Dry cooling system using thermally induced vapor polymerization

Patent metadata

Field	Value
Publication number	US-9920658-B2
Application number	US-201715642388-A
Country	US
Kind code	B2
Filing date	Jul 6, 2017
Priority date	Dec 8, 2015
Publication date	Mar 20, 2018
Grant date	Mar 20, 2018

Abstract

A system and method for providing dry cooling of a source liquid, having a plurality of heat exchangers which depolymerize and polymerize a polymer. Specifically, the depolymerization process is endothermic and draws heat from a source liquid in a first heat exchanger, and the polymerization process is exothermic and expels heat from a second heat exchanger. Additional heat exchangers and holding tanks may be incorporated in the system and method. In some embodiments the system further provides additional cooling of the polymer prior to depolymerization using cooler night ambient air.

First claim

The invention claimed is:

1. A dry-cooling system useful in absorbing heat from a source liquid, the system comprising a depolymerization cooling unit (DCU) in fluid communication with a polymerization heating unit (PHU), wherein:
the DCU comprises a DCU heat exchanger, wherein the source liquid cycles through the DCU;
wherein a first acid based catalyst is disposed within the DCU, and the DCU receives a polymer liquid and water;
wherein contact of the polymer over the first catalyst within the DCU causes an endothermic reaction, converting the polymer to a monomer gas, wherein the endothermic reaction causes at least a portion of the water to vaporize into water vapor, and wherein the endothermic reaction further draws heat from the source liquid as the source liquid cycles through the DCU, and
wherein the DCU expels the monomer gas and water vapor; and

the PHU comprises a PHU heat exchanger,
wherein a second acid based catalyst is disposed within the PHU, and the PHU receive the monomer gas and the water vapor,
wherein flow of the monomer gas over the second acid based catalyst causes an exothermic reaction, converting the monomer gas to the polymer liquid, and wherein the exothermic reaction generates heat which is rejected from the system through the PHU, and
wherein the PHU expels the polymer liquid and the water for conveyance to the DCU.

2. The dry-cooling system of claim 1 , the system further comprising a liquid to liquid separator and a pair of pumps, in fluid communication between the PHU and the DCU, to separate the polymer liquid from the water, and convey the polymer liquid and the water expelled from the PHU to the DCU.

3. The dry-cooling system of claim 1 , further comprising a blower in fluid communication with the DCU and the PHU, wherein the blower is designed and configured to withdraw the monomer vapor and water vapor from the DCU, under pressure of between about 4 to 9 psia, and convey the monomer vapor and water vapor to the PHU under pressure of between about 13 to 25 psia.

4. The dry-cooling system of claim 1 , wherein the polymer is paraldehyde.

5. The dry-cooling system of claim 1 , wherein the first acid based catalyst and the second acid based catalyst are the same.

6. The dry-cooling system of claim 1 , the system further comprising a first polymer separation unit (PSU) in fluid communication between the DCU and the PHU, wherein:
the PSU comprises a PSU heat exchanger, wherein the source liquid cycles through the PSU,
wherein the PSU receives from the DCU the monomer gas and water vapor, which stream also comprises a polymer gas,
wherein heat from the source liquid is transferred to the polymer gas, monomer gas and water vapor, to further separate the monomer gas from the polymer gas, and liquefy the polymer gas, and
wherein the PSU expels the monomer gas to the PHU.

7. The dry-cooling system of claim 6 , wherein the PSU further receives from the PHU the polymer liquid, a monomer liquid and water, and
wherein heat from the source liquid is transferred to the polymer liquid, the monomer liquid and the water, to further separate the polymer liquid from the monomer liquid, and vaporize the monomer liquid to the monomer gas, and
wherein the PSU expels the polymer liquid and the water for conveyance back to the DCU.

8. The dry cooling system of claim 7 , further comprising a cold energy storage assembly comprising a day storage tank (DST), a polymer cooling unit (PCU) and a cold-energy storage tank (CST), wherein:
the DST is in fluid communication with the first PSU to receive the polymer liquid, and with the PCU to expel the polymer liquid,
the PCU comprises a PCU heat exchanger, and receives from the DST the polymer liquid, and expels the cooler polymer liquid from the PCU, and
the CST is in fluid communication with the PCU to receive the cooler polymer liquid, and is further in fluid communication with the DCU for expelling the cooler polymer liquid to the DCU.

