US3956000A
Expired / Lapsed
US
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Fluorocarbon waxes and process for producing them
Assignee: Hoechst AG
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Filing: 1975-01-22
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Granted: 1976-05-11
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Expires: 1995-01-22
Abstract
Abstract Fluorocarbon wax dispersions are produced by telomerization of tetrafluoro-ethylene or mixtures of tetrafluoro-ethylene with other olefinic monomers. The stable wax dispersions and the pulverulent fluorocarbon waxes obtained are, inter alia, valuable additives for lubricants and polishes.
Inventors
- 👤 Jurgen Kuhls
- 👤 Herbert Fitz
- 👤 Peter Haasemann
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 19:38
CPC Classifications
C; C08; C08J; C08J3/00; C08J3/12; C08F; C08F214/00; C08F214/18; C08F214/26; C10; C10M; C10M7/00; C08J2327/00; C08J2327/02; C08J2327/12; C08J2327/18; C10M2205/00; C10M2205/02; C10M2205/024; C10M2209/00; C10M2209/10; C10M2209/101; C10M2211/00; C10M2211/06; C10M2213/00; C10M2213/02; C10M2213/06; C10M2213/062; C10M2217/00; C10M2217/04; C10M2217/044; C10M2217/045; C10N; C10N2040/00; C10N2040/02; C10N2040/20; C10N2040/24; C10N2040/241; C10N2040/242; C10N2040/243; C10N2040/244; C10N2040/245; C10N2040/246; C10N2040/247; C10N2050/00; C10N2050/08; C10N2050/10
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
282 words
Process for the manufacture of fluorocarbon waxes, having a mean molecular weight, determined by elementary analysis of terminal chlorine, bromine, or iodine atoms in relation to the fluorine, in the range of from 10,000 to 200,000, and an apparent melt viscosity of from 0.7 . 10 2 to 1 . 10 8 poises at 380°C under 200 kg/cm 2 , by telomerization of tetrafluoroethylene or mixtures of tetrafluoroethylene with 0.1 to 40 mole % of at least one comonomer having the formula CH 2 = CH 2 , CF 2 = CFX, where X is H, CF 3 , Cl, Br, or I, or CF 2 = CY 2 , where Y is H, Cl, Br or I, which comprises telomerizing without a coating agent at a temperature of from 0° to 40°C and a pressure of from 0 to 25 atmospheres gauge in the presence of from 0.1 to 15 % by weight, calculated on the monomer(s) used, of at least one telogen of the formula CH n Z 4 -n , CH 3 I, C m F 2m + 1 I, CF 2 I-CF 2 I, or CFI 2 -CF 3 , where n is zero or an integer of from 1 to 3, Z is Cl or Br and m is an integer of from 1 to 3, in aqueous weakly alkaline phase in the presence of initiators and emulsifiers known for the dispersion polymerization of tetrafluoroethylene, while applying a specific stirring energy in the range of from 2.4 . 10 - 5 to 4.5 . 10 - 5 kg . m/sec/cc, to obtain a stable fluorocarbon wax dispersion, coagulating the said dispersion and drying the fluorocarbon wax obtained.
Claim 2
Dependent Claim
282 words
Process for the manufacture of fluorocarbon waxes, having a mean molecular weight, determined by elementary analysis of terminal chlorine, bromine, or iodine atoms in relation to the fluorine, in the range of from 10,000 to 200,000, and an apparent melt viscosity of from 0.7 . 10 2 to 1 . 10 8 poises at 380°C under 200 kg/cm 2 , by telomerization of tetrafluoroethylene or mixtures of tetrafluoroethylene with 0.1 to 40 mole % of at least one comonomer having the formula CH 2 = CH 2 , CF 2 = CFX, where X is H, CF 3 , Cl, Br, or I, or CF 2 = CY 2 , where Y is H, Cl, Br or I, which comprises telomerizing without a coating agent at a temperature of from 0° to 40°C and a pressure of from 0 to 25 atmospheres gauge in the presence of from 0.1 to 15 % by weight, calculated on the monomer(s) used, of at least one telogen of the formula CH n Z 4 -n , CH 3 I, C m F 2m + 1 I, CF 2 I-CF 2 I, or CFI 2 -CF 3 , where n is zero or an integer of from 1 to 3, Z is Cl or Br and m is an integer of from 1 to 3, in aqueous weakly alkaline phase in the presence of initiators and emulsifiers known for the dispersion polymerization of tetrafluoroethylene, while applying a specific stirring energy in the range of from 2.4 . 10 - 5 to 4.5 . 10 - 5 kg . m/sec/cc, to obtain a stable fluorocarbon wax dispersion, coagulating the said dispersion and drying the fluorocarbon wax obtained.
Claim 3
Dependent Claim
20 words
The process of claim 1, wherein the telogen is added to the aqueous phase prior to the beginning of telomerization.
Claim 4
Dependent Claim
34 words
The process of claim 1, wherein the telogen is previously mixed with the monomeric tetrafluoroethylene or the monomer mixture in a gas mixing device and the mixture obtained is introduced into the aqueous phase.
Claim 5
Dependent Claim
54 words
The process of claim 1, wherein prior to telomerization the aqueous phase is admixed with fluorocarbon wax dispersion of a previous batch as seed dispersion, the proportion of seeds in the aqueous bath being in the range of from 0.3 to 3 % by weight, calculated on the total weight of the starting bath.
Claim 6
Dependent Claim
27 words
The process of claim 4, wherein the seed dispersion has been prepared from the same monomers and the same telogens as used for making the fluorocarbon wax.
Claim 7
Dependent Claim
165 words
A pulverulent fluorocarbon wax having a mean molecular weight determined by elementary analysis of terminal chlorine, bromine and iodine atoms in relation to fluorine in the range of from 10,000 to 200,000 with an average size of the primary particles of from 0.5 to 6 microns, more than 70 % of the said primary particles being associated to a loose conglomerate having a diameter of from 10 to 20 microns, a size distribution of the primary particles of more than 0.7 and less than 0.9 expressed by the magnitude Δd 1/2/day, a specific surface of the primary particles of from 10 to 26 m 2 /g, measured by the Brunauer-Emmet-Teller method, a total pore volume of the primary particles of from 80 to 120 cc/100 g of dry substance, a transition temperature from crystalline to amorphous of from 270° to 325°C, and an apparent melt viscosity of from 0.7 . 10 2 to 1 . 10 8 poises at 380°C. under 200 kg/cm 2 .
Claim 8
Dependent Claim
165 words
A pulverulent fluorocarbon wax having a mean molecular weight determined by elementary analysis of terminal chlorine, bromine and iodine atoms in relation to fluorine in the range of from 10,000 to 200,000 with an average size of the primary particles of from 0.5 to 6 microns, more than 70 % of the said primary particles being associated to a loose conglomerate having a diameter of from 10 to 20 microns, a size distribution of the primary particles of more than 0.7 and less than 0.9 expressed by the magnitude Δd 1/2/day, a specific surface of the primary particles of from 10 to 26 m 2 /g, measured by the Brunauer-Emmet-Teller method, a total pore volume of the primary particles of from 80 to 120 cc/100 g of dry substance, a transition temperature from crystalline to amorphous of from 270° to 325°C, and an apparent melt viscosity of from 0.7 . 10 2 to 1 . 10 8 poises at 380°C. under 200 kg/cm 2 .
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-05-11 | 1979-11-10 | 1980-05-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-05-11 | 1983-11-10 | 1984-05-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-05-11 | 1987-11-10 | 1988-05-11 | $7700.00 | Window Closed / Lapsed |