Expander for soec applications

Patent metadata

Field	Value
Publication number	US-2021214849-A1
Application number	US-201917058970-A
Country	US
Kind code	A1
Filing date	Jul 9, 2019
Priority date	Jul 12, 2018
Publication date	Jul 15, 2021
Grant date	—

Abstract

In a method for generating various synthesis gases by electrolysis, comprising feeding steam and compressed air to the cathode and anode, respectively, of the electrolysis unit or of the first of a series of electrolysis units into the first of a series of electrolysis units, the electrolysis units are operated under an elevated gas pressure, and the oxygen-rich gas leaving the anode is subsequently expanded down to approximately ambient pressure using a gas expander. The electrolysis units are preferably solid oxide electrolysis cell (SOEC) stacks.

First claim

1 . A method for generating synthesis gas containing hydrogen, carbon monoxide or mixtures of hydrogen, carbon monoxide and carbon dioxide by electrolysis, said method comprising feeding steam and compressed air to the cathode and anode, respectively, of the electrolysis unit or of the first of a series of electrolysis units, wherein
the electrolysis unit or units is/are operated under an elevated gas pressure, and the oxygen-rich gas leaving the anode is subsequently expanded down to approximately ambient pressure using a gas expander.

2 . Method according to claim 1 , wherein the electrolysis units are solid oxide electrolysis cell (SOEC) stacks.

3 . Method according to claim 2 , wherein the SOEC stacks operate in the so-called thermoneutral mode.

4 . Method according to claim 1 , wherein the synthesis gas is selected from methanol synthesis gas, methane synthesis gas, ammonia synthesis gas and dimethyl ether (DME) synthesis gas.

5 . Method according to claim 2 , wherein the synthesis gas is selected from methanol synthesis gas, methane synthesis gas, ammonia synthesis gas and dimethyl ether (DME) synthesis gas.

6 . Method according to claim 3 , wherein the synthesis gas is selected from methanol synthesis gas, methane synthesis gas, ammonia synthesis gas and dimethyl ether (DME) synthesis gas.

7 . Method according to claim 2 , wherein the air is compressed in an amount sufficient to achieve 50% (v/v) oxygen at an exit of the SOEC stacks.

8 . Method according to claim 2 , wherein the steam is mixed with recycled hydrogen and pre-heated in a feed/effluent heat exchanged on a cathode side of the SOEC stacks.

9 . Method according to claim 8 , wherein, on the cathode side, steam is electrolyzed and oxygen is transported across an electrolyte to an anode side of the SOEC stacks.

10 . Method according to claim 8 , wherein a stream of hydrogen mixed with steam is passed through the feed/effluent heat exchanger prior to being further cooled down by generated high pressure steam.

11 . Method according to claim 10 , further comprising splitting the stream into a recycle hydrogen stream and residual steam which is sent to ammonia synthesis.

12 . Method according to claim 1 , wherein a compressor and the gas expander are connected to different lines.

13 . Method according to claim 1 , wherein a compressor and the gas expander are connected to a mutual line.

14 . Method according to claim 1 , wherein the gas is expanded down to a pressure of at most 0.2 barg by the gas expander.

15 . Method according to claim 1 , further comprising pre-heating the air in a feed/effluent heat exchanger to a first elevated temperature T 1 .

16 . Method according to claim 15 , wherein, following pre-heating, the pre-heated air enters an electrical pre-heater which heats the air to a second elevated temperature T 2 , wherein T 2 >T 1 .

17 . Method according to claim 16 , wherein the second elevated temperature T 2 is an inlet temperature of the SOEC stacks.

18 . Method according to claim 15 , wherein, after or as oxygen-enriched air leaves the SOEC stacks, heat is recuperated in the feed/effluent heat exchange, and wherein the oxygen-enriched air subsequently enters the gas expander.

19 . Method according to claim 1 , wherein the compressed air is compressed to a pressure greater than 20 barg and up to 40 barg.

20 . A method for generating synthesis gas containing hydrogen, carbon monoxide or mixtures of hydrogen, carbon monoxide and carbon dioxide by electrolysis, said method comprising feeding steam and compressed air to the cathode and anode, respectively, of the electrolysis unit or of the first of a series of electrolysis units, wherein
the electrolysis unit or units is/are operated under an elevated gas pressure, and the oxygen-rich gas leaving the anode is subsequently expanded down to approximately ambient pressure using a gas expander, wherein the compressed air is compressed to a pressure of up to 40 barg, and the oxygen-rich gas leaving the anode is of temperature from 650 to 850° C.

Assignees

• Haldor Topsoe As

Inventors

• Hansen John Bøgild

Classifications

• C25B1/23

  Carbon monoxide or syngas · CPC title

• C25B1/04

  by electrolysis of water · CPC title

• C25B15/08 Primary

  Supplying or removing reactants or electrolytes; Regeneration of electrolytes · CPC title

• C25B9/60 Primary

  Constructional parts of cells · CPC title

• C25B13/07

  based on ceramics · CPC title