Accepted Papers - 3.pdf - UNESCO
Accepted Papers - 3.pdf - UNESCO
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