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Volume 3: Coal, Biomass and Alternative Fuels; Combustion and Fuels; Oil and Gas Applications; Cycle Innovations | 1996

Next-Generation Integration Concepts for Air Separation Units and Gas Turbines

Arthur Ramsden Smith; Joseph Klosek; Donald Winston Woodward

The commercialization of Integrated Gasification Combined Cycle (IGCC) power has been aided by concepts involving the integration of a cryogenic air separation unit (ASU) with the gas turbine combined-cycle module. Other processes, such as coal-based ironmaking and combined power/industrial gas production facilities, can also benefit from the integration. It is known and now widely accepted that an ASU designed for “elevated pressure” service and optimally integrated with the gas turbine can increase overall IGCC power output, increase overall efficiency, and decrease the net cost of power generation when compared to non-integrated facilities employing low pressure ASU’s. The specific gas turbine, gasification technology. NOx emission specification, and other site specific factors determine the optimal degree of compressed air and nitrogen stream integration.Continuing advancements in both air separation and gas turbine technologies offer new integration opportunities to improve performance and reduce costs. This paper reviews basic integration principles and describes next-generation concepts based on advanced high pressure ratio gas turbines, Humid Air Turbine (HAT) cycles and integration of compression heat and refrigeration sources from the ASU. Operability issues associated with integration are reviewed and control measures are described for the safe, efficient and reliable operation of these facilities.© 1996 ASME


Volume 3: Coal, Biomass and Alternative Fuels; Combustion and Fuels; Oil and Gas Applications; Cycle Innovations | 1998

Air Separation Unit Integration for Alternative Fuel Projects

Arthur Ramsden Smith; Joseph Klosek; James Christian Sorensen; Donald Winston Woodward

Alternative fuel projects often require substantial amounts of oxygen. World scale gas-to-liquids (GTL) processes based on the partial oxidation of natural gas, followed by Fischer-Tropsch chemistry and product upgrading, may require in excess of 10,000 tons per day of pressurized oxygen. The remote location of many of these proposed projects and the availability of low-cost natural gas and byproduct steam from the GTL process disadvantages the use of traditional, motor-driven air separation units in favor of steam or gas turbine drive facilities. Another process of current interest is the partial oxidation of waste materials in industrial areas to generate synthesis gas. Synthesis gas may be processed into fuels and chemicals, or combusted in gas turbines to produce electricity. A key to the economic viability of such oxygen-based processes is cost effective air separation units, and the manner in which they are integrated with the rest of the facility. Because the trade-off between capital and energy is different for the remote gas and the industrial locations, the optimum integration schemes can also differ significantly. This paper examines various methods of integrating unit operations to improve the economics of alternative fuel facilities. Integration concepts include heat recovery, as well as several uses of byproduct nitrogen to enhance gas turbine operation or power production. Start-up, control and operational aspects are presented to complete the review of integrated designs.Copyright


Archive | 1989

IGCC process with combined methanol synthesis/water gas shift for methanol and electrical power production

Alan Thomas Perka; Thomas Hsiao-Ling Hsiung; Joseph Klosek; Robert Byron Moore


Archive | 1996

Gas turbine operation with liquid fuel vaporization

Joseph Klosek; Donald Winston Woodward


Archive | 1991

Solid waste-to-steam incinerator capacity enhancement by combined oxygen enrichment and liquid quench

Stephen Paul Goff; Joseph Klosek; Donald Peter Bucci; Paul Anthony Kinniry


Archive | 1981

Process for enhanced benzene-synthetic natural gas production from gas condensate

Joseph Klosek; John C. Tao


Archive | 1992

Fixation of heavy metals in scrubbed municipal solid waste incinerator ash

Donald Peter Bucci; A. Altemose Ii Francis; Nancy C. Easterbrook; Edwin N. Givens; Joseph Klosek; Kenneth D. Tracy; Kai P. Wong


Archive | 1991

Fixation of heavy metals in municipal solid waste incinerator ash

Donald Peter Bucci; A. Altemose Ii Francis; Nancy C. Easterbrook; Edwin N. Givens; Joseph Klosek; Kenneth D. Tracy; Kai P. Wong


Archive | 2001

Control scheme for conversion of variable composition synthesis gas to liquid fuels in a slurry bubble column reactor

James Christian Sorensen; Douglas Edward Benedict; Tsun-Chiu Robert Tsao; Joseph Klosek


Archive | 1989

IGCC-Verfahren mit kombinierter Methanolsynthese/Wassergasumwandlungsstufe zur Herstellung von Methanol und elektrischer Energie

Thomas Hsiao-Ling Hsiung; Alan Thomas Perka; Joseph Klosek; Robert Byron Moore

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