scholarly journals Repeated batches as a strategy for high 2G ethanol production from undetoxified hemicellulose hydrolysate using immobilized cells of recombinant Saccharomyces cerevisiae in a fixed-bed reactor

2020 ◽  
Vol 13 (1) ◽  
Author(s):  
Thais S. Milessi ◽  
Caroline L. Perez ◽  
Teresa C. Zangirolami ◽  
Felipe A. S. Corradini ◽  
Juliana P. Sandri ◽  
...  
2020 ◽  
Vol 16 (2) ◽  
pp. 75-80
Author(s):  
Thais S. Milessi ◽  
Teresa C. Zangirolami ◽  
Caroline L. Perez ◽  
Juliana P. Sandri ◽  
Felipe A.S. Corradini ◽  
...  

Cellulose ◽  
2020 ◽  
Vol 27 (8) ◽  
pp. 4429-4442
Author(s):  
Thais S. Milessi ◽  
Cláudia R. Silva ◽  
Guilherme S. Moraes ◽  
Patricia M. Aquino ◽  
Roberto C. Giordano ◽  
...  

1985 ◽  
Vol 50 (10) ◽  
pp. 2122-2133 ◽  
Author(s):  
Jindřich Zahradník ◽  
Marie Fialová ◽  
Jan Škoda ◽  
Helena Škodová

An experimental study was carried out aimed at establishing a data base for an optimum design of a continuous flow fixed-bed reactor for biotransformation of ammonium fumarate to L-aspartic acid catalyzed by immobilized cells of the strain Escherichia alcalescens dispar group. The experimental program included studies of the effect of reactor geometry, catalytic particle size, and packed bed arrangement on reactor hydrodynamics and on the rate of substrate conversion. An expression for the effective reaction rate was derived including the effect of mass transfer and conditions of the safe conversion-data scale-up were defined. Suggestions for the design of a pilot plant reactor (100 t/year) were formulated and decisive design parameters of such reactor were estimated for several variants of problem formulation.


2004 ◽  
Vol 39 (12) ◽  
pp. 2097-2108 ◽  
Author(s):  
Tunahan Çakır ◽  
K.Yalçın Arga ◽  
M.Mete Altıntaş ◽  
Kutlu Ö. Ülgen

2010 ◽  
Vol 150 ◽  
pp. 554-555
Author(s):  
Ji-Hye Han ◽  
Ju-Yong Park ◽  
Hyun Woo Kang ◽  
Gi-Wook Choi ◽  
Bong-Woo Chung ◽  
...  

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