Magnetic refrigeration systems for cryogenic applications

Patent metadata

Field	Value
Publication number	US-12163701-B2
Application number	US-202017630443-A
Country	US
Kind code	B2
Filing date	Jul 28, 2020
Priority date	Jul 30, 2019
Publication date	Dec 10, 2024
Grant date	Dec 10, 2024

Abstract

Systems and methods disclosed herein relate to a cryogenic refrigeration system which may use a compression based cryocooler or liquid nitrogen pre-cool to cool a medium to ˜80K, and may in conjunction with a magnetic refrigeration system operating in the sub-80K temperature regime to provide cooling to a medium to temperatures below 80K. In some embodiments, the disclosed system may be useful for cooling on the order of about 3 kg/day to about 300 kg/day of hydrogen gas to liquid form, with higher efficiency than a standard vapor compression based system. This higher efficiency may make the system a more attractive candidate for use in cryogenic cooling applications.

First claim

What is claimed is:

1. A cryogenic refrigeration system for cooling a medium to temperatures below 80K comprising a dual stage system, a closed-loop heat transfer fluid flow system, and at least one heat exchanger, wherein:
a first stage of the dual stage system acts to cool from room temperature down to 80K, and a second stage of the dual stage system acts to cool from 80K down to a desired temperature below 80K, and wherein the first stage comprises either a vapor compression refrigeration system, or a liquid nitrogen tank, or a combination thereof; and wherein the second stage of the dual stage system comprises a magnetocaloric refrigeration system; and wherein
a heat transfer fluid circulates through the closed-loop heat transfer fluid flow system, wherein the closed-loop heat transfer fluid flow system is configured to cool the heat transfer fluid using the first stage, then flowing the heat transfer fluid through the magnetocaloric refrigeration system where a portion of the heat transfer fluid is cooled and then flowed through the at least one heat exchanger to provide cooling to the medium, and then return the heat transfer fluid to a compressor which is configured to transfer the heat transfer fluid into a pressurized tank so that is can be re-circulated in the closed-loop heat transfer fluid flow system; and wherein
the magnetocaloric refrigeration system comprises at least one magnetocaloric bed and an oscillating permanent magnetic field operating at a pre-defined frequency, wherein a frequency of oscillation includes magnetizing a magnetocaloric material in the at least one magnetocaloric bed at a predefined magnetic field ramp-up speed, maintaining the magnetic field on the at least one magnetocaloric bed for a specified holding time, demagnetizing the at least one magnetocaloric bed at a predefined ramp-down speed, and maintaining zero magnetic field on the at least one magnetocaloric bed for a specified removed time; and wherein
application of the permanent magnetic field to the at least one magnetocaloric bed is configured to cause the magnetocaloric material to heat up, and removal of the permanent magnetic field from the at least one magnetocaloric bed is configured to cause the magnetocaloric material to cool down; and wherein
the flow of the heat transfer fluid into and out of the at least one magnetocaloric bed is coupled with the oscillation of the permanent magnetic field so that a portion of the heat transfer fluid is configured to be cooled to the desired temperature below 80K and flowed through the at least one heat exchanger, and wherein;
the at least one heat exchanger is configured to transfer heat from the medium to the heat transfer fluid such that the medium is cooled to the desired temperature below 80K; and wherein
the at least one magnetocaloric bed comprises a magnetocaloric material with a composition of:
(A x B 1−x )Si 1−y−z (Cr y Mn z )

wherein A and B are selected from the group consisting of Ce, Nd, or Gd,
wherein x is in a range of about 0 to about 1,
wherein y is in a range of about 0.05 to about 0.3,
wherein z is in a range of about 0 to about 0.3, and wherein 0.05≤y+z≤0.3.

2. The cryogenic refrigeration system of claim 1 , wherein the medium to be cooled to cryogenic temperatures is Hydrogen or Helium.

3. The cryogenic refrigeration system of claim 1 , wherein the heat transfer fluid is Helium gas or Hydrogen gas.

4. The cryogenic refrigeration system of claim 1 , wherein the at least one permanent magnet field comprises a NdFeB-based permanent magnet.

5. The cryogenic refrigeration system of claim 4 , wherein the NdFeB-based permanent magnet is a Halbach magnet.

6. The cryogenic refrigeration system of claim 1 , wherein the frequency of the oscillating permanent magnet field is about 0.1 Hz to about 10 Hz.

7. The cryogenic refrigeration system of claim 1 , wherein the at least one magnetocaloric bed comprises a magnetocaloric material with a composition of:
(A x B 1−x )Si 0.8 Cr 0.2
wherein A and B are selected from the group consisting of Ce, Nd, or Gd, and
wherein x is in the range of about 0 to about 1.

8. The cryogenic refrigeration system of claim 1 , wherein the permanent magnetic field is oscillated on and off the magnetocaloric material using a linear motion.

9. The cryogenic refrigeration system of claim 1 , wherein the permanent magnetic field is oscillated on and off the magnetocaloric material using a rotational motion.

10. A cryogenic refrigeration system for cooling and liquefying on the order of about 3 kg to about 300 kg per day of hydrogen, the cryogenic refrigeration system comprising a liquid nitrogen first stage, a magnetocaloric refrigeration system as a second stage, a closed-loop heat transfer fluid flow system, and at least four heat exchangers, wherein;
a liquid nitrogen first stage comprises a liquid nitrogen filled tank wherein hydrogen gas is configured to be cooled to 77 K through heat exchange with liquid nitrogen in the liquid nitrogen filled tank prior to entering a first heat exchanger of the at least four heat exchangers; and wherein
the magnetocaloric refrigeration second stage comprises- magnetocaloric beds; and wherein
the at least four heat exchangers are configured to cool the hydrogen gas after the liquid nitrogen first stage by transferring heat from the hydrogen gas to the heat transfer fluid, such that upon exit from a last heat exchanger of the at least four heat exchangers, the hydrogen gas is cooled to below its boiling point so that the hydrogen gas is at least partially condensed into liquid hydrogen; and wherein
the closed-loop heat transfer fluid flow system is configured to circulate a heat transfer fluid comprising helium gas through the liquid nitrogen first stage, the magnetocaloric beds of the magnetocaloric refrigeration second stage, the at least four heat exchangers, and a compressor which transfers the heat transfer fluid into a pressurized tank so that it can be re-circulated in the closed-loop heat transfer system; and wherein
the magnetocaloric beds of the magnetocaloric refrigeration second stage comprise magnetocaloric materials, wherein the magnetocaloric materials comprise:
(A x B 1−x )Si 1−y−z (Cr y Mn z )

wherein A and B are selected from the group consisting of Ce, Nd, or Gd,
wherein x is in a range of about 0 to about 1,
wherein y is in arange of about 0.05 to about 0.3,
wherein z is in a range of about 0 to about 0.3, and wherein 0.05≤y+≤0.3; and
an oscillating permanent magnetic field configured to operating operate at a pre-defined frequency of between about 0 . 1 Hz and about 10 Hz, wherein the frequency of oscillation includes magnetizing the magnetocaloric material at a predefined magnetic field ramp-up speed, maintaining the magnetic field on the magnetocaloric beds for a specified holding time, demagnetizing the magnetocaloric material at a predefined ramp-down speed, and maintaining zero magnetic field on the magnetocaloric bed for a specified removed time; and wherein
application of the permanent magnetic field to the magnetocaloric beds is configured to cause the magnetocaloric material to heat up, and removal of the permanent magnetic field from the magnetocaloric beds causes the magnetocaloric material to cool down; and wherein
flow of the heat transfer fluid into and out of the magnetocaloric beds is coupled with the oscillation of the permanent magnetic field so that portions of the helium heat transfer fluid are configured to be cooled below 80K and flowed through the at least four heat exchangers to provide enough cooling at the last heat exchanger of the at least four heat exchangers to cool the hydrogen gas to below the boiling point of hydrogen

Assignees

• General Engineering & Res L L C
• Univ California
• General Engineering & Res Llc

Inventors

• Ihnfeldt Robin
• Chen Renkun
• Jin Sungho
• Feng Tianshi
• Adapa Sarath

Classifications

• F25B2321/002

  by using magneto-caloric effects · CPC title

• H01F1/015

  Metals or alloys · CPC title

• F25J2270/912

  Liquefaction cycle of a low-boiling (feed) gas in a cryocooler, i.e. in a closed-loop refrigerator · CPC title

• F25J1/0276

  Laboratory or other miniature devices · CPC title

• F25J1/0007

  Helium · CPC title