Integrated enzymatic pretreatment and hydrolysis of apple pomace in a bubble column bioreactor

2019 ◽  
Vol 150 ◽  
pp. 107306 ◽  
Author(s):  
Saverio Niglio ◽  
Alessandra Procentese ◽  
Maria Elena Russo ◽  
Alessandra Piscitelli ◽  
Antonio Marzocchella
2014 ◽  
Vol 28 (12) ◽  
pp. 7552-7559 ◽  
Author(s):  
Jorge L. S. Sonego ◽  
Diego A. Lemos ◽  
Guilherme Y. Rodriguez ◽  
Antonio J. G. Cruz ◽  
Alberto C. Badino

2018 ◽  
Vol 334 ◽  
pp. 691-697 ◽  
Author(s):  
Teresa García-Pérez ◽  
Juan C. López ◽  
Fabiana Passos ◽  
Raquel Lebrero ◽  
Sergio Revah ◽  
...  

Author(s):  
K. Sandesh ◽  
P. Ujwal ◽  
Blecita D. Mascarenhas ◽  
Gayatri Dhamannavar ◽  
Narmada Kumar ◽  
...  

2019 ◽  
Vol 6 (3) ◽  
pp. 84 ◽  
Author(s):  
Moradi ◽  
Rashedi ◽  
Mofradnia ◽  
Khosravi-Darani ◽  
Ashouri ◽  
...  

In this study, the simulation of microorganism ability for the production of poly-β-hydroxybutyrate (PHB) from natural gas (as a carbon source) was carried out. Based on the Taguchi algorithm, the optimum situations for PHB production from natural gas in the columnar bubble reactor with 30 cm length and 1.5 cm diameter at a temperature of 32 °C was evaluated. So, the volume ratio of air to methane of 50:50 was calculated. The simulation was carried out by COMSOL software with two-dimensional symmetric mode. Mass transfer, momentum, density-time, and density-place were investigated. The maximum production of biomass concentration reached was 1.63 g/L, which shows a 10% difference in contrast to the number of experimental results. Furthermore, the consequence of inlet gas rate on concentration and gas hold up was investigated Andres the simulation results were confirmed to experimental results with less than 20% error.


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