IP Library Granted Patent US 7,601,207
Granted Patent B2
US 7,601,207 · App. 11/691,726 · Granted Oct 13, 2009

Gas recovery system

Assignee: Proton Energy Systems, Inc.
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Quick Facts
Patent No.
US 7,601,207
App. No.
11/691,726
Granted
Oct 13, 2009
Kind
B2
Abstract

A gas recovery system is disclosed. The gas recovery system includes a gas source productive of a gaseous stream comprising moisture, a gas dryer in fluid communication with and downstream of the gas source, and an electrochemical compressor in fluid communication with and downstream of the gas dryer. The gas dryer is disposed to receive the gaseous stream and produce a delivery stream absent moisture and a slipstream comprising moisture. The electrochemical compressor is disposed to receive the slipstream at a first pressure and produce a compressed stream at a second pressure greater than the first pressure.

Claims (48)

1. A gas recovery system comprising:

a gas source productive of a gaseous stream comprising moisture;

a gas dryer in fluid communication with and downstream of the gas source, the gas dryer disposed to receive the gaseous stream and produce a delivery stream absent moisture and a slipstream comprising moisture; and

an electrochemical compressor in fluid communication with and downstream of the gas dryer, the electrochemical compressor disposed to receive the slipstream at a first pressure and produce a compressed stream at a second pressure greater than the first pressure.

2. The system of claim 1 , further comprising:

a phase separator in fluid communication with and downstream of the gas source, the phase separator in fluid communication with and downstream of and upstream of the electrochemical compressor, the phase separator in fluid communication with and upstream of the gas dryer.

3. The system of claim 1 , wherein:

the gas source is an electrochemical cell.

4. The system of claim 3 , wherein:

the electrochemical cell and the electrochemical compressor are integrally arranged to define a single cell stack.

5. The system of claim 4 , further comprising:

flow ports within the single cell stack that control flow between the electrochemical cell and the electrochemical compressor.

6. The system of claim 3 , wherein:

the electrochemical cell is an electrolysis cell.

7. The system of claim 6 , wherein:

the gaseous stream, the delivery stream, and the slipstream comprise hydrogen gas.

8. The system of claim 7 , wherein:

the electrochemical compressor is disposed to recover the hydrogen gas from the slipstream to increase a productive efficiency of the electrochemical cell system.

9. The system of claim 6 , wherein:

the electrolysis cell produces hydrogen gas near ambient pressure.

10. The system of claim 6 , wherein:

the electrolysis cell produces hydrogen gas at a pressure less than or equal to 15 bar.

11. The system of claim 6 , wherein:

the electrolysis cell produces hydrogen gas at a pressure greater than 15 bar and less than or equal to 30 bar.

12. The system of claim 6 , wherein:

the electrolysis cell produces hydrogen gas at a pressure greater than 30 bar and less than or equal to 200 bar.

13. The system of claim 1 , wherein:

the gas dryer comprises a Pressure Swing Adsorption unit in fluid communication with and upstream of and downstream of the electrochemical compressor.

14. The system of claim 1 , wherein:

the slipstream is greater than about 5 percent and less than about 15 percent of the gaseous stream.

15. A method to increase a productive efficiency of a gas production system, the method comprising:

producing a gaseous stream comprising moisture by a gas source;

obtaining the gaseous stream and making available a dry delivery stream and a moist slipstream via a gas dryer;

recovering the moist slipstream from the gas dryer by an electrochemical compressor and adding it to the gaseous stream, thereby increasing the productive efficiency of the gas production system.

16. The method of claim 15 , wherein:

the recovering comprises obtaining the slipstream at a first pressure and in response thereto, generating a compressed stream at a second pressure greater than the first pressure.

17. The method of claim 15 , further comprising:

separating hydrogen gas from liquid water in the gaseous stream and the moist slipstream via a phase separator.

18. The method of claim 15 , wherein the producing comprises:

producing a gaseous stream by an electrochemical cell.

19. The method of claim 15 , wherein the producing comprises:

producing a gaseous stream comprising hydrogen gas by an electrolysis cell.

20. The method of claim 19 , wherein the producing comprises:

producing hydrogen gas near ambient pressure.

21. The method of claim 19 , wherein the producing comprises:

producing hydrogen gas at a pressure less than or equal to 15 bar.

22. The method of claim 19 , wherein the producing comprises:

producing hydrogen gas at a pressure greater than 15 bar and less than or equal to 30 bar.

Assignments (3)
RELEASE OF SECURITY INTEREST Recorded Feb 19, 2013
From: PERSEUS PARTNERS VII, L.P.
To: PROTON ENERGY SYSTEMS, INC.
Reel/Frame 029834/0750 →
SECURITY AGREEMENT Recorded Jun 8, 2007
From: PROTON ENERGY SYSTEMS, INC.
To: PERSEUS PARTNERS VII, L.P.
Reel/Frame 019399/0436 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 27, 2007
From: MOULTHROP, LAWRENCE CLINTON; ANDERSON, EVERETT BRAGG
To: PROTON ENERGY SYSTEMS, INC.
Reel/Frame 019070/0748 →
Continuity (4)
Continuation In Part 1104711900 · Jan 31, 2005
Continuation 0996672700 · Sep 28, 2001
Provisional Application 6023627800 · Sep 28, 2000
Related Publication 20080236396A1 · Oct 2, 2008