EP0204478A2
Expired / Lapsed
EP
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Production of technical hydrogen
Assignee: Imperial Chemical Industries Ltd
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Filing: 1986-05-23
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Granted: —
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Expires: 2006-05-23
Abstract
Abstract @ A PSA based process for the production of technical hydrogen wherein the feed to the PSA contains nitrogen and carbon monoxide with a hydrogen/(carbon monoxide + nitrogen) volume ratio in the range 1.2 to 4 and a nitrogen/ carbon monoxide volume ratio of at least 10. The adsorption step in the PSA stage is stopped when the integrated nitrogen content of the unadsorbed product is 1 to 10% by volume. The raw gas fed to the PSA is preferably made by a primary reforming a hydrocarbon feedstock with steam followed by secondary reforming followed by shift and water removal: the heat required for primary reforming is preferably supplied by the secondary reformer outlet gas. The PSA waste gas is preferably combusted in a gas turbine driving the secondary reformer air compressor.
Inventors
- 👤 Alwyn Pinto
Bibliographic Details
Application Number
—
Jurisdiction
EP
Data Source
google_patents
Last Synchronized
2026-11-08 12:42
CPC Classifications
C; C01; C01B; C01B3/00; C01B3/02; C01B3/32; C01B3/34; C01B3/48; C01B3/50; C01B3/56; C01B2203/00; C01B2203/02; C01B2203/0205; C01B2203/0227; C01B2203/0233; C01B2203/0244; C01B2203/025; C01B2203/0261; C01B2203/0283; C01B2203/0288; C01B2203/04; C01B2203/042; C01B2203/043; C01B2203/0465; C01B2203/0475; C01B2203/0495; C01B2203/06; C01B2203/08; C01B2203/0805; C01B2203/0833; C01B2203/0838; C01B2203/0844; C01B2203/0872; C01B2203/0883; C01B2203/10; C01B2203/1005; C01B2203/1023; C01B2203/1041; C01B2203/1047; C01B2203/1052; C01B2203/1064; C01B2203/107; C01B2203/1076; C01B2203/12; C01B2203/1205; C01B2203/1211; C01B2203/1217; C01B2203/1223; C01B2203/1235; C01B2203/1241; C01B2203/1258; C01B2203/14; C01B2203/142; C01B2203/143; C01B2203/146; C01B2203/148; C01B2203/80; C01B2203/82; Y; Y02; Y02E; Y02E20/00; Y02E20/32
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
97 words
A pressure swing adsorption (PSA) process for producing a technical hydrogen stream comprising (a) feeding to the PSA adsorbent a raw gas containing hydrogen, nitrogen, and carbon oxides, wherein the volume ratio of hydrogen to the sum of nitrogen and carbon monoxide is in the range 1.2 to 4.0 and the nitrogen content by volume is at least ten times the carbon monoxide content, and (b) stopping the adsorption step in the PSA cycle when the integrated nitrogen content of the unadsorbed product gas of the PSA stage is in the range 1 to 10X by volume.
Claim 2
Dependent Claim
97 words
A pressure swing adsorption (PSA) process for producing a technical hydrogen stream comprising (a) feeding to the PSA adsorbent a raw gas containing hydrogen, nitrogen, and carbon oxides, wherein the volume ratio of hydrogen to the sum of nitrogen and carbon monoxide is in the range 1.2 to 4.0 and the nitrogen content by volume is at least ten times the carbon monoxide content, and (b) stopping the adsorption step in the PSA cycle when the integrated nitrogen content of the unadsorbed product gas of the PSA stage is in the range 1 to 10X by volume.
Claim 3
Dependent Claim
21 words
A process according to claim 1 wherein the integrated nitrogen content of the product gas is at least 2X by volume.
Claim 4
Dependent Claim
23 words
A process according to claim 1 or claim 2 wherein the nitrogen/carbon monoxide volume ratio of the raw gas is at least 20.
Claim 5
Dependent Claim
23 words
A process according to any one of claims 1 to 3 wherein the raw gas contains less than 2X by volume of methane.
Claim 6
Dependent Claim
34 words
A process according to any one of claims 1 to 4 wherein the volume ratio of nitrogen plus carbon monoxide to carbon dioxide in the raw gas is in the range 0.6 to 4.
Claim 7
Dependent Claim
127 words
A process according to any one of claims 1 to 5 wherein the raw gas is made by reacting a carbonaceous feedstock with steam and an oxygen/nitrogen mixture at superatmospheric pressure using process conditions so as to produce a crude gas in which the molar ratio of the sum of carbon monoxide and hydrogen to nitrogen is in the range 1.2 to 4.0, and the nitrogen content is at least 5X by volume on a dry basis, then subjecting the crude gas to the catalytic shift reaction with steam to convert carbon monoxide to carbon dioxide plus hydrogen to an extent such that the nitrogen content of the shifted gas is at least ten times the carbon monoxide content by volume, and removing any excess of steam.
Claim 8
Dependent Claim
68 words
A process according to claim 6 wherein the carbonaceous feedstock is reacted with steam in a primary reforming step by passing the feedstock/steam gas stream over a catalyst disposed in tubes heated in a furnace and the resultant primary reformed gas is reacted with the oxygen/nitrogen mixture in a secondary reforming step to produce a secondary reformed gas and said tubes being heated by the secondary reformed gas.
Claim 9
Dependent Claim
33 words
A process according to claim 6 or claim 7 wherein the shift reaction is conducted under such conditions that the carbon monoxide content of the shifted gas is less than 1% by volume.
Claim 10
Dependent Claim
42 words
A process according to any one of claims 6 to 8 wherein at least part of the waste gas from the PSA stage is combusted with air and the combustion products thereof power a turbine driving the compressor for the oxygen/nitrogen mixture.
Claim 11
Dependent Claim
27 words
Technical hydrogen containing at least 90X by volume -hydrogen and containing at least 1% by volume nitrogen and less than 200 ppm by volume of carbon monoxide.
Claim 12
Dependent Claim
27 words
Technical hydrogen containing at least 90X by volume -hydrogen and containing at least 1% by volume nitrogen and less than 200 ppm by volume of carbon monoxide.
References Cited (Backward Citations)
No citation records indexed.
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