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US4046520A Expired / Lapsed US ⏱️ 0.0 years remaining

Gasoline production

Assignee: Chevron USA Inc
•
Filing: 1975-06-09
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Granted: 1977-09-06
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Expires: 1995-06-09
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Abstract

Abstract A process for producing a high-octane gasoline having reduced smog-forming tendencies, which comprises: A. thermally dehydrogenating-cracking isobutane to obtain propylene and isobutene; B. hydrating propylene to obtain isopropanol; C. etherating the isopropanol with the isobutene to obtain t-butyl isopropyl ether; and D. blending the t-butyl isopropyl ether with gasoline-boiling-range hydrocarbons. Preferably the thermal dehydrogenation is carried out under conditions, specifically including a temperature between about 1125° and 1275° F., to produce a molar ratio of isobutene to propylene between 1.0 and 1.25.

Inventors

  • 👤 Jacob D. Kemp
  • 👤 Robert P. Sieg

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 14:12
CPC Classifications
C; C10; C10L; C10L1/00; C10L1/02; C10L1/023

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 85 words
In a process for producing a high-octane gasoline by blending a hydrocarbon mixture of the gasoline range with an ether, the improvement which comprises: a. thermally dehydrogenating-cracking isobutane to obtain a mixture of propylene and isobutene; b. separating the mixture into an isobutene-rich stream and a propylene-rich stream; c. hydrating with a solid acidic hydration catalyst the propylene-rich stream to obtain isopropanol; d. etherating the isopropanol with the isobutene-rich stream to obtain t-butyl isopropyl ether; and e. blending the t-butyl isopropyl ether with gasoline-boiling-range hydrocarbons.
Claim 2
Dependent Claim 85 words
In a process for producing a high-octane gasoline by blending a hydrocarbon mixture of the gasoline range with an ether, the improvement which comprises: a. thermally dehydrogenating-cracking isobutane to obtain a mixture of propylene and isobutene; b. separating the mixture into an isobutene-rich stream and a propylene-rich stream; c. hydrating with a solid acidic hydration catalyst the propylene-rich stream to obtain isopropanol; d. etherating the isopropanol with the isobutene-rich stream to obtain t-butyl isopropyl ether; and e. blending the t-butyl isopropyl ether with gasoline-boiling-range hydrocarbons.

References Cited (Backward Citations)

US2816150A Cited
US2848522A Cited
US2813908A Cited
US2861045A Cited
US2891999A Cited
US2803667A Cited
US3224848A Cited
US3285977A Cited
US3482952A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-09-05 1981-03-07 1981-09-06 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-09-05 1985-03-07 1985-09-06 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-09-05 1989-03-07 1989-09-06 $7700.00 Window Closed / Lapsed

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