US4439220A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Dual column high pressure nitrogen process
Assignee: Praxair Technology Inc
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Filing: 1982-12-02
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Granted: 1984-03-27
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Expires: 2002-12-02
Abstract
Abstract A process to efficiently produce large quantities of elevated pressure nitrogen at a high recovery by the cryogenic separation of air employing two separate columns each of which is equipped with a top condenser and wherein the second column processes a feed stream obtained from the first column.
Inventors
- 👤 Walter J. Olszewski
- 👤 Ravindra F. Pahade
- 👤 John H. Ziemer
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 07:38
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04406; F25J3/04424; F25J3/04151; F25J3/04242; F25J3/04248; F25J3/04284; F25J3/0429; F25J3/04303; F25J2200/00; F25J2200/20; F25J2205/00; F25J2205/60
Claims Analysis
Total Claims: 18
Claim 1
Independent Claim
323 words
A process for the production of nitrogen gas at greater than atmospheric pressure by the separation of air by rectification comprising: (A) introducing cleaned, cooled feed air at greater than atmospheric pressure into a high pressure column having a top condenser, and operating at a pressure of from about 80 to 300 psia; (B) separating said feed air by rectification in said high pressure column into a first nitrogen-rich vapor fraction and a first oxygen-enriched liquid fraction; (C) recovering from about 20 to 60 percent of said first nitrogen-rich vapor fraction as high pressure nitrogen gas at a pressure of from about 80 to 300 psia and a purity of at least 99 mole percent; (D) condensing a portion of said first nitrogen-rich vapor fraction by indirect heat exchange with said first oxygen-enriched liquid fraction thereby producing a first nitrogen-rich liquid portion and a first oxygen-enriched vapor fraction; (E) employing said first nitrogen-rich liquid portion as liquid reflux for said high pressure column; (F) introducing said first oxygen-enriched vapor fraction into a medium pressure column having a top condenser, and operating at a pressure, lower than that of said high pressure column pressure, of from about 40 to 150 psia; (G) separating said first oxygen-enriched vapor fraction by rectification in said medium pressure column into a second nitrogen-rich vapor fraction and a second oxygen-enriched liquid fraction; (H) recovering from about 20 to 60 percent of said second nitrogen-rich vapor fraction as medium pressure nitrogen gas at a pressure of from about 40 to 150 psia and a purity of at least 99 mole percent; (I) condensing a portion of said second nitrogen-rich vapor fraction by indirect heat exchange with said second oxygen-enriched liquid fraction thereby producing a second nitrogen-rich liquid portion and a second oxygen-enriched vapor fraction; (J) employing said second nitrogen-rich liquid portion as liquid reflux for said medium pressure column; and (K) removing from the process said second oxygen-enriched vapor fraction.
Claim 2
Dependent Claim
323 words
A process for the production of nitrogen gas at greater than atmospheric pressure by the separation of air by rectification comprising: (A) introducing cleaned, cooled feed air at greater than atmospheric pressure into a high pressure column having a top condenser, and operating at a pressure of from about 80 to 300 psia; (B) separating said feed air by rectification in said high pressure column into a first nitrogen-rich vapor fraction and a first oxygen-enriched liquid fraction; (C) recovering from about 20 to 60 percent of said first nitrogen-rich vapor fraction as high pressure nitrogen gas at a pressure of from about 80 to 300 psia and a purity of at least 99 mole percent; (D) condensing a portion of said first nitrogen-rich vapor fraction by indirect heat exchange with said first oxygen-enriched liquid fraction thereby producing a first nitrogen-rich liquid portion and a first oxygen-enriched vapor fraction; (E) employing said first nitrogen-rich liquid portion as liquid reflux for said high pressure column; (F) introducing said first oxygen-enriched vapor fraction into a medium pressure column having a top condenser, and operating at a pressure, lower than that of said high pressure column pressure, of from about 40 to 150 psia; (G) separating said first oxygen-enriched vapor fraction by rectification in said medium pressure column into a second nitrogen-rich vapor fraction and a second oxygen-enriched liquid fraction; (H) recovering from about 20 to 60 percent of said second nitrogen-rich vapor fraction as medium pressure nitrogen gas at a pressure of from about 40 to 150 psia and a purity of at least 99 mole percent; (I) condensing a portion of said second nitrogen-rich vapor fraction by indirect heat exchange with said second oxygen-enriched liquid fraction thereby producing a second nitrogen-rich liquid portion and a second oxygen-enriched vapor fraction; (J) employing said second nitrogen-rich liquid portion as liquid reflux for said medium pressure column; and (K) removing from the process said second oxygen-enriched vapor fraction.
