Dehydration of ethanol

Claim 2

A process for dehydrating ethanol to more than 199 proof which comprises: passing liquid phase ethanol through a desiccant bed adapted to dehydrate 190 proof ethanol to more than 199 proof ethanol until said desiccant bed is substantially fully saturated with adsorbed water and regenerating the desiccant bed for renewed adsorption use according to the following procedure: heating the bed by indirect heat exchange to above about 212° F. to thereby vaporize absorbed and adsorbed ethanol and water from the bed thereafter; applying sub-atmospheric pressures to the heated bed, desorbing in vapor phase thereby substantial additional proportions of liquid from the bed, and then cooling the bed by indirect heat exchange to temperature levels suited to adsorption service and releasing the sub-atmospheric pressures thereon.

Claim 3

The process of claim 1 including applying an inert gas sweep at about atmospheric pressure levels just prior to regeneration to drain liquid phase ethanol from the bed.

Claim 4

The process of claim 1 wherein the maximum regeneration temperature is in the range of 325° F.-375° F.

Claim 5

In a process for dehydration of ethanol from an ethanol-water mixture by alternatively adsorbing the water from liquid phase ethanol-water stream in one of at least two adsorbent beds arranged for alternatively shifting between cycles of adsorption and desorption, the improvement which comprises regenerating the adsorbent bed by desorbing absorbed and adsorbed water and ethanol by vaporizing same at temperatures exceeding 212° F. through indirect heat exchange from a heating means in the adsorbent bed, and thereafter subjecting the adsorbent bed to sub-atmospheric pressures during final stages of the regeneration thereby sweeping volatilized vapors from the bed, followed by cooling the adsorbent bed by indirect heat exchange with cooling means disposed inside the adsorbent bed.

Claim 6

In a process for dehydration of ethanol from an ethanol-water mixture by alternatively adsorbing the water from liquid phase ethanol-water stream in one of at least two adsorbent beds arranged for alternatively shifting between cycles of adsorption and desorption, the improvement which comprises regenerating the adsorbent bed by desorbing absorbed and adsorbed water and ethanol by vaporizing same at temperatures exceeding 212° F. through indirect heat exchange from a heating means in the adsorbent bed, and thereafter subjecting the adsorbent bed to sub-atmospheric pressures during final stages of the regeneration thereby sweeping volatilized vapors from the bed, followed by cooling the adsorbent bed by indirect heat exchange with cooling means disposed inside the adsorbent bed.

Claim 7

The process of claim 4 which further comprises passing a stream of inert sweep gas through the adsorbent bed during the sub-atmospheric final stages.

Claim 8

The process of claim 4 including condensing the desorbed vapors at from 35°-100° F. to thereby recover the desorbed ethanol.

Claim 9

An ethanol dehydration system which comprises an adsorber unit made up of at least two adsorber vessels that alternatively operate through cycles of adsorption and desorption; each adsorber vessel containing therein a bed of particulate adsorbent and heat exchange means inside said bed adapted to heat and to cool said bed; means for passing liquid phase ethanol through an adsorber vessel of said adsorber unit during an adsorption cycle to adsorb the water content of the ethanol onto the particulate adsorbent therein; means for connecting into the hereinafter defined sub-atmospheric pressure inert sweep gas loop an adsorber vessel of said adsorption unit during only the final stages of a desorption cycle to remove vapors evolved from the adsorbent bed therein being regenerated; means for passing a heating fluid through the heat exchange means in an adsorber vessel from the beginning of the desorption cycle until liquid previously absorbed and adsorbed by the adsorbent bed has been volatilized therefrom thereby regenerating the bed; a condenser connected to the adsorber vessel undergoing desorption to which the volatilized vapors pass; means for passing a cooling fluid through the heat exchange means in an adsorber vessel after regeneration of the bed has been completed; a sub-atmospheric pressure gas loop for inert sweep gas including one of said adsorber vessels, said condenser, a liquid removing means to remove condensate and a compressor, said gas loop serving to circulate sweep gas from the adsorption unit in the final stages of a desorption cycle successively through condenser, liquid removing means, and compressor, then back to the adsorption unit.

Claim 10

An ethanol dehydration system which comprises an adsorber unit made up of at least two adsorber vessels that alternatively operate through cycles of adsorption and desorption; each adsorber vessel containing therein a bed of particulate adsorbent and heat exchange means inside said bed adapted to heat and to cool said bed; means for passing liquid phase ethanol through an adsorber vessel of said adsorber unit during an adsorption cycle to adsorb the water content of the ethanol onto the particulate adsorbent therein; means for connecting into the hereinafter defined sub-atmospheric pressure inert sweep gas loop an adsorber vessel of said adsorption unit during only the final stages of a desorption cycle to remove vapors evolved from the adsorbent bed therein being regenerated; means for passing a heating fluid through the heat exchange means in an adsorber vessel from the beginning of the desorption cycle until liquid previously absorbed and adsorbed by the adsorbent bed has been volatilized therefrom thereby regenerating the bed; a condenser connected to the adsorber vessel undergoing desorption to which the volatilized vapors pass; means for passing a cooling fluid through the heat exchange means in an adsorber vessel after regeneration of the bed has been completed; a sub-atmospheric pressure gas loop for inert sweep gas including one of said adsorber vessels, said condenser, a liquid removing means to remove condensate and a compressor, said gas loop serving to circulate sweep gas from the adsorption unit in the final stages of a desorption cycle successively through condenser, liquid removing means, and compressor, then back to the adsorption unit.

Claim 11

The ethanol dehydration of claim 7 including vacuum pump means disposed in the gas loop between said condenser and compressor adapted to be introduced selectively into the gas loop to apply sub-atmospheric pressures to the adsorber bed undergoing the final stages of the desorption cycle.