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

Gasoline upgrading process

Patent 5318690 Issued on June 7, 1994. Estimated Expiration Date: Icon_subject January 7, 2013. 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

3759821

3767568

Method for reducing the sulfur level of gasoline product
Patent #: 3957625
Issued on: 05/18/1976
Inventor: Orkin

Reduction of sulfur from hydrocarbon feed stock containing olefinic component
Patent #: 4049542
Issued on: 09/20/1977
Inventor: Gibson ,   et al.

Process for desulfurizing and blending naphtha
Patent #: 4062762
Issued on: 12/13/1977
Inventor: Howard ,   et al.

Process for improving the octane number of cracked gasolines
Patent #: 4753720
Issued on: 06/28/1988
Inventor: Morrison

Desulfurization and isomerization of N-paraffins
Patent #: 4827076
Issued on: 05/02/1989
Inventor: Kokayeff ,   et al.

Process for upgrading a sulphur-containing feedstock Patent #: 5143596
Issued on: 09/01/1992
Inventor: Maxwell, et al.

Inventors

Assignee

Application

No. 001681 filed on 01/07/1993

US Classes:

208/89, With hydrogen208/60, With subsequent reforming208/88, Refining208/92, Distillation208/211With preliminary treatment of feed

Examiners

Primary: Myers, Helane

Attorney, Agent or Firm

International Classes

C10G 035/00
C10G 045/00

Abstract

Low sulfur gasoline is produced from a catalytically cracked, sulfur-containing naphtha by fractionating the naphtha feed into a low boiling fraction in which the majority of the sulfur is present in the form of mercaptans and a high-boiling fraction in which the sulfur is predominantly in non-mercaptan form such as thiophenes. The low boiling fraction is desulfurized by a non-hydrogenatile mercaptan extraction process which retains the olefins present in this fraction. The second fraction is desulfurized by hydrodesulfurization, which results in some saturation of olefins and loss of octane. The octane loss is restored by treatment over an acidic catalyst, preferably an intermediate pore size zeolite such as ZSM-5, to form a low sulfur gasoline product with an octane number comparable to that of the feed naphtha but which contains some recombined sulfur in the form or mercaptans which are removed in a final hydrotreatment.

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