EP0081178A2
Expired / Lapsed
EP
⏱️ 0.0 years remaining
Air separation process with single distillation column for combined gas turbine system
Assignee: Air Products and Chemicals Inc
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Filing: 1982-11-29
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Granted: —
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Expires: 2002-11-29
Abstract
Abstract The present invention is directed to an air separation system for the recovery of pressurized, substantially pure oxygen gas. The system uses a single pressure distillation column and bums a nitrogen-oxygen waste stream to provide power for the air compressor, the oxygen product compressor and electric generation. The distillation column has a split feed to develop reflux and reboil and to provide Initial separation of the liquid and vapor components of the column.
Inventors
- 👤 Lee Strohl Gaumer
Bibliographic Details
Application Number
—
Jurisdiction
EP
Data Source
google_patents
Last Synchronized
2026-11-06 08:29
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04006; F25J3/04012; F25J3/04018; F25J3/04036; F25J3/04109; F25J3/04115; F25J3/04121; F25J3/04139; F25J3/04145; F25J3/04248; F25J3/04284; F25J3/0429; F25J3/04296; F25J3/044; F25J3/04521; F25J3/04563; F25J3/04575; F25J3/04593; F25J3/04612; F25J2200/00; F25J2200/70; F25J2205/00; F25J2205/24; F25J2230/00; F25J2230/06; Y; Y10; Y10S; Y10S62/00; Y10S62/915; Y10S62/939
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
275 words
A process for separating high purity oxygen from air in a single pressure distillation column comprising the steps of: (a) compressing an air feed stream wherein the compressor is powered by a gas turbine, (b) cooling the air feed stream in a reversing heat exchanger against a nitrogen waste stream from said column and an oxygen product stream, (c) separating a side air feed stream from a remaining air feed stream and passing the side stream back through the heat exchanger to provide a temperature unbalance to preclude carbon dioxide and water buildup in said exchanger, (d) expanding and cooling the side stream in a turbine before introducing said stream into an intermediate point of said column, (e) heat exchanging the remaining air feed stream with the liquid phase of the bottom of said column to condense said stream and reboil said liquid, (f) further heat exchanging the remaining air feed stream against the overhead product stream of said column before introducing said feed stream as reflux into the top of said column, (g) removing, at pressure, a nitrogen waste stream containing a combustible level of oxygen from the top of said column as the overhead product stream of step (f), (h) combusting said pressurized nitrogen waste stream with a fuel to provide a hot pressurized gas feed to said gas turbine of step (a), (i) removing a high purity oxygen product stream from the bottom of said column and pressurizing the same by a compressor driven by a steam turbine wherein said steam turbine is provided with steam by a cyclic heat exchange of the steam with the exhaust of the gas turbine. -
Claim 2
Dependent Claim
275 words
A process for separating high purity oxygen from air in a single pressure distillation column comprising the steps of: (a) compressing an air feed stream wherein the compressor is powered by a gas turbine, (b) cooling the air feed stream in a reversing heat exchanger against a nitrogen waste stream from said column and an oxygen product stream, (c) separating a side air feed stream from a remaining air feed stream and passing the side stream back through the heat exchanger to provide a temperature unbalance to preclude carbon dioxide and water buildup in said exchanger, (d) expanding and cooling the side stream in a turbine before introducing said stream into an intermediate point of said column, (e) heat exchanging the remaining air feed stream with the liquid phase of the bottom of said column to condense said stream and reboil said liquid, (f) further heat exchanging the remaining air feed stream against the overhead product stream of said column before introducing said feed stream as reflux into the top of said column, (g) removing, at pressure, a nitrogen waste stream containing a combustible level of oxygen from the top of said column as the overhead product stream of step (f), (h) combusting said pressurized nitrogen waste stream with a fuel to provide a hot pressurized gas feed to said gas turbine of step (a), (i) removing a high purity oxygen product stream from the bottom of said column and pressurizing the same by a compressor driven by a steam turbine wherein said steam turbine is provided with steam by a cyclic heat exchange of the steam with the exhaust of the gas turbine. -
Claim 3
Dependent Claim
31 words
The invention of Claim 1 wherein the nitrogen waste stream is passed through the reversing heat exchanger to remove carbon dioxide and water before combusting said stream for the gas turbine.
Claim 4
Dependent Claim
25 words
The invention of Claim 1 or 2 wherein the fuel and the nitrogen waste stream are heat exchanged with the gas turbine exhaust before combustion.
Claim 5
Dependent Claim
34 words
The invention of Claim 1 wherein the waste nitrogen stream removed from the column overhead is in equilibrium with the remaining air feed stream introduced into the top of the distillation column as reflux.
Claim 6
Dependent Claim
28 words
The invention of Claim 1 or 2 wherein the gas turbine drives the air compressor and a generator for the production of electricity for export or process requirements.
Claim 7
Dependent Claim
25 words
The invention of Claim 1 or 2 wherein the oxygen product stream is indirectly heat exchanged with said air feed in the reversing heat exchangers.
Claim 8
Dependent Claim
39 words
The invention of Claim 1 wherein the intermediate point introduction of the expanded side feed air stream occurs at a column tray level sufficient to increase the liquid/vapor reflux ratio to separate argon as well as nitrogen from oxygen.
References Cited (Backward Citations)
No citation records indexed.
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