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US6041621A Expired / Lapsed US ⏱️ 0.0 years remaining

Single circuit cryogenic liquefaction of industrial gas

Assignee: Edwards Vacuum LLC
•
Filing: 1998-12-30
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Granted: 2000-03-28
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Expires: 2018-12-30
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Abstract

Abstract A method for more efficiently liquefying industrial gas wherein refrigeration for the liquefaction is generated using a defined multicomponent refrigerant fluid and provided by a single flow circuit over a wide temperature range from ambient to cryogenic temperature.

Inventors

  • 👤 Walter Joseph Olszewski
  • 👤 Bayram Arman
  • 👤 Joseph Alfred Weber
  • 👤 Arun Acharya

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 13:51
CPC Classifications
F; F25; F25J; F25J1/00; F25J1/0002; F25J1/0022; C; C09; C09K; C09K5/00; C09K5/02; C09K5/04; C09K5/041; C09K5/044; C09K5/045; F25B; F25B9/00; F25B9/002; F25B9/006; F25J1/0012; F25J1/0015; F25J1/0017; F25J1/002; F25J1/0027; F25J1/003; F25J1/0032; F25J1/004; F25J1/0042; F25J1/0047; F25J1/0052; F25J1/0055; F25J1/006; F25J1/0097; F25J1/02; F25J1/0211; F25J1/0212; F25J1/0219; C09K2205/00; C09K2205/10; C09K2205/11; C09K2205/112; C09K2205/13; C09K2205/132; C09K2205/22

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 133 words
A method for liquefying an industrial gas comprising: (A) compressing a multicomponent refrigerant fluid comprising at least one component from the group consisting of fluorocarbons, hydrofluorocarbons and fluoroethers and at least one component from the group consisting of fluorocarbons, hydrofluorocarbons, fluoroethers and atmospheric gases; (B) cooling the compressed multicomponent refrigerant fluid to at least partially condense the multicomponent refrigerant fluid; (C) expanding the cooled compressed multicomponent refrigerant fluid to generate refrigeration; (D) warming the expanded multicomponent refrigerant fluid by indirect heat exchange with the compressed multicomponent refrigerant fluid to effect said cooling of the compressed multicomponent refrigerant fluid; and (E) bringing the expanded multicomponent refrigerant fluid into heat exchange relation with industrial gas and warming the expanded multicomponent refrigerant fluid by indirect heat exchange with said industrial gas to liquefy the industrial gas.
Claim 2
Independent Claim 133 words
A method for liquefying an industrial gas comprising: (A) compressing a multicomponent refrigerant fluid comprising at least one component from the group consisting of fluorocarbons, hydrofluorocarbons and fluoroethers and at least one component from the group consisting of fluorocarbons, hydrofluorocarbons, fluoroethers and atmospheric gases; (B) cooling the compressed multicomponent refrigerant fluid to at least partially condense the multicomponent refrigerant fluid; (C) expanding the cooled compressed multicomponent refrigerant fluid to generate refrigeration; (D) warming the expanded multicomponent refrigerant fluid by indirect heat exchange with the compressed multicomponent refrigerant fluid to effect said cooling of the compressed multicomponent refrigerant fluid; and (E) bringing the expanded multicomponent refrigerant fluid into heat exchange relation with industrial gas and warming the expanded multicomponent refrigerant fluid by indirect heat exchange with said industrial gas to liquefy the industrial gas.
Claim 3
Dependent Claim 29 words
The method of claim 1 further comprising compressing the industrial gas through a compressor prior to the heat exchange of the industrial gas with the expanded multicomponent refrigerant fluid.
Claim 4
Dependent Claim 38 words
The method of claim 2 further comprising reducing the pressure of the liquefied industrial gas to flash a portion of the liquefied industrial gas to an industrial gas vapor, and passing said industrial gas vapor to the compressor.
Claim 5
Dependent Claim 32 words
The method of claim 3 further comprising warming the industrial gas vapor by indirect heat exchange with the liquefying compressed industrial gas prior to passing the industrial gas vapor to the compressor.
Claim 6
Dependent Claim 30 words
The method of claim 1 wherein the multicomponent refrigerant fluid comprises at least two components from the group consisting of fluorocarbons, hydrofluorocarbons and fluoroethers and at least one atmospheric gas.
Claim 7
Dependent Claim 30 words
The method of claim 1 wherein the multicomponent refrigerant fluid comprises at least two components from the group consisting of fluorocarbons, hydrofluorocarbons and fluoroethers and at least two atmospheric gases.
Claim 8
Dependent Claim 31 words
The method of claim 1 wherein the multicomponent refrigerant fluid comprises at least one fluoroether and at least one component from the group consisting of fluorocarbons, hydrofluorocarbons, fluoroethers and atmospheric gases.
Claim 9
Dependent Claim 44 words
The method of claim 1 wherein each of the components of the multicomponent refrigerant fluid has a normal boiling point which differs by at least 5 degrees Kelvin from the normal boiling point of each of the other components of the multicomponent refrigerant fluid.
Claim 10
Dependent Claim 41 words
The method of claim 1 wherein the normal boiling point of the highest boiling component of the multicomponent refrigerant fluid is at least 50° K. greater than the normal boiling point of the lowest boiling component of the multicomponent refrigerant fluid.
Claim 11
Dependent Claim 136 words
The method of claim 1 wherein the multicomponent refrigerant fluid comprises at least two components from the group consisting of C 5 F 12 , CHF 2 O-- C 2 HF 4 , C 4 HF 9 , C 3 H 3 F 5 , C 2 F 5 --O--CH 2 F, C 3 H 2 F 6 , CHF 2 --O--CHF 2 , C 4 F 10 , CF 3 --O--C 2 H 2 F 3 , C 3 HF 7 , CH 2 F--O--CF 3 , C 2 H 2 F 4 , CHF 2 --O--CF 3 , C 3 F 8 , C 2 HF 5 , CF 3 --O--CF 3 , C 2 F 6 , CHF 3 , CF 4 , O 2 , Ar, N 2 , Ne and He.
Claim 12
Dependent Claim 25 words
The method of claim 1 wherein the multicomponent refrigerant fluid is a variable load multicomponent refrigerant fluid throughout the whole temperature range of the method.

References Cited (Backward Citations)

US3733845A Cited
US3932154A Cited
US3970441A Cited
US3992167A Cited
US5157925A Cited
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US5502972A Cited
US5579654A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 2003-03-28 2003-09-27 2004-03-28 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 2007-03-28 2007-09-27 2008-03-28 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2011-03-28 2011-09-27 2012-03-28 $7700.00 Window Closed / Lapsed

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