Patent US4895583A successfully refreshed from Google Patents.
US4895583A
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Apparatus and method for separating air
Assignee: Messer LLC
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Filing: 1989-01-12
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Granted: 1990-01-23
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Expires: 2009-01-12
Abstract
Abstract Method and Apparatus for separating a gaseous mixture into component gases wherein a portion of a compressed cooled stream of the gaseous mixture is substantially liquefied and respective portions sent to high and low pressure columns and either one of the gaseous components or a portion of the gaseous mixture is utilized for refrigeration from expansion with a portion of the work utilized for compression of the gaseous mixture.
Inventors
- 👤 Scott Flanagan
- 👤 Robert A. Mostello
- 👤 Anne P. Ko
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 15:04
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04151; F25J3/04163; F25J3/04169; F25J3/04187; F25J3/04193; F25J3/04206; F25J3/04248; F25J3/04284; F25J3/0429; F25J3/04303; F25J3/04309; F25J3/04406; F25J3/04418; F25J2200/00; F25J2200/50; F25J2200/54; F25J2205/00; F25J2205/60; F25J2205/62; F25J2250/00; F25J2250/30; F25J2250/40; F25J2250/50
Claims Analysis
Total Claims: 15
Claim 1
Independent Claim
253 words
A process for the production of oxygen by the separation of air comprising: (a) separating air which has been compressed and cooled into first and second portions; (b) liquefying substantially all of the first portion and introducing a first part thereof and the second portion into a high pressure fractionating means to obtain a crude liquid oxygen stream and substantially pure gaseous nitrogen; (c) introducing the second part of the first portion of liquid air formed in step (b) into a low pressure fractionating means to obtain a substantially pure gaseous nitrogen product and a substantially pure liquid oxygen stream, wherein the crude liquid oxygen stream produced in step (b) is introduced into the low pressure fractionating means at an intermediate stage; (d) condensing the substantially pure gaseous nitrogen formed in step (b) in heat exchange with a boiling liquid withdrawn from an intermediate stage in the low pressure fractionating means, introducing a portion of the resulting liquid nitrogen to each of the high and low pressure fractionating means as reflux and returning the resulting vapor to the low pressure fractionating means; (e) forming substantially pure gaseous oxygen from the liquid stream formed in step (d) by heat exchange with the first portion of cooled, compressed air being liquefied in step (b); and (f) withdrawing said substantially pure oxygen gas as product, wherein the ratio of the liquid air introduced into the high pressure fractionating means to the liquid air introduced into the low pressure fractionating means is from about 1:9 to 1:1.
Claim 2
Dependent Claim
253 words
A process for the production of oxygen by the separation of air comprising: (a) separating air which has been compressed and cooled into first and second portions; (b) liquefying substantially all of the first portion and introducing a first part thereof and the second portion into a high pressure fractionating means to obtain a crude liquid oxygen stream and substantially pure gaseous nitrogen; (c) introducing the second part of the first portion of liquid air formed in step (b) into a low pressure fractionating means to obtain a substantially pure gaseous nitrogen product and a substantially pure liquid oxygen stream, wherein the crude liquid oxygen stream produced in step (b) is introduced into the low pressure fractionating means at an intermediate stage; (d) condensing the substantially pure gaseous nitrogen formed in step (b) in heat exchange with a boiling liquid withdrawn from an intermediate stage in the low pressure fractionating means, introducing a portion of the resulting liquid nitrogen to each of the high and low pressure fractionating means as reflux and returning the resulting vapor to the low pressure fractionating means; (e) forming substantially pure gaseous oxygen from the liquid stream formed in step (d) by heat exchange with the first portion of cooled, compressed air being liquefied in step (b); and (f) withdrawing said substantially pure oxygen gas as product, wherein the ratio of the liquid air introduced into the high pressure fractionating means to the liquid air introduced into the low pressure fractionating means is from about 1:9 to 1:1.
Claim 3
Dependent Claim
30 words
A process in accordance with claim 1, wherein a portion of the substantially pure gaseous oxygen formed in step (e) is returned to the low pressure fractionating means as reboil.
Claim 4
Dependent Claim
28 words
A process in accordance with claim 1, wherein a portion of the substantially pure gaseous nitrogen formed in step (b) is expanded to provide refrigeration for the process.
Claim 5
Dependent Claim
29 words
A process in accordance with claim 3, wherein the gaseous nitrogen is expanded in a turbo expander and the energy provided thereby is utilized to compress air for separation.
Claim 6
Dependent Claim
29 words
A process in accordance with claim 4, wherein the portion of the substantially pure gaseous nitrogen expanded in the turbo expander exceeds 10 percent of the total air compressed.
Claim 7
Dependent Claim
38 words
A process in accordance with claim 1, wherein the ratio of the liquid air introduced into the high pressure fractionating means to the liquid air introduced into the low pressure fractionating means is from about 1:5 to 1:3.
Claim 8
Dependent Claim
24 words
A process in accordance with claim 1, wherein the first portion of air formed in step (a) is further compressed prior to being liquefied.
Claim 9
Dependent Claim
29 words
A process in accordance with claim 1, wherein said first portion of air liquefied in step (b) comprises from about 25 to 50 percent of the total air compressed.
Claim 10
Dependent Claim
29 words
A process in accordance with claim 8, wherein said first portion of air liquefied in step (b) comprises from about 35 to 40 percent of the total air compressed.
Claim 11
Dependent Claim
24 words
A process in accordance with claim 1, wherein step (a), the air is separated into said first and second portion prior to being compressed.
Claim 12
Dependent Claim
23 words
A process in accordance with claim 1, wherein air is separated into said first and second portions prior to being compressed and cooled.
Claim 13
Dependent Claim
37 words
A process in accordance with claim 1, wherein a part of the second portion of air formed in step (a) is expanded to provide refrigeration for the process and then introduced into the low pressure fractionating means.
Claim 14
Dependent Claim
28 words
A process in accordance with claim 12, wherein the air is expanded in a turbo expander and the energy provided thereby is utilized to compress air for separation.
Claim 15
Dependent Claim
30 words
A process in accordance with claim 1, wherein the second portion of air formed in step (a) is further compressed prior to being introduced into the high pressure fractionating means.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1993-01-22 | 1993-07-24 | 1994-01-23 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1997-01-22 | 1997-07-24 | 1998-01-23 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2001-01-22 | 2001-07-24 | 2002-01-23 | $7700.00 | Window Closed / Lapsed |