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

Process for the manufacture of lubricating base oils

Patent 5098551 Issued on March 24, 1992. Estimated Expiration Date: Icon_subject May 16, 2010. 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

3658689

3861005

Catalytic dewaxing process
Patent #: 4419220
Issued on: 12/06/1983
Inventor: LaPierre ,   et al.

Three-step catalytic dewaxing and hydrofinishing
Patent #: 4747932
Issued on: 05/31/1988
Inventor: Miller

Process for hydrodewaxing hydrocracked lube oil base stocks Patent #: 4822476
Issued on: 04/18/1989
Inventor: Ziemer ,   et al.

Inventors

Application

No. 523806 filed on 05/16/1990

US Classes:

208/111.3, With group VI metal or metal oxide (i.e., Cr, Mo, W, Po, or oxide thereof)208/27, Chemical treatment (refining or modification except mere solvent extraction)208/31, With solvent208/46, CHEMICAL CONVERSION OF HYDROCARBONS208/111.35, With group VIII metal or metal oxide (i.e., iron, or platinum group metal, or oxide thereof)208/135, With Group III metal or metal oxide containing catalyst208/136, With Group VI metal or metal oxide208/137With Group VIII metal or metal oxide

Examiners

Primary: Myers, Helane

Foreign Patent References

  • 19980 EP. 12/21/1980
  • 104807 EP. 04/21/1984
  • 178710 EP. 04/21/1986
  • 752925 GB. 07/21/2013
  • 1429291 GB. 03/21/1976
  • 1493620 GB. 11/21/1977
  • 1546398 GB. 05/21/1979

International Classes

C10G 023/04
C10G 047/00

Foreign Application Priority Data

1989-05-30 FR

Abstract

Lubricating base oils having a high viscosity index, preferably at least 135, are manufactured by catalytic hydroisomerization of a hydrocarbonaceous feedstock, derived from a waxy crude oil, which feedstock has not been treated to remove a lubricating base oil fraction and which feedstock contains at least 30% by weight wax and has at least 80% by weight boiling above 300° C. and at most 30% by weight boiling above 540° C.

Other References

  • Karzhev et al., Proceedings of 9th World Petroleum Congress, vol. 5, Processing and Storage, pp. 191-19
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