CO/sub 2/ Acceptor Process Gasification Pilot Plant: commercial plant conceptual design and cost estimate. Final report, Volume 10: Book 1 of 3, North Dakota lignite gasification, economics and description, August 1976--December 1977
This report presents the results of work to design and estimate the capital cost of a Carbon Dioxide (CO/sub 2/) Acceptor Coal Gasification plant. This plant is designed to produce 250 billion Btu/day of synthetic natural gas. Plant processes were, in part, optimized and the design is tailored to a specific lignite and plant location in North Dakota. This design was modified for gasification of Texas lignite. Plant operating costs and gas costs were calculated for the North Dakota lignite case and the Texas lignite case. These costs are compared with published data for a Lurgi Coal Gasification Plant.
- Research Organization:
- Conoco Coal Development Co., Library, PA (USA). Research Div.; Stearns-Roger Engineering Co., Denver, CO (USA)
- DOE Contract Number:
- EX-76-C-01-1734
- OSTI ID:
- 6318271
- Report Number(s):
- FE-1734-43(Vol.10)(Bk.1)
- Country of Publication:
- United States
- Language:
- English
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Related Subjects
01 COAL, LIGNITE, AND PEAT
010404* -- Coal
Lignite
& Peat-- Gasification
015000 -- Coal
Lignite
& Peat-- Economic
Industrial
& Business Aspects
BROWN COAL
CARBON DIOXIDE ACCEPTOR PROCESS
CARBONACEOUS MATERIALS
COAL
COAL GASIFICATION
COAL GASIFICATION PLANTS
COST
DESIGN
ECONOMICS
ENERGY SOURCES
FLUIDS
FOSSIL FUELS
FUEL GAS
FUELS
FUNCTIONAL MODELS
GAS FUELS
GASES
GASIFICATION
HIGH BTU GAS
INDUSTRIAL PLANTS
LIGNITE
PILOT PLANTS
SNG PROCESSES
THERMOCHEMICAL PROCESSES
010404* -- Coal
Lignite
& Peat-- Gasification
015000 -- Coal
Lignite
& Peat-- Economic
Industrial
& Business Aspects
BROWN COAL
CARBON DIOXIDE ACCEPTOR PROCESS
CARBONACEOUS MATERIALS
COAL
COAL GASIFICATION
COAL GASIFICATION PLANTS
COST
DESIGN
ECONOMICS
ENERGY SOURCES
FLUIDS
FOSSIL FUELS
FUEL GAS
FUELS
FUNCTIONAL MODELS
GAS FUELS
GASES
GASIFICATION
HIGH BTU GAS
INDUSTRIAL PLANTS
LIGNITE
PILOT PLANTS
SNG PROCESSES
THERMOCHEMICAL PROCESSES