IP Library Granted Patent US 7,959,710
Granted Patent B2
US 7,959,710 · App. 12/648,900 · Granted Jun 14, 2011

System and method for removing water and siloxanes from gas

Assignee: FlexEnergy Energy Systems, Inc.
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Quick Facts
Patent No.
US 7,959,710
App. No.
12/648,900
Granted
Jun 14, 2011
Kind
B2
Abstract

A method of removing siloxanes from a gas that contains siloxanes and water, the method comprising: (a) expanding the gas to cool the gas and freeze at least some of the water in the gas; and (b) removing the siloxanes and frozen water from the expanded and cooled gas. The method may also include compressing the gas prior to expanding it. The step of expanding the gas may include expanding it through a turbine. The method may also include using an energy input mechanism to drive one or both of the compressor or turbine. The ice and siloxanes may be removed from the gas with a cyclonic separator.

Claims (19)

1. A system for processing gas that contains water vapor and siloxanes, the system comprising:

means for expanding the gas to freeze at least some of the water vapor into ice;

means for separating the ice and siloxanes from the gas; and

means for consuming the gas after removal of the water and siloxanes.

2. The system of claim 1 , wherein the means for expanding includes a turbine.

3. The system of claim 1 , wherein the means for separating includes one of a cyclonic separator, a coalescing filter, and a low-velocity plenum.

4. The system of claim 1 , wherein the means for consuming includes a flare.

5. The system of claim 1 , wherein the means for consuming includes an engine.

6. The system of claim 1 , further comprising a compressor compressing the gas to a pressure of about 90 psig prior to the fuel entering the means for consuming.

7. The system of claim 1 , further comprising a heat exchanger exchanging heat from the gas upstream of the means for expanding to the gas flowing out of the means for separating.

8. A method for conditioning and consuming gas, the method comprising:

(a) receiving wet, dirty gas containing water and siloxanes from a source of gas;

(b) expanding the wet, dirty gas to a temperature below the freezing temperature of water to create a flow of gas containing ice;

(c) separating ice and siloxanes from the flow of gas containing ice to create a dry, clean flow of gas; and

(d) consuming the dry, clean gas in a fuel consuming device.

9. The method of claim 8 , wherein step (a) includes receiving the wet, dirty gas from a landfill or waste water treatment facility.

10. The method of claim 8 , further comprising, prior to step (b), lowering the temperature of the gas to below the dew point of the gas but above the freezing temperature of water to condense at least some of the water in the gas, and removing at least some of the condensed water.

11. The method of claim 8 , wherein step (b) is performed with a turbine.

12. The method of claim 8 , further comprising boosting the pressure of the gas to about 90 psig prior to step (d).

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 24, 2011
From: INGERSOLL-RAND ENERGY SYSTEMS CORPORATION
To: FLEXENERGY ENERGY SYSTEMS, INC.
Reel/Frame 026018/0334 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 6, 2010
From: OLSEN, ANDREW J.; SULLIVAN, SHAUN D.
To: INGERSOLL RAND ENERGY SYSTEMS CORPORATION
Reel/Frame 023740/0244 →
Continuity (2)
Division 11532167 · Sep 15, 2006
Related Publication 20100107876A1 · May 6, 2010