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Accepted Papers - 3.pdf - UNESCO

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granular amorphous peat, fly ash, peanut skin, and<br />

coconut husk hull.<br />

Zinc salts heavy doses (165 mg) in<br />

continuation causes vomiting, renal damage, and<br />

cramps. Discharge standard as per EPA and I:S for<br />

zinc is 5.0 mg/l. Zinc concentration was highest in<br />

site AB 4 (24 mg/l), least in site AB 1 (2.08 mg/l).<br />

Concentration in site AB 2 and AB 3 was 6.52mg/l and<br />

14.2 mg/l respectively. Zinc in decreasing order of<br />

concentration was as follows: AB 4 >AB 3 >AB 2 >AB 1 .<br />

Nano filtration is effective membrane technology<br />

for the removal or separation of zinc in solution or<br />

waste waters. Suggested natural adsorbent for zinc<br />

adsorption are blast furnace slag, china clay waste<br />

tea leaves and cement matrix.<br />

Conclusion<br />

It is thus concluded that AB 1 waste water was<br />

alkaline , highly organically polluted indicated by<br />

high BOD and COD values and low in metal<br />

pollution, AB 2 site waste water was slightly acidic ,<br />

highest in organic pollution, second lowest in metal<br />

pollution, AB 3 waste water sample was acidic , with<br />

highest metal pollution and low organic pollution.<br />

AB 4 site waste water was highly acidic, lowest in<br />

organic pollution, and second highest in metal<br />

pollution. In all these electroplating units, certainly<br />

there is a need to treat the waste water for certain<br />

heavy metals and for chemical and organic pollution<br />

before it discharges in to open drains. As these<br />

effluents from electroplating units are highly<br />

corrosive due to the presence of acids and toxic<br />

metals, there discharge directly in to rivers (Yamuna<br />

river in case of Agra) without neutralization<br />

decreases the pH of river water and results in mass<br />

mortality of aquatic culture. Certainly there is a need<br />

for scientific disposal of effluents, which to certain<br />

extent can be achieved by membrane technologies<br />

and adsorbents referred in the present paper. Beside<br />

* All values except pH are in mg/l<br />

this sincere execution of policies which restrict the<br />

effluent discharge exceeding the tolerance limits<br />

prescribed by IS: Standards, CPCB and EPA for<br />

discharge of industrial effluents is urgently needed<br />

in case of present industry.<br />

References<br />

• APHA, AWWA and WEF. 1992. Standard<br />

Methods for Examination of Water and Wastewater.<br />

18th ed. New York: American Public Health<br />

Association.<br />

• Dahiya, Sudhir Mishra D.G, Karpe Rupali and<br />

Gurg R.P 2003 Removal of lead and copper from<br />

aqueous solution using chemically activated<br />

sugarcane bagasse carbon. Proc.xii Natinal<br />

symposium on environment 400-406.<br />

• Gupta, K.V., Gupta , M., and Sharma, S. 2001.<br />

Process development for the removal of lead and<br />

chromiu- m from aqueous solutions using red mud<br />

an aluminium industry waste. Water Res 35, 1125-<br />

1134.<br />

• Joshi, Sandeep. 2000. Ecotechnological<br />

treatment for the industrial waste water containing<br />

heavy metals. J. IAEM 27: 98-102.<br />

• Kosarek, L.J. 1981. Removal of Various Toxic<br />

Heavy Metals and Cyanide from Water by<br />

Membrane Processes. J.Chemistry in Water Reuse<br />

, 261-280.<br />

• Sezin Islamoglu and levent yilmaz 2001.<br />

Removal and recovery of heavy metals from<br />

industrial waste streams by means of a hybrid<br />

precipitation and polymer enhanced ultrafiltration.<br />

Desalination. 105-110.<br />

• Srisuwan, G. and Thongchai, P. 2002. Removal<br />

of heavy metals from electroplating wastewater by<br />

membrane. J. Sci. Technol. 24(Suppl.) 965-976.<br />

• Upadhyay,Y.D., Upadhyay, S.N., Haribabu, E.<br />

1992. Removal of chromium (VI) by fly ash. Chem.<br />

Environ.Res1 (3): 289.<br />

Table 1. Indian Standards and average of readings observed for period from January-December<br />

for pH, BOD and COD *<br />

400

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