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US4507404A Expired / Lapsed US ⏱️ 0.0 years remaining

Preparation of hydrocarbon mixtures from syngas

Assignee: Shell USA Inc
•
Filing: 1984-02-24
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Granted: 1985-03-26
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Expires: 2004-02-24
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Abstract

Abstract A process is described for preparing gasoline boiling range hydrocarbons with a high iso-paraffins content from syngas having a H 2 /CO mol. ratio between 1.0 and 5.0 over a catalyst mixture comprising a methanol synthesis component which contains zinc and one or more metals selected from the group consisting of chromium, copper and aluminum and a crystalline metal silicate with ZSM-5 structure which contains SiO 2 and one or more oxides of a trivalent metal A selected from the group consisting of aluminum, iron, gallium, rhodium, chromium and scandium, and wherein the SiO 2 /A 2 O 3 molar ratio is higher than 10; and which catalyst mixture has been prepared by spray-drying followed by calcining at a temperature between 425° and 525° C.

Inventors

  • 👤 Johannes K. Minderhoud
  • 👤 Martin F. M. Post

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 00:41
CPC Classifications
B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/40; B01J29/405; C; C07; C07C; C07C1/00; C07C1/02; C07C1/04; C07C1/0425; C07C1/0445; C07C2523/00; C07C2523/06; C07C2523/16; C07C2523/24; C07C2523/26; C07C2529/00; C07C2529/04; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 222 words
A process for the preparation of a hydrocarbon mixture from a mixture of carbon monoxide and hydrogen, characterized in that for the preparation of a hydrocarbon mixture whose C 5 + fraction has a high content of branched C 5 and C 6 paraffins, a H 2 /CO mixture having a H 2 /CO molar ratio between 1.0 and 5.0 is contacted with a catalyst mixture which has been prepared by dispersing a crystalline metal silicate which after one hour's calcination in air at 500° C. has the following properties: (a) an X-ray powder diffraction pattern in which the strongest lines are the four lines given in Table A Table A d(Å) 11.1±0.2 10.0±0.2 3.84±0.07 3.72±0.06; and (b) in which, in addition to SiO 2 , one or more oxides of a trivalent metal A chosen from aluminum, iron, gallium, rhodium, chromium and scandium occur, the SiO 2 /A 2 O 3 molar ratio is higher than 10; in water together with one or more precipitates which contain zinc and one or more metals chosen from chromium, copper and aluminum and which precipitates have been obtained by adding a basic reacting substance to one or more aqueous solutions of salts of the metals concerned, spray-drying the dispersion thus obtained and calcining the spray-dried material at a temperature between 425° and 525° C.
Claim 2
Dependent Claim 222 words
A process for the preparation of a hydrocarbon mixture from a mixture of carbon monoxide and hydrogen, characterized in that for the preparation of a hydrocarbon mixture whose C 5 + fraction has a high content of branched C 5 and C 6 paraffins, a H 2 /CO mixture having a H 2 /CO molar ratio between 1.0 and 5.0 is contacted with a catalyst mixture which has been prepared by dispersing a crystalline metal silicate which after one hour's calcination in air at 500° C. has the following properties: (a) an X-ray powder diffraction pattern in which the strongest lines are the four lines given in Table A Table A d(Å) 11.1±0.2 10.0±0.2 3.84±0.07 3.72±0.06; and (b) in which, in addition to SiO 2 , one or more oxides of a trivalent metal A chosen from aluminum, iron, gallium, rhodium, chromium and scandium occur, the SiO 2 /A 2 O 3 molar ratio is higher than 10; in water together with one or more precipitates which contain zinc and one or more metals chosen from chromium, copper and aluminum and which precipitates have been obtained by adding a basic reacting substance to one or more aqueous solutions of salts of the metals concerned, spray-drying the dispersion thus obtained and calcining the spray-dried material at a temperature between 425° and 525° C.
Claim 3
Dependent Claim 37 words
A process as claimed in claim 1, characterized in that the catalyst mixture has been prepared by using a crystalline silicate comprising only one trivalent metal A chosen from the group consisting of aluminum, iron and gallium.
Claim 4
Dependent Claim 35 words
A process as claimed in claim 1, characterized in that the catalyst mixture has been prepared by using a crystalline silicate having a SiO 2 /A 2 O 3 molar ratio between 20 and 500.
Claim 5
Dependent Claim 35 words
A process as claimed in claim 2, characterized in that the catalyst mixture has been prepared by using a crystalline silicate having a SiO 2 /A 2 O 3 molar ratio between 20 and 500.
Claim 6
Dependent Claim 36 words
A process as claimed in claim 1, characterized in that the catalyst mixture has been prepared by using a co-precipitate obtained by adding a basic reacting substance to an aqueous solution comprising all the metals involved.
Claim 7
Dependent Claim 36 words
A process as claimed in claim 3, characterized in that the catalyst mixture has been prepared by using a co-precipitate obtained by adding a basic reacting substance to an aqueous solution comprising all the metals involved.
Claim 8
Dependent Claim 46 words
A process as claimed in claim 1, characterized in that in the catalyst mixture has been prepared by using a precipitate which, in addition to zinc, comprises chromium and in which the atomic percentage of zinc calculated on the sum of zinc and chromium is 60-80%.
Claim 9
Dependent Claim 46 words
A process as claimed in claim 5, characterized in that in the catalyst mixture has been prepared by using a precipitate which, in addition to zinc, comprises chromium and in which the atomic percentage of zinc calculated on the sum of zinc and chromium is 60-80%.
Claim 10
Dependent Claim 59 words
A process as claimed in claim 1, characterized in that in the preparation of the catalyst mixture the ratio between the quantities of metal-containing precipitate and crystalline silicate in the dispersion is chosen such that after spray-drying a catalyst mixture is obtained which per part by weight of silicate comprises 1-7.5 pbw of metal oxides coming from the precipitate.
Claim 11
Dependent Claim 59 words
A process as claimed in claim 7, characterized in that in the preparation of the catalyst mixture the ratio between the quantities of metal-containing precipitate and crystalline silicate in the dispersion is chosen such that after spray-drying a catalyst mixture is obtained which per part by weight of silicate comprises 1-7.5 pbw of metal oxides coming from the precipitate.

References Cited (Backward Citations)

US4086262A Cited
GB2006260A Cited
GB2037315A Cited
US4338089A Cited
US4385193A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-03-25 1988-09-24 1989-03-26 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-03-25 1992-09-24 1993-03-26 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-03-25 1996-09-24 1997-03-26 $7700.00 Window Closed / Lapsed

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