US4548618A
Expired / Lapsed
US
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Process and apparatus for the separation of a mixture of gases
Assignee: Linde GmbH
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Filing: 1983-07-29
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Granted: 1985-10-22
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Expires: 2003-07-29
Abstract
Abstract A mixture of gases containing hydrogen and at least one further component, for example nitrogen and argon, is enriched in hydrogen in a separation stage by adsorption, or cooling and partial condensation and/or rectification and/or scrubbing. Upstream of this separation stage, at least part of the hydrogen is separated by membrane diffusion, thereby resulting in a highly improved process as compared to using either the separation stage or membrane diffusion alone, especially in connection with gaseous mixtures having components which are to be used at high pressures, e.g., a purge gas from an ammonia synthesis gas process.
Inventors
- 👤 Gerhard Linde
- 👤 Wolfgang Schmid
- 👤 Manfred Boelt
- 👤 Peter S. Burr
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-23 19:49
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/0228; F25J3/028; F25J3/0285; B; B01; B01D; B01D53/00; C; C01; C01B; C01B3/00; C01B3/50; C01B3/501; F25J3/0204; F25J3/0219; F25J3/0257; F25J3/06; F25J3/0605; F25J3/062; F25J3/063; F25J3/0655; C01B2203/00; C01B2203/04; C01B2203/0405; C01B2203/0465; C01B2203/048; C01B2203/0495; F25J2200/00; F25J2200/02; F25J2200/38; F25J2200/74; F25J2200/76; F25J2205/00; F25J2205/02; F25J2205/04; F25J2205/40; F25J2205/80; F25J2210/00; F25J2210/20; F25J2210/42; F25J2240/00; F25J2240/02; F25J2240/60; F25J2270/00; F25J2270/02; F25J2270/42; F25J2270/90; F25J2270/904; Y; Y10; Y10S; Y10S62/00; Y10S62/931; Y10S62/934
Claims Analysis
Total Claims: 21
Claim 1
Independent Claim
115 words
A process for the separation of hydrogen from a mixture of gases containing about 50 to 70% by volume of hydrogen, said process comprising separating more than 60% of the hydrogen up to 95% from the gaseous mixture by diffusion through a semipermeable membrane, thereby forming a residual mixture of gases depleted in hydrogen, expanding the residual gaseous mixture and passing resultant cooled residual gaseous mixture into indirect heat exchange with liquefied gas, the latter being obtained as bottoms from a rectification stage wherein at least a fraction of said residual gaseous mixture is subjected to rectification downstream of said indirect heat exchange, with the proviso that the process does not comprise a shift reaction.
Claim 2
Dependent Claim
115 words
A process for the separation of hydrogen from a mixture of gases containing about 50 to 70% by volume of hydrogen, said process comprising separating more than 60% of the hydrogen up to 95% from the gaseous mixture by diffusion through a semipermeable membrane, thereby forming a residual mixture of gases depleted in hydrogen, expanding the residual gaseous mixture and passing resultant cooled residual gaseous mixture into indirect heat exchange with liquefied gas, the latter being obtained as bottoms from a rectification stage wherein at least a fraction of said residual gaseous mixture is subjected to rectification downstream of said indirect heat exchange, with the proviso that the process does not comprise a shift reaction.
Claim 3
Dependent Claim
33 words
A process according to claim 1, wherein said residual gas is directly cooled and is subjected to a first rectification, and bottoms from said rectification stage is withdrawn and evaporated under subatmospheric pressure.
Claim 4
Dependent Claim
39 words
A process according to claim 2, wherein the evaporation is conducted with heat of compression supplied by fluid in a cooling circuit, and resultant cooled fluid is further used as a cooling medium in at least one rectification stage.
Claim 5
Dependent Claim
23 words
A process according to claim 3, wherein the fluid circulated in the cooling circuit is a component of the residual mixture of gases.
Claim 6
Dependent Claim
36 words
A process according to claim 3, wherein the fluid circulated in the cooling circuit is introduced as reflux to the top of a second rectification stage and to the head condenser of said first rectification stage.
Claim 7
Dependent Claim
26 words
A process according to claim 2, wherein the components of the gaseous mixture to be separated have boiling points of not more than approximately 120° K.
Claim 8
Dependent Claim
31 words
A process according to claim 2, wherein the subatmospheric pressure is generated by passing a gaseous component of partially liquefied residual mixture of gases through an ejector, as the driving jet.
