Characteristics and kinetics of the gas releasing during oil shale pyrolysis in a micro fluidized bed reactor

Author(s):  
Hairat Abduhani ◽  
Yalkunjan Tursun ◽  
Abulikemu Abulizi ◽  
Dilinuer Talifu ◽  
Xu li Huang
Fuel ◽  
1986 ◽  
Vol 65 (2) ◽  
pp. 218-222 ◽  
Author(s):  
Robert L. Braun ◽  
Alan K. Burnham

2019 ◽  
Vol 2 (3) ◽  
pp. 217-224 ◽  
Author(s):  
Yuming Zhang ◽  
Mengxuan Zhao ◽  
Rongxuan Linghu ◽  
Chengxiu Wang ◽  
Shu Zhang

1993 ◽  
Vol 28 (2) ◽  
pp. 135-144 ◽  
Author(s):  
S. Matsui ◽  
R. Ikemoto Yamamoto ◽  
Y. Tsuchiya ◽  
B. Inanc

Using a fluidized bed reactor, experiments on glucose decomposition with and without sulfate reduction were conducted. Glucose in the reactor was mainly decomposed into lactate and ethanol. Lactate was mainly decomposed into propionate and acetate, while ethanol was decomposed into propionate, acetate, and hydrogen. Sulfate reduction was not involved in the decomposition of glucose, lactate, and ethanol, but was related to propionate and acetate decomposition. The stepwise reactions were modeled using either a Monod expression or first order reaction kinetics in respect to the reactions. The coefficients of the kinetic equations were determined experimentally. The modified Monod and first order reaction equations were effective at predicting concentrations of glucose, lactate, ethanol, propionate, acetate, and sulfate along the beight of the reactor. With sulfate reduction, propionate was decomposed into acetate, while without sulfate reduction, accumulation of propionate was observed in the reactor. Sulfate reduction accelerated propionate conversion into acetate by decreasing the hydrogen concentration.


1995 ◽  
Vol 43 (1) ◽  
pp. 188-193 ◽  
Author(s):  
M. Green ◽  
M. Schnitzer ◽  
S. Tarre

1995 ◽  
Vol 43 (1) ◽  
pp. 188-193
Author(s):  
M. Schnitzer ◽  
S. Tarre ◽  
M. Green

2012 ◽  
Vol 581-582 ◽  
pp. 112-116 ◽  
Author(s):  
Hua Qing Xue ◽  
Hong Yan Wang ◽  
Gang Yan ◽  
Wei Guo ◽  
Xiao Bo Li ◽  
...  

The kinetics of the thermal decomposition of Huadian oil shale was studied at five different isothermal atmospheres of 623K, 648K, 673K, 698K, and 723K. The temperature recorded was that of the sample that the temperature error between furnace and sample will eliminate. According to conversion data, the effect of increased temperature is to decrease the pyrolysis time. The conversion data described the oil shale pyrolysis as two stages, rapid conversion and modest conversion. The Arrhenius equations of ki=1.40×105e-109828/RT and kii=1.76×106e-130463/RT were obtain by isothermal kinetics model for each stage.


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