US4429173A — Production of high-octane, unleaded motor fuel by…

Claim 1

Independent Claim 199 words

A process for production of high-octane alkylate comprising: (a) introducing an isoparaffin selected from the group consisting of isobutane, isopentane, and mixtures thereof, with olefins consisting essentially of amylenes and an HF catalyst into an alkylation reaction zone; (b) reacting the materials so introduced into said alkylation reaction zone to form an effluent comprising an alkylate; (c) separating said effluent into an HF catalyst phase and a hydrocarbon phase; (d) passing said hydrocarbon phase into a first fractionation zone; (e) withdrawing said alkylate from said first fractionation zone as a liquid; (f) withdrawing a first stream comprising isopentane and a second stream comprising isobutane when present from separate leads or trays of said first fractionation zone; (g) recycling at least a portion of said first stream to a dehydrogenation zone in which said portion of said first stream and an isopentane containing feedstream are at least partially dehydrogenated to form the amylenes to be alkylated in said alkylation reaction zone; (h) recycling said second stream comprising isobutane when present to a feed conduit to form at least a portion of the isobutane reacted in said alkylation reaction zone; and (i) recovering said alkylate as the product of the process.

Claim 2

Dependent Claim 199 words

A process for production of high-octane alkylate comprising: (a) introducing an isoparaffin selected from the group consisting of isobutane, isopentane, and mixtures thereof, with olefins consisting essentially of amylenes and an HF catalyst into an alkylation reaction zone; (b) reacting the materials so introduced into said alkylation reaction zone to form an effluent comprising an alkylate; (c) separating said effluent into an HF catalyst phase and a hydrocarbon phase; (d) passing said hydrocarbon phase into a first fractionation zone; (e) withdrawing said alkylate from said first fractionation zone as a liquid; (f) withdrawing a first stream comprising isopentane and a second stream comprising isobutane when present from separate leads or trays of said first fractionation zone; (g) recycling at least a portion of said first stream to a dehydrogenation zone in which said portion of said first stream and an isopentane containing feedstream are at least partially dehydrogenated to form the amylenes to be alkylated in said alkylation reaction zone; (h) recycling said second stream comprising isobutane when present to a feed conduit to form at least a portion of the isobutane reacted in said alkylation reaction zone; and (i) recovering said alkylate as the product of the process.

Claim 3

Dependent Claim 33 words

A process in accordance with claim 1, wherein said alkylate is split in a second fractionation zone into a third stream of high octane gasoline and a fourth stream of higher boiling hydrocarbons.

Claim 4

Dependent Claim 57 words

A process in accordance with claim 1, wherein said alkylate is a mixture of branched hydrocarbons having at least 6 carbon atoms per molecule, a research octane rating of at least about 91, a Reid vapor pressure of less than about 11 psia, and wherein about 1.8 volumes of alkylate are produced per unit volume of isopentane.

Claim 5

Dependent Claim 75 words

A process in accordance with claim 2, wherein said third stream is a high octane gasoline comprising a mixture of branched hydrocarbons having six to eight carbon atoms per molecule, a research octane rating of at least about 100, and a Reid vapor pressure of less than about 2 psia, and wherein said fourth stream is a mixture of branched and normal hydrocarbons having at least eight carbon atoms per molecule suitable as a solvent.

Claim 6

Dependent Claim 21 words

A process in accordance with claim 2, wherein a fifth stream is drawn from said first fractionation zone, comprising normal butane.

Claim 7

Dependent Claim 35 words

A process in accordance with claims 1, 2, 3 or 4, wherein said alkylate is blended with butane to produce a high octane unleaded gasoline having a Reid vapor pressure less than about 11 psia.

Claim 8

Dependent Claim 19 words

A process in accordance with claim 6, wherein said butane comprises butane from the fifth stream of claim 5.

Claim 9

Dependent Claim 24 words

A process in accordance with claims 1, 2 or 5, wherein said high octane alkylate is produced without substantial production of more volatile by-products.

Claim 10

Independent Claim 165 words

A method for producing isopentane-free high octane HF alkylate wherein the fresh feed streams are an isobutane feed stream and an isopentane feed stream, and the recycled streams are an isobutane recycle stream and an isopentane recycle stream comprising steps of: (a) dehydrogenating at least a portion of said isopentane feed stream and a portion of said isopentane recycle stream to produce isopentenes, yielding an isopentenes-isopentane-containing stream; (b) admixing said isopentenes-containing stream from (a) with said isobutane feed stream and said isobutane recycle stream and passing this admixture to an HF alkylation zone wherein at least a portion of the isobutane in said admixture, and at least a portion of the isopentane in said admixture are alkylated in the presence of liquid HF catalyst with the isopentenes in said admixture to produce a hydrocarbon stream comprising unreacted isobutane, unreacted isopentane, and alkylate; (c) fractionating said hydrocarbon stream to yield separately said recycle isobutane stream, said recycle isopentane stream, and said isopentane-free high octane HF alkylate.

