Cryogenic recovery of high purity hydrogen

• US 4,756,730 A
• Filed: 08/08/1986
• Issued: 07/12/1988
• Est. Priority Date: 08/08/1986
• Status: Expired due to Fees

• Current Assignee: Santa Fe Braun, Inc. (Transocean Limited)
• Original Assignee: Santa Fe Braun, Inc. (Transocean Limited)
• Inventors: Stupin, Walter J.
• Primary Examiner(s): Warner, Steven E.
• Application Number:
  US06/894,659
• Time in Patent Office: 704 Days
• Field of Search: 62/17, 62/18, 62/23, 62/24, 62/30, 62/32, 62/36, 62/42
• US Class Current: 62/620
• CPC Class Codes: F25J 2200/02 in a single pressure main column system
• CPC Class Codes: F25J 2200/70 Refluxing the column with a condensed part of the feed stream, i.e. fractionator top is stripped or self-rectified
• CPC Class Codes: F25J 2205/04 in the feed line, i.e. upstream of the fractionation step
• CPC Class Codes: F25J 2210/02 Multiple feed streams, e.g. originating from different sources
• CPC Class Codes: F25J 2215/10 Hydrogen
• CPC Class Codes: F25J 2230/30 Compression of the feed stream
• CPC Class Codes: F25J 3/0219 Refinery gas, cracking gas, coke oven gas, gaseous mixtures containing aliphatic unsaturated CnHm or gaseous mixtures of undefined nature
• CPC Class Codes: F25J 3/0233 separation of CnHm with 1 carbon atom or more
• CPC Class Codes: F25J 3/0238 separation of CnHm with 2 carbon atoms or more
• CPC Class Codes: F25J 3/0252 separation of hydrogen production of hydrogen containing gas in general C01B3/00, e.g. separation of hydrogen or hydrogen containing gases form gaseous mixtures at low temperatures C01B3/506
• CPC Class Codes: Y10S 62/932 From natural gas

Abstract

A process for the cryogenic purification of industrial by-product hydrogen streams to recover a high yield of a high purity hydrogen product is disclosed in which two or more of such by-product streams, one containing detrimental amounts of non-readily condensible impurities having boiling points below that of methane, e.g., nitrogen, helium and the like, the other containing by-product hydrogen gas streams which are substantially free of non-readily condensible impurities. These two feed streams are then separately passed through successive cooling and separation stages. At each separation stage, a liquid bottom fraction containing readily condensible hydrocarbons is separated from the overhead of each of the two feed streams. Successive separations are carried out until the overhead from the stream which is substantially free of non-readily condensible impurities (but which contains a significant amount of readily condensible impurities, including methane) attains the desired degree of purity. At this point, the bottom fraction of this stream is predominantly liquid methane, and this bottom fraction is used to scrub a preponderance of nitrogen and like impurities from the overheads of the stream containing significant amounts of these non-readily condensible impurities.

Claims

1. A process for the cryogenic purification of two or more industrial by-product gas streams containing impure hydrogen in recoverable amounts, at least one of the by-product gas streams being substantially free of non-readily condensible impurities having boiling points below that of methane and containing only hydrocarbons, including methane, as impurities, and at least one of the by-product gas streams containing significant amounts of non-readily condensible impurities having boiling points below that of methane, comprising:

separately passing the by-product gas streams substantially free of non-readily condensible impurities constituting a first feed stream, and the by-product gas streams containing significant amounts of non-readily condensible impurities constituting a second feed stream, through cooling and separation stages to separate, at each stage, a hydrogen containing gas stream overhead fraction from a condensed bottom fraction, the hydrogen containing gas stream overheads from said second feed stream also containing the non-readily condensible impurities,

feeding the hydrogen containing gas stream overhead fraction of said second feed stream from the last of the separation stages to a methane absorber,

feeding the first feed stream'"'"'s bottom fraction from the last of the separation stages to the methane absorber, and

recovering a purified overhead hydrogen gas stream from the methane absorber.

2. A process as recited in claim 1 wherein the first and second feed streams undergo compression, acid gas removal and drying before being separately passed through the series of cooling and separation stages.

3. A process as recited in claim 1 wherein the purified overhead gas stream from the methane absorber comprises greater than 90 mole percent hydrogen and not more than about 1.5 mole percent of non-readily condensible impurities having boiling points below that of methane.

4. A process as recited in claim 1 wherein hydrocarbon impurities having boiling points above that of methane contained in recoverable amounts in the first and second feed streams are recovered in concentrated form from the condensed bottoms fractions from the series of cooling and separation stages.

5. A process as recited in claim 1 in which the bottom fraction of said first feed stream from the last of the separation stages is fed to the methane absorber at a place higher than that at which the hydrogen gas stream overhead fraction of said second feed stream from the last separation stage is fed to the absorber.

6. A process as recited in claim 1 in which the absorber contains trays or packing to facilitate contact between the bottoms liquid of the said first feed stream from the last separation stage and the overhead of the second feed stream from the last separation stage.