Energy storage for combustion turbine using molten carbonate electrolyzer cell

Patent metadata

Field	Value
Publication number	US-2021363920-A1
Application number	US-202117396888-A
Country	US
Kind code	A1
Filing date	Aug 9, 2021
Priority date	Feb 18, 2019
Publication date	Nov 25, 2021
Grant date	—

Abstract

An energy storage system includes: a combustion turbine configured to output heated sweep gas; a reformer configured to receive natural gas and steam and to output reformed natural gas; a molten carbonate electrolyzer cell (“MCEC”) comprising an MCEC anode and an MCEC cathode, wherein the MCEC is configured to operate in a hydrogen-generation mode in which: the MCEC anode receives the reformed natural gas from the reformer, and outputs MCEC anode exhaust that contains hydrogen, and the MCEC cathode is configured to receive heated sweep gas from the combustion turbine, and to output MCEC cathode exhaust; and a storage tank configured to receive the MCEC anode exhaust that contains hydrogen.

First claim

What is claimed is:

1 . An energy storage system comprising:
a combustion turbine configured to output heated sweep gas; a reformer configured to receive natural gas and steam and to output reformed natural gas; a molten carbonate electrolyzer cell (“MCEC”) comprising an MCEC anode and an MCEC cathode, wherein the MCEC is configured to operate in a hydrogen-generation mode in which:
the MCEC anode is configured to receive the reformed natural gas from the reformer, and outputs MCEC anode exhaust that contains hydrogen, and
the MCEC cathode is configured to receive heated sweep gas from the combustion turbine, and to output MCEC cathode exhaust; and
a storage tank configured to receive the MCEC anode exhaust that contains hydrogen.

2 . The energy storage system of claim 1 , further comprising:
an electrochemical hydrogen compressor (“EHC”) comprising:
an EHC anode configured to receive the MCEC anode exhaust, and
an EHC cathode configured to output a purified hydrogen-containing stream to the storage tank.

3 . The energy storage system of claim 2 , wherein the EHC anode is configured to output an EHC anode exhaust that contains excess fuel.

4 . The energy storage system of claim 3 , further comprising:
a burner configured to receive the MCEC cathode exhaust and the EHC anode exhaust, and to increase a temperature of the reformer.

5 . The energy storage system of claim 3 , further comprising:
a burner configured to receive the heated sweep gas from the combustion turbine and the EHC anode exhaust, and to further heat the heated sweep gas before the heated sweep gas is received by the MCEC cathode.

6 . The energy storage system of claim 2 , further comprising:
a methanation catalyst configured to receive the MCEC anode exhaust and to convert carbon monoxide in the MCEC anode exhaust into methane.

7 . The energy storage system of claim 2 ,
a proton exchange membrane (PEM) fuel cell configured to receive a purified hydrogen-containing stream from the EHC cathode and/or the storage tank, and to output electricity.

8 . The energy storage system of claim 1 , further comprising:
a proton exchange membrane (PEM) fuel cell configured to receive the MCEC anode exhaust from the MCEC and/or a hydrogen-containing stream from the storage tank, and to output electricity.

9 . The energy storage system of claim 8 , wherein:
the PEM fuel cell is configured to output excess fuel, and the energy storage system further comprises a burner configured to receive the MCEC cathode exhaust, EHC anode exhaust, and the excess fuel from the PEM fuel cell, and to increase a temperature of the reformer.

10 . The energy storage system of claim 1 , further comprising:
a compressor configured to receive and pressurize hydrogen from the MCEC anode exhaust.

11 . The energy storage system of claim 1 , wherein the combustion turbine is configured to receive part of the reformed natural gas from the reformer.

12 . The energy storage system of claim 1 , wherein the MCEC is configured to operate in a power-generation mode in which the MCEC operates in reverse relative to the hydrogen-generation mode.

13 . The energy storage system of claim 1 , further comprising:
a heat recovery steam generator configured to generate the steam and supply the steam to the reformer.

14 . The energy storage system of claim 13 , wherein the heat recovery steam generator is configured to generate low-pressure steam.

15 . The energy storage system of claim 13 , wherein the heat recovery steam generator is configured to generate medium-pressure steam.

16 . An energy storage method utilizing a molten carbonate electrolyzer cell (“MCEC”) comprising an MCEC anode and an MCEC cathode, wherein the MCEC is configured to operate in a hydrogen-generation mode and the method comprises:
outputting heated sweep gas from a combustion turbine;
receiving natural gas and steam at a reformer and outputting reformed natural gas from the reformer;
receiving the reformed natural gas from the reformer at the MCEC anode and outputting MCEC anode exhaust that contains hydrogen from the MCEC anode;
receiving the heated sweep gas from the combustion turbine at the MCEC cathode and outputting MCEC cathode exhaust from the MCEC cathode; and
receiving the MCEC anode exhaust that contains hydrogen at a storage tank.

17 . The energy storage method of claim 16 , further comprising an electrochemical hydrogen compressor (“EHC”), the method comprising:
receiving the MCEC anode exhaust at an EHC anode; and
outputting a purified hydrogen-containing stream from an EHC cathode to the storage tank.

18 . The energy storage method of claim 17 , comprising:
receiving the MCEC anode exhaust at a methanation catalyst; and converting carbon monoxide in the MCEC anode exhaust into methane.

19 . The energy storage method of claim 17 ,
receiving a purified hydrogen-containing stream from the EHC cathode and/or the storage tank; and outputting electricity.

20 . The energy storage method of claim 17 ,
outputting excess fuel from a proton exchange membrane (PEM) fuel cell; receiving the MCEC cathode exhaust, EHC anode exhaust, and the excess fuel from the PEM fuel cell at a burner, and increasing a temperature of the reformer using the burner.

Assignees

• Fuelcell Energy Inc

Inventors

• Jahnke Fred C

Classifications

• Y02P20/129

  Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines · CPC title

• Y02B90/10

  Applications of fuel cells in buildings · CPC title

• H01M2250/405

  Cogeneration of heat or hot water · CPC title

• F05D2220/72

  a steam turbine · CPC title

• C01B2203/0233

  the reforming step being a steam reforming step · CPC title