DISTILLERY INDUSTRY :

The main source of pollution from distilleries is the spentwash. Spentwash is a non-toxic, biodegradable effluent with the following characteristics (Table-3) :

Table 3: Characterstics of Distileery Effluent
S.No.
Parameter
Range*
1.
pH
4.3-5.3
2.
Total Suspended Solids
12,000-14,000
3.
Total Dissolved Solids
45,000-75,000
4.
B.O.D., 20 C, 5 days
40,000-50,000
5.
C.O.D.
80,000-1,00,000
* Values are in mg/l except for pH.

Technologies for Treatment of Spentwash:

During the 80's following technologies were developed and adopted by distilleries to treat the spentwash:
  1. Anaerobic Digestion with bio-gas recovery (Bio- methanation)
  2. Composting; and
  3. Incineration
Biomethanation
Biomethanation is the process involving decomposition of organic matters (and to some extent inorganic matters) in the absence of molecular oxygen. Bio-conversion of the wastes results in methane rich gas.

      The advantages of biomethanation in case of spentwash are:

  1. generation of bio-gas which can meet more than 60% of the fuel requirements of the distillery and,
  2. About 80-90% of BOD is removed from spentwash
Over the years, a number of distilleries in the country have adopted bio-methanation for treatment of spentwash. The investment made in this system is paid back within 4-5 years. No doubt, the distilleries which adopted bio- methanation are reaping, the environmental and economic dividend.

Table 4: Pollution Prevention Pays
(For a 30 kl/day alcohal producing distillery)
Spentwash generation: 450 kl
Bio-gas production during bio-methanation: 25-30 Nm3/kl
Average total biogas production:12000 Nm3/day
Based on the net calorific value,
Therefore, Coal saving

:12 tonnes/day
Saving @Rs. 2000/tonne of coal:Rs. 24,000 /day
Total saving through biogas in one year: Rs. 72 lakh

Composting
In this process, the spentwash is mixed with filler materials, such as press mud, rice husk, wood chips, bagasse pith etc. The mixture . is seeded with cowdung or specially developed micro-organisms to hasten the process. The process takes 12-14 weeks to be completed and results in black compost, which can be used as manure.


Incineration
This process is base on the principal that the spentwash, when concentrate to 60% W/W, develops sufficient calorific value and can burn by itself without any external input of energy. This process results in potash rich ash which can be used as a fertilizer.

More recently the Vasantdada Sugar , Pune, has developed a process called DIEG (Drying Incineration and Energy Generation) , where coke like material is obtained and used as fuel in boiler to produce steam and energy. M/s. Zucker Gassification & Co-generation Ltd., Pune also has developed a process based on gasification of mixture of spentwash and bagasse to produce gas which can be used to drive gas turbines to generate power . There is one more process developed m/s. Consafe Science Ltd., Pune, in which the spentwash is thermally hydrolysed unde pressure to generate coke which in turn can be used in generation of steam.

         However, the above processes are yet to .be tried on a wider side.

Efforts of CPCB in Evolving Standards for Distillery
Recognising the problem of treating distillery effluent to a level suitable for disposal ) into the river/land, the Central Board constituted an expert group way back in 1980 to evolve Standards (MINAS) developed by the CPCB The MINAS are:

BOD,(200C, 5 days): 30 mg/ I for disposal into inland surface   water
:100 mg/I for disposal on land for   irrigation

Based on the MINAS developed by CPCB, Ministry of Environment & Forests, through the EPA Notification, dated January 8, 1990, specified effluent standards according to the disposal conditions, i,e, the recipient environment, The BOD (200, C, 5 days) standards so specified are as follows :

Disposal on stream/river: 30 mg/I
Disposal on land:100 mg/I
Disposal on land when land is considred as a treatment medium (land treatment): 500 mg/I
Land treatment with effective monitoring systems for ground water quality: 700 mg/I

The standards also include stipulations regarding net additional contribution to ground water quality in terms of BOD not to exceed 3 mg/1 and nitrate not to exceed 10 mg/l,

The method of land treatment, involves designing of the hydraulic loading, nutrient loading, crop pattern etc" after considering the porosity/permeability of the soil.

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