LC-finer catalyst testing. Final report

Technical Report · Thu Sep 01 00:00:00 EDT 1983

DOI:https://doi.org/10.2172/6661131· OSTI ID:6661131

Garg, D.; Bronfenbrenner, J. C.

The activity and aging rate of modified Shell 324 Ni-Mo-Al catalyst were studied in ICRC's process development unit (PDU) under SRC-I Demonstration Plant hydroprocessing conditions. The studies determined variations in SRC conversion, hydrocarbon gas production, hydrogen consumption, and heteroatom removal at both constant and increasing reaction temperatures. Samples of spent catalyst were analyzed to ascertain the reasons for catalyst deactivation. Finally, the PDU hydroprocessing results were compared with those generated at Lummus and Wilsonville pilot plants. 14 references, 25 figures, 16 tables.

• Research Organization: International Coal Refining Co., Allentown, PA (USA)
• DOE Contract Number: AC05-78OR03054
• OSTI ID: 6661131
• Report Number(s): DOE/OR/03054-36; ON: DE84015762
• Country of Publication: United States
• Language: English

Related Subjects

01 COAL, LIGNITE, AND PEAT
CATALYSTS
DEACTIVATION
PERFORMANCE TESTING
COAL LIQUIDS
HYDROGENATION
LC-FINING
MOLYBDENUM
CATALYTIC EFFECTS
NICKEL
COAL LIQUEFACTION
CONSUMPTION RATES
DENITRIFICATION
DESULFURIZATION
EXPERIMENTAL DATA
FLOWSHEETS
HYDROGEN
NITROGEN
OXYGEN
PROCESS DEVELOPMENT UNITS
REFINING
REMOVAL
SRC PROCESS
SULFUR
TEMPERATURE DEPENDENCE
CHEMICAL REACTIONS
DATA
DIAGRAMS
ELEMENTS
FLUIDS
FUNCTIONAL MODELS
INFORMATION
LIQUEFACTION
LIQUIDS
METALS
NONMETALS
NUMERICAL DATA
PROCESSING
TESTING
THERMOCHEMICAL PROCESSES
TRANSITION ELEMENTS
010405* - Coal
Lignite
& Peat- Hydrogenation & Liquefaction