← Back to Patent Explorer
US4270929A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing gasoline of high octane number, in particular lead-free gasoline

Assignee: IFP Energies nouvelles
•
Filing: 1979-08-31
•
Granted: 1981-06-02
•
Expires: 1999-08-31
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract Process for producing gasoline of high octane number from C3 and C4 olefinic cuts, such as those obtained by fractional distillation of a C3 / C4 catalytic cracking cut, comprising the steps of: (a) oligomerizing propylene of the C3 cut to obtain a first gasoline fraction, (b) reacting the isobutene of the C4 cut with methanol to produce methyl tert.-butyl ether which is separated from the unreacted C4 hydrocarbons to form a second gasoline fraction, (c) alkylating said unreacted C4 hydrocarbons with isobutane in the presence of an alkylation catalyst such as hydrofluoric acid, to form a third gasoline fraction, and (d) admixing, at least partially, said first, second and third gasoline fractions, so as to obtain gasoline of high octane number.

Inventors

  • 👤 Quang Dang Vu
  • 👤 Yves Chauvin
  • 👤 Jean Gaillard
  • 👤 Bernard Torck
  • 👤 Michel Hellin

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 05:21
CPC Classifications
C; C07; C07C; C07C2/00; C07C2/02; C07C2/04; C07C2/06; C07C2/08; C07C2/26; C07C2/30; C10; C10L; C10L1/00; C10L1/02; C10L1/023; C07C2527/00; C07C2527/06; C07C2527/08; C07C2527/12; C07C2527/1206; C07C2531/00; C07C2531/02; C07C2531/12; C07C2531/14; Y; Y02; Y02P; Y02P30/00; Y02P30/20

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 157 words
A process for producing a blended high octane gasoline, comprising the steps of: (a) oligomerizing an olefinic C 3 cut comprising propylene, and recovering an oligomerizate boiling in the gasoline range; (b) contacting a mixture of methanol and an olefinic C 4 cut comprising isobutene, isobutane and at least one n-butene with an acid catalyst under isobutene etherification conditions to produce methyl tert.-butyl ether and unreacted C 4 hydrocarbons; (c) fractionating the effluent from step (b) and separately recovering a methyl tert.-butyl ether fraction and an unreacted C 4 hydrocarbon fraction comprising said at least one n-butene; (d) subjecting the unreacted C 4 hydrocarbon fraction from step (c) to aliphatic alkylation conditions, and recovering an alkylate boiling in the gasoline range; and (e) blending at least a portion of said oligomerizate with at least a portion of said methyl tert.-butyl ether fraction and at least a portion of said alkylate, and recovering a blended high octane gasoline.
Claim 2
Dependent Claim 157 words
A process for producing a blended high octane gasoline, comprising the steps of: (a) oligomerizing an olefinic C 3 cut comprising propylene, and recovering an oligomerizate boiling in the gasoline range; (b) contacting a mixture of methanol and an olefinic C 4 cut comprising isobutene, isobutane and at least one n-butene with an acid catalyst under isobutene etherification conditions to produce methyl tert.-butyl ether and unreacted C 4 hydrocarbons; (c) fractionating the effluent from step (b) and separately recovering a methyl tert.-butyl ether fraction and an unreacted C 4 hydrocarbon fraction comprising said at least one n-butene; (d) subjecting the unreacted C 4 hydrocarbon fraction from step (c) to aliphatic alkylation conditions, and recovering an alkylate boiling in the gasoline range; and (e) blending at least a portion of said oligomerizate with at least a portion of said methyl tert.-butyl ether fraction and at least a portion of said alkylate, and recovering a blended high octane gasoline.
Claim 3
Dependent Claim 39 words
A process according to claim 1 wherein the C 3 cut used in step (a) and the C 4 cut used in step (b) are each produced by fractional distillation of a C 3 /C 4 catalytic cracking cut.
Claim 4
Dependent Claim 34 words
A process according to claim 1, wherein the oligomerization in step (a) is effected in the presence of a catalyst obtained by contacting a group IV to VIII metal compound with an alkylaluminum compound.
Claim 5
Dependent Claim 22 words
A process according to claim 3, wherein the alkylaluminum compound is a hydrocarbylaluminum halide and the metal compound is a nickel compound.
Claim 6
Dependent Claim 26 words
A process according to claim 1, wherein the etherification reaction between the C 4 cut and methanol is effected in the presence of a sulfonated resin.
Claim 7
Dependent Claim 20 words
A process according to claim 1, wherein the alkylation in step (d) is effected in the presence of hydrofluoric acid.
Claim 8
Dependent Claim 44 words
A process according to claim 1, wherein the isobutane/C 4 olefins ratio in the unreacted C 4 hydrocarbon fraction from step (c) is lower than 1, and isobutane is added to increase this ratio to at least 1 in the feed to step (d).
Claim 9
Dependent Claim 37 words
A process according to claim 2, wherein said C 3 /C 4 catalytic cracking cut has the following composition, by weight: ______________________________________ propylene 15-35% isobutane 15-30% isobutene 5-15% 1-butene 3-10% 2-butenes 10-25% propane + n-butane 8-30% ______________________________________
Claim 10
Dependent Claim 45 words
A process according to claim 1, wherein the C 3 art used in step (a) and the C 4 cut used in step (b) have the following respective compositions, by weight: ______________________________________ C.sub.3 cut C.sub.4 cut ______________________________________ propane:15-50% n-butane:5-20% propylene:50-85% isobutane:20-50% isobutene:10-25% 1-butene:5-15% 2-butene:10-40% ______________________________________

References Cited (Backward Citations)

US2403869A Cited
US3912463A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-06-01 1984-12-01 1985-06-02 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-06-01 1988-12-01 1989-06-02 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-06-01 1992-12-01 1993-06-02 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag