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US4331774A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the preparation of hydrocarbons

Assignee: Shell USA Inc
•
Filing: 1980-07-17
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Granted: 1982-05-25
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Expires: 2000-07-17
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Abstract

Abstract A process is disclosed for the preparation of aromatic hydrocarbon mixtures from a feed mixture of carbon monoxide and hydrogen by contacting said feed at elevated temperature and pressure with a mixture of two catalysts; one capable of converting said feed into acyclic oxygen containing hydrocarbons and the other certain crystalline gallium silicates.

Inventors

  • 👤 Michael A. M. Boersma
  • 👤 Martin F. M. Post
  • 👤 Lambert Schaper

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 10:15
CPC Classifications
B; B01; B01J; B01J29/00; B01J29/87; C; C07; C07C; C07C1/00; C07C1/02; C07C1/04; C07C1/0425; C07C1/043; C07C2523/00; C07C2523/06; C07C2523/16; C07C2523/24; C07C2523/26; C07C2529/00; C07C2529/87

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 204 words
A process for the preparation of an aromatic hydrocarbon mixture from a feed mixture of carbon monoxide and hydrogen wherein the molar ratio of hydrogen to carbon monoxide in the feed lies between 0.25 and 1.0 which comprises contacting said feed in a contacting zone at a temperature of 200°-500° C., a pressure of 1-150 bar and a space velocity of 50-5000 Nl gas/l catalyst/h with a mixture of two catalysts, a catalyst X containing zinc together with chromium and having the capability of catalyzing the conversion of an H 2 /CO mixture into acyclic oxygen-containing hydrocarbons and a catalyst Y being a crystalline gallium silicate, having the following properties: (a) thermally stable up to a temperature above 600° C., (b) an X-ray powder diffraction pattern showing, inter alia, the reflections given in Table A of the specification, (c) in the formula which gives the composition of the silicate, expressed in moles of the oxides, and in which, in addition to oxides of hydrogen, alkali metal and/or alkaline-earth metal and silicon, gallium oxide is present, the Ga 2 O 3 /SiO 2 molar ratio (m) is less than 0.1 to produce a contact product, and separating an aromatic hydrocarbon mixture from said contact product.
Claim 2
Dependent Claim 204 words
A process for the preparation of an aromatic hydrocarbon mixture from a feed mixture of carbon monoxide and hydrogen wherein the molar ratio of hydrogen to carbon monoxide in the feed lies between 0.25 and 1.0 which comprises contacting said feed in a contacting zone at a temperature of 200°-500° C., a pressure of 1-150 bar and a space velocity of 50-5000 Nl gas/l catalyst/h with a mixture of two catalysts, a catalyst X containing zinc together with chromium and having the capability of catalyzing the conversion of an H 2 /CO mixture into acyclic oxygen-containing hydrocarbons and a catalyst Y being a crystalline gallium silicate, having the following properties: (a) thermally stable up to a temperature above 600° C., (b) an X-ray powder diffraction pattern showing, inter alia, the reflections given in Table A of the specification, (c) in the formula which gives the composition of the silicate, expressed in moles of the oxides, and in which, in addition to oxides of hydrogen, alkali metal and/or alkaline-earth metal and silicon, gallium oxide is present, the Ga 2 O 3 /SiO 2 molar ratio (m) is less than 0.1 to produce a contact product, and separating an aromatic hydrocarbon mixture from said contact product.
Claim 3
Dependent Claim 32 words
A process according to claim 1, wherein said contacting is carried out at a temperature of 300°-450° C., a pressure of 5-100 bar and a space velocity of 300-3000 Nl gas/l catalyst/h.
Claim 4
Dependent Claim 26 words
A process according to claim 1, wherein said catalyst X has the capability of converting an H 2 /CO mixture into substantially methanol and/or dimethyl ether.
Claim 5
Dependent Claim 28 words
A process according to claim 3, wherein in the catalyst X the atomic percentage of zinc, based on the sum of zinc and chromium, is at least 60%.
Claim 6
Dependent Claim 26 words
A process according to claim 4, wherein in the catalyst X the atomic percentage of zinc, based on the sum of zinc and chromium, is 60-80%.
Claim 7
Dependent Claim 25 words
A process according to claim 3, wherein the catalyst mixture contains per part by volume of catalyst Y 1-5 parts by volume of catalyst X.
Claim 8
Dependent Claim 21 words
A process according to claim 1, wherein the catalyst mixture contains a crystalline gallium silicate whose m is at least 0.0015.
Claim 9
Dependent Claim 12 words
A process according to claim 7, wherein m is at least 0.0020.
Claim 10
Dependent Claim 24 words
A process according to claim 1, wherein the catalyst mixture contains a crystalline silicate with an alkali metal content of less than 0.05% w.

References Cited (Backward Citations)

US1728732A Cited
US4138442A Cited
US4213921A Cited
US4238318A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-05-24 1985-11-23 1986-05-25 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-05-24 1989-11-23 1990-05-25 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-05-24 1993-11-23 1994-05-25 $7700.00 Window Closed / Lapsed

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