Process and apparatus for the production of hydrogen by steam reforming of hydrocarbon
Patent
·
OSTI ID:873156
- Wescosville, PA
- Fogelsville, PA
- Allentown, PA
In the steam reforming of hydrocarbon, particularly methane, under elevated temperature and pressure to produce hydrogen, a feed of steam and hydrocarbon is fed into a first reaction volume containing essentially only reforming catalyst to partially reform the feed. The balance of the feed and the reaction products of carbon dioxide and hydrogen are then fed into a second reaction volume containing a mixture of catalyst and adsorbent which removes the carbon dioxide from the reaction zone as it is formed. The process is conducted in a cycle which includes these reactions followed by countercurrent depressurization and purge of the adsorbent to regenerate it and repressurization of the reaction volumes preparatory to repeating the reaction-sorption phase of the cycle.
- Research Organization:
- Air Products and Chemicals, Inc. (Allentown, PA)
- DOE Contract Number:
- FC36-95GO10059
- Assignee:
- Air Products and Chemicals, Inc. (Allentown, PA)
- Patent Number(s):
- US 6103143
- OSTI ID:
- 873156
- Country of Publication:
- United States
- Language:
- English
Dehydrogenation of Cyclohexane in a PSA Reactor Using Hydrogen Storage Alloy. [PSA型反応器による水素吸蔵合金を用いたシクロヘキサンの脱水素]
|
journal | January 1993 |
Equilibrium-limited periodic separating reactors
|
journal | August 1987 |
Hydrogen Production from Methane Steam Reforming Assisted by Use of Membrane Reactor
|
book | January 1991 |
Sorption-enhanced reaction process
|
journal | October 1996 |
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Related Subjects
/252/95/423/
adsorbent
apparatus
balance
carbon
carbon dioxide
catalyst
conducted
containing
containing essentially
countercurrent
cycle
depressurization
dioxide
elevated
elevated temperature
essentially
fed
feed
followed
formed
hydrocarbon
hydrogen
methane
mixture
partially
particularly
phase
preparatory
pressure
process
produce
produce hydrogen
production
products
purge
reaction
reaction product
reaction products
reaction volume
reaction zone
reaction-sorption
reactions
reform
reforming
reforming catalyst
regenerate
removes
repeating
repressurization
steam
steam reforming
temperature
volume
volume containing
volumes
zone
adsorbent
apparatus
balance
carbon
carbon dioxide
catalyst
conducted
containing
containing essentially
countercurrent
cycle
depressurization
dioxide
elevated
elevated temperature
essentially
fed
feed
followed
formed
hydrocarbon
hydrogen
methane
mixture
partially
particularly
phase
preparatory
pressure
process
produce
produce hydrogen
production
products
purge
reaction
reaction product
reaction products
reaction volume
reaction zone
reaction-sorption
reactions
reform
reforming
reforming catalyst
regenerate
removes
repeating
repressurization
steam
steam reforming
temperature
volume
volume containing
volumes
zone