Catalyst for coal liquefaction process
Patent
·
OSTI ID:864825
An improved catalyst for a coal liquefaction process; e.g., the H-Coal Process, for converting coal into liquid fuels, and where the conversion is carried out in an ebullated-catalyst-bed reactor wherein the coal contacts catalyst particles and is converted, in addition to liquid fuels, to gas and residual oil which includes preasphaltenes and asphaltenes. The improvement comprises a catalyst selected from the group consisting of the oxides of nickel molybdenum, cobalt molybdenum, cobalt tungsten, and nickel tungsten on a carrier of alumina, silica, or a combination of alumina and silica. The catalyst has a total pore volume of about 0.500 to about 0.900 cc/g and the pore volume comprises micropores, intermediate pores and macropores, the surface of the intermediate pores being sufficiently large to convert the preasphaltenes to asphaltenes and lighter molecules. The conversion of the asphaltenes takes place on the surface of micropores. The macropores are for metal deposition and to prevent catalyst agglomeration. The micropores have diameters between about 50 and about 200 angstroms (.ANG.) and comprise from about 50 to about 80% of the pore volume, whereas the intermediate pores have diameters between about 200 and 2000 angstroms (.ANG.) and comprise from about 10 to about 25% of the pore volume, and the macropores have diameters between about 2000 and about 10,000 angstroms (.ANG.) and comprise from about 10 to about 25% of the pore volume. The catalysts are further improved where they contain promoters. Such promoters include the oxides of vanadium, tungsten, copper, iron and barium, tin chloride, tin fluoride and rare earth metals.
- Research Organization:
- Hydrocarbon Research, Inc., Lawrenceville, NJ (United States)
- Sponsoring Organization:
- USDOE
- DOE Contract Number:
- AC22-78ET10742
- Assignee:
- Hydrocarbon Research, Inc. (Lawrenceville, NJ)
- Patent Number(s):
- 4,424,109
- Application Number:
- 06/251,828
- OSTI ID:
- 864825
- Country of Publication:
- United States
- Language:
- English
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Related Subjects
/208/
000
10
200
2000
25
50
500
80
900
addition
agglomeration
alumina
ang
angstroms
asphaltenes
barium
bed reactor
carried
carrier
catalyst
catalyst particle
catalyst particles
catalyst selected
catalysts
cc
chloride
coal
coal liquefaction
coal process
cobalt
combination
comprise
comprises
consisting
contacts
contain
conversion
convert
converted
converting
converting coal
copper
deposition
diameters
earth
earth metal
earth metals
ebullated-catalyst-bed
fluoride
fuels
gas
h-coal
h-coal process
improved
improved catalyst
improvement
improvement comprises
intermediate
iron
lighter
liquefaction
liquefaction process
liquid
liquid fuel
liquid fuels
macropores
metal
metal deposit
metal deposition
metals
micropores
molecules
molybdenum
nickel
oil
oxides
particles
pore
pore volume
pores
preasphaltenes
prevent
prevent catalyst
process
promoters
rare
rare earth
reactor
residual
residual oil
selected
silica
sufficiently
surface
takes
total
tungsten
vanadium
volume
volume comprises
000
10
200
2000
25
50
500
80
900
addition
agglomeration
alumina
ang
angstroms
asphaltenes
barium
bed reactor
carried
carrier
catalyst
catalyst particle
catalyst particles
catalyst selected
catalysts
cc
chloride
coal
coal liquefaction
coal process
cobalt
combination
comprise
comprises
consisting
contacts
contain
conversion
convert
converted
converting
converting coal
copper
deposition
diameters
earth
earth metal
earth metals
ebullated-catalyst-bed
fluoride
fuels
gas
h-coal
h-coal process
improved
improved catalyst
improvement
improvement comprises
intermediate
iron
lighter
liquefaction
liquefaction process
liquid
liquid fuel
liquid fuels
macropores
metal
metal deposit
metal deposition
metals
micropores
molecules
molybdenum
nickel
oil
oxides
particles
pore
pore volume
pores
preasphaltenes
prevent
prevent catalyst
process
promoters
rare
rare earth
reactor
residual
residual oil
selected
silica
sufficiently
surface
takes
total
tungsten
vanadium
volume
volume comprises