IP Library Granted Patent US 7,163,636
Granted Patent B2
US 7,163,636 · App. 11/208,316 · Granted Jan 16, 2007

Multi-phase separation system

Assignee: Advanced Phase Separation, LLC
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Quick Facts
Patent No.
US 7,163,636
App. No.
11/208,316
Granted
Jan 16, 2007
Kind
B2
Abstract

A multi-phase separation system utilized to remove contaminants from fluids includes a pre-filtering module for filtering a contaminated fluid to provide a filtered contaminated fluid. A condenser module receives the filtered contaminated fluid and a contaminated gas phase for condensing the contaminated gas phase to a contaminated liquid. A phase reaction chamber converts the filtered contaminated fluid to a contaminated mist wherein the mist is subjected to a low energy, high vacuum environment for providing a first change of phase by separating into a contaminated gas phase and a liquid mist phase. The contaminated gas phase is carried out of the phase reaction chamber by a carrier air. A vacuum pump provides the low energy, high vacuum environment in the phase reaction chamber and delivers the contaminated gas phase to the condenser module for condensation providing a second change of phase.

Claims (28)

1. A method of removing contaminants from fluids comprising:

converting a contaminated fluid into a contaminated mist in a phase reaction chamber;

converting said contaminated mist into a contaminated gas and a liquid mist by subjecting said contaminated mist to a low energy, high vacuum environment within said phase reaction chamber;

condensing said contaminated gas into a contaminated liquid phase;

wherein the contaminated gas is condensed by passing said contaminated gas over coils comprising the contaminated fluid.

2. The method of claim 1 comprising the further step of continuously transporting said contaminated gas phase out of the phase reactor chamber using a carrier air.

3. The method of claim 2 comprising the further step of:

pre-filtering said contaminated fluid to form a filtered contaminated fluid before it is converted into said contaminated mist.

4. The method of claim 3 wherein said pre-filtering step comprises removing suspended solids from said contaminated fluid using a specific gravity separator.

5. The method of claim 3 wherein said pre-filtering step comprises removing oils from said contaminated fluid using a polypropylene screen.

6. The method of claim 3 comprising the further step of re-filtering said filtered contaminated fluid using a micron filtration bank module to remove particulate matter greater then five microns in diameter.

7. The method of claim 2 comprising the further step of storing said contaminated fluid in a primary flow control module to control the flow of said contaminated fluid to said phase reaction chamber.

8. The method of claim 2 comprising the further step of filtering the carrier air after it exits the condenser using at least one vapor carbon polisher.

9. The method of claim 2 comprising the further step of collecting the contaminated liquid phase.

10. The method of claim 2 comprising the further step of equalizing the temperature of the contaminated fluid and the carrier air before it enters the phase reaction chamber using a temperature equalization module.

11. The method of claim 2 comprising the further step of collecting the liquid mist.

12. A method of removing contaminants from fluids comprising:

heating a contaminated fluid in a condensation module with a contaminated gas;

condensing the contaminated gas to a contaminated liquid in said condensation module;

converting said contaminated fluid to a contaminated mist;

separating said contaminated mist into said contaminated gas and a liquid mist by subjecting said contaminated mist to a low energy high vacuum environment in a phase reaction chamber; and

transporting said contaminated gas to said condensation module.

13. A method as set forth in claim 12 comprising the further step of storing said contaminated liquid after condensation.

14. A method as set forth in claim 12 wherein the transport of said contaminated gas to said condensation module is accomplished through the use of a carrier air.

15. A method as set forth in claim 14 comprising the further step of passing said carrier air through at least one carbon polisher after it exits said condenser to remove any residual contaminants.

16. A method as set forth in claim 14 comprising the further step of equalizing the temperature of said contaminated fluid and said carrier air before it enters said phase reaction chamber.

17. The method of claim 12 , further comprising filtering the contaminated fluid to provide a filtered contaminated fluid.

18. The method of claim 12 , further comprising collecting said liquid mist.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 30, 2007
From: ADVANCED PHASE SEPARATION, LLC
To: KENDZIORSKI, E. ROBERT
Reel/Frame 018828/0810 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 30, 2007
From: KENDZIORSKI, E. ROBERT
To: LIQUID SEPARATION TECHNOLOGY AND EQUIPMENT, LLC
Reel/Frame 018828/0869 →
Continuity (2)
Continuation 1061907100 · Jul 12, 2003
Related Publication 20060037918A1 · Feb 23, 2006