Method of steam reforming methanol to hydrogen
Abstract
The production of hydrogen by the catalyzed steam reforming of methanol is accomplished using a reformer of greatly reduced size and cost wherein a mixture of water and methanol is superheated to the gaseous state at temperatures of about 800.degree. to about 1,100.degree. F. and then fed to a reformer in direct contact with the catalyst bed contained therein, whereby the heat for the endothermic steam reforming reaction is derived directly from the superheated steam/methanol mixture.
- Inventors:
-
- Lower Makefield, PA
- Issue Date:
- OSTI Identifier:
- 867477
- Patent Number(s):
- 4946667
- Assignee:
- Engelhard Corporation (Edison, NJ)
- Patent Classifications (CPCs):
-
B - PERFORMING OPERATIONS B01 - PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL B01B - BOILING
C - CHEMISTRY C01 - INORGANIC CHEMISTRY C01B - NON-METALLIC ELEMENTS
- Resource Type:
- Patent
- Country of Publication:
- United States
- Language:
- English
- Subject:
- method; steam; reforming; methanol; hydrogen; production; catalyzed; accomplished; reformer; greatly; reduced; size; cost; mixture; water; superheated; gaseous; temperatures; 800; degree; 100; fed; direct; contact; catalyst; bed; contained; therein; whereby; heat; endothermic; reaction; derived; directly; superheated steam; direct contact; contained therein; steam reforming; catalyst bed; greatly reduced; reforming reaction; reduced size; methanol mixture; greatly reduce; heated steam; /423/252/502/
Citation Formats
Beshty, Bahjat S. Method of steam reforming methanol to hydrogen. United States: N. p., 1990.
Web.
Beshty, Bahjat S. Method of steam reforming methanol to hydrogen. United States.
Beshty, Bahjat S. Mon .
"Method of steam reforming methanol to hydrogen". United States. https://www.osti.gov/servlets/purl/867477.
@article{osti_867477,
title = {Method of steam reforming methanol to hydrogen},
author = {Beshty, Bahjat S},
abstractNote = {The production of hydrogen by the catalyzed steam reforming of methanol is accomplished using a reformer of greatly reduced size and cost wherein a mixture of water and methanol is superheated to the gaseous state at temperatures of about 800.degree. to about 1,100.degree. F. and then fed to a reformer in direct contact with the catalyst bed contained therein, whereby the heat for the endothermic steam reforming reaction is derived directly from the superheated steam/methanol mixture.},
doi = {},
journal = {},
number = ,
volume = ,
place = {United States},
year = {1990},
month = {1}
}