EFFLUENT
FROM TEXTILE DYEING INDUSTRIES
The effluent from the Textile Dyeing Industries generally consists of high
amount of inorganic salts like sodium sulphate or sodium chloride. For the
purpose of treating this effluent, first Evaporation, then Crystallization
of Salts and thereafter centrifuging is done to dewater the salt output from
crystallizer. A combination of Industrial Evaporators like Falling film
Evaporator, Forced Circulation Evaporator and the Industrial Dryers like
Agitated Thin Film Dryer, Fluid Bed Dryer etc are used. Other auxiliary
techniques such as centrifuging are also employed.
The effluent containing high amount of inorganic salts is preheated and
then it enters the multiple effects falling film evaporator for further
concentration. In the evaporation process where the concentration is done to
a level close to the saturation point of the salt present.
After concentration in the falling film evaporator, we get a concentrated
stream of effluent which can be then further fed to the evaporative/cooling
crystallizer where evaporation/cooling encourage the crystallization
process.
Finally, the output from the crystallizer centrifuged to separate the salts
from the stream. The salt after centrifuging can further be dried using a
Fluid Bed Dryer.
SCHEME
FOR EFFLUENT TREATMENT FOR TEXTILE/DYEING INDUSTRY:
EFFLUENT
FROM PHARMACEUTICALS BULK DRUG INDUSTRIES
The effluent from the bulk drug industries generally consists of high
organic content thereby making the effluent as high COD effluent. For the
purpose of treating this effluent, Evaporation and Drying methods are used.
A combination of Industrial Evaporators like Flash Evaporator, Falling film
Evaporator, Forced Circulation Evaporator and the Industrial Dryers like
Agitated Thin Film Dryer, Fluid Bed Dryer etc are used. Other auxiliary
techniques such as centrifuging, filtration, incineration are also employed.
But the condensate water generated after condensation of the vapours formed
in evaporation process of this particular effluent tends to carry the
volatile organic compounds thereby increasing the COD of condensate water
and making it unfit for use/disposal. The COD of the condensate water can be
brought down by rectification/ carbon treatment or aeration with a high
pressure blower for prolonged periods.
The effluent containing high amount of organics is preheated and then high
heated using steam as heating media and then it enters into flashing chamber
where due to flash evaporation, the maximum quantity of low boiling organics
leave the effluent stream and their vapours are condensed into a condenser.
This condensed vapours can be incinerated in an incinerator for making the
facility a complete zero pollution plant.
The output liquid stream from the flashing chamber enters the multiple
effect falling film evaporator for further concentration. After
concentration in the falling film evaporator, we get a concentrated stream
of effluent which can be then further concentrated or dried in different
types of evaporators and dryers depending upon the actual composition of the
individual stream.
Finally, whole of the effluent is converted into solid/sludge form so that
it can be disposed using various ways like land filling.
SSPs strong background and its Research Team at the Research &
Development Centre tried and tested various techniques to bring down the COD
of this condensate water so that it can be used back in the industry/
discharged with COD limits well within the range as specified by the
Pollution Control Boards.
SCHEME
FOR EFFLUENT TREATMENT FOR BULK DRUG INDUSTRY:
EFFLUENT
FROM COMMON EFFLUENT TREATMENT PLANT
The concept of effluent treatment, by means, of a collective effort, has
assumed reasonable gravity by being especially purposeful for cluster of
small scale industrial units. Common Effluent Treatment Plant (CETP) not
only help the industries in easier control of pollution, but also act as a
step towards cleaner environment and service to the society at large. Small
scale industries, by their very nature of job- cannot benefit much from
economies of scale and therefore the burden of installing pollution- control
equipment, falls heavy on them.
The concerted approach of joint or common effluent treatment provisions has
many advantages. Wastewater of individual industries often contain
significant concentration of pollutants; and to reduce them by individual
treatment upto the desired concentration, become techno- economically
difficult The combined treatment provides a better and economical option
because of the equalization and neutralization taking place in the CETP.
SSP is one of the most successfull in seting up a project alike these which
can handle different type of waste water in a single unit which is
economical and need of the hour.