US 4,381,220 AGranted

Production of concentrated alcohol and distillery slop

AssigneeResources Conservation, Inc.

InventorFerris C. Standiford

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Abstract

Concentrated alcohol and distillery slop are produced from fermented beer with a reduced amount of energy by employing a vapor recompression distillery slop evaporator in which evaporator vapors are used to strip alcohol from the fermented liquor before they are returned as the heat source for evaporation. Vents in the evaporator permit passage of uncondensed vapors used to drive the evaporator to a rectifier, in which they constitute the principal heat and alcohol source. Condensed vapors from the evaporator and the bottom stream from the rectifier are stripped of their remaining alcohol content in a condensate stripper, which is also driven by the recompressed vapors from the evaporator. This prevents dilution of the slops and the additional energy cost that would be necessary if the water content of these streams had to be removed in the slop evaporator.

Claims7

Dependent claims

A system for producing concentrated alcohol and distillery slop from fermented beer with a reduced amount of energy comprising:

(a) a beer still;
(b) means for feeding said beer to said still;
(c) means for feeding a portion of a water vapor, withdrawn from evaporating means (f) hereinbelow, to said still;
(d) means for withdrawing an alcohol-rich vapor as the overhead from said still;
(e) means for withdrawing an alcohol-poor distillery slop as the bottom stream from said still;
(f) evaporator means for concentrating said slop by evaporating water vapor therefrom;
(g) means for passing said slop from said still to said evaporator means;
(h) means for passing said vapor from said overhead of said still to said evaporator means into indirect heat exchange contact with said slop to condense a portion of said vapor and form a condensate;
(i) condensate stripper means for separating said condensate into an alcohol-rich overhead stream and an alcohol-poor bottom stream;
(j) means for passing said condensate from said evaporator means to condensate stripper means;
(k) means for feeding a portion of said water vapor withdrawn from said evaporator means to said stripper means;
(l) rectifier means for separating uncondensed vapor from said evaporator means into a concentrated alcohol overhead stream and an alcohol-containing mixture as a bottom stream;
(m) means for passing the uncondensed vapor from said evaporator means to said rectifier means;
(n) means for passing said alcohol-containing mixture from said rectifier means to said stripper means for admixture with said condensate from said evaporator;
(o) compressor means for forming a compressed vapor;
(p) means for passing at least a portion of at least one of said water vapor from said evaporator means and said vapor from said still to said compressor means;
and
(q) means for withdrawing said concentrated slop from said evaporator means.

15 more elements

Dependencies are inferred from the claim text.

Facts

Application: 06/331,205Filed 16 Dec 1981 · division
Priority: 12 Nov 1980
Granted: 26 Apr 1983
Term ends: Not estimatedThe source records don’t support an estimate.

Classification6 codes

B01D 1/12
Evaporators with vertical tubes: and forced circulation
B01D 1/26
Evaporating: multiple-effect evaporating
B01D 1/2812
Special features relating to the vapour to be compressed: the vapour is coming from different sources
B01D 1/284
With vapour compression: special features relating to the compressed vapour