Systems and methods for providing continuous cooling at cryogenic temperatures

Patent metadata

Field	Value
Publication number	US-11486609-B2
Application number	US-202016934992-A
Country	US
Kind code	B2
Filing date	Jul 21, 2020
Priority date	May 25, 2016
Publication date	Nov 1, 2022
Grant date	Nov 1, 2022

Abstract

Systems and methods of continuous cooling at cryogenic temperatures. One exemplary aspect involves a refrigeration system that includes: a chamber adapted to hold liquid and gaseous coolant received from a cooling pot; a first adsorption pump having an inlet end in fluid communication with the chamber, the first adsorption pump configured to capture gas from the liquid and gaseous coolant when the first adsorption pump is enabled; a second adsorption pump having an inlet end in fluid communication with the chamber, the second adsorption pump configured to capture gas from the liquid and gaseous coolant when the second adsorption pump is enabled; a means for desorbing the gas captured by the first adsorption pump; and a means for desorbing the gas captured by the second adsorption pump.

First claim

The invention claimed is:

1. A closed refrigeration system that provides continuous cooling at cryogenic temperatures, the closed refrigeration system comprising:
a chamber adapted to hold liquid and gaseous coolant received from a cooling pot;
a first adsorption pump having an inlet end in fluid communication with the chamber, the first adsorption pump configured to capture gas from the liquid and gaseous coolant when the first adsorption pump is enabled;
a second adsorption pump having an inlet end in fluid communication with the chamber, the second adsorption pump configured to capture gas from the liquid and gaseous coolant when the second adsorption pump is enabled;
a means for desorbing the gas captured by the first adsorption pump;
a means for desorbing the gas captured by the second adsorption pump;
means for condensing the gas desorbed from the first adsorption pump, wherein the means for condensing comprises a first condensing line arranged between an outlet end of the first adsorption pump and the chamber, the first condensing line comprising a condenser and only one heat exchanger arranged downstream of the condenser; and
a closed cycle cryocooler, the closed cycle cryocooler configured to dissipate heat generated by the adsorption.

2. The refrigeration system of claim 1 , further comprising a valve configured to isolate the first and second adsorption pumps from the cooling pot while the gas captured by the first and second adsorption pumps is desorbed.

3. The refrigeration system of claim 2 , wherein the valve comprises a solenoid valve comprising a valve body, a valve seat disposed in the valve body, and a valve disk movably disposed in the valve body relative to the valve seat to control fluid flow through the solenoid valve, wherein the valve disk is made of an elastomeric material.

4. The refrigeration system of claim 1 , further comprising a first valve configured to isolate the first adsorption pump from the cooling pot while the gas captured by the first adsorption pump is desorbed, and a second valve configured to isolate the second adsorption pump from the cooling pot while the gas captured by the second adsorption pump is desorbed.

5. The refrigeration system of claim 1 , wherein the means for desorbing the gas captured by the first adsorption pump comprises a first heater or a first heat switch, and wherein the means for desorbing the gas captured by the second adsorption pump comprises a second heater or a second heat switch.

6. The refrigeration system of claim 1 , wherein the liquid and gaseous coolant comprises helium with an isotopic weight of 3, helium with an isotopic weight of 4, or a mixture of the two helium isotopes.

7. The refrigeration system of claim 1 , further comprising means for condensing the gas desorbed from the second adsorption pump, wherein the means for condensing the gas desorbed from the first adsorption pump further comprises a first expansion valve arranged between the outlet end of the first adsorption pump and the chamber, and wherein the means for condensing the gas desorbed from the second adsorption pump comprises at least one of a second heat exchanger and a second expansion valve arranged between an outlet end of the second adsorption pump and the chamber.

8. The refrigeration system of claim 7 , further comprising a condensing line, wherein the cooling pot and the condensing line are arranged to pass liquid produced by the means for condensing the gas desorbed from the first adsorption pump and liquid produced by the means for condensing the gas desorbed from the second adsorption pump to the cooling pot.

