IP Library › Granted Patent US 10,039,996
Granted Patent B2
US 10,039,996 · App. 14/711,759 · Granted Aug 7, 2018

Methods and systems for heating and manipulating fluids

Inventor: Franklin Alan Frick (Houston, TX)
Assignee: Phoenix Callente LLC
B01D3/007B01D1/0058B01D3/06C02F1/16
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Quick Facts
Patent No.
US 10,039,996
App. No.
14/711,759
Granted
Aug 7, 2018
Kind
B2
Abstract

Systems and methods are provided for heating and manipulating a fluid comprising a closed loop heating assembly thermally coupled to a fluid manipulation assembly.

Claims (69)

1. A method of evaporating water, comprising:

providing a first fluid-to-fluid heat exchanger having first and second fluid paths there through;

providing a closed-loop fluid heating subsystem comprising:

a fluid heater

a fluid pump, and

a fluid reservoir

all configured and arranged to heat the heating subsystem fluid to less than an atmospheric boiling point of the fluid and to circulate the fluid through the first fluid path of the first fluid-to-fluid heat exchanger;

providing an evaporation subsystem comprising:

a first flash tank configured to operate at a first pressure and to separate a water-containing mixture into liquid and vapor phases, and

a second fluid-to-fluid heat exchanger having third and fourth fluid paths there through,

a second flash tank configured to operate at a pressure less than the operating pressure of the first flash tank, and to separate a water-containing mixture into liquid and vapor phases;

pumping at least a portion of a water-containing liquid mixture from the second flash tank through the second fluid path of the first fluid-to-fluid heat exchanger;

transferring heat from the closed-loop heating subsystem fluid to the mixture in the second fluid path of the first fluid-to-fluid heat exchanger;

flashing the mixture heated in the first heat exchanger into its liquid and vapor phases in the first flash tank;

extracting at least a portion of the vapor from the first flash tank through the third fluid path of the second fluid-to-fluid heat exchanger to remove water from the mixture heated in the second fluid path of the first heat exchanger;

pumping a second portion of the mixture through the fourth fluid path of the second fluid-to-fluid heat exchanger;

transferring heat from the first flash tank vapor to the second portion of the mixture in the second fluid-to-fluid heat exchanger to thereby condense the first flash tank vapor to liquid;

flashing the heated second portion of the mixture into its liquid and vapor phases in the second flash tank; and

extracting at least a portion of the vapor from the second flash tank to remove water from the mixture heated in the second heat exchanger.

2. The method of claim 1 , further comprising:

operating the first flash tank at less than atmospheric pressure.

3. The method of claim 2 , further comprising:

pumping a portion of the liquid phase of the mixture in the second flash tank to an evaporation chamber;

spraying the mixture into the evaporation chamber; and

blowing air heated into the evaporation chamber to evaporate a portion of water from the mixture sprayed into the evaporation chamber.

4. The method of claim 2 , wherein the fluid heater is a gas fired boiler.

5. The method of claim 2 , wherein the fluid heater comprises an internal combustion genset.

6. The method of claim 5 , wherein the fluid heating subsystem comprises a heat exchanger configured to transfer thermal energy from genset exhaust gasses to the heating subsystem fluid.

7. The method of claim 2 , wherein the fluid heater comprises an internal combustion genset and an electric boiler.

8. The method of claim 1 , further comprising removing water condensed from flash tank

vapor from the evaporation subsystem.

9. A method of removing water from a water-containing mixture, comprising:

providing a closed-loop heating subsystem comprising a hydrocarbon-fueled fluid heater, a fluid pump, a fluid expansion tank and a first path through a primary fluid-to-fluid heat exchanger, all configured to heat and circulate a first fluid to less than an atmospheric boiling point of the first fluid;

providing an evaporation subsystem comprising a second path through the primary fluid-to-fluid heat exchanger, a secondary fluid-to-fluid heat exchanger, a plurality of flash tanks, and a condensing heat exchanger;

pumping a first portion of a water-containing mixture through the primary fluid-to-fluid heat exchanger;

transferring heat from the heating subsystem fluid to the first portion of the mixture in the primary fluid-to-fluid heat exchanger;

flashing the first portion of the mixture into its liquid and vapor phases in a first flash tank operating at a first pressure to evaporate a portion of water from the first portion of the mixture;

drawing the vapor from the first flash tank into the secondary fluid-to-fluid heat exchanger;

pumping a second portion of the mixture through the secondary fluid-to-fluid heat exchanger;

transferring heat from the first flash tank vapor to the second portion of the mixture in the secondary fluid-to-fluid heat exchanger;

flashing the second portion of the mixture into its liquid and vapor phases in a second flash tank operating at a second pressure less than the first pressure to evaporate a portion of water from the second portion of the mixture;

drawing the vapor from the second flash tank into the condensing heat exchanger to condense the vapor to liquid by transferring heat from the vapor; and

wherein the first portion of the mixture comprises liquid from both the first and second flash tanks.

