System and method for high pressure, passive condensing of water from hydrogen in a reversible solid oxide fuel cell system

Patent metadata

Field	Value
Publication number	US-2016377342-A1
Application number	US-201514748979-A
Country	US
Kind code	A1
Filing date	Jun 24, 2015
Priority date	Jun 24, 2015
Publication date	Dec 29, 2016
Grant date	—

Abstract

A method for passively removing water from a stream of hydrogen gas includes receiving a stream of hydrogen gas that is water-saturated, having an initial pressure below about 1 psig and an initial temperature above about 25° C., compressing the stream of hydrogen gas to an elevated pressure, chilling the compressed stream of hydrogen gas to a low temperature, and condensing water from the compressed and chilled stream of hydrogen gas until the water content of the stream of hydrogen gas is below about 100 ppm.

First claim

What is claimed is:

1 . A method for passively removing water from a stream of hydrogen gas, comprising:
receiving a stream of hydrogen gas that is water-saturated, having an initial pressure below about 1 psig and an initial temperature above about 25° C.; compressing the stream of hydrogen gas to an elevated pressure; chilling the compressed stream of hydrogen gas to a low temperature; and condensing water from the compressed and chilled stream of hydrogen gas until the water content of the stream of hydrogen gas is below about 100 ppm.

2 . A method in accordance with claim 1 , further comprising removing condensed water from the stream of hydrogen gas in the compressor.

3 . A method in accordance with claim 1 , wherein condensing water from the compressed and chilled stream of hydrogen gas comprises passing the compressed and chilled stream of hydrogen gas through water trap.

4 . A method in accordance with claim 3 , further comprising removing condensed water from the water trap, reducing pressure of the condensed water, and draining the condensed water into a drain line through a ball float drain valve.

5 . A method in accordance with claim 1 , further comprising storing the compressed hydrogen gas in a storage container for later use as fuel for a solid oxide fuel cell.

6 . A method in accordance with claim 1 , wherein the stream of hydrogen gas has an initial pressure below 0.25 psig and an initial temperature of about 40° C.

7 . A method in accordance with claim 1 , wherein the stream of hydrogen gas has an initial water content of about 7%.

8 . A method in accordance with claim 1 , wherein the compressed stream of hydrogen gas prior to chilling has a water content of about 500 ppm.

9 . A method in accordance with claim 1 , wherein the elevated pressure is at least 250 psi.

10 . A method in accordance with claim 1 , wherein chilling the compressed stream of hydrogen gas comprises chilling the compressed stream of hydrogen gas to a temperature below about 10° C.

11 . A method for passively removing water from a stream of saturated hydrogen gas produced from a Reversible Solid Oxide Fuel Cell (RSOFC) unit operating in electrolysis mode, comprising:
receiving a stream of saturated hydrogen gas produced from a Reversible Solid Oxide Fuel Cell (RSOFC) unit operating in electrolysis mode, the stream of hydrogen gas having an initial pressure below about 0.5 psig and an initial temperature above about 25° C.; compressing the stream of hydrogen gas with a compressor to a pressure above 1000 psig; chilling the compressed stream of hydrogen gas to a temperature below about 10° C.; passively condensing water from the compressed and chilled stream of hydrogen gas to produce a water content of the stream of hydrogen gas below about 100 ppm; separating the water condensate from the H 2 gas; and storing the compressed hydrogen gas in a storage container for later use as fuel for the RSOFC unit.

12 . A method in accordance with claim 11 , further comprising removing condensed water from the stream of hydrogen gas in the compressor.

13 . A method in accordance with claim 11 , wherein compressing the stream of hydrogen gas comprises compressing the stream of hydrogen gas to a pressure of at least about 2500 psig.

14 . A method in accordance with claim 11 , wherein condensing water from the compressed and chilled stream of hydrogen gas comprises passing the compressed and chilled stream of hydrogen gas through a water trap.

15 . A system for passively removing water from a stream of hydrogen gas, comprising:
a conduit, coupled to deliver a stream of saturated hydrogen gas having an initial pressure below about 1 psig and an initial temperature above about 25° C.; a compressor, configured to compress the stream of hydrogen gas to an elevated pressure; a chiller, configured to chill the compressed stream of hydrogen gas to a low temperature; and a water trap, configured to passively receive water condensate from the compressed and chilled stream of hydrogen gas as the stream passes therethrough, and to separate the compressed and dewatered hydrogen from the condensate, the compressed and dewatered hydrogen having a water content of less than about 100 ppm.

16 . A system in accordance with claim 15 , further comprising a heat exchanger, associated with the compressor, configured to reduce a temperature of the compressed hydrogen gas

17 . A system in accordance with claim 16 , wherein the elevated pressure is above 250 psi.

18 . A system in accordance with claim 15 , wherein the chiller is configured to chill the compressed stream of hydrogen gas to a temperature below about 10° C.

19 . A system in accordance with claim 15 , wherein the water trap comprises a coalescing filter, configured to draw condensate from the compressed and chilled stream of hydrogen gas, and further comprising:
a pressure regulator, coupled to receive the condensate from the coalescing filter, configured to reduce a pressure of the condensate; and a ball float drain valve, coupled to the receive the condensate from the pressure regulator, configured to periodically transfer the condensate to a drain.

20 . A system in accordance with claim 15 , further comprising a suction vent and buffer tank, in fluid communication with an intake of the compressor, configured to maintain the initial pressure below about 0.5 psig.

Assignees

• Boeing Co

Inventors

• Mermelstein Joshua M

Classifications

• F25J3/0655 Primary

  separation of hydrogen (production of hydrogen containing gas in general C01B3/00, e.g. separation of hydrogen or hydrogen containing gases form gaseous mixtures at low temperatures C01B3/506) · CPC title

• C01B2203/0495

  the impurity being water · CPC title

• C01B3/50 Primary

  Separation of hydrogen or hydrogen-containing gases from gaseous mixtures, e.g. purification · CPC title

• C25B9/73

  of the filter-press type · CPC title

• C25B1/04

  by electrolysis of water · CPC title