US4343633A
Expired / Lapsed
US
⏱️ 0.0 years remaining
High pressure purification of hydrogen
Assignee: Linde GmbH
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Filing: 1980-11-24
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Granted: 1982-08-10
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Expires: 2000-11-24
Abstract
Abstract In the purification of a hydrogen stream contaminated with at least methane and ethane, e.g. a hydrogen cycle gas from a coal hydrogenation process, where the hydrogen stream is subjected to multistage partial condensation and separation of the respectively formed condensates, the improvement of subjecting the hydrogen stream under a pressure of above about 100 bar to the multistage partial condensation and separation of having in the final condensate 5-40 molar percent of ethane, thereby favorably altering the K-value of methane and its ease of removal from the hydrogen which is only altered in the manner desired when the process is conducted under pressures in excess of about 100 bar.
Inventors
- 👤 Helmut Kick
- 👤 Hans Kistenmacher
- 👤 Walter Schramm
- 👤 Berndt Hoerner
- 👤 Udo Lang
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 14:44
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/06; F25J3/063; F25J3/0655; C; C01; C01B; C01B3/00; C01B3/50; C01B3/506; F25J3/02; F25J3/0204; F25J3/0219; F25J3/0228; F25J3/0238; F25J3/0242; F25J3/0252; F25J3/0605; F25J3/062; F25J3/0645; C01B2203/00; C01B2203/04; C01B2203/0465; C01B2203/047; C01B2203/048; C01B2203/0485; C01B2203/0495; F25J2205/00; F25J2205/02; F25J2205/04; F25J2210/00; F25J2210/04; F25J2210/12; F25J2215/00; F25J2215/62; F25J2215/64; F25J2245/00; F25J2245/02; F25J2270/00; F25J2270/42; F25J2270/60; F25J2270/90; Y; Y10; Y10S; Y10S62/00; Y10S62/931; Y10S62/932
Claims Analysis
Total Claims: 21
Claim 1
Independent Claim
98 words
In a process for the purification of a hydrogen stream contaminated with at least methane and ethane, said process comprising subjecting the hydrogen stream to multistage partial condensation and separation of the respectively formed condensates, the improvement which comprises subjecting the hydrogen stream to the multistage partial condensation under a pressure above about 100 bar and adjusting said process so as to yield in the final condensate 5-40 molar percent of ethane with a predominating amount of methane thereby ensuring extensive condensation of the methane contained in the hydrogen stream to produce a hydrogen stream of high purity.
Claim 2
Dependent Claim
98 words
In a process for the purification of a hydrogen stream contaminated with at least methane and ethane, said process comprising subjecting the hydrogen stream to multistage partial condensation and separation of the respectively formed condensates, the improvement which comprises subjecting the hydrogen stream to the multistage partial condensation under a pressure above about 100 bar and adjusting said process so as to yield in the final condensate 5-40 molar percent of ethane with a predominating amount of methane thereby ensuring extensive condensation of the methane contained in the hydrogen stream to produce a hydrogen stream of high purity.
Claim 3
Dependent Claim
44 words
A process according to claim 1 wherein said adjusting comprises operating the partial condensation stages upstream of the final condensation so as to leave sufficient ethane in the gas entering the final condensation stage to be condensed therein to attain said 5-40 molar percent.
Claim 4
Dependent Claim
87 words
A process according to claim 2 wherein said hydrogen stream contains additional contaminant having a freezing point higher than the temperature of the last condensation stage, and wherein the next-to-last condensate separation is conducted at a temperature at which one or more contaminants which would be precipitated as solids at the temperature of the final condensation stage, are condensed out to such an extent that their solubility limit in the final condensation stage is not attained so that solids are not precipitated in the final condensation stage.
Claim 5
Dependent Claim
21 words
A process according to claim 1 wherein said adjusting comprises admixing a stream containing C 2 -hydrocarbon to the hydrogen stream.
Claim 6
Dependent Claim
39 words
A process according to claim 4 wherein said hydrogen stream contains contaminant having a higher boiling point than C 2 -hydrocarbon, and said admixing is conducted after condensation and separation of components boiling higher than said C 2 -hydrocarbon.
Claim 7
Dependent Claim
31 words
A process according to claim 4 wherein the C 2 -hydrocarbon stream is admixed to the hydrogen stream after cooling of the latter to temperatures of between 170 and 200 K.
Claim 8
Dependent Claim
31 words
A process according to claim 4, said admixed stream containing C 2 -hydrocarbon being a recycle stream derived from a downstream step of separating C 2 -hydrocarbon from a cold condensate.
