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A Study on Utilization of Discharged Hot Water for dm/potable Water by LTTD Method at Ennore Thermal Station


Affiliations
1 Centre for Remote Sensing and Geo informatics, Sathyabama University, Chennai, India
2 Department of Chemical & Environmental Engineering, Sathyabama University, Chennai, India
 

Thermal stations use coal as combustion material for fuel and the chemical energy stored in coal is converted successively into thermal energy, mechanical energy and finally electrical energy for continuous use and distribution across a wide geographic area. The steam exits the boiler, turbines and passes over cool tubes in the condenser. The condensers capture the used steam and transform it back to water. The cooled water is then pumped back to the boiler to repeat the heating processes. At the same time, water is piped from sea to keep the condensers constantly cool. This cooling water, now warm from the heat exchange in the condensers, is released from the plant. Large quantity of sea water is drawn to the tune of 1760 MLD in the Ennore thermal power station for cooling of condenser tubes. After the cooling purposes the return warm water is cooled and discharged back into the sea through tunnel of 2.50m diameter and subsequently through an open channel near outfall structure of the coast. Discharged hot water at the very first source of exit from the thermal station with a temperature of about 8°C can be used for heat conversion. The method of LTTD (Low Temperature Thermal Desalination) offers ideal scope for utilization of the already hot water which need not require pre-heating as the method of desalination utilizes 38°C of temperature in the flash chambers by evaporation and subsequent condensation in the shell and tube condensers of the steam using the sea water with low temperature. Thus an emphasis is made here for avoidance of purchase of raw water for all purposes and avoids tapping of ground water with zero environmental pollution. The brine thus emulated from the process is diluted using the already drawn effluent and discharged into the sea. The study of desalination is to determine and combine available technologies to optimize water production costs and quality. For which a number of factors determine the capital and operating costs for desalination: capacity and type of facility, location, feed water, labour, energy, financing, and concentrate disposal.

Keywords

Coolant Water, Desalination, Flash Chamber, Vacuum Pump, Brine
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  • Bhausaheb L. Pangarkar, Sane MG, Saroj B. Parjane, Rajendra M. Abhang and Mahendra Guddad (2010) The Heat and Mass Transfer Phenomena in Vacuum Membrane Distillation for Desalination. International Journal of Chemical and Biological Engineering 3, 1.

  • Low Temperature Thermal Desalination Applications For Drinking Water (2010) National Institute of Ocean Technology, (Ministry of Earth Sciences), Velachery Tambaram Main Road, Narayanapuram, Chennai 600100.

  • Metcalf and Eddy (2002) Waste water Engineering Treatment and Reuse, 4th edition, McGraw-Hill Science Engineering.

  • Phanikumar VS Sistla, Venkatesan G, Purnima Jalihal and Kathiroli S (2009) Low Temperature Thermal Desalination Plants, National Institute of Ocean Technology, Chennai, India, Proceedings of The Eighth ISOPE Ocean Mining Symposium Chennai, India, September 20-24.

  • Shanthi V and Gajendran N (2009) The impact of water pollution on the socio-economic status of the stakeholders of Ennore Creek, Bay of Bengal (India): Part I. Indian Journal of Science and Technology, 2(3), 66-79.

  • Yashpal Singh, Chief Environmental Officer (2007) The Ecology of Thermal Power, U.P. Pollution Control Board, PICUP Building, Vibhuti Khand, Gomti Nagar, Lucknow –INDIA.


Abstract Views: 568

PDF Views: 72




  • A Study on Utilization of Discharged Hot Water for dm/potable Water by LTTD Method at Ennore Thermal Station

Abstract Views: 568  |  PDF Views: 72

Authors

P. Balasubramanian
Centre for Remote Sensing and Geo informatics, Sathyabama University, Chennai, India
V. E. Nethaji Mariappan
Centre for Remote Sensing and Geo informatics, Sathyabama University, Chennai, India
Joshua Amarnat
Department of Chemical & Environmental Engineering, Sathyabama University, Chennai, India

Abstract


Thermal stations use coal as combustion material for fuel and the chemical energy stored in coal is converted successively into thermal energy, mechanical energy and finally electrical energy for continuous use and distribution across a wide geographic area. The steam exits the boiler, turbines and passes over cool tubes in the condenser. The condensers capture the used steam and transform it back to water. The cooled water is then pumped back to the boiler to repeat the heating processes. At the same time, water is piped from sea to keep the condensers constantly cool. This cooling water, now warm from the heat exchange in the condensers, is released from the plant. Large quantity of sea water is drawn to the tune of 1760 MLD in the Ennore thermal power station for cooling of condenser tubes. After the cooling purposes the return warm water is cooled and discharged back into the sea through tunnel of 2.50m diameter and subsequently through an open channel near outfall structure of the coast. Discharged hot water at the very first source of exit from the thermal station with a temperature of about 8°C can be used for heat conversion. The method of LTTD (Low Temperature Thermal Desalination) offers ideal scope for utilization of the already hot water which need not require pre-heating as the method of desalination utilizes 38°C of temperature in the flash chambers by evaporation and subsequent condensation in the shell and tube condensers of the steam using the sea water with low temperature. Thus an emphasis is made here for avoidance of purchase of raw water for all purposes and avoids tapping of ground water with zero environmental pollution. The brine thus emulated from the process is diluted using the already drawn effluent and discharged into the sea. The study of desalination is to determine and combine available technologies to optimize water production costs and quality. For which a number of factors determine the capital and operating costs for desalination: capacity and type of facility, location, feed water, labour, energy, financing, and concentrate disposal.

Keywords


Coolant Water, Desalination, Flash Chamber, Vacuum Pump, Brine

References