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US3966651A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the production of fine-cell polyolefin foams

Assignee: Bayer AG
•
Filing: 1974-10-08
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Granted: 1976-06-29
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Expires: 1994-10-08
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Abstract

Abstract A process for the production of a fine-celled foam from a mixture of a polyolefin, a peroxide capable of peroxidically cross-linking the polyolefin and a principal blowing agent having a decomposition point or decomposition range above about 190°C, wherein a further blowing agent, an auxiliary blowing agent, having a decomposition range of from 130° to about 190°C is added in a quantity of from 0.1 to 1.5 percent by weight, based on said principal blowing agent, to said mixture, the mixture thus obtained is worked up under such conditions that neither cross-linking nor appreciable foaming takes place to a moulding, which is subsequently, cross-linked and foamed by heating to temperatures above 190°C.

Inventors

  • 👤 Frank Gerald Kleiner
  • 👤 Karl Heinz Muller

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 05:24
CPC Classifications
C; C08; C08J; C08J9/00; C08J9/04; C08J9/06; C08J2323/00; C08J2323/02; Y; Y10; Y10S; Y10S521/00; Y10S521/91

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 219 words
A process for the production of a fine-celled foam which comprises forming a mixture of a polyolefin, a crosslinking amount of an organic peroxide capable of crosslinking the polyolefin, 2 to 30 percent by weight, based on the weight of the mixture, of a principal blowing agent having a decomposition point or decomposition range above about 190°C. and 0.1 to 1.5 percent by weight, based on the weight of said principal blowing agent, of an auxiliary blowing agent working up said mixture to form a shaped object under conditions that neither crosslinking nor appreciable foaming thereof takes place and subsequently crosslinking and foaming said shaped object by heating it to a temperature above 190°C., said auxiliary blowing agent being a disulfonylhydrazide of the formula H.sub.2 NHNO.sub.2 S-X-SO.sub.2 NHNH.sub.2 wherein X is an alkyl radical having up to 6 carbon atoms, a cycloalkyl radical having 4 to 7 carbon atoms, an aryl radical having 6 to 12 carbon atoms or an aromatic radical of the formula ##SPC2## wherein Y is 0, SO 2 , S or a bond or a sulfonylhydrazide of the formula X-SO.sub.2 -NH-NHR wherein X is as aforesaid and R is acyl having 3 to 6 carbon atoms or -R'COR" wherein R' and R" are the same or different aliphatic radicals having 1 to 5 carbon atoms.
Claim 2
Dependent Claim 219 words
A process for the production of a fine-celled foam which comprises forming a mixture of a polyolefin, a crosslinking amount of an organic peroxide capable of crosslinking the polyolefin, 2 to 30 percent by weight, based on the weight of the mixture, of a principal blowing agent having a decomposition point or decomposition range above about 190°C. and 0.1 to 1.5 percent by weight, based on the weight of said principal blowing agent, of an auxiliary blowing agent working up said mixture to form a shaped object under conditions that neither crosslinking nor appreciable foaming thereof takes place and subsequently crosslinking and foaming said shaped object by heating it to a temperature above 190°C., said auxiliary blowing agent being a disulfonylhydrazide of the formula H.sub.2 NHNO.sub.2 S-X-SO.sub.2 NHNH.sub.2 wherein X is an alkyl radical having up to 6 carbon atoms, a cycloalkyl radical having 4 to 7 carbon atoms, an aryl radical having 6 to 12 carbon atoms or an aromatic radical of the formula ##SPC2## wherein Y is 0, SO 2 , S or a bond or a sulfonylhydrazide of the formula X-SO.sub.2 -NH-NHR wherein X is as aforesaid and R is acyl having 3 to 6 carbon atoms or -R'COR" wherein R' and R" are the same or different aliphatic radicals having 1 to 5 carbon atoms.
Claim 3
Dependent Claim 14 words
A process as claimed in claim 1 wherein the polyolefin is polypropylene or polyethylene.
Claim 4
Dependent Claim 13 words
A process as claimed in claim 2 wherein the polyolefin is high-pressure polyethylene.
Claim 5
Dependent Claim 16 words
A process as claimed in claim 1, wherein the peroxide has a decomposition temperature above 150°C.
Claim 6
Dependent Claim 20 words
A process as claimed in claim 1, wherein the peroxide is dicumyl peroxide, 2,5-dimethyl-2,5-di-(t-butylperoxy)-hexane, 2,5-dimethyl-2,5-di-(t-butylperoxy)-hexyne, t-butylhydroperoxide, cumyl-t-butylperoxide, di-t-butylperoxide or bis-(t-butylperoxy-isopropyl)-benzene.
Claim 7
Dependent Claim 27 words
A process as claimed in claim 1, wherein the peroxide is used in an amount of from 0.3 to 1.5 percent by weight, based on the mixture.
Claim 8
Dependent Claim 18 words
A process as claimed in claim 1, wherein the principal blowing agent has a decomposition temperature above 190°C.
Claim 9
Dependent Claim 17 words
A process as claimed in claim 1, wherein the principal blowing agent is azodicarbonamide or dinitrosopentamethylene tetramine.
Claim 10
Dependent Claim 23 words
A process as claimed in claim 1, wherein the auxiliary blowing agent has a decomposition temperature or range of from 150° to 185°C.
Claim 11
Dependent Claim 31 words
A process as claimed in claim 1, wherein the auxiliary blowing agent is used in an amount of from 0.1 to 0.8 % by weight, based on the principal blowing agent.
Claim 12
Dependent Claim 16 words
A process as claimed in claim 1, wherein the mixture is worked up in an extruder.
Claim 13
Dependent Claim 18 words
A process as claimed in claim 1, wherein the moulding is cross-linked and expanded in a hot-air oven.
Claim 14
Dependent Claim 31 words
A process as claimed in claim 1 wherein the auxiliary blowing agent is 1,4-butane disulfonylhydrazide, cyclohexane disulfonylhydrazide, 1,3-benzene disulfonylhydrazide, naphthalene-1,5-disulfonylhydrazide, N'-acetonyl-benzene sulfonylhydrazide, N'-acetylbenzene sulfonylhydrazide, diphenylsulfone-3,3'-disulfonylhydrazide, diphenylene oxide-3,3'-disulfonylhydrazide, 3,3'-diphenyldisulfonylhydrazide or diphenyl ether-3,3'-disulfonylhydrazide.

References Cited (Backward Citations)

US3098831A Cited
US3278466A Cited
US3645931A Cited
US3645930A Cited
US3882209A Cited
US3876566A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-06-29 1979-12-29 1980-06-29 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-06-29 1983-12-29 1984-06-29 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-06-29 1987-12-29 1988-06-29 $7700.00 Window Closed / Lapsed

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