Systems and methods for providing continuous cooling at cryogenic temperatures

Patent metadata

Field	Value
Publication number	US-10724768-B2
Application number	US-201715605701-A
Country	US
Kind code	B2
Filing date	May 25, 2017
Priority date	May 25, 2016
Publication date	Jul 28, 2020
Grant date	Jul 28, 2020

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 first heater or heat switch for desorbing the gas captured by the first adsorption pump; and a second heater or heat switch for desorbing the gas captured by the second adsorption pump.

First claim

The invention claimed is:

1. A 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 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; and
means for condensing the gas desorbed from the second adsorption pump, wherein the means for condensing the gas desorbed from the second adsorption pump is structurally separate from the means for condensing the gas desorbed from the first adsorption pump, and
wherein the means for condensing the gas desorbed from the first adsorption pump comprises a first condensing line comprising a first condenser and a first heat exchanger arranged downstream of the first condenser, and wherein the means for condensing the gas desorbed from the second adsorption pump comprises a second condensing line comprising a second condenser and a second heat exchanger arranged downstream of the second condenser.

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 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.

4. The refrigeration system of claim 1 , further comprising a closed cycle cryocooler arranged to dissipate heat generated by the adsorption.

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 each of the first and second adsorption pumps comprise an adsorbent that captures the gas from the liquid and gaseous coolant.

7. The refrigeration system of claim 6 , further comprising first and second heat switches configured to control the temperature of the adsorbent of the first and second adsorption pumps, respectively.

8. 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.

9. The refrigeration system of claim 1 , wherein the means for condensing the gas desorbed from the first adsorption pump is arranged between an outlet end of the first adsorption pump and the chamber, and wherein the means for condensing the gas desorbed from the second adsorption pump is arranged between an outlet end of the second adsorption pump and the chamber.

10. The refrigeration system of claim 1 , 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.

11. The refrigeration system of claim 10 , 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.

12. The refrigeration system of claim 1 , wherein the first condensing line further comprises a first expansion valve arranged downstream of the first heat exchanger, and wherein the second condensing line further comprises a second expansion valve arranged downstream of the second heat exchanger.

13. The refrigeration system of claim 12 , further comprising:
a third heat exchanger arranged within the chamber; and
a third condensing line arranged between each of the first and second condensing lines and the cooling pot, the third condensing line configured to pass liquid produced by the first condensing line and liquid produced by the second condensing line through the third heat exchanger and to the cooling pot.

14. A method of continuously cooling at cryogenic temperatures, 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;
isolating the second adsorption pump from the chamber;
responsive to the isolation of the second adsorption pump from the chamber, desorbing the gas captured by the second adsorption pump;
condensing the gas desorbed from the first adsorption pump via a first condensing line arranged between the first adsorption pump and the chamber, wherein the first condensing line comprises a first condenser and a first heat exchanger arranged downstream of the first condenser; and
condensing the gas desorbed from the second adsorption pump via a second condensing line arranged between the second adsorption pump and the chamber, wherein the second condensing line is structurally separate from the first condensing line, wherein the second condensing line comprises a second condenser and a second heat exchanger arranged downstream of the second condenser.

15. The method of claim 14 , wherein desorbing the gas captured by the first adsorption pump comprises heating the first adsorption pump, and wherein desorbing the gas captured by the second adsorption pump comprises heating the second adsorption pump.

16. The method of claim 14 , wherein isolating the first adsorption pump comprises isolating the first adsorption pump when an adsorbent of the first adsorption pump is saturated, and wherein isolating the second adsorption pump comprises isolating the second adsorption pump when an adsorbent of the second adsorption pump is saturated.

17. The method of claim 14 , 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 comprise

Assignees

• Univ Chicago

Inventors

• Schuster David I
• Oriani Andrew E

Classifications

• F25B9/145

  pulse-tube cycle · CPC title

• Y02B30/00

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

• Y02A30/27

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

• F25B25/00

  Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00 · CPC title

• F25B17/083 Primary

  with two or more boiler-sorbers operating alternately · CPC title