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US5349824A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the mixed production of high and low purity oxygen

Assignee: Liquid Air Engineering Corp Canada
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Filing: 1993-06-30
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Granted: 1994-09-27
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Expires: 2013-06-30
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Abstract

Abstract An apparatus for simultaneously producing both high and low purity oxygen, which contains a double rectification column having therein a lower pressure fractionating column with two reboilers therein, and a higher pressure fractionating column, wherein an intermediate outlet is provided between the two reboilers of the lower pressure fractionating column for extracting a lower purity oxygen stream therefrom, and a high purity liquid oxygen stream from a bottom portion of the column simultaneously.

Inventors

  • 👤 Bao Ha
  • 👤 Catherine Garnier

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 04:47
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04006; F25J3/04078; F25J3/0409; B; B01; B01D; B01D3/00; B01D3/14; B01D3/32; B01D3/322; F25J3/04151; F25J3/04163; F25J3/04169; F25J3/04175; F25J3/04187; F25J3/04193; F25J3/04206; F25J3/04248; F25J3/04284; F25J3/0429; F25J3/04296; F25J3/04406; F25J3/04418; F25J2200/00; F25J2200/50; F25J2200/54; F25J2215/00; F25J2215/50; F25J2215/52; F25J2250/00; F25J2250/30; F25J2250/40; F25J2250/50; Y; Y10; Y10S; Y10S62/00; Y10S62/923; Y10S62/924; Y10S62/939; Y10S62/94

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 262 words
A process for simultaneously producing both high and low purity oxygen from a double column, double reboiler apparatus, the double columns being low and high pressure columns, and said low pressure column having a lower and an upper reboiler, which comprises: a) condensing a first compressed and cooled feed stream fraction containing at least nitrogen and oxygen in a reboiler located at the bottom of the lower pressure column; b) feeding at least a fraction of the resulting liquefied feed stream to either high or low pressure columns or both as feed; c) introducing a second fraction of a feed stream to a bottom of the high pressure column as gaseous feed, whereby a bottom oxygen-rich liquid stream and an overhead nitrogen-rich gaseous stream are formed; d) passing the oxygen-rich liquid stream to the low pressure column as feed; e) condensing the nitrogen-rich gaseous stream against a boiling liquid in an upper reboiler of the low pressure column, thereby serving as a second reboil for distillation; f) returning a portion of the condensed nitrogen-rich stream to the high pressure column as reflux, and passing at least a fraction of a remaining portion of the nitrogen-rich stream to the top of the low pressure column as reflux, whereby the low pressure column separates its feeds into bottom stream oxygen product and top stream-rich in nitrogen; g) recovering the bottom stream oxygen product as high purity liquid oxygen; and h) drawing from a tray or a stage between the two reboilers of the low pressure column, an oxygen product stream as low purity oxygen.
Claim 2
Dependent Claim 262 words
A process for simultaneously producing both high and low purity oxygen from a double column, double reboiler apparatus, the double columns being low and high pressure columns, and said low pressure column having a lower and an upper reboiler, which comprises: a) condensing a first compressed and cooled feed stream fraction containing at least nitrogen and oxygen in a reboiler located at the bottom of the lower pressure column; b) feeding at least a fraction of the resulting liquefied feed stream to either high or low pressure columns or both as feed; c) introducing a second fraction of a feed stream to a bottom of the high pressure column as gaseous feed, whereby a bottom oxygen-rich liquid stream and an overhead nitrogen-rich gaseous stream are formed; d) passing the oxygen-rich liquid stream to the low pressure column as feed; e) condensing the nitrogen-rich gaseous stream against a boiling liquid in an upper reboiler of the low pressure column, thereby serving as a second reboil for distillation; f) returning a portion of the condensed nitrogen-rich stream to the high pressure column as reflux, and passing at least a fraction of a remaining portion of the nitrogen-rich stream to the top of the low pressure column as reflux, whereby the low pressure column separates its feeds into bottom stream oxygen product and top stream-rich in nitrogen; g) recovering the bottom stream oxygen product as high purity liquid oxygen; and h) drawing from a tray or a stage between the two reboilers of the low pressure column, an oxygen product stream as low purity oxygen.
Claim 3
Dependent Claim 12 words
The process of claim 1, wherein the feed stream further contains argon.
Claim 4
Dependent Claim 12 words
The process of claim 2, wherein the feed stream is atmospheric air.
Claim 5
Dependent Claim 30 words
The process of claim 3, which further comprises recovering argon by means of an argon side arm column and a tray or a stage between the two oxygen product outlets.
Claim 6
Dependent Claim 23 words
The process of claim 1, wherein in step a) the feed stream is compressed to a pressure of about 6 to 50 bar.
Claim 7
Dependent Claim 20 words
The process of claim 5, wherein the feed stream is compressed to a pressure of about 10 to 35 bar.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1997-09-26 1998-03-28 1998-09-27 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 2001-09-26 2002-03-28 2002-09-27 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2005-09-26 2006-03-28 2006-09-27 $7700.00 Window Closed / Lapsed

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