Abstract

Almost all coal based thermal power plants (CTPP) in India use electrostatic precipitator (ESP) for reduction of particulate matter (PM) in flue gas generated due to the combustion of Indian coal. This coal is characterized by high ash content, low calorific value and low sulfur content resulting in the generation of a very large amount of highly electrically‐resistive fly‐ash; thereby requiring a very large size ESP to minimize the fly‐ash emissions. However, the flue‐gas particle size distribution analysis showed that 60% of the particles are above 15 μm size, which can be conveniently removed using a low‐cost inertial separator such as a cyclone separator. It is proposed that a cyclone be used, as a pre‐cleaner to ESP so that the large size fraction of fly‐ash can be removed in the pre‐cleaning and the remaining flue‐gas entering the ESP will then contain only small size particles with low dust loading, thereby requiring a small ESP, and improving overall efficiency of dust removal. A low efficiency (65%), high throughput cyclone is considered for pre‐cleaning flue gas and the ESP is designed for removal of the remaining 35% fly‐ ash from the flue gas. It is observed that with 100% dust load, the ESP requires six fields per pass, whereas with cyclone as a pre‐cleaner, it requires only five fields per pass. Introducing cyclone into the flue gas path results in additional head loss, which needs to be overcome by providing additional power to induced draft (ID) fan. The permissible head loss due to the cyclone is estimated by comparing the power requirement in the bag filter control unit and cyclone‐ESP combined unit. It is estimated that a head loss of 10 cm of water can be permitted across the cyclone so as to design the same for 65% efficiency.

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