Pilot plant for gasoline production from coal in the U. S. [After solvent extraction, coal extract is hydrogenated on fixed bed of Co--Mo--Al oxide catalyst at 425/sup 0/C and 210 atm; pilot plant is testing new catalyst based on Zn chloride that may be capable of direct conversion of coal into gasoline]
Journal Article
·
· Oil Gas J.
OSTI ID:5305619
- OSTI ID:
- 5305619
- Journal Information:
- Oil Gas J., Vol. 65:23
- Country of Publication:
- United States
- Language:
- English
Similar Records
Process for producing hydrogen-enriched hydrocarbonaceous products from coal. [Solvent extraction at 300 to 500/sup 0/C; catalytic hydrogenation of extract; use of Co oxide--Mo oxide--Al oxide catalyst at 440/sup 0/C, 245 atm, and residence time of 2. 8 hr]
Synthetic oil from coal. [Catalytic hydrogenation in autoclave at 140-210 atm up to 475/sup 0/ in presence of ammonium molybdate and Sn chloride or Zn chloride gave crude oil, gas, coke, and water; hydrorefining with CoO and Mo oxide on Al oxide followed by cracking]
Studies on hydrogenation of low-temperature tar products. Hydrorefining of neutral oil. Part I. [Hydrorefining of neutral oil (boiling 200 to 305/sup 0/C) obtained from noncaking coal studied in laboratory plant at 350 to 450/sup 0/C and 25 to 100 atm using Co--Mo--Al oxide catalyst; at 400/sup 0/C conversion level of stock decreased, and at 450/sup 0/C catalyst lost its activity]
Patent
·
Fri Jun 18 00:00:00 EDT 1965
·
OSTI ID:5305619
Synthetic oil from coal. [Catalytic hydrogenation in autoclave at 140-210 atm up to 475/sup 0/ in presence of ammonium molybdate and Sn chloride or Zn chloride gave crude oil, gas, coke, and water; hydrorefining with CoO and Mo oxide on Al oxide followed by cracking]
Journal Article
·
Wed Jan 01 00:00:00 EST 1969
· Brennst.-Chem.
·
OSTI ID:5305619
Studies on hydrogenation of low-temperature tar products. Hydrorefining of neutral oil. Part I. [Hydrorefining of neutral oil (boiling 200 to 305/sup 0/C) obtained from noncaking coal studied in laboratory plant at 350 to 450/sup 0/C and 25 to 100 atm using Co--Mo--Al oxide catalyst; at 400/sup 0/C conversion level of stock decreased, and at 450/sup 0/C catalyst lost its activity]
Journal Article
·
Mon Jan 01 00:00:00 EST 1968
· Chem. Age India
·
OSTI ID:5305619
+1 more
Related Subjects
01 COAL, LIGNITE, AND PEAT
COAL
SOLVENT EXTRACTION
COAL EXTRACTS
HYDROGENATION
COAL LIQUEFACTION
CSF PROCESS
CATALYSTS
GASOLINE
PRODUCTION
ALUMINIUM OXIDES
COBALT
HIGH PRESSURE
HIGH TEMPERATURE
MOLYBDENUM
PILOT PLANTS
WEST VIRGINIA
ZINC CHLORIDES
ALUMINIUM COMPOUNDS
CARBONACEOUS MATERIALS
CHALCOGENIDES
CHEMICAL REACTIONS
CHLORIDES
CHLORINE COMPOUNDS
ELEMENTS
ENERGY SOURCES
EXTRACTION
FOSSIL FUELS
FUELS
FUNCTIONAL MODELS
HALIDES
HALOGEN COMPOUNDS
LIQUEFACTION
METALS
NORTH AMERICA
OXIDES
OXYGEN COMPOUNDS
PETROLEUM PRODUCTS
REFRACTORY METALS
SEPARATION PROCESSES
TRANSITION ELEMENTS
USA
ZINC COMPOUNDS
ZINC HALIDES
010405* - Coal
Lignite
& Peat- Hydrogenation & Liquefaction
COAL
SOLVENT EXTRACTION
COAL EXTRACTS
HYDROGENATION
COAL LIQUEFACTION
CSF PROCESS
CATALYSTS
GASOLINE
PRODUCTION
ALUMINIUM OXIDES
COBALT
HIGH PRESSURE
HIGH TEMPERATURE
MOLYBDENUM
PILOT PLANTS
WEST VIRGINIA
ZINC CHLORIDES
ALUMINIUM COMPOUNDS
CARBONACEOUS MATERIALS
CHALCOGENIDES
CHEMICAL REACTIONS
CHLORIDES
CHLORINE COMPOUNDS
ELEMENTS
ENERGY SOURCES
EXTRACTION
FOSSIL FUELS
FUELS
FUNCTIONAL MODELS
HALIDES
HALOGEN COMPOUNDS
LIQUEFACTION
METALS
NORTH AMERICA
OXIDES
OXYGEN COMPOUNDS
PETROLEUM PRODUCTS
REFRACTORY METALS
SEPARATION PROCESSES
TRANSITION ELEMENTS
USA
ZINC COMPOUNDS
ZINC HALIDES
010405* - Coal
Lignite
& Peat- Hydrogenation & Liquefaction