Author/Authors :
Kim، نويسنده , , Y.J and Lee، نويسنده , , S.H and Kim، نويسنده , , S.D، نويسنده ,
Abstract :
Subbituminous coal (Shenwha) was gasified at atmospheric pressure in a downer reactor (0.1 m I.D.×5.0 m high). The effects of reaction temperature (750–850°C), steam/coal mass ratio (0.23–0.86), O2/H2O mole ratio (0–1.81) and coal feeding rate (5.3–9.0 kg h−1) on the composition of product gas, carbon conversion, cold gas efficiency, gas yield and calorific value have been determined. In the case of steam injection into the loop-seal, compositions of the product gas (vol. %; N2 free basis) in the gasification region are H2 (35.8–39.4%), CH4 (6.8–15.5%), CO (14.9–15.9%), CO2 (20.7–29.5%), C2H4 (2.8–4.9%), C2H6 (2.5–3.5%), C3H6 (1.6–3.3%) and C3H8 (1.7–2.5%) with a calorific value of 13.0–15.2 MJ/m3. By changing the reactant gas supplied into the loop-seal for solid circulation from steam to air, product gas yield and carbon conversion increase, whereas calorific value of the product gas decreases from 13.0–15.2 to 6.3–10.6 with reaction temperature.
Keywords :
Downer , Circulating fluidized bed , coal gasification , Medium calorific value gas