Trans-critical thermodynamic system and method for removing solutes from fluid

Patent metadata

Field	Value
Publication number	US-12222147-B2
Application number	US-202017761429-A
Country	US
Kind code	B2
Filing date	Sep 3, 2020
Priority date	Sep 26, 2019
Publication date	Feb 11, 2025
Grant date	Feb 11, 2025

Abstract

A trans-critical thermodynamic system includes an expansion device and a separator. The expansion device receives a supercritical fluid containing solutes. The expansion device is operable to expand the supercritical fluid to produce a sub-critical gas by reducing a temperature and/or a pressure of the supercritical fluid. The separator removes the solutes from the sub-critical gas.

First claim

The invention claimed is:

1. A trans-critical thermodynamic system, comprising:
an expansion device configured to receive a supercritical fluid containing solutes, the expansion device operable to expand the supercritical fluid to produce a sub-critical gas by reducing a temperature and/or a pressure of the supercritical fluid;
a separator configured to remove the solutes from the sub-critical gas;
a high pressure circuit configured for the supercritical fluid to flow therethrough; and
a fluid extraction point operable to extract a portion of the supercritical fluid from the high pressure circuit, wherein the expansion device is operable to expand the portion of the supercritical fluid.

2. The trans-critical thermodynamic system of claim 1 , further comprising:
a low pressure circuit; and
a compressor operable to compress a working fluid from the low pressure circuit into the high pressure circuit such that the working fluid becomes the supercritical fluid.

3. The trans-critical thermodynamic system of claim 2 , further comprising:
a first heat exchanger in the high pressure circuit configured to receive the supercritical fluid from the compressor, wherein the fluid extraction point is located after the first heat exchanger, wherein the first heat exchanger is configured to cool the supercritical fluid to a thermodynamic state such that the reduction in the temperature and/or the pressure when the portion of the supercritical fluid is passed through the expansion device produces the sub-critical gas having a thermodynamic state matching a position in the low pressure circuit, and wherein the thermodynamic state of the sub-critical gas has a temperature less than a temperature at an inlet of the compressor.

4. The trans-critical thermodynamic system of claim 3 , further comprising a controller operable to control a rate of energy transfer in the first heat exchanger based on a measure of one or more thermodynamic properties of the supercritical fluid at the fluid extraction point.

5. The trans-critical thermodynamic system of claim 3 , further comprising:
a bypass circuit configured to divert a fraction of the supercritical fluid around the first heat exchanger;
a mixing valve configured to mix the supercritical fluid that has passed through the first heat exchanger with the supercritical fluid that has bypassed the first heat exchanger; and
a controller configured to control the mixing valve based on a measure of one or more thermodynamic properties of the supercritical fluid at the fluid extraction point.

6. The trans-critical thermodynamic system of claim 3 , further comprising:
one or more control members operable to control a rate of flow of a heat transfer fluid across the first heat exchanger; and
a controller configured to control the one or more control members based on a measure of one or more thermodynamic properties of the supercritical fluid at the fluid extraction point.

7. The trans-critical thermodynamic system of claim 1 , further comprising:
a solute sensor operable to measure a value representative of an amount of solute in the supercritical fluid, and wherein the portion of the supercritical fluid extracted to pass through the expansion device is controlled based on the value to maintain the amount of solute in the supercritical fluid below a threshold.

8. The trans-critical thermodynamic system of claim 7 , wherein the solute sensor is operable to measure a rate of solute collection in the separator.

9. The trans-critical thermodynamic system of claim 1 , wherein the fluid extraction point is in fluid communication with a cooling circuit, wherein the supercritical fluid in the high pressure circuit that is not extracted at the fluid extraction point is circulated through the cooling circuit, the cooling circuit comprising:
at least one heat exchanger; and
another expansion device.

10. The trans-critical thermodynamic system of claim 1 , further comprising a second heat exchanger configured to receive the sub-critical gas from the separator.

11. The trans-critical thermodynamic system of claim 1 , further comprising:
a high pressure circuit;
a low pressure circuit;
a pump operable to pressurize a working fluid from the low pressure circuit into the high pressure circuit such that the working fluid becomes a pressurized liquid; and
a heat recovery heat exchanger in the high pressure circuit configured to receive the pressurized liquid and heat the pressurized liquid such that the pressurized liquid becomes the supercritical fluid;
wherein the expansion device is configured to receive the supercritical fluid from the heat recovery heat exchanger.

12. A method of removing solutes from a working fluid in a trans-critical circuit, the method comprising:
identifying a position in the trans-critical circuit where the working fluid is a sub-critical gas;
positioning a separator such that the separator receives at least a portion of the working fluid when the working fluid is the sub-critical gas, the separator operable to remove solutes from the sub-critical gas,
identifying a fluid extraction point in the trans-critical circuit where the working fluid is a supercritical fluid;
extracting a portion of the supercritical fluid from the fluid extraction point in the trans-critical circuit; and
passing the portion of the supercritical fluid through an expansion device such that the portion of the supercritical fluid becomes the sub-critical gas.

13. The method of claim 12 , further comprising:
compressing the working fluid upstream of the fluid extraction point such that the working fluid becomes the supercritical fluid;
passing at least a fraction of the supercritical fluid through a first heat exchanger located upstream of the fluid extraction point; and
controlling a rate of energy transfer in the first heat exchanger based on a measure of one or more thermodynamic properties of the supercritical fluid at the fluid extraction point.

Assignees

• Rolls Royce Plc

Inventors

• Bunce Ian M
• Palmer Chloe J

Classifications

• F25B2309/061

  with cycle highest pressure above the supercritical pressure · CPC title

• F25B43/043

  for compression type systems · CPC title

• F25B9/008

  the refrigerant being carbon dioxide · CPC title

• F25B2400/0403

  for condensers · CPC title

• F25B6/04

  arranged in series · CPC title