10. The method of claim 9 , further comprising: operating the first flash tank at less than atmospheric pressure.

11. The method of claim 10 , wherein the condensing heat exchanger is a third fluid-to-fluid heat exchanger; and further comprising:

pumping a third portion of the mixture through the third heat exchanger to transfer heat from the second flash tank vapor to the third mixture portion;

exposing the third mixture portion to atmosphere to evaporate a portion of water from the third portion of the mixture; and

returning the remainder of the third portion of the mixture to a storage facility from which the first, second and third portions of the mixture are drawn.

12. The method of claim 9 , wherein the fluid heater comprises an internal combustion genset.

13. The method of claim 12 , wherein genset combusts waste gas.

14. The method of claim 13 , further comprising removing condensed vapor from the evaporation subsystem.

15. The method of claim 12 , wherein the fluid heater comprises an internal combustion genset and an electric boiler.

16. The method of claim 15 , wherein at least a portion of electrical power generated by the genset is sold back onto the electrical grid.

17. The method of claim 15 , wherein the genset is configured to combust waste gas.

18. The method of claim 4 , wherein the primary heat source comprises waste heat from the genset.

19. A method of removing water from a water-containing mixture, comprising:

providing a closed-loop heating subsystem configured to heat and circulate a fluid;

providing an evaporation subsystem comprising a plurality of flash tanks each configured to separate a mixture into vapor and liquid phases;

operating a first flash tank at a first pressure less than atmospheric pressure;

operating a second flash tank at a second pressure less than the first pressure;

mixing the water-containing mixture with liquid from the second flash tank to create a second flash tank mixture;

heating the second flash tank mixture with vapor from the first flash tank to a first temperature;

flashing the heated second flash tank mixture into its liquid and vapor phases in the second flash tank;

mixing liquid from the second flash tank with liquid from the first flash tank to create a first flash tank mixture;

heating the first flash tank mixture with the closed-loop fluid to a temperature greater than the first temperature;

flashing the heated first flash tank mixture into its liquid and vapor phases in the first flash tank;

removing condensed vapor from the evaporation subsystem; and

removing liquid in the first flash tank from the evaporation subsystem.

20. The method of claim 19 , further comprising monitoring one or more properties of the liquid from the first flash tank, and removing first flash tank liquid from the evaporation subsystem based on one or more of the monitored fluid properties.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 30, 2018
From: FRICK, F. ALAN, MR
To: PHOENIX CALIENTE LLC
Reel/Frame 046499/0054 →
Continuity (25)
Continuation In Part 14026842 · Sep 13, 2013
Division 13947082 · Jul 21, 2013
Continuation 13555122 · Jul 21, 2012
Continuation In Part 12638984 · Dec 16, 2009
Continuation In Part 11934645 · Nov 2, 2007
Continuation In Part 12615331 · Nov 10, 2009
Continuation 11748475 · May 14, 2007
Continuation In Part 11764270 · Jun 18, 2007
Continuation 11741570 · Apr 27, 2007
Continuation In Part 11738644 · Apr 23, 2007
Continuation In Part 13467551 · May 9, 2012
Continuation In Part 13069363 · Mar 22, 2011
Provisional Application 60794413 · Apr 24, 2006
Provisional Application 61992296 · May 13, 2014
Provisional Application 61993731 · May 15, 2014
Provisional Application 62034858 · Aug 8, 2014
Provisional Application 61249841 · Oct 8, 2009
Provisional Application 60883178 · Jan 3, 2007
Provisional Application 60864160 · Nov 2, 2006
Provisional Application 60800495 · May 15, 2006
Provisional Application 60795983 · Apr 28, 2006
Provisional Application 61510485 · Jul 22, 2011
Provisional Application 61484210 · May 9, 2011
Provisional Application 61316362 · Mar 22, 2010
Related Publication 20160114260A1 · Apr 28, 2016