Claim 11

Independent Claim 165 words

A method for producing isopentane-free high octane HF alkylate wherein the fresh feed streams are an isobutane feed stream and an isopentane feed stream, and the recycled streams are an isobutane recycle stream and an isopentane recycle stream comprising steps of: (a) dehydrogenating at least a portion of said isopentane feed stream and a portion of said isopentane recycle stream to produce isopentenes, yielding an isopentenes-isopentane-containing stream; (b) admixing said isopentenes-containing stream from (a) with said isobutane feed stream and said isobutane recycle stream and passing this admixture to an HF alkylation zone wherein at least a portion of the isobutane in said admixture, and at least a portion of the isopentane in said admixture are alkylated in the presence of liquid HF catalyst with the isopentenes in said admixture to produce a hydrocarbon stream comprising unreacted isobutane, unreacted isopentane, and alkylate; (c) fractionating said hydrocarbon stream to yield separately said recycle isobutane stream, said recycle isopentane stream, and said isopentane-free high octane HF alkylate.

Claim 12

Dependent Claim 27 words

The method according to claim 9 wherein said isopentane-free high octane HF alkylate is further upgraded in octane value by fractionation to remove higher boiling hydrocarbon components.

Claim 13

Dependent Claim 19 words

A process in accordance with claim 1 wherein said amylenes are produced by dehydrogenation of said isopentane-containing feed stream.

Claim 14

Dependent Claim 142 words

A process for production of high octane alkylate comprising the steps of: (a) dehydrogenating a stream comprising isopentane to produce a stream comprising amylenes; (b) introducing a stream comprising isobutane and said stream comprising amylenes produced by dehydrogenation of isopentane into a reaction zone with an HF catalyst; (c) reacting the materials of (b) so introduced into said reaction zone to form an effluent comprising an HF catalyst, alkylate, isobutane, normal butane, and isopentane; (d) separating said effluent into an HF catalyst phase and a hydrocarbon phase; (e) recovering isopentane from said hydrocarbon phase; (f) recovering normal butane from said hydrocarbon phase; (g) recovering isobutane from said hydrocarbon phase; (h) recovering said alkylate as a product from said hydrocarbon phase; and (i) recycling said isopentane of (e) to said dehydrogenation of (a) as at least a portion of said isopentane of (a).

Claim 15

Dependent Claim 142 words

A process for production of high octane alkylate comprising the steps of: (a) dehydrogenating a stream comprising isopentane to produce a stream comprising amylenes; (b) introducing a stream comprising isobutane and said stream comprising amylenes produced by dehydrogenation of isopentane into a reaction zone with an HF catalyst; (c) reacting the materials of (b) so introduced into said reaction zone to form an effluent comprising an HF catalyst, alkylate, isobutane, normal butane, and isopentane; (d) separating said effluent into an HF catalyst phase and a hydrocarbon phase; (e) recovering isopentane from said hydrocarbon phase; (f) recovering normal butane from said hydrocarbon phase; (g) recovering isobutane from said hydrocarbon phase; (h) recovering said alkylate as a product from said hydrocarbon phase; and (i) recycling said isopentane of (e) to said dehydrogenation of (a) as at least a portion of said isopentane of (a).

Annuity Stage	Window Opens	Payment Deadline	Surcharge Period Until	Estimated Fee	Status
3.5 Years (Year 4)	1987-01-30	1987-08-01	1988-01-31	$2000.00	Window Closed / Lapsed
7.5 Years (Year 8)	1991-01-30	1991-08-01	1992-01-31	$3760.00	Window Closed / Lapsed
11.5 Years (Year 12)	1995-01-30	1995-08-01	1996-01-31	$7700.00	Window Closed / Lapsed

Production of high-octane, unleaded motor fuel by alkylation of isobutane with isoamylenes obtained by dehydrogenation of isopentane

Abstract

Inventors

Bibliographic Details

Claims Analysis

References Cited (Backward Citations)

USPTO Annuity & Maintenance Windows

Assigned Categories & Tags

Assign Category Tag