Process and apparatus for producing hydrogen
View Patent ↗A process and apparatus for producing hydrogen for a fuel cell by (a) reacting a fuel comprising a hydrocarbon and/or an oxygenate with steam, under steam reforming conditions in a reforming reactor to produce a product stream comprising hydrogen, (b) feeding at least part of the hydrogen produced in step a) to a fuel cell, to produce electric power and a waste stream comprising hydrogen, (c) reacting at least part of the waste stream from step b) with an oxygen-containing gas in a combustion reactor, and (d) using the heat energy produced in step c) to supply energy to the steam reforming reaction in step a) in which the combustion reactor is positioned within the reforming reactor to facilitate heat transfer between the stages.
1. A process for producing hydrogen for a fuel cell, said process comprising:
a) reacting a fuel comprising a hydrocarbon and/or an oxygenate with steam, under steam reforming conditions in a reforming reactor to produce a product stream comprising hydrogen,
b) feeding at least part of the hydrogen produced in step a) to a fuel cell, to produce electric power and a waste stream comprising hydrogen,
c) reacting at least part of the waste stream from step b) with an oxygen-containing gas in a combustion reactor positioned within the reforming reactor,
d) using a first portion of the heat energy produced in step c) to supply energy to the steam reforming reaction in step a), and
e) using a second portion of the heat energy from the effluent emerging from the combustion reactor of step c) to heat a feed to the process,
wherein the fuel is pre-treated prior to the reforming step a) by pre-reforming in a pre-reformer to produce methane and further wherein the reforming reactor is positioned within the pre-reformer.
2. A process as claimed in claim 1 in which the combustion chamber is positioned concentrically within the reformer reactor.
3. A process as claimed in claim 1 in which the steam reforming step a) is performed at a temperature in the range from 1 to 30 bara.
4. A process as claimed in claim 3 in which the steam reforming step a) is performed at a pressure greater than atmospheric pressure.
5. A process as claimed in claim 1 in which the Steam reforming step a) is performed at a temperature in the range from 700 to 1000° C.
6. A process as claimed in claim 4 in which the steam reformer is operated in excess of 2 bara and hydrogen from step a) is purified using a membrane before being introduced into the fuel cell.
7. A process as claimed in claim 1 in which the hydrogen is fed to a storage system.
8. A process as claimed in claim 2 in which the steam reforming step a) is performed at a pressure in the range from 1 to 30 bara.
9. A process as claimed in claim 2 in which the steam reforming step a) is performed at a temperature in the range from 700 to 1000° C.
10. A process as claimed in claim 2 in which the product stream produced in step a) comprises carbon monoxide and in which said carbon monoxide is converted to carbon dioxide in one or more of the reactions selected from the group consisting of (i) reacting with an oxygen-containing gas to produce carbon dioxide, (ii) reacting with steam to produce carbon dioxide and hydrogen and (iii) contacting with an oxygen-containing gas under partial oxidation conditions to oxidize carbon monoxide in preference to hydrogen.
11. A process as claimed in claim 2 in which the hydrogen is fed to a storage system.
12. A process as in claim 7 wherein the hydrogen storage system comprises a tank, a metal hydride or both.
13. A process as in claim 11 wherein the hydrogen storage system comprises a tank, a metal hydride or both.
14. A process as for producing hydrogen for a fuel cell, said process comprising:
a) reacting a fuel comprising a hydrocarbon and/or an oxygenate with steam under steam reforming conditions in a reforming reactor to produce a product stream comprising hydrogen,
b) feeding at least part of the hydrogen produced in step a) to a fuel cell to produce electric power and a waste stream comprising hydrogen,
c) reacting at least part of the waste stream from step b) with an oxygen-containing gas in a combustion reactor positioned within the reforming reactor,
d) using a first portion of the heat energy produced in step c) to supply energy to the steam reforming reaction in step a), and
e) using a second portion of the heat energy from the effluent emerging from the combustion reactor of step c) to heat a feed to the process, wherein the product stream produced in step a) comprises carbon monoxide and in which said carbon monoxide is converted to carbon dioxide in one or more of the reactions selected from the group consisting of (i) reacting with an oxygen-containing gas to produce carbon dioxide, (ii) reacting with steam to produce carbon dioxide and hydrogen and (iii) contacting with an oxygen-containing gas under partial oxidation conditions to oxidize carbon monoxide in preference to hydrogen, in which heat produced in one or more of steps (i), (ii) and (iii) is used as a source of energy for the steam reforming step a).