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US4556645A Expired / Lapsed US ⏱️ 0.0 years remaining

Enhanced catalyst for conversion of syngas to liquid motor fuels

Assignee: Katalistiks International Inc
•
Filing: 1984-06-27
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Granted: 1985-12-03
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Expires: 2004-06-27
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Abstract

Abstract Synthesis gas comprising carbon monoxide and hydrogen is converted to C5+ hydrocarbons suitable for use as liquid motor fuels by contact with a dual catalyst system capable of enhancing the selectivity of said conversion to motor fuel range hydrocarbons and the quality of the resulting motor fuel product. The catalyst composition employs a Fischer-Tropsch catalyst, together with a co-catalyst/support component comprising SAPO silicoaluminophosphate, non-zeolitic molecular sieve catalyst.

Inventors

  • 👤 Peter K. Coughlin
  • 👤 Jule A. Rabo

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 14:06
CPC Classifications
C; C07; C07C; C07C1/00; C07C1/02; C07C1/04; C07C1/0425; C07C1/043; C07C1/0435; C07C1/044; B; B01; B01J; B01J29/00; B01J29/82; B01J29/84; B01J29/85; B01J37/00; B01J37/04; C07C2523/00; C07C2523/70; C07C2523/74; C07C2523/745; C07C2523/75; C07C2529/00; C07C2529/04; C07C2529/06; C07C2529/08; C07C2529/82; C07C2529/84; C07C2529/85

