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US 4,382,843 AGranted
Method for producing gasoline-alcohol fuels
AssigneeSimulation Sciences, Inc.
InventorCline Black
Life of this patent
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Abstract
A process for producing gasoline-ethanol blends comprises purifying dilute ethanol by extractive distillation and concentrating the ethanol by distillation followed by one or both of the following steps: (a) liquid extraction of ethanol into heated gasoline or (b) azeotropic distillation of ethanol with an entrainer followed by blending with gasoline.
Claims10
A method of preparing a gasoline-ethanol blend suitable as a fuel for internal combustion engines comprising:
- (a) passing a feed consisting of a dilute aqueous ethanol solution to a distillation zone;
- (b) heating said dilute aqueous ethanol solution in said distillation zone and recovering, as a top product, concentrated aqueous ethanol containing about 45 to 89 percent m ethanol, and heated water as a bottom product;
- (c) passing a gasoline feed to a heating zone where it is heated;
- (d) introducing said concentrated aqueous ethanol and heated gasoline into a mixing zone to form a gasoline-ethanol-water mixture having a temperature of about 60.degree. to 110.degree. C.;
- (e) passing said heated gasoline-ethanol-water mixture to a first separation zone wherein the mixture separates into a first upper gasoline-ethanol phase and a first lower aqueous phase containing some ethanol;
- (f) passing said gasoline-ethanol phase through a cooling zone wherein the temperature is lowered to the minimum temperature under which the gasoline-ethanol is to be used as a fuel and into a second separation zone maintained at said minimum temperature wherein said mixture separates into a second upper gasoline-ethanol phase and a second lower aqueous phase;
- and
- (g) withdrawing said second gasoline-ethanol phase from said second separation zone as a final gasoline-ethanol fuel blend.
5 more elements
A method of preparing a gasoline-ethanol blend suitable as a fuel for internal combustion engines comprising:
- (a) passing a feed consisting of a dilute aqueous ethanol solution to a distillation zone;
- (b) heating said dilute aqueous ethanol solution in said distillation zone and recovering from said zone a top product consisting of about 75 to 89 percent m ethanol, a side draw product consisting of about 45 to 80 percent m ethanol and heated water as a bottom product;
- (c) passing said top product into an azeotropic distillation zone containing an entrainer selected from the group consisting of n-pentane and a heart cut gasoline and azeotropically distilling said product with said entrainer to remove overhead a mixture consisting of entrainer, ethanol and water and a bottom product of dry ethanol;
- (d) allowing said mixture to phase separate into an entrainer phase and an aqueous ethanol phase and recycling the entrainer phase back to the azeotropic distillation zone and the aqueous phase back to the distillation zone;
- (e) passing a gasoline feed to a heating zone where it is heated;
- (f) introducing the side draw ethanol product from the distillation zone and heated gasoline into a mixing zone to form a gasoline-ethanol-water mixture having a temperature of about 60.degree. to 110.degree. C.;
- (g) passing said heated gasoline-ethanol water mixture to a first separation zone wherein the mixture separates into a first upper gasoline-ethanol phase and a first lower aqueous phase containing some ethanol;
- (h) passing said gasoline-ethanol phase through a cooling zone wherein the temperature is lowered to the minimum temperature under which the gasoline-ethanol is to be used as a fuel and into a second separation zone maintained at said minimum temperature wherein said mixture separates into a second upper gasoline-ethanol phase and a second lower aqueous phase, and
- (i) withdrawing said second gasoline-ethanol phase from said second separation zone and blending a measured amount of said second gasoline-ethanol phase with a measured amount of dry ethanol from said azeotropic distillation zone to form a final gasoline-ethanol fuel blend.
6 more elements
Dependencies are inferred from the claim text.