Please use this identifier to cite or link to this item: http://10.1.7.192:80/jspui/handle/123456789/3040
Title: Simulation of Coal Gasification Process using ASPEN PLUS
Authors: Nayak, Rajul
Mewada, R. K.
Keywords: Aspen Plus Simulation
Coal Gasification
Combustion
Fischer-Tropsch
Fluidized Bed
Chemical Faculty Paper
Faculty Paper
ITFCH027
10MCHC09
NUiCONE
NUiCONE-2011
Issue Date: 8-Dec-2011
Publisher: Institute of Technology
Citation: 2nd International Conference on Current Trends in Technology, NUiCONE-2011, Institute of Technology, Nirma University, December 8-10, 2011
Series/Report no.: ITFCH027-7
Abstract: Gasification is an important route for conversion of coal or solid wastes materials to useful gaseous products for direct firing in thermal applications and as well as raw gas for production of fuels or chemicals. Gasification with O2, H2O, CO2 and H2 produces combustibles such as CH4 and CO/H2 mixtures for use as gaseous fuels or chemical feed stocks. Among the coal-gasification processes, the fluidized-bed process with inherent advantages of high heat transfer and easy handling of solids is a natural choice. Coal gasification with O2 and H2O in a fluidized-bed reactor involves pyrolysis, combustion and steam gasification. Gasification in fluidized bed offers advantages, since fluidized beds are capable of being scaled up to medium and large scale, overcoming limitations found in smaller scale, fixed-bed designs. This paper gives overview of the coal gasification process. Simulation of coal gasification process was carried out using Aspen Plus. Effect of various parameters like steam to coal ratio and oxygen flow rate effects on product gas composition were studied.
URI: http://10.1.7.181:1900/jspui/123456789/3040
ISBN: 9788192304908
Appears in Collections:Faculty Papers, Chemical

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