Catalysts for conversion of methane to higher hydrocarbons
Patent
·
OSTI ID:868626
- Morgantown, WV
Catalysts for converting methane to higher hydrocarbons such as ethane and ethylene in the presence of oxygen at temperatures in the range of about 700.degree. to 900.degree. C. are described. These catalysts comprise calcium oxide or gadolinium oxide respectively promoted with about 0.025-0.4 mole and about 0.1-0.7 mole sodium pyrophosphate. A preferred reaction temperature in a range of about 800.degree. to 850.degree. C. with a preferred oxygen-to-methane ratio of about 2:1 provides an essentially constant C.sub.2 hydrocarbon yield in the range of about 12 to 19 percent over a period of time greater than about 20 hours.
- Research Organization:
- National Energy Technology Laboratory (NETL), Pittsburgh, PA, Morgantown, WV (United States)
- Assignee:
- United States of America as represented by United States (Washington, DC)
- Patent Number(s):
- US 5177294
- OSTI ID:
- 868626
- Country of Publication:
- United States
- Language:
- English
Oxidative dimerization of methane over a lithium-promoted magnesium oxide catalyst
|
journal | September 1985 |
Active and selective catalysts for the synthesis of C2H4 and C2H6 via oxidative coupling of methane
|
journal | August 1986 |
The oxidative conversion of methane to higher hydrocarbons over alkali-promoted Mn/SiO2
|
journal | February 1987 |
Similar Records
Catalysts for conversion of methane to higher hydrocarbons
Catalysts for conversion of methane to higher hydrocarbons
Oxidative conversion of methane to higher hydrocarbons over alkali-promoted Mn/SiO/sub 2/
Patent Application
·
Wed May 15 00:00:00 EDT 1991
·
OSTI ID:868626
Catalysts for conversion of methane to higher hydrocarbons
Patent
·
Tue Jan 05 00:00:00 EST 1993
·
OSTI ID:868626
Oxidative conversion of methane to higher hydrocarbons over alkali-promoted Mn/SiO/sub 2/
Journal Article
·
Sun Feb 01 00:00:00 EST 1987
· J. Catal.; (United States)
·
OSTI ID:868626
Related Subjects
catalysts
conversion
methane
hydrocarbons
converting
ethane
ethylene
presence
oxygen
temperatures
range
700
degree
900
described
comprise
calcium
oxide
gadolinium
respectively
promoted
025-0
mole
1-0
sodium
pyrophosphate
preferred
reaction
temperature
800
850
oxygen-to-methane
ratio
provides
essentially
constant
hydrocarbon
yield
12
19
percent
period
time
20
hours
calcium oxide
reaction temperature
essentially constant
gadolinium oxide
converting methane
/585/
conversion
methane
hydrocarbons
converting
ethane
ethylene
presence
oxygen
temperatures
range
700
degree
900
described
comprise
calcium
oxide
gadolinium
respectively
promoted
025-0
mole
1-0
sodium
pyrophosphate
preferred
reaction
temperature
800
850
oxygen-to-methane
ratio
provides
essentially
constant
hydrocarbon
yield
12
19
percent
period
time
20
hours
calcium oxide
reaction temperature
essentially constant
gadolinium oxide
converting methane
/585/