Integrated two-stage coal liquefaction steady-state performance. The Advanced Coal Liquefaction R and D Facility, Wilsonville, Alabama. Final report

Technical Report · Wed May 01 04:00:00 EDT 1985

OSTI ID:5814817

This report presents the operating results for Run 245 at the Advanced Coal Liquefaction R and D Facility in Wilsonville, Alabama. This run was made in an ''all-distillate'' Integrated Two-Stage Liquefaction (ITSL) mode using Illinois 6 coal from the Burning Star mine. The primary run objective was to obtain steady-state ITSL performance by replacing spent HTR reactor catalyst with fresh, sulfided catalyst. Secondary objectives were to maintain an ''all-distillate'' (minimum resid production) product slate and to demonstrate the effects of catalyst addition on the net gas production and hydrogen consumption. Run 245 began on 7 November, 1983, and continued through 12 February, 1984. During this period, 179.0 tons of coal was fed in 2045 hours of operation. Eight special product workup material balances were defined, and the results are presented herein. 6 refs., 32 figs., 20 tabs.

• Research Organization: Catalytic, Inc., Wilsonville, AL (USA)
• DOE Contract Number: AC22-82PC50041
• OSTI ID: 5814817
• Report Number(s): EPRI-AP-4030; ON: DE85012872
• Country of Publication: United States
• Language: English

Related Subjects

01 COAL, LIGNITE, AND PEAT
010405* -- Coal
Lignite
& Peat-- Hydrogenation & Liquefaction
CATALYSTS
CATALYTIC EFFECTS
CHEMICAL REACTIONS
COAL LIQUEFACTION
DATA
DIAGRAMS
ELEMENTS
EXPERIMENTAL DATA
EXTRACTION
FLOWSHEETS
HYDROGEN
INFORMATION
LIQUEFACTION
MATERIAL BALANCE
METALS
MOLYBDENUM
NICKEL
NONMETALS
NUMERICAL DATA
PERFORMANCE TESTING
SEPARATION PROCESSES
SOLVENT EXTRACTION
SULFIDATION
TESTING
THERMOCHEMICAL PROCESSES
TRANSITION ELEMENTS
TSL PROCESS
YIELDS