Effect of micro-aeration on the growth of Candida pseudotropicalis and production of ethanol during batch fermentation of cheese whey

1995 ◽  
Vol 52 (3) ◽  
pp. 203-217 ◽  
Author(s):  
A.E. Ghaly ◽  
A.A. El-Taweel
1988 ◽  
Vol 2 (6) ◽  
pp. 359-364 ◽  
Author(s):  
Shahriar Alam ◽  
David Stevens ◽  
Rakesh Bajpai

2010 ◽  
Vol 34 (10) ◽  
pp. 1590-1596 ◽  
Author(s):  
Alessandra Saraceno ◽  
Stefano Curcio ◽  
Vincenza Calabrò ◽  
Gabriele Iorio

3 Biotech ◽  
2021 ◽  
Vol 11 (8) ◽  
Author(s):  
Philip Isaac Omwene ◽  
Meltem Yağcıoğlu ◽  
Zehra Betül Öcal-Sarihan ◽  
Fatma Ertan ◽  
Ülker Diler Keris-Sen ◽  
...  

1981 ◽  
Vol 44 (8) ◽  
pp. 588-590 ◽  
Author(s):  
B. J. DEMOTT ◽  
F. A. DRAUGHON ◽  
P. J. HERALD

Kluyveromyces fragilis was more suitable than Candida pseudotropicalis or Kluyveromyces lactis for production of ethanol from whey. Direct-acid-set cottage cheese whey and the supernatant fluid resulting from heat treatment of the whey at 95 C for 20 min showed similar rates of fermentation when inoculated with K. fragilis. Inoculation rates of 10, 12 and 14 ml of active K. fragilis culture per 100 ml of media were not significantly different in rate of ethanol production. Samples incubated with K. fragilis at 35, 37, 40 and 42 C showed more rapid reduction in specific gravity than samples incubated at room temperature or 30 C. Lactose conversion in whey was 83% complete and in whey supernatant fluid, 77%.


2014 ◽  
Vol 32 (5) ◽  
pp. 434-440 ◽  
Author(s):  
KM Muñoz-Páez ◽  
HM Poggi-Varaldo ◽  
J García-Mena ◽  
MT Ponce-Noyola ◽  
AC Ramos-Valdivia ◽  
...  

The aim of this work was to evaluate the effect of buffer addition and process temperature (ambient and 35°C) on H2 production in batch fermentation of cheese whey (CW). When the H2 production reached a plateau, the headspace of the reactors were flushed with N2 and reactors were re-incubated. Afterwards, only the reactors with phosphate buffer showed a second cycle of H2 production and 48% more H2 was obtained. The absence of a second cycle in non-buffered reactors could be related to a lower final pH than in the buffered reactors; the low pH could drive the fermentation to solvents production. Indeed a high solvent production was observed in non-buffered bioreactors as given by low ρ ratios (defined as the ratio between sum of organic acid production and sum of solvents production). Regarding the process temperatures, no significant difference between the H2 production of reactors incubated at ambient temperature and at 35°C was described. After flushing the headspace of bioreactors with N2 at the end of the second cycle, the H2 production did not resume (in all reactors).


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