9. The refrigeration system of claim 8 , further comprising a third heat exchanger arranged in the chamber and along the condensing line, the third heat exchanger configured to cool the liquid to the temperature of the liquid and gaseous coolant in the chamber.

10. The refrigeration system of claim 1 , wherein the means for condensing the gas desorbed from the first adsorption pump further comprises a first expansion valve arranged between the only one heat exchanger and the chamber.

11. A method of continuously cooling at cryogenic temperatures in a closed refrigeration system, the method comprising:
fluidly coupling a first adsorption pump to a chamber containing liquid and gaseous coolant received from a cooling pot;
when the first adsorption pump is fluidly coupled to the chamber, capturing, using the first adsorption pump, gas from the liquid and gaseous coolant, thereby lowering the temperature of the liquid and gaseous coolant in the chamber;
isolating the first adsorption pump from the chamber;
responsive to the isolation of the first adsorption pump from the chamber, (i) fluidly coupling a second adsorption pump to the chamber, and (ii) desorbing the gas captured by the first adsorption pump;
capturing, when the second adsorption pump is fluidly coupled to the chamber, gas from the liquid and gaseous coolant using the second adsorption pump, thereby lowering the temperature of the liquid and gaseous coolant in the chamber;
condensing the desorbed gas by passing the desorbed gas though a first condensing line arranged between an outlet end of the first adsorption pump and the chamber, thereby producing a liquid, the first condensing line comprising a condenser and only one heat exchanger arranged downstream of the condenser; and
dissipating heat generated by the adsorption via a closed cycle cryocooler.

12. The method of claim 11 , wherein desorbing the gas captured by the first adsorption pump comprises heating the first adsorption pump, and further comprising desorbing the gas captured by the second adsorption pump, wherein desorbing the gas captured by the second adsorption pump comprises heating the second adsorption pump.

13. The method of claim 11 , wherein isolating the first adsorption pump comprises isolating the first adsorption pump when an adsorbent of the first adsorption pump is saturated, and further comprising isolating the second adsorption pump, wherein isolating the second adsorption pump comprises isolating the second adsorption pump when an adsorbent of the second adsorption pump is saturated.

14. The method of claim 11 , wherein the acts of fluidly coupling the first adsorption pump to the chamber and fluidly coupling the second adsorption pump each comprise opening a valve arranged between the chamber and the first and second adsorption pumps, and wherein the act of isolating the first adsorption pump comprises closing the valve.

15. The method of claim 14 , wherein the valve comprises a solenoid valve comprising a valve body, a valve seat disposed in the valve body, and a valve disk movably disposed in the valve body relative to the valve seat to control fluid flow through the solenoid valve, wherein the valve disk is made of an elastomeric material.

16. The method of claim 11 , wherein the first condensing line further comprises a first expansion valve arranged between the only one heat exchanger and the chamber.

17. The method of claim 11 , further comprising condensing the desorbed gas by passing the desorbed gas through at least one of a second heat exchanger and a second expansion valve arranged between the second adsorption pump and the chamber, thereby producing a liquid.

18. A closed refrigeration system that provides continuous cooling at cryogenic temperatures, the refrigeration system comprising:
a chamber adapted to hold liquid and gaseous coolant received from a cooling pot;
a first adsorption pump having an inlet end in fluid communication with th

Assignees

• Univ Chicago

Inventors

• Schuster David I
• Oriani Andrew E

Classifications

• Y02A30/27

  Relating to heating, ventilation or air conditioning [HVAC] technologies · CPC title

• F25B9/10

  with several cooling stages · CPC title

• F25B9/145

  pulse-tube cycle · CPC title

• Y02B30/00

  Energy efficient heating, ventilation or air conditioning [HVAC] · CPC title

• F25B9/02

  using Joule-Thompson effect; using vortex effect · CPC title