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- W2353468938 abstract "The experimental results of mixing-gas(air/steam) catalytic gasification for the pulverized coal by using two kinds of industrial alkali as the catalyst in a fluidized bed with I.D.28?mm were reported by this study.The optimum reactive time and catalytic gasification temperature is respectively forty minutes and 900?℃ and the loading saturation levels(LSL) for above two catalysts in pulverized coal are about 8%.The wasted liquid of viscose fiber has showed better catalytic effect than that of industrial sodium hydroxide,whether for gas yield or calorific value of gas transformed from unit weight coal.Under the optimum gasification temperature being equal to 900?℃,the value of gas yield is on the increase from 2.57?m~3/kg with no catalyst to 3.62?m~3/kg with industrial sodium hydroxide 8% and 3.97?m~3/kg with wasted liquid of viscose fiber 8%.Moreover,the calorific value of gas transformed from unit weight coal adds to 2.78 times than that obtained with no catalyst and 0.66 times than that resulted from sodium hydroxide." @default.
- W2353468938 created "2016-06-24" @default.
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- W2353468938 date "2005-01-01" @default.
- W2353468938 modified "2023-09-23" @default.
- W2353468938 title "Investigation on technical conditions of mixing-gas catalytic gasification for pulverized coal with industrial alkali in fluidized beds" @default.
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