US5040370A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Integrated air separation/metallurgical process
Assignee: BOC Group Ltd
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Filing: 1990-06-06
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Granted: 1991-08-20
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Expires: 2010-06-06
Abstract
Abstract Air is separated into oxygen and nitrogen in rectification columns 28 and 30. A stream of nitrogen is withdrawn from the top of the column 30 through an outlet 54, is warmed to about ambient temperature by passage through heat exchangers 34, 46 and 24, and is then heated at a pressure in the range 2 to 7 atmospheres absolute by heat exchange in heat exchanger 56 with a hot stream of fluid initially at a temperature of less than 600° C. without said fluid undergoing a change of phase. The resulting hot nitrogen is then expanded in turbine 58 with the performance of external work, e.g. the generation of electricity.
Inventors
- 👤 Thomas Rathbone
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 20:49
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04521; F25J3/04527; F25J3/04539; F25J3/04248; F25J3/04284; F25J3/0429; F25J3/04303; F25J3/04406; F25J3/04412; F25J3/04545; F25J3/04551; F25J3/04557; F25J3/04563; F25J3/04575; F25J3/04581; F25J3/04612; F25J2200/00; F25J2200/20
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
145 words
A combined process comprising: performing a first process including separating air into oxygen and nitrogen in a distillation column; withdrawing a stream of the oxygen from the distillation column; supplying the stream of the oxygen to a second process that takes place at an elevated temperature and that produces a hot stream of fluid having a temperature of no less than about 200° C. and no greater than about 600° C.; withdrawing a stream of the nitrogen from the distillation column; heating the stream of the nitrogen at a pressure of no less than about 2 atmospheres absolute and no greater than about 7 atmospheres absolute by heat exchange with the hot stream of fluid and without the hot stream of fluid undergoing a change of phase; and expanding the thus heated stream of the nitrogen in a turbine with the performance of external work.
Claim 2
Dependent Claim
145 words
A combined process comprising: performing a first process including separating air into oxygen and nitrogen in a distillation column; withdrawing a stream of the oxygen from the distillation column; supplying the stream of the oxygen to a second process that takes place at an elevated temperature and that produces a hot stream of fluid having a temperature of no less than about 200° C. and no greater than about 600° C.; withdrawing a stream of the nitrogen from the distillation column; heating the stream of the nitrogen at a pressure of no less than about 2 atmospheres absolute and no greater than about 7 atmospheres absolute by heat exchange with the hot stream of fluid and without the hot stream of fluid undergoing a change of phase; and expanding the thus heated stream of the nitrogen in a turbine with the performance of external work.
Claim 3
Dependent Claim
18 words
The combined process as claimed in claim 1, in which the external work is the production of electricity.
Claim 4
Dependent Claim
31 words
The combined process as claimed in claim 1, in which the temperature of the hot stream of fluid is in a range of between about 200° C. and about 400° C.
Claim 5
Dependent Claim
32 words
The combined process according to claim 3, in which the pressure of the stream of the nitrogen is in a range of between about 2 atmospheres absolute and about 5 atmospheres absolute.
Claim 6
Dependent Claim
31 words
The combined process according to claim 1, in which the second process is an industrial process and the hot stream of fluid is a waste gas stream from the industrial process.
Claim 7
Dependent Claim
17 words
The combined process according to claim 5, in which the oxygen is used in the industrial process.
Claim 8
Dependent Claim
44 words
The combined process according to claim 1, in which the second process comprises an industrial process and the hot stream of fluid is a heat transfer oil which has been heated without change of phase by a waste gas stream from an industrial process.
Claim 9
Dependent Claim
28 words
The combined process according to claim 7, in which the second process comprises an industrial process and the stream of the oxygen is used in said industrial process.
Claim 10
Dependent Claim
29 words
The combined process according to claim 1, in which the stream of the nitrogen is not compressed intermediate said distillation column and its heat exchange with said fluid stream.
Claim 11
Dependent Claim
22 words
The combined process according to claim 9, in which the distillation column is the lower pressure column of a double column arrangement.
Claim 12
Dependent Claim
131 words
A combination comprising: means for separating air into oxygen and nitrogen and for producing a stream of the nitrogen; and a stream of the oxygen means receiving said stream of oxygen for generating a stream of heated fluid having a temperature of no less than about 200° C. and no greater than about 600° C.; a heat exchanger connected to the air separation means and the heated fluid generation means for heat exchanging the stream of the nitrogen at a pressure in a range of between about 2 and about 7 atmospheres with the stream of heated fluid and without said fluid undergoing a change of phase; and an expansion turbine connected to the heat exchanger for expanding the thus heated stream of the nitrogen with the performance of external work.
Claim 13
Dependent Claim
131 words
A combination comprising: means for separating air into oxygen and nitrogen and for producing a stream of the nitrogen; and a stream of the oxygen means receiving said stream of oxygen for generating a stream of heated fluid having a temperature of no less than about 200° C. and no greater than about 600° C.; a heat exchanger connected to the air separation means and the heated fluid generation means for heat exchanging the stream of the nitrogen at a pressure in a range of between about 2 and about 7 atmospheres with the stream of heated fluid and without said fluid undergoing a change of phase; and an expansion turbine connected to the heat exchanger for expanding the thus heated stream of the nitrogen with the performance of external work.
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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) | 1994-08-19 | 1995-02-18 | 1995-08-20 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1998-08-19 | 1999-02-18 | 1999-08-20 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2002-08-19 | 2003-02-18 | 2003-08-20 | $7700.00 | Window Closed / Lapsed |