The distilleries have been generating huge quantities of high toxic
effluents and in spite of the best efforts made so far a comprehensive
treatment has not been possible. In most of the conventional technologies,
the treated effluent also yields very high BOD, COD, TSS, and TDS level with
black colored and odor effluent to rivers & natural water streams.
Based on the above mentioned fact, a treatment by which it will be possible
to overcome all the problems have been worked out. The concept and the
treatment is based on the belief that all the BOD requirement should go down
and the condensate coming out should not be polluted.
As per the practical experience 1 KL alcohol production gives out 10 to 15
KL distillery effluent (spent wash). A number of distilleries have gone for
a primary treatment of this spent wash by setting up a biomethanation plant
but could not make the environment free from pollution.
SSP PVT. LIMTED (SSP) have developed Zero Pollution Effluent Treatment
System for handling distillery effluent. The system is based on evaporation
and drying technology.
SSP has executed 13 such plant for handling distillery effluent by
evaporation and drying technology.
SALIENT
FEATURES :
The zero discharge system for grain based
distillery effluent handling (DDGS Plant) consists of following main
processes.
The grain stillage from the bottom of
analyzer column of grain based distillery is introduced to a continuous
decanter centrifuge. Suspended particles are separated as a wet cake from
the decanter and thin liquor is further processed to the evaporation
section.
The thin liquor from decanter is concentrated in multiple effects falling
film vacuum evaporator to get maximum water evaporation per kg steam energy
supplied. The total process is under vacuum and the vapours generated in the
system are re-used to economize steam consumption. In order to reduce steam
consumption in multiple effect evaporation system the thermal vapour
recompression system is used. The thermal vapour recompression system use
vapours generated in the evaporator and compress it by steam and the
compressed vapours are used as heating medium in the evaporator. The
concentrate obtained from the evaporator is stored and fed to the mixing
section. The wet cake and the concentrate is mixed and blended to for a
uniform mix. The so formed mix is fed to the spin flash dryer to dry the wet
mix to get dried powder DDGS. Fraction of DDGS at 10% moisture content is
re-circulated through the blending section so to reduce the water
evaporation load on spin flash dryer.
The DDGS thus obtained is a high protein content product and can be used as
catlle feed of good nutritional value.