Claims Analysis

Total Claims: 33
Claim 1
Independent Claim 78 words
A catalyst composition adapted for the enhanced conversion of synthesis gas comprising carbon monoxide and hydrogen to C 5 + hydrocarbon mixtures having enhanced suitability for use as liquid motor fuels comprising: (a) a Fischer-Tropsch catalyst component; and (b) a co-catalyst/support component comprising a crystalline, microporous silicoaluminophosphate, non-zeolitic molecular sieve catalyst, whereby said catalyst composition is capable of enhancing the selectivity of said conversion to motor fuel range hydrocarbons and the quality of the resulting motor fuel product.
Claim 2
Dependent Claim 78 words
A catalyst composition adapted for the enhanced conversion of synthesis gas comprising carbon monoxide and hydrogen to C 5 + hydrocarbon mixtures having enhanced suitability for use as liquid motor fuels comprising: (a) a Fischer-Tropsch catalyst component; and (b) a co-catalyst/support component comprising a crystalline, microporous silicoaluminophosphate, non-zeolitic molecular sieve catalyst, whereby said catalyst composition is capable of enhancing the selectivity of said conversion to motor fuel range hydrocarbons and the quality of the resulting motor fuel product.
Claim 3
Dependent Claim 12 words
The composition of claim 1 in which said silicoaluminophosphate catalyst comprises SAPO-11.
Claim 4
Dependent Claim 12 words
The composition of claim 1 in which said silicoaluminophosphate catalyst comprises SAPO-31.
Claim 5
Dependent Claim 12 words
The composition of claim 1 in which said Fischer-Tropsch catalyst comprises cobalt.
Claim 6
Dependent Claim 12 words
The composition of claim 1 in which said Fischer-Tropsch catalyst comprises iron.
Claim 7
Dependent Claim 13 words
The composition of said claim 2 in which said Fischer-Tropsch catalyst comprises cobalt.
Claim 8
Dependent Claim 12 words
The composition of claim 3 in which said Fischer-Tropsch catalyst comprises cobalt.
Claim 9
Dependent Claim 12 words
The composition of claim 2 in which said Fischer-Tropsch catalyst comprises iron.
Claim 10
Dependent Claim 12 words
The composition of claim 3 in which said Fischer-Tropsch catalyst comprises iron.
Claim 11
Dependent Claim 29 words
The composition of claim 1 and including a steam-stabilized, hydrophobic zeolite Y additional co-catalyst/support component, said Fischer-Tropsch catalyst being supported mainly inside the crystals of said zeolite Y component.
Claim 12
Dependent Claim 12 words
The composition of claim 10 in which said Fischer-Tropsch catalyst comprises cobalt.
Claim 13
Dependent Claim 12 words
The composition of claim 11 in which said silicoaluminophosphate catalyst comprises SAPO-11.
Claim 14
Dependent Claim 12 words
The composition of claim 11 in which said silicoaluminophosphate catalyst comprises SAPO-31.
Claim 15
Dependent Claim 12 words
The composition of claim 10 in which said Fischer-Tropsch catalyst comprises iron.
Claim 16
Dependent Claim 12 words
The composition of claim 14 in which said silicoaluminophosphate catalyst comprises SAPO-11.
Claim 17
Dependent Claim 12 words
The composition of claim 14 in which said silicoaluminophosphate catalyst comprises SAPO-31.
Claim 18
Dependent Claim 15 words
The composition of claim 10 in which said zeolite Y component is in aluminum-extracted form.
Claim 19
Dependent Claim 21 words
The composition of claim 17 in which the alumina content of said aluminum-extracted zeolite is less than about 3 weight %.
Claim 20
Dependent Claim 20 words
The composition of claim 18 in which said Fischer-Tropsch catalyst comprises cobalt or iron and said silicoaluminophosphate catalyst comprises SAPO-11.
Claim 21
Dependent Claim 20 words
The composition of claim 18 in which said Fischer-Tropsch catalyst comprises cobalt or iron and said silicoaluminophosphate catalyst comprises SAPO-31.
Claim 22
Dependent Claim 70 words
The composition of claim 10 in which said zeolite Y has an SiO 2 /Al 2 O 3 molar ratio equal to or greater than 4.5, the essential X-ray powder diffraction pattern of zeolite Y, a unit cell dimension, A o , of less than 24.45 Angstroms, and a sorptive capacity for water vapor at 25° C. and a p/p o value of 0.10 of less than 10.0 weight percent.
Claim 23
Dependent Claim 37 words
The composition of claim 21 in which said SiO 2 /Al 2 O 3 molar ratio of the catalyst is from 4.5 to 9.0, and in which said unit cell dimension is from 24.20 to 24.45 Angstroms.
Claim 24
Dependent Claim 29 words
The composition of claim 19 in which the water adsorption capacity of the catalyst, at 25° C. and a p/p o of 0.10, is less than 6.0 weight percent.
Claim 25
Dependent Claim 70 words
The composition of claim 18 in which said zeolite Y has an SiO 2 /Al 2 O 3 molar ratio equal to a greater than 4.5, the essential X-ray powder diffraction pattern of zeolite Y, a unit cell dimension, A o , of less than 24.45 Angstroms, and a sorptive capacity for water vapor at 25° C. and a p/p o value of 0.10 of less than 10.0 weight percent.
Claim 26
Dependent Claim 35 words
The composition of claim 1 in which said silicoaluminophosphate comprises catalyst characterized by an adsorption of triethylamine of less than 5% by weight at a pressure of 2.6 torr and a temperature of 22° C.
Claim 27
Dependent Claim 36 words
The composition of claim 1 in which said silicoaluminophosphate comprises catalyst further characterized by an adsorption of cyclohexane of at least 2% by weight at a pressure of 90 torr and a temperature of 24° C.
Claim 28
Dependent Claim 12 words
The composition of claim 25 in which said Fischer-Tropsch catalyst comprises cobalt.
Claim 29
Dependent Claim 12 words
The composition of claim 26 in which said Fischer-Tropsch catalyst comprises iron.
Claim 30
Dependent Claim 35 words
The composition of claim 10 in which said silicoaluminophosphate comprises catalyst characterized by an adsorption of triethylamine of less than 5% by weight at a pressure of 2.6 torr and a temperature of 22° C.
Claim 31
Dependent Claim 36 words
The composition of claim 29 in which said silicoaluminophosphate comprises catalyst further characterized by an adsorption of cyclohexane of at least 2% by weight at a pressure of 90 torr and a temperature of 24° C.
Claim 32
Dependent Claim 15 words
The composition of claim 29 in which said zeolite Y compound is in aluminum-extracted form.
Claim 33
Dependent Claim 21 words
The composition of claim 29 in which said aluminia content of said aluminum-extracted zeolite is less than about 3 weight %.

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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-12-02 1989-06-03 1989-12-03 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-12-02 1993-06-03 1993-12-03 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-12-02 1997-06-03 1997-12-03 $7700.00 Window Closed / Lapsed

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