Modified polytetrafluoroethylene fine powder and production of the same

Claim 2

Modified polytetrafluoroethylene fine powder, which comprises primary particles having a core-shell structure and having an average particle size of 0.1 to 0.6 μm, wherein the core comprises a copolymer consisting essentially of tetrafluoroethylene and 0.01 to 0.15% by weight, based on the total weight of the particles, of at least one olefinically unsaturated compound selected from the group consisting of a fluoroalkyl vinyl ether of the formula: X(CF.sub.2).sub.n OCF═CF.sub.2 wherein X is a hydrogen atom, a fluorine atom or a chlorine atom and n is an integer of 1, 2, 4, 5 or 6 and a fluoroalkyl vinyl ether of the formula: C.sub.3 F.sub.7 (OCF.sub.2 CF.sub.2 CF.sub.2).sub.m [OCF(CF.sub.3)CF.sub.2 ].sub.l OCF═CF.sub.2 wherein m is an integer of 0 to 2 and l is an integer of 0 to 2 and the shell comprises a copolymer consisting essentially of tetrafluoroethylene and 0.04 to 0.25% by weight, based on the total weight of the particles, of chlorotrifluoroethylene.

Claim 3

The modified polytetrafluoroethylene fine powder according to claim 1, which has a thermal instability index of less than 30.

Claim 4

The modified polytetrafluoroethylene fine powder according to claim 1, wherein a weight ratio of the core part and the shell part is from 50:50 to 98:2.

Claim 5

The modified polytetrafluoroethylene fine powder according to claim 1, wherein the content of chlorotrifluoroethylene is from 0.06 to 0.20% by weight, the content of the fluoroalkyl vinyl ether is from 0.02 to 0.04% by weight, and the weight ratio of the core part and the shell part is from 70:30 to 95:5.

Claim 6

The modified polytetrafluoroethylene fine powder according to claim 1, wherein the content of chlorotrifluoroethylene is from 0.06 to 0.15% by weight, and the TII is less than 20.

Claim 7

The modified polytetrafluoroethylene fine powder according to claim 1, wherein the fluoroalkyl vinyl ether is perfluoropropyl vinyl ether.

Claim 8

A process for preparing modified polytetrafluoroethylene fine powder comprising primary particles having a core-shell structure and having an average particle size of 0.1 to 0.6 μm wherein the core comprises a copolymer consisting essentially of tetrafluoroethylene and 0.01 to 0.15% by weight, based on the total weight of the particles, of at least one olefinically unsaturated compound selected from the group consisting of a fluoroalkyl vinyl ether of the formula: X(CF.sub.2).sub.n OCF═CF.sub.2 wherein X is a hydrogen atom, a fluorine atom or a chlorine atoms and n is an integer of 1, 2, 4, 5 or 6 and a fluoroalkyl vinyl ether of the formula: C.sub.3 F.sub.7 (OCF.sub.2 CF.sub.2 CF.sub.2).sub.m [OCF(CF.sub.3)CF.sub.2 ].sub.l OCF═CF.sub.2 wherein m is an integer of 0 to 2 and l is an integer of 0 to 2 and the shell comprises a copolymer consisting essentially of tetrafluoroethylene and 0.04 to 0.25% by weight, based on the total weight of the particles, of chlorotrifluoroethylene, which process comprises polymerizing tetrafluoroethylene in an aqueous medium in the presence of a fluorine-containing dispersant at a temperature of 10° to 90° C. under average pressure of 6 to 30 kg/cm 2 by charging at least one olefinically unsaturated compound selected from the above fluoroalkyl vinyl ethers in an initial reaction stage, after consumption of at least 50% of tetrafluoroethylene to be polymerised, and further polymerizing tetrafluoroethylene with charging chlorotrifluoroethylene, wherein said chlorotrifluoroethylene is present in gaseous phase in an amount of at least 0.01% by mole until the total amount of the tetrafluoroethylene to be polymerized is consumed.

Claim 9

A process for preparing modified polytetrafluoroethylene fine powder comprising primary particles having a core-shell structure and having an average particle size of 0.1 to 0.6 μm wherein the core comprises a copolymer consisting essentially of tetrafluoroethylene and 0.01 to 0.15% by weight, based on the total weight of the particles, of at least one olefinically unsaturated compound selected from the group consisting of a fluoroalkyl vinyl ether of the formula: X(CF.sub.2).sub.n OCF═CF.sub.2 wherein X is a hydrogen atom, a fluorine atom or a chlorine atoms and n is an integer of 1, 2, 4, 5 or 6 and a fluoroalkyl vinyl ether of the formula: C.sub.3 F.sub.7 (OCF.sub.2 CF.sub.2 CF.sub.2).sub.m [OCF(CF.sub.3)CF.sub.2 ].sub.l OCF═CF.sub.2 wherein m is an integer of 0 to 2 and l is an integer of 0 to 2 and the shell comprises a copolymer consisting essentially of tetrafluoroethylene and 0.04 to 0.25% by weight, based on the total weight of the particles, of chlorotrifluoroethylene, which process comprises polymerizing tetrafluoroethylene in an aqueous medium in the presence of a fluorine-containing dispersant at a temperature of 10° to 90° C. under average pressure of 6 to 30 kg/cm 2 by charging at least one olefinically unsaturated compound selected from the above fluoroalkyl vinyl ethers in an initial reaction stage, after consumption of at least 50% of tetrafluoroethylene to be polymerised, and further polymerizing tetrafluoroethylene with charging chlorotrifluoroethylene, wherein said chlorotrifluoroethylene is present in gaseous phase in an amount of at least 0.01% by mole until the total amount of the tetrafluoroethylene to be polymerized is consumed.

Claim 10

The process according to claim 7, wherein a mixture of disuccinic acid peroxide and a persulfate in a weight ratio of 50:1 to 8:1 is used as a polymerization initiator, said disuccinic acid peroxide is used in an amount of 20 to 1,000 ppm based on the weight of the aqueous medium.

Claim 11

The process according to claim 7, wherein the charge of the chlorotrifluoroethylene is initiated after the consumption of at least 70% of the tetrafluoroethylene to be polymerized.