US4659351A
Expired / Lapsed
US
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Combined process to produce liquid helium, liquid nitrogen, and gaseous nitrogen from a crude helium feed
Assignee: Air Products and Chemicals Inc
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Filing: 1986-01-29
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Granted: 1987-04-21
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Expires: 2006-01-29
Abstract
Abstract The present invention is directed to a process for the purification and liquefaction of helium from a feed stream consisting essentially of nitrogen and helium with some minor impurities, wherein the helium is purified in a two step process: the first purification step comprising refrigerating the feed stream to condense nitrogen and any impurities from the feed stream, feeding the cooled feed stream to a separator, and removing from the bottom of the separator the condensed nitrogen and impurities in the feed stream and from the top of the separator a gaseous, high-helium-content stream; the second purification step comprising warming the gaseous, high-helium-content stream from the first purification step, feeding said stream to a pressure swing adsorber, and removing from the pressure swing adsorber an essentially pure helium stream, which is liquefied by feeding said essentially pure helium stream to a liquefier; wherein refrigeration is provided for the warm end of the liquefier and the two step purification; the improvement comprising providing said refrigeration by compressing a side stream of the essentially pure helium in a compressor and expanding said compressed stream in an expansion engine thereby producing a cold helium gas stream; splitting said cold helium stream into two substreams and circulating said cold helium gas stream to the warm end of the liquefier and to the two step purification to provide refrigeration duty.
Inventors
- 👤 Wayne G. Stuber
- 👤 David W. Studer
- 👤 Arthur R. Winters Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 16:14
CPC Classifications
F; F25; F25J; F25J1/00; F25J1/0002; F25J1/0005; F25J1/0007; F25J1/0012; F25J1/0015; F25J1/003; F25J1/0032; F25J1/0035; F25J1/0037; F25J1/0047; F25J1/0052; F25J1/006; F25J1/007; F25J1/0072; F25J1/02; F25J1/0201; F25J1/0202; F25J1/0203; F25J1/0208; F25J1/0228; F25J1/0235; F25J1/0237; F25J3/00; F25J3/06; F25J3/0605; F25J3/061; F25J3/063; F25J3/066; F25J3/0685; F25J3/069; F25J3/08; F25J2205/00; F25J2205/40; F25J2205/60; F25J2215/00; F25J2215/04; F25J2215/30; F25J2220/00; F25J2220/02; F25J2245/00; F25J2245/02; F25J2260/00; F25J2260/20
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
247 words
A process for providing refrigeration for the purification and liquefaction of helium from a feed stream consisting essentially of nitrogen and helium with some minor impurites, of the type wherein the helium is purified in a two step process: the first purification step comprising refrigeration the feed stream to condense nitrogen and any impurities from the feed stream, and separating the cooled feed stream into a condensed nitrogen and impurities stream and a gaseous, high-helium content stream; the second purification step comprising warming the gaseous, high-helium-content stream from the first purification step, feeding said stream to a pressure swing adsorber, and removing from the pressure swing adsorber an essentially pure helium stream; and feeding said essentially pure helium stream to a liquefier comprising: (a) providing said refrigeration by compressing a side stream of the essentially pure helium in a compressor and expanding said compressed stream in an expansion engine thereby producing a cold helium gas stream; (b) splitting said cold helium stream into two substreams; (c) circulating a first substream of said cold helium gas stream to the warm end of the liquefier to provide refrigeration duty; (d) circulating a second substream of said cold helium gas stream to the two step purification to provide refrigeration duty; (e) separating a portion of said second substream for return to the warm end of the liquefier to provide refrigeration duty; and (f) recycling the remaining portion of said second substream to the inlet of the compressor in step (a).
Claim 2
Dependent Claim
247 words
A process for providing refrigeration for the purification and liquefaction of helium from a feed stream consisting essentially of nitrogen and helium with some minor impurites, of the type wherein the helium is purified in a two step process: the first purification step comprising refrigeration the feed stream to condense nitrogen and any impurities from the feed stream, and separating the cooled feed stream into a condensed nitrogen and impurities stream and a gaseous, high-helium content stream; the second purification step comprising warming the gaseous, high-helium-content stream from the first purification step, feeding said stream to a pressure swing adsorber, and removing from the pressure swing adsorber an essentially pure helium stream; and feeding said essentially pure helium stream to a liquefier comprising: (a) providing said refrigeration by compressing a side stream of the essentially pure helium in a compressor and expanding said compressed stream in an expansion engine thereby producing a cold helium gas stream; (b) splitting said cold helium stream into two substreams; (c) circulating a first substream of said cold helium gas stream to the warm end of the liquefier to provide refrigeration duty; (d) circulating a second substream of said cold helium gas stream to the two step purification to provide refrigeration duty; (e) separating a portion of said second substream for return to the warm end of the liquefier to provide refrigeration duty; and (f) recycling the remaining portion of said second substream to the inlet of the compressor in step (a).
Claim 3
Dependent Claim
221 words
A process for providing refrigeration for the purification and liquefaction of helium from a feed stream consisting essentially of nitrogen and helium with some minor impurities, of the type wherein the helium is purified in a two step process: the first purification step comprising refrigerating the feed stream to condense nitrogen and any impurities from the feed stream, and separating the cooled feed stream into a condensed nitrogen and impurities stream and a gaseous, high-helium content stream; the second purification step comprising warming the gaseous, high-helium-content stream from the first purification step, feeding said stream to a pressure swing adsorber, and removing from the pressure swing adsorber an essentially pure helium stream; and feeding said essentially pure helium stream to a liquefier comprising: (a) providing said refrigeration by compressing a side stream of the essentially pure helium in a compressor and expanding said compressed stream in an expansion engine thereby producing a cold helium gas stream; (b) splitting said cold helium stream into two substreams; (c) circulating a first substream of said cold helium gas stream to the warm end of the liquefier to provide refrigeration duty; (d) circulating a second substream of said cold helium gas stream to the two step purification to provide refrigeration duty; (e) recycling said second substream to the inlet of the compressor in step (a).
Claim 4
Dependent Claim
221 words
A process for providing refrigeration for the purification and liquefaction of helium from a feed stream consisting essentially of nitrogen and helium with some minor impurities, of the type wherein the helium is purified in a two step process: the first purification step comprising refrigerating the feed stream to condense nitrogen and any impurities from the feed stream, and separating the cooled feed stream into a condensed nitrogen and impurities stream and a gaseous, high-helium content stream; the second purification step comprising warming the gaseous, high-helium-content stream from the first purification step, feeding said stream to a pressure swing adsorber, and removing from the pressure swing adsorber an essentially pure helium stream; and feeding said essentially pure helium stream to a liquefier comprising: (a) providing said refrigeration by compressing a side stream of the essentially pure helium in a compressor and expanding said compressed stream in an expansion engine thereby producing a cold helium gas stream; (b) splitting said cold helium stream into two substreams; (c) circulating a first substream of said cold helium gas stream to the warm end of the liquefier to provide refrigeration duty; (d) circulating a second substream of said cold helium gas stream to the two step purification to provide refrigeration duty; (e) recycling said second substream to the inlet of the compressor in step (a).
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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) | 1990-04-20 | 1990-10-20 | 1991-04-21 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-04-20 | 1994-10-20 | 1995-04-21 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-04-20 | 1998-10-20 | 1999-04-21 | $7700.00 | Window Closed / Lapsed |