scholarly journals Kinetics of Metal Oxide-Catalyzed CO2Gasification of Coal in a Fluidized-Bed Reactor for Solar Thermochemical Process.2001,15, 1200−1206

2002 ◽  
Vol 16 (3) ◽  
pp. 802-802
Author(s):  
T. Kodama ◽  
A. Funatoh ◽  
K. Shimizu ◽  
Y. Kitayama
2015 ◽  
Vol 69 ◽  
pp. 1741-1749 ◽  
Author(s):  
T. Etori ◽  
N. Gokon ◽  
A. Takeuchi ◽  
T. Miki ◽  
M. Yokota ◽  
...  

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

2019 ◽  
Vol 33 (6) ◽  
pp. 5610-5619 ◽  
Author(s):  
Nicholas C. Means ◽  
Ward A. Burgess ◽  
Bret H. Howard ◽  
Mark W. Smith ◽  
Ping Wang ◽  
...  

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