Claim 9
Dependent Claim
26 words
A process according to claim 1, wherein the components of the gaseous mixture to be separated have boiling points of not more than approximately 120° K.
Claim 10
Dependent Claim
93 words
A process for the separation of hydrogen from a mixture of gases comprising separating at least part of the hydrogen from the gaseous mixture by diffusion through a semipermeable membrane, thereby forming a residual mixture of gases depleted in hydrogen, and further comprising work expanding the residual gaseous mixture and passing resultant cooled residual gaseous mixture into indirect heat exchange with liquified gas, the latter being obtained as bottoms from a rectification stage wherein at least a fraction of said residual gaseous mixture is subjected to rectification downstream of said indirect heat exchange.
Claim 11
Dependent Claim
93 words
A process for the separation of hydrogen from a mixture of gases comprising separating at least part of the hydrogen from the gaseous mixture by diffusion through a semipermeable membrane, thereby forming a residual mixture of gases depleted in hydrogen, and further comprising work expanding the residual gaseous mixture and passing resultant cooled residual gaseous mixture into indirect heat exchange with liquified gas, the latter being obtained as bottoms from a rectification stage wherein at least a fraction of said residual gaseous mixture is subjected to rectification downstream of said indirect heat exchange.
Claim 12
Dependent Claim
26 words
A process according to claim 9, wherein the components of the gaseous mixture to be separated have boiling points of not more than approximately 120° K.
Claim 13
Dependent Claim
22 words
A process according to claim 9, wherein not more than 60% of the hydrogen is separated from the gaseous by membrane diffusion.
Claim 14
Dependent Claim
24 words
A process according to claim 9, wherein more than 60% up to 95% of the hydrogen is separated from the gases by membrane diffusion.
Claim 15
Dependent Claim
69 words
A process for the separation of hydrogen from a mixture of gases comprising separating at least part of the hydrogen from the gaseous mixture by diffusion through a semipermeable membrane, thereby forming a residual mixture of gases depleted in hydrogen, directly cooling said residual mixture, subjecting resultant cooled gaseous mixture to a first stage rectification, and withdrawing bottoms from said rectification stage and evaporating said bottoms under subatmospheric pressure.
Claim 16
Dependent Claim
69 words
A process for the separation of hydrogen from a mixture of gases comprising separating at least part of the hydrogen from the gaseous mixture by diffusion through a semipermeable membrane, thereby forming a residual mixture of gases depleted in hydrogen, directly cooling said residual mixture, subjecting resultant cooled gaseous mixture to a first stage rectification, and withdrawing bottoms from said rectification stage and evaporating said bottoms under subatmospheric pressure.
Claim 17
Dependent Claim
39 words
A process according to claim 13, wherein the evaporation is conducted with heat of compression supplied by fluid in a cooling circuit, and resultant cooled fluid is further used as a cooling medium in at least one rectification stage.
Claim 18
Dependent Claim
23 words
A process according to claim 14, wherein the fluid circulated in the cooling circuit is a component of the residual mixture of gases.
Claim 19
Dependent Claim
36 words
A process according to claim 14, wherein the fluid circulated in the cooling circuit is introduced as reflux to the top of a second rectification stage and to the head condenser of said first rectification stage.
Claim 20
Dependent Claim
31 words
A process according to claim 13, wherein the subatmospheric pressure is generated by passing a gaseous component of partially liquefied residual mixture of gases through an ejector, as the driving jet.
Claim 21
Dependent Claim
26 words
A process according to claim 13, wherein the components of the gaseous mixture to be separated have boiling points of not more than approximately 120° K.
References Cited (Backward Citations)
US2583601A
Cited
US3026683A
Cited
US3251652A
Cited
US3336730A
Cited
US3324626A
Cited
US3553972A
Cited
US3838553A
Cited
US4264328A
Cited
US4180553A
Cited
US4255591A
Cited
US4266957A
Cited
US4238204A
Cited
US4229188A
Cited
US4367135A
Cited
US4374657A
Cited
US4398926A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1988-10-21 | 1989-04-22 | 1989-10-22 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-10-21 | 1993-04-22 | 1993-10-22 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-10-21 | 1997-04-22 | 1997-10-22 | $7700.00 | Window Closed / Lapsed |