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US5076837A Expired / Lapsed US ⏱️ 0.0 years remaining

Air separation in combination with a chemical process

Assignee: BOC Group Ltd
•
Filing: 1989-10-16
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Granted: 1991-12-31
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Expires: 2009-10-16
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Abstract

Abstract A method and apparatus for recovering work from a nitrogen stream, wherein the nitrogen is preheated via heat exchange with hot fluid from a chemical process, which process utilizes the oxygen product of the air separation. Preferably at least a part of the expanded nitrogen is utilized to preheat at least one fluid reactant of the chemical process. The chemical process may be gasification or direct reduction of iron oxide, as well as the conversion of natural gas into synthesis gas.

Inventors

  • 👤 Thomas Rathbone
  • 👤 John T. Lavin

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 18:16
CPC Classifications
C; C01; C01B; C01B3/00; C01B3/02; C01B3/32; C01B3/34; C01B3/36; F; F02; F02C; F02C6/00; F02C6/04; F02C6/10; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04521; F25J3/04527; F25J3/04539; F25J3/04545; F25J3/04551; F25J3/04557; F25J3/04563; F25J3/04575; F25J3/04581; F25J3/04612; Y; Y02; Y02T; Y02T50/00; Y02T50/60; Y10; Y10S; Y10S75/00; Y10S75/958

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 83 words
A combined process comprising: separating air into oxygen and nitrogen; supplying a stream of the oxygen to a chemical process that takes place at elevated temperature and that produces as product or waste a hot gaseous stream; heating a stream of the nitrogen at a pressure of at least 5 atmospheres to a temperature of at least 700° C. by heat exchange with the hot gaseous stream; and expanding the thus heated nitrogen stream in a turbine with the performance of external work.
Claim 2
Dependent Claim 83 words
A combined process comprising: separating air into oxygen and nitrogen; supplying a stream of the oxygen to a chemical process that takes place at elevated temperature and that produces as product or waste a hot gaseous stream; heating a stream of the nitrogen at a pressure of at least 5 atmospheres to a temperature of at least 700° C. by heat exchange with the hot gaseous stream; and expanding the thus heated nitrogen stream in a turbine with the performance of external work.
Claim 3
Dependent Claim 31 words
A process as claimed in claim 1, in which the stream of nitrogen is heated to a temperature of at least 1000° C. at a pressure of at least 10 atmospheres.
Claim 4
Dependent Claim 17 words
A process as claimed in claim 2, in which the external work is the generation of electricity.
Claim 5
Dependent Claim 32 words
A process as claimed in claim 2, in which at least a part of the expanded nitrogen is used to pre-heat at least one fluid reactant that partakes in the chemical process.
Claim 6
Dependent Claim 36 words
A process as claimed in claim 1, in which at least a part of the expanded nitrogen is used to heat the said stream of nitrogen that is at a pressure of at least 5 atmospheres.
Claim 7
Dependent Claim 26 words
A process as claimed in claim 2, in which the chemical process includes the gasification of a carbonaceous material or the direct reduction of iron oxide.
Claim 8
Dependent Claim 19 words
A process as claimed in claim 1, in which the chemical process is a partial oxidation of a hydrocarbon.
Claim 9
Dependent Claim 23 words
A process as claimed in claim 7, in which the chemical process is the partial oxidation of natural gas to produce synthesis gas.
Claim 10
Dependent Claim 46 words
A process as claimed in claim 8, further including the steps of purifying the natural gas to yield pure methane and preheating the methane by at least part of the expanded nitrogen to a temperature of at least 600° C. upstream of the partial oxidation reaction.
Claim 11
Dependent Claim 57 words
A process as claimed in claim 1, in which the stream of nitrogen is taken at a pressure in the range of about 3 to 4 atmospheres from the lower pressure column of a double distillation column for the separation of air and is then compressed to raise it to a pressure of at least 5 atmospheres.

References Cited (Backward Citations)

JPS5683506A Cited
US4729217A Cited
US4697413A Cited
US4861369A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1994-12-30 1995-07-01 1995-12-31 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1998-12-30 1999-07-01 1999-12-31 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2002-12-30 2003-07-01 2003-12-31 $7700.00 Window Closed / Lapsed

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