期刊名称：Indian Journal of Innovations and Developments
印刷版ISSN：2277-5382
电子版ISSN：2277-5390
出版年度：2012
卷号：1
期号：3
页码：155-161
出版社：Indian Society for Education and Environment
摘要：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.
