Electrolyzer system including a heat pump and method of operating thereof

Patent metadata

Field	Value
Publication number	US-12529153-B2
Application number	US-202418950977-A
Country	US
Kind code	B2
Filing date	Nov 18, 2024
Priority date	Nov 21, 2023
Publication date	Jan 20, 2026
Grant date	Jan 20, 2026

Abstract

An electrolyzer system includes stacks of electrolyzer cells configured receive steam and air, and output a hydrogen product stream and an oxygen exhaust stream, and a first heat pump configured to extract heat from the oxygen exhaust stream to generate a first portion of the steam provided to the stacks.

First claim

The invention claimed is:

1 . An electrolyzer system, comprising:
stacks of electrolyzer cells configured receive steam and air, and output a hydrogen product stream and an oxygen exhaust stream; a first heat pump configured to extract heat from the oxygen exhaust stream to generate a first portion of the steam provided to the stacks; a water conduit fluidly connected to a water source; an exhaust conduit fluidly connecting an oxygen outlet of the stacks to an oxygen inlet of the first heat pump, and configured to receive the oxygen exhaust stream from the stacks; and a second heat pump having a water inlet fluidly connected to the water conduit, a water outlet fluidly connected to a water inlet of the first heat pump by a second connecting conduit, and an air inlet fluidly connected to the exhaust conduit, wherein the second heat pump is configured to extract heat from the oxygen exhaust stream output from the first heat pump to preheat liquid water provided from the water conduit.

2 . The electrolyzer system of claim 1 , further comprising a heat exchanger configured to extract heat from the oxygen exhaust stream to generate a second portion of the steam provided to the stacks.

3 . The electrolyzer system of claim 2 , further comprising:
a steam conduit fluidly connected to a steam outlet of the heat exchanger and to a steam inlet of the stacks, and configured to provide the steam to the stacks, wherein the exhaust conduit fluidly connects the oxygen outlet of the stacks in series to an oxygen inlet of the heat exchanger and to the oxygen inlet of the first heat pump.

4 . The electrolyzer system of claim 3 , further comprising a first connecting conduit fluidly connecting a steam outlet of the first heat pump to a water inlet of the heat exchanger, wherein heat exchanger is configured to receive liquid water and the first portion of the steam from the first heat pump via the first connecting conduit and to generate the second portion of the steam provided to the stacks.

5 . The electrolyzer system of claim 3 , wherein the water conduit fluidly connects the water source to the water inlet of the first heat pump and to a water inlet of the heat exchanger in parallel.

6 . The electrolyzer system of claim 3 , wherein the first and second heat pumps each comprise:
a compressor configured to compress a working fluid; a condenser configured to condense the compressed working fluid; an expansion value configured to lower a pressure of the condensed working fluid; and an evaporator configured to evaporate the lowered pressure working fluid.

7 . The electrolyzer system of claim 6 , wherein:
the exhaust conduit is fluidly connected to the evaporators of the first and second heat pumps; and the steam conduit is fluidly connected to the condensers of the first and second heat pumps.

8 . The electrolyzer system of claim 7 , further comprising:
a hydrogen processor configured to compress the hydrogen product stream; a product conduit fluidly connecting the hydrogen processor to the stacks, and configured to transfer the hydrogen product stream from the stacks to the hydrogen processor; and a steam generator configured to generate a third portion of the steam provided to the steam conduit.

9 . The electrolyzer system of claim 8 , wherein:
the electrolyzer system further comprises a plurality of electrolyzer modules that each comprise a hotbox housing at least one of the stacks; the stacks comprise solid oxide electrolyzer cell stacks; the water conduit fluidly connects the water source to the steam generator and the second heat pump in parallel; the steam conduit fluidly connects inlets of the electrolyzer modules to outlets of the heat exchanger and the steam generator; and the exhaust conduit fluidly connects the outlets of electrolyzer modules to inlets of the heat exchanger and the first and second heat pumps.

10 . A method of operating an electrolyzer system, comprising:
providing steam and air to stacks of electrolyzer cells to generate and output a hydrogen product steam and an oxygen exhaust stream; providing the oxygen exhaust stream from an oxygen exhaust of the stacks to an oxygen inlet of a first heat pump through an exhaust conduit; extracting heat from the oxygen exhaust stream in the first heat pump to generate a first portion of the steam provided to the stacks; providing the oxygen exhaust stream from the first heat pump to an air inlet of a second heat pump through the exhaust conduit; providing liquid water from a water source to a water inlet of the second heat pump through a water conduit; preheating the liquid water in the second heat pump by extracting heat from the oxygen exhaust stream output from the first heat pump; and providing the preheated liquid water from a water outlet of the second heat pump to a water inlet of the first heat pump through a second connecting conduit.

11 . The method of claim 10 , further comprising:
providing the oxygen exhaust stream to a heat exchanger; and extracting heat from the oxygen exhaust stream in the heat exchanger to generate a second portion of the steam provided to the stacks, wherein the step of providing the oxygen exhaust stream to the first heat pump comprises providing the oxygen exhaust stream from the heat exchanger to the first heat pump.

12 . The method of claim 11 , further comprising:
providing a portion of the preheated liquid water and the first portion of the steam from the first heat pump to the heat exchanger.

13 . The method of claim 12 , wherein:
the oxygen exhaust stream provided to the heat exchanger has a temperature ranging from about 200° C. to about 250° C.; the oxygen exhaust stream provided from the heat exchanger to the first heat pump has a temperature ranging from about 110° C. to about 130° C.; and the oxygen exhaust stream provided from the first heat pump to the second heat pump has a temperature ranging from about 70° C. to about 90° C.

14 . The method of claim 13 , wherein:
the liquid water provided to the second heat pump has a temperature below 80° C.; the preheated liquid water provided from the second heat pump to the first heat pump has a temperature ranging from about 80° C. to about 100° C.; and the preheated liquid water and the first portion of the steam provided from the first heat pump to the heat exchanger has a temperature ranging from about 110° C. to about 130° C.

15 . The method of claim 11 , further comprising providing the liquid water to the heat exchanger to generate the second portion of the steam in parallel with the providing the liquid water to first heat pump.

16 . The method of claim 11 , further comprising providing the liquid water to a steam generator to generate a third portion of the steam in parallel with the providing the liquid water to first heat pump.

17 . The method of claim 16 , wherein more of the liquid water is provided to the first heat pump during a steady state operating mode of the stacks than during a startup mode of the stacks.

18 . The method of claim 10 , wherein:
the electrolyzer system further comprises a plurality of electrolyzer modules that each comprise a hotbox housing at least one of the stacks; the stacks comprise solid oxide electrolyzer cell stacks; the steam is provided from the first heat pump to the plurality of the electrolyzer modules; and the oxygen exhaust stream is provided from the plurality of the electrolyzer modules to the first heat pump.

19 . An electrolyzer system, comprising:
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Assignees

• Bloom Energy Corp

Inventors

• Prasher Ravi
• Sridhar K R
• Petrucha Michael
• Weingaertner David

Classifications

• C25B15/08

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

• C25B15/021 Primary

  of heating or cooling · CPC title

• C25B9/77

  having diaphragms · CPC title

• C25B1/042

  by electrolysis of steam · CPC title

• Y02E60/36

  Hydrogen production from non-carbon containing sources, e.g. by water electrolysis · CPC title