US2013032472A1PendingUtilityA1
Apparatus for the electrical production of hydrogen
Est. expiryApr 9, 2030(~3.7 yrs left)· nominal 20-yr term from priority
C01B 3/56C01B 2203/04C01B 2203/043C01B 3/506C01B 2203/0465C01B 2203/145C01B 2203/146B01D 2256/16B01D 53/265Y02E60/36C25B 9/23C25B 15/083C25B 1/04C25B 15/08
30
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Claims
Abstract
An apparatus for the electrical production of hydrogen from water includes an electrolyzer ( 1 ) of the PEM type. The electrolyzer ( 1 ) has an inlet ( 2 ) for the introduction of water and a first outlet ( 3 ) for the hydrogen which is enriched with water and/or water vapor and is produced in the electrolyzer ( 1 ) and also a second outlet ( 4 ) for oxygen. A water separation device ( 7 ) which has at least a thermal separation stage ( 10 ) adjoins the electrolyzer ( 1 ).
Claims
exact text as granted — not AI-modified1 . An apparatus for the electrical production of hydrogen from water, the apparatus comprising:
an electrolyzer of the PEM type, which has an inlet for introducing water and a first outlet for the hydrogen enriched with water and/or water vapor and produced in the electrolyzer, as well as a second outlet for oxygen and water; and a water separation device with an inlet connected to the first outlet of the electrolyzer by means of a line and with a gas-carrying outlet leading to a hydrogen removal port in or at the apparatus, wherein the water separation device comprises a thermal separation stage.
2 . An apparatus in accordance with claim 1 , wherein the water separation stage further comprises a second separation stage wherein the thermal separation stage is followed by the second separation stage.
3 . An apparatus in accordance with claim 2 , wherein the second separation stage is also a thermal separation stage such that there are first and second thermal separation stages.
4 . An apparatus in accordance with claim 3 , further comprising a common cooling circuit wherein the first and second thermal separation stages are connected to the common cooling circuit.
5 . An apparatus in accordance with claim 2 , wherein the second separation stage has a pressure swing adsorption apparatus.
6 . An apparatus in accordance with claim 1 , further comprising a mechanical preseparator between the first outlet of the electrolyzer and the inlet of the thermal separation stage.
7 . An apparatus in accordance with claim 6 , wherein the water separated in the separation stage is introduced into the preseparator via return lines.
8 . An apparatus in accordance with claim 7 , wherein the return lines are provided with shut-off valves and a bypass line, which bypasses the preseparator and can be shut off by means of a valve, and wherein gas-carrying inlet and outlet lines of the preseparator can be shut off by means of valves.
9 . An apparatus in accordance with claim 7 , wherein the preseparator is connected to the inlet for introducing water by means of a line in the form of a return line that can be shut off by means of a valve.
10 . An apparatus in accordance with claim 1 , wherein the water separation device has a water-carrying outlet of at least the first separation stage, which said outlet is connected to the inlet of the electrolyzer for returning the water by means of a line at least from time to time.
11 . An apparatus in accordance with claim 1 , wherein the thermal separation stage has an electrically operated cooling apparatus.
12 . An apparatus in accordance with claim 11 , wherein the cooling apparatus comprises an absorber cooling apparatus, a compressor cooling apparatus or a cooling apparatus operated with Peltier elements.
13 . An apparatus in accordance with claim 1 , wherein the separation stage is designed such that hydrogen arriving from the electrolyzer and enriched with water and/or hydrogen is cooled to a temperature below 5° C. and above the freezing point.
14 . An apparatus in accordance with claim 2 , wherein the second separation stage is a thermal separation stage, which is designed such that the hydrogen discharged from the first separation stage and enriched with water and/or water vapor is cooled to below 0° C.
15 . An apparatus in accordance with claim 2 , wherein the second separation stage is a thermal separation stage and is operated intermittently.
16 . An apparatus in accordance with claim 1 , wherein hydrogen that is produced is maintained under a pressure of 20 bar or more.
17 . An electrical hydrogen from water production apparatus comprising:
a polymer electrolyte membrane electrolyzer comprising an electrolyzer body with an electrolyzer inlet for introducing water, an electrolyzer first outlet for hydrogen enriched with water and/or water vapor and a second electrolyzer outlet for oxygen and water; an electrolyzer outlet line; and a water separator with a separator inlet connected to the electrolyzer first outlet via said electrolyzer outlet line and with a gas-carrying outlet leading to a hydrogen removal port, the water separator comprising a thermal separation stage.
18 . An apparatus in accordance with claim 17 , wherein said water separator further comprises another separation stage wherein the thermal separation stage is followed by the another separation stage.
19 . An apparatus in accordance with claim 18 , wherein the another separation stage is also a thermal separation stage such that there are first and second thermal separation stages.
20 . An apparatus in accordance with claim 19 , further comprising a cooling apparatus cooling the first and second thermal separation stages.Join the waitlist — get patent alerts
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