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US4836836A Expired / Lapsed US ⏱️ 0.0 years remaining

Separating argon/oxygen mixtures using a structured packing

Assignee: Air Products and Chemicals Inc
•
Filing: 1987-12-14
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Granted: 1989-06-06
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Expires: 2007-12-14
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Abstract

Abstract The present invention relates to improvements to a process and apparatus for the cryogenic distillation of mixtures, which comprise oxygen, nitrogen and argon, e.g. air. The improvement comprises effectuating intimate contact of the liquid and vapor phase streams utilizing a structured packing to effectuate the intimate contact in at least those regions of the distillation column system where argon concentration is within the range from about 0.6 to about 75 volume percent, and operating the process such that the densimetric superficial gas velocity in those regions is at least 0.06 feet per second. The present invention also relates to a method for improving a cryogenic distillation apparatus having at least one distillation column for the separation of mixtures containing oxygen and argon, comprising the step of replacing the distillation trays with a structured packing in at least those regions of the distillation column system where the concentration of argon is in the range from about 0.6 to about 75 volume percent.

Inventors

  • 👤 Douglas L. Bennett
  • 👤 Keith A. Ludwig
  • 👤 George S. Witmer
  • 👤 Charles M. Woods

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 23:21
CPC Classifications
B; B01; B01D; B01D3/00; B01D3/14; B01D3/32; F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04763; F25J3/04866; F25J3/04896; F25J3/04915; B01D53/00; B01D53/14; F25J3/04406; F25J3/04412; F25J3/04642; F25J3/04648; F25J3/04654; F25J3/04666; F25J3/04672; F25J3/04678; F25J3/04909; B01J; B01J2219/00; B01J2219/32; B01J2219/326; F25J2290/00; F25J2290/10; Y; Y10; Y10S; Y10S62/00; Y10S62/902; Y10S62/905; Y10S62/906; Y10S62/923; Y10S62/924

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 152 words
In a process for the separation of mixtures, which comprise oxygen, nitrogen, and argon, by cryognic distillation, wherein in certain regions of a distillation column system having at least one column, a liquid phase stream containing oxygen, argon and nitrogen, and a vapor phase stream containing oxygen, argon and nitrogen, are intimately contacted thereby allowing mass transfer which enriches the liquid phase stream with oxygen and strips argon from the liquid phase stream, and enriches the vapor phase stream with argon and strips oxygen from the vapor phase stream, the improvement comprising effectuating intimate contact of the liquid and vapor phase streams utilizing a structured packing in at least those regions of the distillation column system where argon concentration is within the range from about 0.6 to about 75 volume percent, and operating the process such that the densimetric superficial gas velocity in those regions is at least 0.06 feet per second.
Claim 2
Dependent Claim 152 words
In a process for the separation of mixtures, which comprise oxygen, nitrogen, and argon, by cryognic distillation, wherein in certain regions of a distillation column system having at least one column, a liquid phase stream containing oxygen, argon and nitrogen, and a vapor phase stream containing oxygen, argon and nitrogen, are intimately contacted thereby allowing mass transfer which enriches the liquid phase stream with oxygen and strips argon from the liquid phase stream, and enriches the vapor phase stream with argon and strips oxygen from the vapor phase stream, the improvement comprising effectuating intimate contact of the liquid and vapor phase streams utilizing a structured packing in at least those regions of the distillation column system where argon concentration is within the range from about 0.6 to about 75 volume percent, and operating the process such that the densimetric superficial gas velocity in those regions is at least 0.06 feet per second.
Claim 3
Dependent Claim 10 words
The process of claim 1 wherein the mixture is air.
Claim 4
Dependent Claim 149 words
In a process for the separation of mixtures, which comprise oxygen and argon, by cryogenic distillation, wherein in certain regions of a distillation column system having at least one column, a liquid phase stream containing oxygen and argon, and a vapor phase stream containing oxygen and argon, are intimately contacted thereby allowing mass transfer which enriches the liquid phase stream with oxygen and strips argon from the liquid phase stream, and enriches the vapor phase stream with argon and strips oxygen from the vapor phase stream, the improvement comprising effectuating intimate contact of the liquid and vapor phase streams utilizing a sutructured packing in at least those regions of the distillation column system where argon concentration is within the range from about 0.06 to about 75 volume percent, and operating the process such that the densimetric superficial gas velocity in those regions is at least 0.06 feet per second.
Claim 5
Dependent Claim 149 words
In a process for the separation of mixtures, which comprise oxygen and argon, by cryogenic distillation, wherein in certain regions of a distillation column system having at least one column, a liquid phase stream containing oxygen and argon, and a vapor phase stream containing oxygen and argon, are intimately contacted thereby allowing mass transfer which enriches the liquid phase stream with oxygen and strips argon from the liquid phase stream, and enriches the vapor phase stream with argon and strips oxygen from the vapor phase stream, the improvement comprising effectuating intimate contact of the liquid and vapor phase streams utilizing a sutructured packing in at least those regions of the distillation column system where argon concentration is within the range from about 0.06 to about 75 volume percent, and operating the process such that the densimetric superficial gas velocity in those regions is at least 0.06 feet per second.
Claim 6
Independent Claim 62 words
A method for improving a cryogenic distillation apparatus having at least one distillation column for the separation of mixtures containing oxygen and argon, comprising the step of replacing the distillation trays with a structured packing in at least those regions of the distillation column system where the concentration of argon is in the range from about 0.6 to about 75 volume percent.
Claim 7
Independent Claim 62 words
A method for improving a cryogenic distillation apparatus having at least one distillation column for the separation of mixtures containing oxygen and argon, comprising the step of replacing the distillation trays with a structured packing in at least those regions of the distillation column system where the concentration of argon is in the range from about 0.6 to about 75 volume percent.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1992-06-05 1992-12-05 1993-06-06 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1996-06-05 1996-12-05 1997-06-06 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2000-06-05 2000-12-05 2001-06-06 $7700.00 Window Closed / Lapsed

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