Direct process for the production of gasohol from fermentation mixtures

Claim 2

A process for the direct preparation of gasohol from a low-content alcohol-containing solution from a fermentation broth, which process comprises: (a) mixing in a liquid-liquid extraction process a fermentation broth containing a methanol- or ethanol-water solution, the broth containing up to about 12% by volume of the methanol or ethanol, a gasoline composition and a small amount of up to about 30%, based on the alcohol content of the water-alcohol solution, of a solvent for the methanol or ethanol and miscible in the gasoline; (b) removing from the extraction process an essentially alcohol-free water; (c) removing a gasohol composition containing water of saturation, which composition contains from up to about 15% by volume of combined alcohol; (d) removing at least some of the water of saturation from the gasohol composition; and (e) recovering a substantially anhydrous gasohol.

Claim 3

The process of claim 1 wherein the solvent comprises from about 0.5% to 3% by weight of the gasoline of a C 3 to C 6 aliphatic alcohol.

Claim 4

The process of claim 2 wherein the organic alcohol is selected from the group consisting of isopropyl alcohol, butyl alcohol, amyl alcohol, hexanol and combinations thereof.

Claim 5

The process of claim 1 wherein the water of saturation is removed by employing water adsorbents.

Claim 6

The process of claim 1 wherein the water of saturation is removed by chilling the gasohol composition to a low temperature to reduce the solubility of the water of saturation and, thereafter, removing the water of saturation.

Claim 7

The process of claim 5 wherein the water of saturation is removed by decanting the water of saturation from the chilled gasohol composition.

Claim 8

The process of claim 5 which includes chilling the gasohol composition containing the water of saturation to a temperature of less than about -30° F. and, thereafter, decanting the insoluble water of saturation.

Claim 9

The process of claim 1 wherein the gasoline composition comprises an unblended, naphtha-type, straight-run gasoline composition.

Claim 10

The process of claim 1 wherein the anhydrous gasohol comprises from about 85% to 93% by weight gasoline and 7% to 15% by weight of combined alcohol.

Claim 11

The process of claim 1 which includes the step of extracting butanol or amyl alcohol from a butyl or amyl-alcohol-containing fermentation broth employing gasoline and, thereafter, employing the butyl or amyl-alcohol-gasoline-extracted solution to extract the methanol or ethanol from the water-alcohol solution.

Claim 12

The substantially anhydrous gasohol produced by the process of claim 1.

Claim 13

A process for the direct preparation of substantially anhydrous gasohol suitable for use in an internal-combustion engine from a fermentation broth containing methanol or ethanol, which process comprises: (a) extracting in a liquid-liquid extraction process, from a methanol- or ethanol-containing fermentation broth, a methanol or ethanol from the broth employing as a solvent extractant an unblended, naphtha, straight-run gasoline composition in the presence of from about 0.1% to 5% by weight of a C 3 to C 6 alcohol to increase the solubility of the methanol or ethanol in the gasoline composition; (b) recovering a gasohol composition which comprises from about 85% to 93% gasoline and from about 7% to 15% of combined alcohol and contains water of saturation; (c) reducing the temperature of the extracted gasohol composition to approximately -10° F. or below to render insoluble in such solution at least part of the water of saturation present therein; and (d) removing the water of saturation to provide a substantially anhydrous gasohol.

Claim 14

A process for the direct preparation of substantially anhydrous gasohol suitable for use in an internal-combustion engine from a fermentation broth containing methanol or ethanol, which process comprises: (a) extracting in a liquid-liquid extraction process, from a methanol- or ethanol-containing fermentation broth, a methanol or ethanol from the broth employing as a solvent extractant an unblended, naphtha, straight-run gasoline composition in the presence of from about 0.1% to 5% by weight of a C 3 to C 6 alcohol to increase the solubility of the methanol or ethanol in the gasoline composition; (b) recovering a gasohol composition which comprises from about 85% to 93% gasoline and from about 7% to 15% of combined alcohol and contains water of saturation; (c) reducing the temperature of the extracted gasohol composition to approximately -10° F. or below to render insoluble in such solution at least part of the water of saturation present therein; and (d) removing the water of saturation to provide a substantially anhydrous gasohol.

Claim 15

The substantially anhydrous gasohol produced by the process of claim 12.

Claim 16

The process of claim 1 which includes admixing the alcohol solvent with the alcohol-containing fermentation broth prior to mixing the fermentation broth with the gasoline composition.

Claim 17

The process of claim 1 which includes mixing the fermentation broth, the solvent and the gasoline composition in a liquid-liquid extraction column, wherein the fermentation broth is introduced as the heavy phase and the gasoline composition is introduced as the light phase, and wherein the solvent is in either phase.

Claim 18

A process for the direct preparation of substantially anhydrous gasohol from a fermentation broth containing ethanol or methanol, which process comprises: (a) introducing the aqueous fermentation broth, containing the ethanol or methanol as the heavy phase, in a liquid-liquid extraction column; (b) introducing a gasoline composition, into which gasoline composition it is desired to introduce alcohol to form a gasohol as the light phase in the liquid-liquid extraction column; (c) introducing into the light- or heavy-phase composition a solvent for the ethanol or methanol, and which solvent is also miscible in the gasoline composition; (d) admixing the broth, gasoline composition and solvent in a series of stages in the extraction column; (e) withdrawing from the extraction column a gasohol composition which comprises the gasoline composition, the solvent, the ethanol or methanol of the fermentation broth and water of saturation; (f) withdrawing from the extraction column an essentially methanol- or ethanol-free, aqueous, fermentation broth; (g) removing at least some of the water of saturation from the gasohol composition; and (h) recovering a substantially anhydrous gasohol.

Claim 19

A process for the direct preparation of substantially anhydrous gasohol from a fermentation broth containing ethanol or methanol, which process comprises: (a) introducing the aqueous fermentation broth, containing the ethanol or methanol as the heavy phase, in a liquid-liquid extraction column; (b) introducing a gasoline composition, into which gasoline composition it is desired to introduce alcohol to form a gasohol as the light phase in the liquid-liquid extraction column; (c) introducing into the light- or heavy-phase composition a solvent for the ethanol or methanol, and which solvent is also miscible in the gasoline composition; (d) admixing the broth, gasoline composition and solvent in a series of stages in the extraction column; (e) withdrawing from the extraction column a gasohol composition which comprises the gasoline composition, the solvent, the ethanol or methanol of the fermentation broth and water of saturation; (f) withdrawing from the extraction column an essentially methanol- or ethanol-free, aqueous, fermentation broth; (g) removing at least some of the water of saturation from the gasohol composition; and (h) recovering a substantially anhydrous gasohol.

Claim 20

The process of claim 16 wherein the solvent comprises a C 3 to C 6 , volatile, low-molecular-weight alcohol.

Claim 21

The process of claim 17 wherein the anhydrous gasohol comprises from about 8% to 15% by volume of combined alcohol.

Claim 22

The process of claim 16 which includes reducing the temperature of the gasohol composition to -10° F. or lower, to reduce the solubility of the water of saturation, and recanting from the low-temperature gasohol composition the separated water of saturation.

Claim 23

The process of claim 16 wherein the solvent comprises from about 0.1% to 5.0% by weight of the gasoline composition.

Claim 24

The process of claim 16 wherein the liquid-liquid extraction column contains a plurality of sieve plates.

Claim 25

The anhydrous gasohol produced by the process of claim 16.