Claim 3
Dependent Claim
22 words
The process of claim 1 wherein said high pressure column is operating at a pressure of from about 90 to 200 psia.
Claim 4
Dependent Claim
22 words
The process of claim 1 wherein said high pressure column is operating at a pressure of from about 100 to 160 psia.
Claim 5
Dependent Claim
22 words
The process of claim 1 wherein said medium pressure column is operating at a pressure of from about 45 to 100 psia.
Claim 6
Dependent Claim
22 words
The process of claim 1 wherein said medium pressure column is operating at a pressure of from about 50 to 80 psia.
Claim 7
Dependent Claim
20 words
The process of claim 1 wherein a portion of said first nitrogen-rich liquid portion is recovered as product liquid nitrogen.
Claim 8
Dependent Claim
20 words
The process of claim 1 wherein a portion of said second nitrogen-rich liquid portion is recovered as product liquid nitrogen.
Claim 9
Dependent Claim
24 words
The process of claim 1 wherein up to about 5 percent of said first oxygen-enriched liquid fraction is introduced into said medium pressure column.
Claim 10
Dependent Claim
21 words
The process of claim 1 wherein said second oxygen-enriched vapor fraction is warmed and expanded prior to removal from the process.
Claim 11
Dependent Claim
50 words
The process of claim 1 wherein from about 10 to 30 percent of said cleaned cooled feed air is warmed, expanded and introduced into said medium pressure column as feed wherein it is separated into parts which make up said second nitrogen-rich vapor fraction and said second oxygen-enriched liquid fraction.
Claim 12
Dependent Claim
28 words
The process of claim 1 wherein from about 30 to 50 percent of said first nitrogen-rich vapor fraction in step (C) is recovered as high pressure nitrogen gas.
Claim 13
Dependent Claim
28 words
The process of claim 1 wherein from about 35 to 45 percent of said first nitrogen-rich vapor fraction in step (C) is recovered as high pressure nitrogen gas.
Claim 14
Dependent Claim
28 words
The process of claim 1 wherein from about 30 to 50 percent of said second nitrogen-rich vapor fraction in step (H) is recovered as medium pressure nitrogen gas.
Claim 15
Dependent Claim
28 words
The process of claim 1 wherein from about 35 to 45 percent of said second nitrogen-rich vapor fraction in step (H) is recovered as medium pressure nitrogen gas.
Claim 16
Dependent Claim
23 words
The process of claim 1 wherein at least some of the said second oxygen-enriched vapor fraction is recovered as product lower purity oxygen.
Claim 17
Dependent Claim
41 words
The process of claim 1 wherein from about 1 to 3 percent of the cleaned cooled feed air is condensed by indirect heat exchange with product or waste streams and introduced into either the high pressure or the medium pressure column.
Claim 18
Dependent Claim
27 words
The process of claim 1 wherein at least some of the first nitrogen-rich vapor fraction which is recovered as product nitrogen gas is expanded prior to recovery.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-03-27 | 1987-09-26 | 1988-03-27 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-03-27 | 1991-09-26 | 1992-03-27 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-03-27 | 1995-09-26 | 1996-03-27 | $7700.00 | Window Closed / Lapsed |