2016
DOI: 10.1016/j.bej.2016.03.007
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Production of pectinases by solid-state fermentation of a mixture of citrus waste and sugarcane bagasse in a pilot-scale packed-bed bioreactor

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Cited by 107 publications
(41 citation statements)
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“…The velocity required to calculate the Reynolds number in Eqs. (17) and (18) was estimated assuming uniform distribution of the air over the bed surface. The available area for the fluid to flow was 0.17 m 2 , resulting in a linear velocity equal to 0.0005 m/s and a Reynolds number equal to 21.3, confirming the assumption of laminar flow in the headspace.…”
Section: Experimental Determination Of the Convective Heat Transfer Bmentioning
confidence: 99%
See 1 more Smart Citation
“…The velocity required to calculate the Reynolds number in Eqs. (17) and (18) was estimated assuming uniform distribution of the air over the bed surface. The available area for the fluid to flow was 0.17 m 2 , resulting in a linear velocity equal to 0.0005 m/s and a Reynolds number equal to 21.3, confirming the assumption of laminar flow in the headspace.…”
Section: Experimental Determination Of the Convective Heat Transfer Bmentioning
confidence: 99%
“…wheat, rice, soybean), and straws (e.g. wheat, corn, oat) and sugar cane bagasse [8][9][10][11][12][13][14][15][16][17]. The concentration and quality of the bioproduct in SSC depends on the capacity of controlling the operational variables close to the optimal conditions for the microbial metabolism.…”
Section: Introductionmentioning
confidence: 99%
“…Some solid-state fermentations are already performed at the commercial scale in the food industry or for waste management and bioremediation processes. Knowledge on bioreactor design is strong and many novel processes have been performed in pilot scale bioreactors [10,11].…”
Section: Introductionmentioning
confidence: 99%
“…There are only a few reports tackling the mentioned operational strategies, but most of them are focused either on inoculation strategies (Cerda et al, 2016;Martinez-Ávila et al, 2017), operational configuration (Cheirsilp and Kitcha, 2015;Cerda et al, 2017a;Martinez-Ávila et al, 2018;Mejias et al, 2018), process control and/or reactor design (Astolfi et al, 2011;Biz et al, 2016;Martinez-Ávila et al, 2018). The last parameter is of great relevance, as it is the main factor hindering the development of large-scale processes (Mitchell et al, 2006;Thomas et al, 2013).…”
Section: Process Developmentmentioning
confidence: 99%