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US4592767A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for separating methane and nitrogen

Assignee: Praxair Technology Inc
•
Filing: 1985-05-29
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Granted: 1986-06-03
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Expires: 2005-05-29
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Abstract

Abstract A process for the separation of methane and nitrogen in a cryogenic distillation column driven by a closed loop recirculating fluid heat pump wherein additional column refrigeration is generated by rejecting process heat into a product stream thereby reducing the need for expansion of process streams and enabling recovery of product at relatively high pressure.

Inventors

  • 👤 Ravindra F. Pahade
  • 👤 John B. Saunders
  • 👤 James J. Maloney

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 04:46
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/0228; F25J3/0257; F25J3/0204; F25J3/0209; F25J3/0233; F25J2200/00; F25J2200/02; F25J2200/50; F25J2200/74; F25J2205/00; F25J2205/02; F25J2270/00; F25J2270/12; F25J2270/66; Y; Y10; Y10S; Y10S62/00; Y10S62/927

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 234 words
A process for the separation of methane and nitrogen comprising providing added refrigeration to the process at required column temperature levels by a recirculating fluid heat pump, while precluding the need for significant amounts of outside added refrigeration or large expansion of process streams, by the steps of: (a) introducing a feed comprising methane and nitrogen into a rectification column operating at a pressure in the range of from 200 to 450 psia; (b) separating the feed in said column into a nitrogen-enriched vapor and a methane-enriched liquid; (c) partially condensing nitrogen-enriched vapor by indirect heat exchange with heat pump fluid to warm the heat pump fluid; (d) employing at least some of the resulting liquid of step (c) as reflux liquid for the column; (e) partially vaporizing methane-enriched liquid by indirect heat exchange with warm heat pump fluid; (f) employing at least some of the resulting vapor of step (e) as reflux vapor for the column; (g) warming remaining methane-enriched liquid of step (e) by indirect heat exchange with warm heat pump fluid wherein not more than 75 percent of said remaining methane-enriched liquid is vaporized; (h) further warming the warmed methane-enriched fluid of step (g) by indirect heat exchange with feed prior to the introduction of said feed into the column; and (i) recovering resulting methane-enriched fluid as product methane, thereby providing refrigeration to the column at or below column temperature levels.
Claim 2
Dependent Claim 234 words
A process for the separation of methane and nitrogen comprising providing added refrigeration to the process at required column temperature levels by a recirculating fluid heat pump, while precluding the need for significant amounts of outside added refrigeration or large expansion of process streams, by the steps of: (a) introducing a feed comprising methane and nitrogen into a rectification column operating at a pressure in the range of from 200 to 450 psia; (b) separating the feed in said column into a nitrogen-enriched vapor and a methane-enriched liquid; (c) partially condensing nitrogen-enriched vapor by indirect heat exchange with heat pump fluid to warm the heat pump fluid; (d) employing at least some of the resulting liquid of step (c) as reflux liquid for the column; (e) partially vaporizing methane-enriched liquid by indirect heat exchange with warm heat pump fluid; (f) employing at least some of the resulting vapor of step (e) as reflux vapor for the column; (g) warming remaining methane-enriched liquid of step (e) by indirect heat exchange with warm heat pump fluid wherein not more than 75 percent of said remaining methane-enriched liquid is vaporized; (h) further warming the warmed methane-enriched fluid of step (g) by indirect heat exchange with feed prior to the introduction of said feed into the column; and (i) recovering resulting methane-enriched fluid as product methane, thereby providing refrigeration to the column at or below column temperature levels.
Claim 3
Dependent Claim 26 words
The process of claim 1 wherein not more than 50 percent of said remaining methane-enriched liquid is vaporized by the indirect heat exchange of step (g).
Claim 4
Dependent Claim 26 words
The process of claim 1 wherein not more than 25 percent of said remaining methane-enriched liquid is vaporized by the indirect heat exchange of step (g).
Claim 5
Dependent Claim 21 words
The process of claim 1 wherein the remaining methane-enriched liquid is expanded prior to the indirect heat exchange of step (g).
Claim 6
Dependent Claim 20 words
The process of claim 1 wherein the warmed methane-enriched fluid is expanded after the indirect heat exchange of step (g).
Claim 7
Dependent Claim 22 words
The process of claim 1 wherein a portion of the heat pump fluid is warmed by indirect heat exchange with the feed.
Claim 8
Dependent Claim 31 words
The process of claim 1 wherein a portion of the heat pump fluid is warmed by indirect heat exchange with a stream taken from an intermediate location of the rectification column.
Claim 9
Dependent Claim 22 words
The process of claim 7 wherein another portion of the heat pump fluid is warmed by indirect heat exchange with the feed.

References Cited (Backward Citations)

US2823523A Cited
US3797261A Cited
US3818714A Cited
US4352685A Cited
US4415345A Cited
US4411677A Cited
US4501600A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1989-06-02 1989-12-02 1990-06-03 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1993-06-02 1993-12-02 1994-06-03 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1997-06-02 1997-12-02 1998-06-03 $7700.00 Window Closed / Lapsed

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