Dark fermentative biohydrogen production from vinicultural biomass without exogenous inoculum in a semi-batch reactor: A kinetic study

2022 ◽  
Vol 305 ◽  
pp. 114393
Author(s):  
Zineb Guellout ◽  
Emilie Francois-Lopez ◽  
Yacine Benguerba ◽  
Christine Dumas ◽  
Krishna Kumar Yadav ◽  
...  
2016 ◽  
Vol 24 (33) ◽  
pp. 25667-25675 ◽  
Author(s):  
Juan Antonio Salas-Cortés ◽  
Flor de María Cuervo-López ◽  
Anne-Claire Texier

2018 ◽  
Vol 16 (2) ◽  
pp. 159-170 ◽  
Author(s):  
Ensiyeh Taheri ◽  
Mohammad Mehdi Amin ◽  
Ali Fatehizadeh ◽  
Hamidreza Pourzamani ◽  
Bijan Bina ◽  
...  

2014 ◽  
Vol 20 (7) ◽  
pp. 1248-1255 ◽  
Author(s):  
Sumit Kumar Bansal ◽  
Yogita Singhal ◽  
T. R. Sreekrishnan ◽  
Radhika Singh

2017 ◽  
Vol 23 (4) ◽  
pp. 573-580 ◽  
Author(s):  
Sema Akyalcin

The kinetics of the hydration of propylene oxide was studied using a pressurized batch reactor for both uncatalyzed and heterogeneously catalyzed reactions. Lewatit MonoPlus M500/HCO3 - was used as heterogeneous catalyst, which showed better performance than Dowex Marathon A/HCO3 -. The effects of the parameters, namely internal and external diffusion resistances, temperature, catalyst loading and mole ratios of reactants, on the reaction rate were studied. The uncatalyzed and heterogeneously catalyzed reactions were proven to follow a series-parallel irreversible homogeneous mechanism. The temperature dependencies of the rate constants appearing in the rate expressions were determined.


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