9. The dry-cooling system of claim 8 , further comprising:
a pump in fluid communication between the PSU, the DST and the DCU,
a three-way valve in fluid communication with the pump, which three-way valve directs flow of the polymer liquid among the PSU, DCU, DST, PCU and CST.

10. The dry-cooling system of claim 6 , further comprising a second PSU in fluid communication between the PHU and the DCU, wherein:
the second PSU receives from the PHU the polymer liquid, a monomer liquid and water,
wherein heat from the source liquid is transferred to the polymer liquid, the monomer liquid and water, to further separate the polymer liquid from the monomer liquid, and vaporize the monomer liquid to the monomer gas; and
wherein the second PSU expels the polymer liquid and water for conveyance back to the DCU.

11. A method for a dry-cooling system useful in absorbing heat from a source liquid, the method comprising the steps of:
providing a polymer, water and a source liquid;
in a first heat exchanger through which the source liquid flows, converting the polymer to a monomer vapor over a first catalyst, causing an endothermic reaction over the catalyst, the endothermic reaction drawing heat from the source liquid and causing the water to vaporize into a water vapor;
withdrawing the monomer vapor and water vapor from the first heat exchanger;
in a second heat exchanger in fluid communication with the first heat exchanger, receiving the monomer vapor and water vapor and converting the monomer vapor to a polymer liquid over a second catalyst, causing an exothermic reaction over the catalyst, the exothermic reaction expelling heat through the heat exchanger to an environment; and
discharging the polymer liquid and the water from the second heat exchanger back to the first heat exchanger.

12. The process of claim 11 , wherein the source liquid is power plant condenser water.

13. The process of claim 11 , wherein the source liquid is exhausted steam from power plant steam turbine last stage.

14. The method for a polymerization cycle of claim 11 , further comprising the steps of
in a third heat exchanger through which the source liquid also flows, receiving the monomer vapor from the first heat exchanger and the polymer liquid from the second heat exchanger, and further separating the monomer gas from the polymer liquid, using the source liquid as a heat source;
discharging the polymer liquid to the first heat exchanger, and discharging the monomer vapor to the second heat exchanger.

15. The method for a polymerization cycle of claim 14 , further comprising the steps of:
in a first tank, receiving the polymer liquid from the third heat exchanger before it is delivered to the first heat exchanger;
in a fourth heat exchanger, receiving the polymer liquid from the first tank and flowing air past the fourth heat exchanger to lower the temperature of the polymer liquid;
in a second tank, receiving and storing the cooler polymer liquid from the fourth heat exchanger; and
discharging the stored cooler polymer liquid to the first heat exchanger.

16. A method for cooling a source liquid, the method comprising:
in a first heat exchanger through which a source liquid flows, depolymerizing a polymer in an endothermic reaction, thereby drawing heat from the source liquid and producing a monomer gas, and vaporizing water to form a water vapor;
withdrawing the monomer gas and the water vapor from the first heat exchanger;
in a second heat exchanger, polymerizing the monomer gas and condensing the water vapor, producing the polymer and the water; and
delivering the polymer and the water to the

Assignees

• Applied Res Associates Inc

Inventors

• Shaaban Aly H
• Zhou gong
• Escobar Sergio
• Mormile Joshua J
• Kettell Desiree

Classifications

• F28D20/003

  using thermochemical reactions · CPC title

• F25B23/00

  Machines, plants or systems, with a single mode of operation not covered by groups F25B1/00 - F25B21/00, e.g. using selective radiation effect · CPC title

• F01K3/004

  Accumulation in the liquid branch of the circuit · CPC title

• F25B13/00

  Compression machines, plants or systems, with reversible cycle (defrosting cycles F25B47/02) · CPC title

• F01K7/16

  the engines being only of turbine type (the engines using steam of critical or overcritical pressure F01K7/32; the engines being of extraction or non-condensing type F01K7/34) · CPC title