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OCTOBER 19-20, 2012 - YMCA University of Science & Technology

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Proceedings <strong>of</strong> the National Conference on<br />

Trends and Advances in Mechanical Engineering,<br />

<strong>YMCA</strong> <strong>University</strong> <strong>of</strong> <strong>Science</strong> & <strong>Technology</strong>, Faridabad, Haryana, Oct <strong>19</strong>-<strong>20</strong>, <strong>20</strong>12<br />

and the H2O is removed . High – Btu gas is thus largely methane , with a heating value <strong>of</strong> 950 to 1000 Btu<br />

/ scf , approaching that <strong>of</strong> natural gas , which is 950 – 1100 Btu / scf .It has all the characteristics <strong>of</strong> natural<br />

gas but without the sulfur and other pollutants .Various methods under development for the production <strong>of</strong><br />

high Btu gas , is more complex and expensive than low – Btu gas . Purified low – Btu gas can be fired<br />

directly in a conventional steam generator. It has the advantages <strong>of</strong> being sulphur and ash – free, thus<br />

eliminating the need for precipitators and scrubbers. The lack <strong>of</strong> SO2 in the flue gases also permits lower<br />

stack temperatures, which results in improved efficiency .<br />

An attractive utilization <strong>of</strong> low – Btu gas for electric generation is a fuel for Combined – cycle power plant<br />

.A combined cycle is one which uses a gas turbine at the high temperature end and a steam turbine at the<br />

low temperature end .Low – Btu gasifiers operate at different pressures and temperatures , depending<br />

upon the process used . They operate at exit temperatures between 1000degree F and <strong>20</strong>00degree F . The<br />

exit gas must be cooled for purification and cleaning .Normally this cooling represents a large loss <strong>of</strong><br />

energy to the environment . A combined cycle takes advantage <strong>of</strong> the high gasifier and recovers much <strong>of</strong><br />

that heat loss by a gas to gas heat exchanger .The gas turbine drives one <strong>of</strong> two electric generators and<br />

the compressor. Superheated steam is generated in HRSG , expands through a steam turbine that drives the<br />

second electric generator and exhausts to a condenser.<br />

Gasification reactors are designed to suit coal characteristics. Three well-known configurations are the fixed bed,<br />

fluidized bed, and entrained bed systems.<br />

• Fixed Bed Gasifier reactor has different zones for each operation such as drying, devolatilizing, gasification,<br />

and combustion. Coal <strong>of</strong> 10–50mm size is fed from the top and air or oxygen is blown through the fuel bed. The<br />

crude gas leaves the gasifier from above. This type <strong>of</strong> gasifier obviates the need for a heat exchanger, has lower<br />

oxygen consumption, and has the lowest energy requirement <strong>of</strong> all gasification processes. This technology has<br />

been commercialized and about <strong>20</strong>0 fixed bed gasifiers are operating around the world[4].<br />

• Fluidized Bed Gasifier works on the counter-current principle and allows coal particles to move vigorously.<br />

It consists <strong>of</strong> a vertical cylindrical refractory lined vessel with recycle cyclone. The temperature in the reactor<br />

goes up to 850–1,050°C. It is a non-slagging gasifier and has been tested with all types <strong>of</strong> coal and lignite, and is<br />

found attractive for high ash coals as well as high reactive coals. The chemical reaction in this gasifier is<br />

accelerated by turbulent mixing and close contact. There are no separate de-gasification and gasification zones.<br />

Dust-laden gas leaves the reactor at the top, and is cooled and purified before use[14].<br />

• Entrained Bed Process is the third configuration. Finely ground coal <strong>of</strong> 0.1 mm is entrained at high<br />

temperatures <strong>of</strong> the order <strong>of</strong> 1,400 to 1,600°C. Coal gasifies instantly and volatile matter in coal also contributes<br />

to the gas at the reaction temperatures. The product gas has almost 80 per cent <strong>of</strong> the energy <strong>of</strong> the feed coal.<br />

The ash in the coal melts and runs down the refractory-lined walls.<br />

2b(ii) Coal Liquefaction : It is the conversion <strong>of</strong> coal into a liquid fuel for direct energy production or a<br />

liquid substitute for refinery feedstock from which other liquid fuels may be obtained. In coal<br />

liquefaction, the long molecules are shortened by adding hydrogen. The needed hydrogen is generated , and<br />

desulfurization is accomplished , in the same manner as for coal gasification. The Fischer – Tropsch process<br />

first produces a mixture <strong>of</strong> CO and H2 from coal and steam.This is followed by catalytic reactions at<br />

about 300 degree F and 150 bar , which yield a range <strong>of</strong> hydrocarbons from gaseous methane to higher<br />

liquid hydrocarbons. These are then separated with methane going as pipeline gas and the rest going to<br />

different liquid fuels.<br />

2(c) Coal Firing / Combustion <strong>Technology</strong><br />

38

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