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US4096163A Expired / Lapsed US ⏱️ 0.0 years remaining

Conversion of synthesis gas to hydrocarbon mixtures

Assignee: Mobil Oil AS
•
Filing: 1976-10-08
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Granted: 1978-06-20
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Expires: 1996-10-08
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Abstract

Abstract Synthesis gas is contacted with an intimate mixture of a carbon monoxide hydrogen reduction catalyst, comprising a methanol synthesis catalyst in combination with a selective class of acidic crystalline aluminosilicate having a silica/alumina ratio greater than 12, a pore dimension greater than about 5 Angstroms to produce hydrocarbon mixtures useful in the manufacture of heating fuels, gasoline, aromatic hydrocarbons, and chemicals intermediates.

Inventors

  • 👤 Clarence D. Chang
  • 👤 William H. Lang
  • 👤 Anthony J. Silvestri
  • 👤 Robert L. Smith

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 13:21
CPC Classifications
B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/40; B01J29/405; B01J29/42; B01J29/46; C; C07; C07C; C07C1/00; C07C1/02; C07C1/04; C07C1/0425; C07C1/043; B01J2229/00; B01J2229/10; B01J2229/26; B01J2229/30; B01J2229/42; B01J29/65; B01J29/70; C07C2523/00; C07C2523/16; C07C2523/24; C07C2523/26; C07C2523/70; C07C2523/72; C07C2529/00; C07C2529/04; C07C2529/06; C07C2529/40; C07C2529/65; C07C2529/70; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52; Y10; Y10S; Y10S585/00; Y10S585/929; Y10S585/943

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 122 words
In the process of converting synthesis gas, comprising carbon monoxide and hydrogen, to a hydrocarbon product by contacting such at about 450 to 1000° F with a catalyst comprising as a first component a metal carbon monoxide reduction catalyst and as a second component an acidic crystalline aluminosilicate zeolite having a silica to alumina ratio of at least 12 and a constraint index of about 1 to 12; the improvement which comprises utilizing as said carbon monoxide reducing catalyst component a methanol synthesis catalyst comprising copper or chromium containing catalysts or mixtures thereof in a finely ground form and thereby converting said synthesis gas to substantially only C 1 - C 6 paraffins composed mainly of C 2 - C 4 paraffins.
Claim 2
Dependent Claim 122 words
In the process of converting synthesis gas, comprising carbon monoxide and hydrogen, to a hydrocarbon product by contacting such at about 450 to 1000° F with a catalyst comprising as a first component a metal carbon monoxide reduction catalyst and as a second component an acidic crystalline aluminosilicate zeolite having a silica to alumina ratio of at least 12 and a constraint index of about 1 to 12; the improvement which comprises utilizing as said carbon monoxide reducing catalyst component a methanol synthesis catalyst comprising copper or chromium containing catalysts or mixtures thereof in a finely ground form and thereby converting said synthesis gas to substantially only C 1 - C 6 paraffins composed mainly of C 2 - C 4 paraffins.
Claim 3
Dependent Claim 24 words
The method of claim 1 wherein said crystalline aluminosilicate is selected from a class of crystalline zeolites comprising ZSM-5, ZSM-11, ZSM-12, ZSM-35 and ZSM-38.
Claim 4
Dependent Claim 25 words
The method of claim 1 wherein the synthesis gas hydrogen to carbon oxides volume ratio is maintained within the range of from 0.2 to 6.0
Claim 5
Dependent Claim 41 words
The method of claim 1 wherein said methanol synthesis catalyst comprises: metals or oxides of zinc together with chromia; metals or oxides of zinc and copper together with chromia or alumina; or metals or oxides of zinc, copper, chromium and lanthanum.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-06-19 1981-12-19 1982-06-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-06-19 1985-12-19 1986-06-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-06-19 1989-12-19 1990-06-20 $7700.00 Window Closed / Lapsed

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