2015
DOI: 10.1016/j.bej.2014.09.010
|View full text |Cite
|
Sign up to set email alerts
|

Mathematical model of decolourization in a rotating disc reactor

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
1
1

Citation Types

0
2
0

Year Published

2016
2016
2023
2023

Publication Types

Select...
5
1

Relationship

0
6

Authors

Journals

citations
Cited by 6 publications
(2 citation statements)
references
References 30 publications
(40 reference statements)
0
2
0
Order By: Relevance
“…Today's scientific literature is abundant with data on fungi cultivation on various lignocellulose materials where significant efforts related to the bioreactor design improvement and solid-state fermentation (SSF) process development have been made. SSF may be carried out in different types of bioreactors, such as tray bioreactors (Ali and Zulkali, 2011;Figueroa-Montero et al, 2011;Pouryafar et al, 2015;Rodrígues Couto and Sandromán, 2006;Rodrígues Couto et al, 2003;Zhang et al, 2014), rotating disc reactors (Skybová et al, 2015), packed-bed bioreactors (Ali and Zulkali, 2011;Rodrígues Couto and Sandromán, 2006;Rodrígues Couto et al, 2003), columntray bioreactors (Ruiz et al, 2012), air-pressure pulsation solidstate bioreactors (Chen and He, 2013), rotating horizontal drum bioreactors (Ali and Zulkali, 2011;Domíniguez et al, 2001;Rodrígues Couto and Sandromán, 2006), stirred-drum bioreactors (Ali and Zulkali, 2011), fluidized bed bioreactors (Ali and Zulkali, 2011;Krishnaiah et al, 2005;Sandromán, 2006), air-lift bioreactors (Ali andZulkali, 2011) and immersion bioreactors (Rodrígues Couto et al, 2003).…”
Section: Introductionmentioning
confidence: 99%
“…Today's scientific literature is abundant with data on fungi cultivation on various lignocellulose materials where significant efforts related to the bioreactor design improvement and solid-state fermentation (SSF) process development have been made. SSF may be carried out in different types of bioreactors, such as tray bioreactors (Ali and Zulkali, 2011;Figueroa-Montero et al, 2011;Pouryafar et al, 2015;Rodrígues Couto and Sandromán, 2006;Rodrígues Couto et al, 2003;Zhang et al, 2014), rotating disc reactors (Skybová et al, 2015), packed-bed bioreactors (Ali and Zulkali, 2011;Rodrígues Couto and Sandromán, 2006;Rodrígues Couto et al, 2003), columntray bioreactors (Ruiz et al, 2012), air-pressure pulsation solidstate bioreactors (Chen and He, 2013), rotating horizontal drum bioreactors (Ali and Zulkali, 2011;Domíniguez et al, 2001;Rodrígues Couto and Sandromán, 2006), stirred-drum bioreactors (Ali and Zulkali, 2011), fluidized bed bioreactors (Ali and Zulkali, 2011;Krishnaiah et al, 2005;Sandromán, 2006), air-lift bioreactors (Ali andZulkali, 2011) and immersion bioreactors (Rodrígues Couto et al, 2003).…”
Section: Introductionmentioning
confidence: 99%
“…A minimization of time-cost is often sought by designers of biotechnological processes [18,31]. The batch time required to achieve a certain conversion of the reactants is usually assumed as the main characteristic of the process duration [13].…”
Section: Problem Statementmentioning
confidence: 99%