Blended gasolines and process for making same

Claim 2

A process for producing gasoline, comprising the steps of: a) blending liquid components comprising a low-weight hydrocarbon component, a natural gasoline component, and at least one octane-enhancing component, said octane-enhancing components having an (R+M)/2 of at least about 85 and a vapor pressure less than about 8 psia; and, b) withdrawing a vapor stream of light-weight hydrocarbons from said liquid components, whereby the vapor pressure of the resulting blended liquid product is lower than that of the original combined components.

Claim 3

The process of claim 1, wherein said blending step a) comprises an initial blending step wherein said low-weight hydrocarbon component is blended with said natural gasoline component to produce an intermediate blended product, said intermediate blended product subsequently being blended with said octane-enhancing component.

Claim 4

The process of claim 1, wherein said blending step a) comprises the agitation of said liquid components, whereby said vapor withdrawal step b) will be facilitated.

Claim 5

The process of claim 3, wherein said agitation step comprises the step of directing a stream of said liquid components against a solid object in an enclosure having a vapor space, said vapor stream being withdrawn from said vapor space.

Claim 6

The process of claim 4, wherein said agitation step comprises the step of pumping said liquid components to the top of a column, and directing a stream of said liquid components downwardly against a mechanical device within said column, said liquid components collecting in a bottom, liquid space portion of said column, said vapors flowing to an upper, vapor space portion of said column, said vapor stream being withdrawn from said vapor space portion of said column.

Claim 7

The process of claim 5, wherein said vapor stream of step b) is subjected to a liquid removal step comprising at least one of a coalescing or a condensation step, liquid product from said liquid removal step being returned to said blending step a).

Claim 8

The process of claim 6, wherein said coalescing step comprises passing said vapor stream through an enclosure having high surface area coalescing means.

Claim 9

The process of claim 7, wherein said liquid removal step comprises passing said vapor stream through a column containing packing.

Claim 10

The process of claim 1, wherein said process is performed as a batch operation.

Claim 11

The process of claim 9, wherein said process continues as a batch operation for between about 8 and about 12 hours.

Claim 12

The process of claim 1, wherein said process is performed at pressures of between about 0 and about 15 psig.

Claim 13

The process of claim 1, wherein vapors removed from said vapor withdrawal step b) are passed through a power generating station, said vapors being combusted by power-generating means to generate power to run said process.

Claim 14

The process of claim 1, wherein liquid product from said blending step a) is passed to intermediate storage tanks, liquid from said storage tanks being returned to said blending step a) through a continuous recycling process.

Claim 15

The process of claim 1, wherein said blending step a) continues until the composition of said liquid comprises between about 10 and about 35 volume percent low-weight hydrocarbons, between about 30 and about 60 volume percent natural gasoline, and between about 20 and about 40 volume percent octane-enhancing components.

Claim 16

The process of claim 1, wherein said process produces a winter, low-octane gasoline, said process continuing until the composition of said product comprises between about 25 and about 35 volume percent low-weight hydrocarbons, between about 40 and about 50 volume percent natural gasoline, and between about 20 and about 30 volume percent octane-enhancing components.

Claim 17

The process of claim 1, said process producing a winter, high-octane gasoline, said process continuing until said liquid composition comprises between about 25 and about 35 volume percent low-weight hydrocarbons, between about 30 and about 40 volume percent natural gasoline, and between about 30 and about 40 volume percent octane-enhancing components.

Claim 18

The process of claim 1, said process producing a summer, low-octane gasoline, said process continuing until said liquid composition comprises between about 10 and about 15 volume percent low-weight hydrocarbons, between about 50 and about 60 volume percent natural gasoline, and between about 20 and about 30 volume percent octane-enhancing components.

Claim 19

The process of claim 1, wherein said process produces a summer, high-octane gasoline, said process continuing until said liquid composition comprises between about 10 and about 15 volume percent low-weight hydrocarbons, between about 45 and about 55 volume percent natural gasoline, and between about 30 and about 40 volume percent octane-enhancing components.

Claim 20

The process of claim 1, wherein said octane-enhancing components are selected from the group consisting of toluene, methyl tertiary butyl ether, ethylbenzene, m-xylene, p-xylene, o-xylene, eight carbon aromatic mixtures, nine carbon aromatic mixtures, isopropylbenzene, n-propylbenzene, alkylates, catalytic cracked naptha, catalytic reformate, and pyrolysis gasoline.

Claim 21

The process of claim 1, wherein said octane-enhancing component is toluene.

Claim 22

A process for producing gasoline, comprising the steps of: a) blending liquid components comprising a low-weight hydrocarbon component and a natural gasoline component in about a 1:3 volume ratio, respectively, and an octane-enhancing component in about a 1:3 volume ratio to both of said low-weight hydrocarbon component and said natural gasoline component; b) agitating said liquid components of step a) by directing a stream of said liquid components against a mechanical device in an enclosure having a vapor space substantially above said mechanical device and a liquid space substantially below said mechanical device, said liquid components collecting in a bottom, liquid space portion of said enclosure, vapors accumulating in said vapor space portion of said enclosure, as vapor stream being withdrawn from said vapor space portion of said enclosure; c) a liquid removal step in which low-weight hydrocarbons present in said vapor stream are removed and returned to said blending step a), said liquid removal step further producing a light-weight hydrocarbon vapor product; d) said light-weight hydrocarbon vapor product of said liquid removal step c) being burned to generate power, said power being utilized to provide energy for said agitation step b); and, e) said process continuing until said liquid components have a composition of between about 10 and about 35 volume percent low-weight hydrocarbons, between about 30 and about 60 volume percent natural gasoline, and between about 20 and about 40 volume percent octane-enhancing components.

Claim 23

A process for producing gasoline, comprising the steps of: a) blending liquid components comprising a low-weight hydrocarbon component and a natural gasoline component in about a 1:3 volume ratio, respectively, and an octane-enhancing component in about a 1:3 volume ratio to both of said low-weight hydrocarbon component and said natural gasoline component; b) agitating said liquid components of step a) by directing a stream of said liquid components against a mechanical device in an enclosure having a vapor space substantially above said mechanical device and a liquid space substantially below said mechanical device, said liquid components collecting in a bottom, liquid space portion of said enclosure, vapors accumulating in said vapor space portion of said enclosure, as vapor stream being withdrawn from said vapor space portion of said enclosure; c) a liquid removal step in which low-weight hydrocarbons present in said vapor stream are removed and returned to said blending step a), said liquid removal step further producing a light-weight hydrocarbon vapor product; d) said light-weight hydrocarbon vapor product of said liquid removal step c) being burned to generate power, said power being utilized to provide energy for said agitation step b); and, e) said process continuing until said liquid components have a composition of between about 10 and about 35 volume percent low-weight hydrocarbons, between about 30 and about 60 volume percent natural gasoline, and between about 20 and about 40 volume percent octane-enhancing components.

Claim 24

The process of claim 21, wherein said liquid removal step comprises at least one of a condensation step and a coalescing step.

Claim 25

The process of claim 21, wherein said octane-enhancing components are selected from the group consisting of methyl tertiary butyl ether, ethylbenzene, m-xylene, p-xylene, o-xylene, eight carbon aromatic mixtures, nine carbon aromatic mixtures, isopropylbenzene, n-propylbenzene, alkylates, catalytic cracked naptha, catalytic reformate, and pyrolysis gasoline.

Claim 26

The process of claim 21, wherein said octane-enhancing component is toluene.