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AuthorAbu Reesh, I.M.
AuthorAbu Reesh, Ibrahim M.
Available date2022-12-28T06:31:08Z
Publication Date2021-08-01
Publication NameProcesses
Identifierhttp://dx.doi.org/10.3390/pr9081419
CitationAbu Reesh, I. M. (2021). Optimum Design of N Continuous Stirred-Tank Bioreactors in Series for Fermentation Processes Based on Simultaneous Substrate and Product Inhibition. Processes, 9(8), 1419.‏
URIhttps://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=85113446544&origin=inward
URIhttp://hdl.handle.net/10576/37697
AbstractOptimization of the continuous fermentation process is important for increasing efficiency and decreasing cost, especially for complicated biochemical processes described by substrate and product inhibition. The optimum design (minimum volume) of CSTRs in series assuming substrate and product inhibition was determined in this study. The effect of operating parameters on the optimum design was investigated. The optimum substrate concentration in the feed to the first reactor was determined for N reactors in series. The nonlinear, constrained optimization problem was solved using the MATLAB function “fmincon”. It was found that the optimum design is more beneficial at high substrate conversion and at a medium level of feed substrate concentration. The best number of reactors is two to three for optimum arrangements and two for equal-size arrangements. The presence of biomass in the feed to the first reactor reduces the reactor volume, while the presence of product in the feed slightly increases the required total volume. The percentage reduction in the total volume using the optimum design compared to equal-volume design (R%) was determined as a function of substrate conversion and substrate concentration in the feed to the first reactor. The obtained R% values agree with experimental data available in the literature for ethanol fermentation.
Languageen
PublisherMDPI AG
SubjectCSTRs in series
Fmincon MATLAB function
Optimization of bioreactors
Product inhibition
Substrate inhibition
TitleOptimum design of n continuous stirred-tank bioreactors in series for fermentation processes based on simultaneous substrate and product inhibition
TypeArticle
Issue Number8
Volume Number9
dc.accessType Open Access


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