U.S. patents available from 1976 to present.
U.S. patent applications available from 2005 to present.

Process of reclaiming rubber

Patent 4264481 Issued on April 28, 1981. Estimated Expiration Date: Icon_subject July 3, 1999. Estimated Expiration Date is calculated based on simple USPTO term provisions. It does not account for terminal disclaimers, term adjustments, failure to pay maintenance fees, or other factors which might affect the term of a patent.

Patent References

2088920

2783213

2800462

2804651

2871205

2939850

3272761

3896059

Reclaimed vulcanized rubber
Patent #: 4125578
Issued on: 11/14/1978
Inventor: Sear

Process of reclaiming rubber and refining reclaimed rubber Patent #: 4146508
Issued on: 03/27/1979
Inventor: Maxwell

Inventor

Assignee

Application

No. 06/054496 filed on 07/03/1979

US Classes:

521/44.5, Treating with hydrocarbon or halogenated hydrocarbon material521/41, Treating rubber (or rubberlike materials) or polymer derived from a monomer having at least two ethylenic unsaturated moieties521/42Treating with organic nitrogen-containing material

Examiners

Primary: Welsh, Maurice J.

Attorney, Agent or Firm

International Classes

C08J 11/00 (20060101)
C08J 11/16 (20060101)

Foreign Application Priority Data

1979-06-25 SE

Abstract

Chemical direct reclaiming of rubber by mixing pulverulent scrap rubber having a particle size of at most 1 mm with a reducing agent, an oxidizable iron metal chloride and at least one plasticizer. The mixture is agitated for a short time, in the solid phase in air at a temperature of not more than 100° C., in a powder mixer for direct degradation of double bonds in the rubber. The reducing agent is from 0.2 to 1 weight % of phenyl hydrazine or diphenyl guanidine. The iron metal chloride is admixed in an amount of from 0.1 to 0.4 weight %. The plasticizer shall comprise at least one member from the group tall oil pitch and dipentene, and this plasticizer may be used in mixture with some other plasticizer. The amount of dipentene is at most 5 weight % and is from 0.5 to 5 weight % if the dipentene is used as the only plasticizer or is used in mixture with another plasticizer. The amount of tall oil pitch is at most 17.5 weight % and is from 7 to 17.5 weight % if the tall oil pitch is used as the only plasticizer or is used in mixture with a plasticizer other than dipentene. If tall oil pitch is used in mixture with dipentene, the amount of tall oil pitch varies in inverse proportion to the amount of dipentene and is from 8 to 16 weight % with dipentene amounts of from 5 to 0.5 weight %.

Other References

  • Yamashita et al., Internatioal Polymer Science & Technology, vol. 3, No. 8, 1976, pp. T75-T81
  • Yoshioka et al., Chem. Abs. 84, 45783h, 1976
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