Claim 9
Dependent Claim
15 words
A process according to claim 7 wherein said downstream step comprises rectification of the condensate.
Claim 10
Dependent Claim
19 words
A process according to claim 8 wherein several condensates together including the final condensate are subjected to the rectification.
Claim 11
Dependent Claim
15 words
A process according to claim 8 wherein the condensate is expanded prior to the rectification.
Claim 12
Dependent Claim
71 words
A process according to claim 1 wherein said hydrogen stream contains additional contaminant having a lower boiling point than methane, and additional contaminant having a higher boiling point than ethane, and condensing and separating said contaminants having a higher boiling point than ethane, and admixing additional methane to resultant hydrogen stream, said methane functioning to condense out a higher amount of said contaminant boiling below methane during a next condensation stage.
Claim 13
Dependent Claim
58 words
A process according to claim 11 further comprising cooling said hydrogen stream containing admixed methane, partially condensing and separating condensate from resultant cooled stream, and wherein said adjusting of said process so as to yield in the final condensate 5-40 molar percent of ethane, comprises admixing to resultant cooled gaseous hydrogen stream, a stream containing C 2 -hydrocarbon.
Claim 14
Dependent Claim
31 words
A process according to claim 12 wherein the C 2 -hydrocarbon stream is admixed to the hydrogen stream after cooling of the latter to temperatures of between 170 and 200 K.
Claim 15
Dependent Claim
19 words
A process according to claim 1 wherein the pressure of the hydrogen stream ranges between 200 and 300 bar.
Claim 16
Dependent Claim
20 words
A process according to claim 1 wherein the lower boiling contaminant comprises at least one of nitrogen and carbon monoxide.
Claim 17
Dependent Claim
82 words
In a process for the purification of a hydrogen stream containing contaminant having a boiling point less than methane, said process comprising subjecting said contaminant to partial condensation and separation, the improvement wherein said process is conducted under pressures above about 100 bar, and methane is added to said hydrogen stream prior to partial condensation thereby effecting a larger degree of condensation of the lower boiling contaminant and resulting in a gaseous stream of hydrogen containing a relatively large amount of methane.
Claim 18
Dependent Claim
82 words
In a process for the purification of a hydrogen stream containing contaminant having a boiling point less than methane, said process comprising subjecting said contaminant to partial condensation and separation, the improvement wherein said process is conducted under pressures above about 100 bar, and methane is added to said hydrogen stream prior to partial condensation thereby effecting a larger degree of condensation of the lower boiling contaminant and resulting in a gaseous stream of hydrogen containing a relatively large amount of methane.
Claim 19
Dependent Claim
68 words
A process according to claim 16, further comprising admixing a stream containing essentially C 2 -hydrocarbons to the gaseous stream of hydrogen remaining, which contains a relatively large amount of methane, after the addition of the methane and the cooling and separating of the lower boiling contaminant condensate thereby ensuring extensive condensation of the methane contained in the hydrogen stream to produce a hydrogen stream of high purity.
Claim 20
Dependent Claim
107 words
In a process for the purification of a hydrogen stream containing contaminant having a boiling point higher than C 2 -hydrocarbons, as well as containing methane and ethane, said process comprising subjecting the hydrogen stream to multistage partial condensation and separation of the respectively formed condensates, the improvement which comprises subjecting the hydrogen stream to the multistage partial condensation under a pressure above about 100 bar, and admixing to the hydrogen stream, after condensation and separation of the components having a boiling point higher than C 2 -hydrocarbons, a stream which contains C 2 -hydrocarbons to thereby increase condensation of the methane contained in the hydrogen stream.
Claim 21
Dependent Claim
107 words
In a process for the purification of a hydrogen stream containing contaminant having a boiling point higher than C 2 -hydrocarbons, as well as containing methane and ethane, said process comprising subjecting the hydrogen stream to multistage partial condensation and separation of the respectively formed condensates, the improvement which comprises subjecting the hydrogen stream to the multistage partial condensation under a pressure above about 100 bar, and admixing to the hydrogen stream, after condensation and separation of the components having a boiling point higher than C 2 -hydrocarbons, a stream which contains C 2 -hydrocarbons to thereby increase condensation of the methane contained in the hydrogen stream.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1985-08-09 | 1986-02-08 | 1986-08-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-08-09 | 1990-02-08 | 1990-08-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-08-09 | 1994-02-08 | 1994-08-10 | $7700.00 | Window Closed / Lapsed |