USED 165 TPD DRINKING ETHANOL PLANT.
CONSISTING OF THE FOLLOWING SHOPS:
a) FERMENTATION , MAINLY BUILT IN 1980-S IN STAINLESS STEEL,
CONVERTS MOLASSES TO WINE. POSSIBLE FEEDSTOCK ARE RAW SUGAR, BEET MOLASSES/SYRUP, CANE MOLASSES.
INCLUDES FERMENTERS, HEAT EXCHANGERS, COOLING TOWERS, PUMPS&PIPING, STEEL STRUCTURE.
b) DISTILLATION , BUILT IN 2001
CONVERTS WINE TO ETHANOL AND VINASSE/STILLAGE, POSSIBLE FEEDSTOCK ARE RAW SUGAR, BEET MOLASSES/SYRUP, CANE MOLASSES.
INCLUDES DISTILLATION, PURIFICATION AND RECTIFICATION COLUMNS, ETHANOL DEHYDRATION COLUMN, PUMPS&PIPING, STEEL STRUCTURE, INSTRUMENTATION
c) EVAPORATION OF VINASSE, BUILT IN 2001
ELIMINATES WATER EXCESS FROM VINASSE/STILLAGE, POSSIBLE FEEDSTOCK ARE RAW SUGAR, BEET MOLASSES/SYRUP, UP TO 10% CANE MOLASSES.
BUT NOT SUITABLE FOR HIGHER MOLASSES CONTENT IN FEEDSTOCK.
INCLUDES (6) 4-EFFECT EVAPORATION COLUMNS, SPECIAL VALVES, PUMPS&PIPING, STEEL STRUCTURE, INSTRUMENTATION
d) OTHERS,
INCLUDES COOLING TOWERS & BOILERS.
PARAMETERS:
A) PRODUCTION CAPACITY:
ETHANOL..........................GRADE..........PRODUCTION CAPACITY
BEVERAGE-INDUSTRIAL........95.95º GL......31 110 CUB.M/YEAR
ANHYDROUS-BIOFUEL..........99.95º GL.......6 900 CUB.M/YEAR
DRIED.VINASSE/STILLAGE.....60º BRIX........2 700 CUB.M/YEAR
B)YELD
FEEDSTOCK..........CONSUMPTION PER 1.000 LTR OF PURE ETHANOL
RAW SUGAR.....................1,2 TONS/1000 LTR
SUGAR BEET MOLASSES.....3,5 TONS/1000 LTR
C)STEAM DEMAND
ETHANOL.....................GRADE.......HOURLY PRODUCTION........STEAM DEMAND
BEVERAGE-INDUSTRIAL.....95.95º GL...5 210 LTR/HOUR.........16.8 TONS/HOUR
ANHYDROUS-BIOFUEL.......99.95º GL...1 666 LTR/HOUR........+ 1.12 TONS/HOUR
D)POWER DEMAND
ETHANOL.....................GRADE.......HOURLY PRODUCTION.....POWER DEMAND
BEVERAGE-INDUSTRIAL.....95.95º GL...5 210 LTR/HOUR........1 035 MWH
ANHYDROUS-BIOFUEL.......99.95º GL...1 666 LTR/HOUR..........165 MWH
