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

Heavy oil recovery process

Patent 4160479 Issued on July 10, 1979. Estimated Expiration Date: Icon_subject April 24, 1998. 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

2474345

3118746

3687629

Coal treatment process and apparatus
Patent #: 3966583
Issued on: 06/29/1976
Inventor: Cramer

Process for production of hydrocarbon liquid from oil shale
Patent #: 4003821
Issued on: 01/18/1977
Inventor: Weil ,   et al.

Secondary recovery of oil by steam stimulation plus the production of electrical energy and mechanical power
Patent #: 4007786
Issued on: 02/15/1977
Inventor: Schlinger

Process for obtaining oil, gas, sulfur and other products from oil shale
Patent #: 4060479
Issued on: 11/29/1977
Inventor: Barcellos

Oil shale retorting process with desulfurization of flue gas
Patent #: 4069132
Issued on: 01/17/1978
Inventor: Deering

Hydroconversion and desulfurization process
Patent #: 4087349
Issued on: 05/02/1978
Inventor: Baird, Jr.

Methods of fluidized production of coal in situ Patent #: 4089372
Issued on: 05/16/1978
Inventor: Terry

Inventors

Application

No. 05/899758 filed on 04/24/1978

US Classes:

166/267, Separating outside of well166/256, In situ combustion166/272.1, Involving the step of heating166/65.1, WITH ELECTRICAL MEANS208/414, With hydrogen production from water208/427Including burning of feed or product

Examiners

Primary: Novosad, Stephen J.

Attorney, Agent or Firm

International Classes

C10G 1/06 (20060101)
C10G 1/00 (20060101)

Abstract

A process incorporating integrated units and combined cycle energy production is provided for the recovery and upgrading of oil containing deposits which are not readily amenable to recovery and upgrading, to produce therefrom a light oil and elemental sulphur. Residual hydrocarbons generated in the process are gasified to produce hot gases which are used as a source of energy for process use, including electric power. The electric power is utilized to electrolyze water and produce hydrogen for use in upgrading and oxygen for use in gasification. The integration of gasification of residual hydrocarbons to produce, inter alia, electric power with the electrolysis of water to produce hydrogen for upgrading, and efficient use, distribution and recovery of energy in combined energy cycles provides an economical and essentially energy sufficient process with the flexibility to be adapted for the recovery and upgrading of various low yield oil deposits.

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