80°C.
Claim 8
Dependent Claim
16 words
The process as claimed in claim 2 wherein the reaction temperature is from 40°C. to 80°C.
Claim 9
Dependent Claim
17 words
The process as claimed in claim 1 wherein the reaction pressure is from 250 to 350 p.s.i.g.
Claim 10
Dependent Claim
17 words
The process as claimed in claim 2 wherein the reaction pressure is from 250 to 350 p.s.i.g.
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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) | 1979-01-19 | 1979-07-21 | 1980-01-20 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-01-19 | 1983-07-21 | 1984-01-20 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-01-19 | 1987-07-21 | 1988-01-20 | $7700.00 | Window Closed / Lapsed |