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US4894394A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the manufacture of methanol in combination with steam reforming of light hydrocarbons

Assignee: Shell USA Inc
•
Filing: 1988-10-12
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Granted: 1990-01-16
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Expires: 2008-10-12
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Abstract

Abstract Process for the manufacture of methanol by the reaction of a carbon monoxide and hydrogen mixture obtained by steam reforming of light hydrocarbons in the liquid phase in the presence of the catalyst system obtainable by combination of at least: (a) the salt containing a cation of a metal of group VIII of the Periodic Table of the Elements, (b) an alcoholate from an alkaline metal or alkaline earth metal, in a single pass through reactor, by conversion of the hydrogen-carbon monoxide gas mixture, which has been treated after steam treatment of natural gas by scrubbing carbon dioxide from the obtained gas mixture, and which has a hydrogen-carbon monoxide molar ratio in the range of from 2.8-4.5, and using the off-gas from the reaction after recovery of methanol as fuel to the reformer furnace.

Inventors

  • 👤 Arjan Van Dijk
  • 👤 Swan T. Sie

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 15:27
CPC Classifications
C; C07; C07C; C07C29/00; C07C29/15; C07C29/151; C07C29/153; C07C29/156; C07C29/157

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 257 words
Process for the production of methanol which comprises: (a) reacting a mixture of steam, carbon dioxide and light hydrocarbons at a pressure from 20-30 bar in a reforming zone heated by the oxidation of carbonaceous fuel to obtain steam reformate containing hydrogen and carbon monoxide in a molar ratio of hydrogen to carbon monoxide in the range from 2.8 to 4.5; (b) passing said steam reformate to a carbon dioxide separation zone to obtain a carbon dioxide steam and a treated stream reformate stream having substantially less carbon dioxide than said feed to step (b); (c) recycling at least part of said carbon dioxide stream from step (b) as feed to step (a); (d) reacting said treated stream reformate from step (b) in a single pass through a reaction zone at a temperature in the range from 70°-140° C. and a pressure from 15-25 bar in the presence of a catalyst system resulting from combining (1) a nickel salt; (2) an alcoholate of an alkali or an alkaline earth metal, and at least one of the following components: (3) a hydride of an alkali metal or an alkaline earth metal, or (4) an alcohol or an in-situ alcohol providing agent to obtain a reaction product containing methanol formed in the liquid phase, carbon monoxide and a mixture of other gases; (e) partially condensing said reaction product from step (d) to obtain a methanol product stream and an uncondensed off-gas stream; and (f) passing said uncondensed off-gas stream as fuel to heat the reforming zone of step (a).
Claim 2
Dependent Claim 257 words
Process for the production of methanol which comprises: (a) reacting a mixture of steam, carbon dioxide and light hydrocarbons at a pressure from 20-30 bar in a reforming zone heated by the oxidation of carbonaceous fuel to obtain steam reformate containing hydrogen and carbon monoxide in a molar ratio of hydrogen to carbon monoxide in the range from 2.8 to 4.5; (b) passing said steam reformate to a carbon dioxide separation zone to obtain a carbon dioxide steam and a treated stream reformate stream having substantially less carbon dioxide than said feed to step (b); (c) recycling at least part of said carbon dioxide stream from step (b) as feed to step (a); (d) reacting said treated stream reformate from step (b) in a single pass through a reaction zone at a temperature in the range from 70°-140° C. and a pressure from 15-25 bar in the presence of a catalyst system resulting from combining (1) a nickel salt; (2) an alcoholate of an alkali or an alkaline earth metal, and at least one of the following components: (3) a hydride of an alkali metal or an alkaline earth metal, or (4) an alcohol or an in-situ alcohol providing agent to obtain a reaction product containing methanol formed in the liquid phase, carbon monoxide and a mixture of other gases; (e) partially condensing said reaction product from step (d) to obtain a methanol product stream and an uncondensed off-gas stream; and (f) passing said uncondensed off-gas stream as fuel to heat the reforming zone of step (a).
Claim 3
Dependent Claim 10 words
Process according to claim 1 wherein step (c) the reaction
Claim 4
Dependent Claim 24 words
Process according to claim 1 wherein said in-situ alcohol providing agent is selected from alkyl formates, alkyl oxalates or alkyl carbonates and mixtures thereof.
Claim 5
Dependent Claim 14 words
Process according to claim 3 wherein said in-situ alcohol providing agent is a formate.
Claim 6
Dependent Claim 20 words
Process according to claim 1 wherein component (a) is selected from nickel formate, nickel acetate, nickel oxalate and nickel tolysate.
Claim 7
Dependent Claim 16 words
Process according to claim 1 wherein catalyst component (b) is a sodium alcoholate or potassium alcoholate.
Claim 8
Dependent Claim 27 words
Process according to claim 6 wherein said component (b) is selected from sodium methoxide, sodium ethoxide, sodium propoxide, sodium butoxide, sodium isobutoxide, sodium tert-pentoxide and potassium 2-methyldodec-2-oxide.

References Cited (Backward Citations)

US4271086A Cited
DE3244302A1 Cited
US4614749A Cited
US4619946A Cited
US4613623A Cited
US4623634A Cited
US4628066A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1993-01-15 1993-07-17 1994-01-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1997-01-15 1997-07-17 1998-01-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2001-01-15 2001-07-17 2002-01-16 $7700.00 Window Closed / Lapsed

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