← Back to Patent Explorer
US5472986A Expired / Lapsed US ⏱️ 0.0 years remaining

Methanol production process using a high nitrogen content synthesis gas with a hydrogen recycle

Assignee: Starchem Inc
•
Filing: 1994-11-08
•
Granted: 1995-12-05
•
Expires: 2014-11-08
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A method for preparing methanol from a synthesis gas having less than 90% the stoichiometric amount of H 2 to convert the CO and CO 2 content of the synthesis gas to methanol by recycling into combination with such synthesis gas a sufficient amount of a hydrogen rich gas stream obtained as a permeate gas by diffusion of the process tail gas to provide a combined synthesis-recycle gas stream having at least about 95% of the stoichiometric amount of H 2 to convert its CO and CO 2 content to methanol. In a preferred embodiment of the invention compressed air is taken from a gas turbine to form the oxidant steam used in forming the synthesis gas, such synthesis gas in combination with the hydrogen rich recycle gas is processed through a series of methanol convertors to methanol and the non-permeate portion of the tail gas from this methanol process is returned as fuel to the gas turbine.

Inventors

  • 👤 Christiaan P. VAN Dijk

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 07:29
CPC Classifications
C; C07; C07C; C07C29/00; C07C29/15; C07C29/151; C07C29/1516; C07C29/1518

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 195 words
A process for converting natural gas to methanol or products derivative of methanol, comprising the steps of: partially oxidizing natural gas with an oxidant stream to form a synthesis gas containing H 2 , CO and CO 2 in a ratio of (H 2 )/(2CO+3CO 2 ) less than 1.0; combining the synthesis gas with a hydrogen rich recycle gas stream secured as a permeate gas stream from diffusion of a tail gas stream remaining after completion of methanol recovery through a semipermeable membrane preferential for permeation of H 2 in preference to N 2 , said hydrogen rich recycle gas stream being used in an amount that provides a combined synthesis-recycle gas stream containing H 2 , CO and CO 2 in a ratio of (H 2 )/(2CO+3CO 2 ) which is greater than that of the synthesis gas; passing said combined synthesis-recycle gas stream into a plurality of contacts with a methanol conversion catalyst with recovery of methanol from said gas stream between contacts with a methanol conversion catalyst to form after the last methanol recovery step a tail gas stream from which the hydrogen rich recycle gas stream is secured by diffusion.
Claim 2
Dependent Claim 195 words
A process for converting natural gas to methanol or products derivative of methanol, comprising the steps of: partially oxidizing natural gas with an oxidant stream to form a synthesis gas containing H 2 , CO and CO 2 in a ratio of (H 2 )/(2CO+3CO 2 ) less than 1.0; combining the synthesis gas with a hydrogen rich recycle gas stream secured as a permeate gas stream from diffusion of a tail gas stream remaining after completion of methanol recovery through a semipermeable membrane preferential for permeation of H 2 in preference to N 2 , said hydrogen rich recycle gas stream being used in an amount that provides a combined synthesis-recycle gas stream containing H 2 , CO and CO 2 in a ratio of (H 2 )/(2CO+3CO 2 ) which is greater than that of the synthesis gas; passing said combined synthesis-recycle gas stream into a plurality of contacts with a methanol conversion catalyst with recovery of methanol from said gas stream between contacts with a methanol conversion catalyst to form after the last methanol recovery step a tail gas stream from which the hydrogen rich recycle gas stream is secured by diffusion.
Claim 3
Dependent Claim 22 words
The process of claim 1, wherein said synthesis gas has a ratio of (H 2 )/(2CO+3CO 2 ) of 0.85 or less.
Claim 4
Dependent Claim 26 words
The process of claim 2, wherein the combined synthesis-recycle gas stream has a ratio of (H 2 )/(2 CO+3 CO 2 ) of 0.95 or greater.
Claim 5
Dependent Claim 23 words
The process of claim 3, wherein the combined synthesis-recycle gas stream is passed into at least three contacts with a methanol conversion catalyst.
Claim 6
Dependent Claim 44 words
The process of claim 4, wherein the oxidant stream is secured from compressed air taken from a gas turbine and the non-permeate portion of the tail gas following recovery of the hydrogen rich recycle gas stream is utilized as fuel for the gas turbine.
Claim 7
Dependent Claim 22 words
The process of claim 5, wherein the non-permeate portion of the tail gas has a heating value of 100 BTU/scf or greater.
Claim 8
Dependent Claim 22 words
The process of claim 6, wherein the non-permeate portion of the tail gas is used in its entirety as gas turbine fuel.
Claim 9
Dependent Claim 26 words
The process of claim 6, wherein the non-permeate portion of the tail gas has at least 30% of its heat of combustion content supplied by hydrogen.
Claim 10
Dependent Claim 29 words
The process of claim 8, wherein no more than 30% of the heat of combustion content of the non-permeate portion of the tail gas is supplied by a hydrocarbon.

References Cited (Backward Citations)

US4093029A Cited
US4181675A Cited
US5173513A Cited
US4650814A Cited
US5063250A Cited
US5079267A Cited
US5177114A Cited
US5245110A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1998-12-04 1999-06-05 1999-12-05 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 2002-12-04 2003-06-05 2003-12-05 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2006-12-04 2007-06-05 2007-12-05 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag