System comprising the gasification of fossil fuels to process unconventional oil sources

a fossil fuel and oil processing technology, applied in gasification process details, gas purification by non-gaseous material condensation, inorganic chemistry, etc., can solve the problems of high cost of injecting steam, uneconomical cost of steam injection, and difficulty in small-scale economics

Inactive Publication Date: 2009-01-22
PLASCO ENERGY GROUP INC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, most of these methods are still in the experimental phase.
This process is repeated until the cost of injecting steam becomes uneconomical, for instance if the cost is higher than the money made from producing oil.
The CSS method has the advantage that recovery factors are around 20 to 25% and the disadvantage that the cost to inject steam is high.
The upgrading process (also called cracking or distillation) into lighter oil products has been around for a while; however, doing so in an economic fashion has been difficult in small scale fields.
Typically more petcoke is produced than is used in the upgrading process, resulting in stockpiling of excess petcoke at or near the upgrading site.
Such coal includes low grade, high sulfur coal, which is not suitable for use in coal-fired power generators due to the production of emissions having high sulfur content.

Method used

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  • System comprising the gasification of fossil fuels to process unconventional oil sources
  • System comprising the gasification of fossil fuels to process unconventional oil sources
  • System comprising the gasification of fossil fuels to process unconventional oil sources

Examples

Experimental program
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example 1

Plasma Gasification System Integrated with an IGCC

[0698]This example describes a plasma Gasification System integrated with an IGCC. The plasma Gasification System comprises a converter, solid residue conditioner, a GCS, and a gas storage or regulation system, integrated with use of a combined-cycle to produce electricity.

[0699]As shown in FIG. 119, coal 106 is combined with oxygen from an oxygen plant 105 in the converter 100 to produce syngas, which is mainly hydrogen and carbon monoxide. The syngas is then cooled in a heat recovery steam generator (HRSG) 120 and then cleaned by a gas cleanup process in a GCS which includes the steps of scrubbing the syngas in a scrubber 130, removing particulate matter and heavy metals from the syngas in a baghouse 140, and H2S removal in an H2S removal system 150. The cleaned or conditioned gas is then stored or regulated in a gas storage or regulation system 160 prior to being fed to a gas turbine 170 for the production of electricity.

Combined-...

example 2

Configurations of Gasifiers Suitable for Use

[0701]FIG. 121A to D depicts various examples of gasifiers that can be used in the system of the invention.

example 3

Design of a GCS for Use in the System of the Invention

[0702]FIG. 122 depicts an example of a GCS that is designed for use in tar sands applications. As shown in FIG. 122, gas from the gasifier is cooled, particulates are removed, as is heavy metal and H2S. The conditioned gas is then fed to a gas boiler for the production of steam.

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Abstract

A facility comprising integrated systems for the extraction, and optionally upgrading and / or refinement, of unconventional oil sources, using fossil fuels as a primary source of energy. In particular, this facility provides a means to gasify one or more fossil fuels in an efficient manner, converting it into intermediate products such as heat, steam and electricity, which are then used by the system to obtain useful fuel products from unconventional oil sources such as tar sands and oil shale. The design of the components of this facility is optimized such that the overall costs are competitive with an equivalent unconventional oil source processing facility that uses natural gas as a source of processing energy. The facility can be used on its own, may use supplemental natural gas energy sources, or may be used in conjunction with an existing facility that uses natural gas as an energy source in order to improve the overall cost effectiveness of the processing and / or reduce the requirement for other energy sources, such as natural gas.

Description

CROSS-REFERENCE TO RELATED APPLICATIONS[0001]This application claims benefit of priority under 35 U.S.C. § 119(e) from U.S. Provisional Application Ser. No. 60 / 917,612, filed May 11, 2007. This application also claims benefit of priority under 35 U.S.C. § 119(e) from U.S. Provisional Application Ser. No. 60 / 917,410, filed May 11, 2007. This application also claims the benefit of priority to International Patent Application No. PCT / U.S.07 / 70456, filed Jun. 5, 2007. This application also claims benefit of priority under 35 U.S.C. § 119(e) from U.S. Provisional Application Ser. No. 60 / 950,322, filed Jul. 17, 2007. This application also claims benefit of priority under 35 U.S.C. § 119(e) from U.S. Provisional Application Ser. No. 60 / 986,213, filed Nov. 7, 2007. This application also claims benefit of priority under 35 U.S.C. §119(e) from U.S. Provisional Application Ser. No. 60 / 986,212, filed Nov. 7, 2007. This application also claims the benefit of priority to International Patent Appl...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C10G35/00C10G35/24
CPCC01B2203/84Y02E20/18C10G2/30C10J3/32C10J3/34C10J3/466C10J3/482C10J3/523C10J3/86C10J2300/0956C10J2300/0959C10J2300/0973C10J2300/0989C10J2300/1238C10J2300/165C10J2300/1659C10K1/04C10K1/101F01K23/068C10G1/002
Inventor TSANGARIS, ANDREASBACON, MARC
Owner PLASCO ENERGY GROUP INC
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