Pregled bibliografske jedinice broj: 1096560
Model-to-model: Comparison of mathematical process models of lipase catalysed biodiesel production in a microreactor
Model-to-model: Comparison of mathematical process models of lipase catalysed biodiesel production in a microreactor // Computers & chemical engineering, 145 (2021), 107200, 14 doi:10.1016/j.compchemeng.2020.107200 (međunarodna recenzija, članak, znanstveni)
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Naslov
Model-to-model: Comparison of mathematical
process models of lipase catalysed biodiesel
production in a microreactor
Autori
Gojun, Martin ; Ljubić, Anabela ; Bačić, Matea ; Jurinjak Tušek, Ana ; Šalić, Anita ; Zelić, Bruno
Izvornik
Computers & chemical engineering (0098-1354) 145
(2021);
107200, 14
Vrsta, podvrsta i kategorija rada
Radovi u časopisima, članak, znanstveni
Ključne riječi
biodiesel ; lipase ; mathematical process model ; enzyme kinetics ; microreactor
Sažetak
Based on the experimental results and model simulation it was shown that Bi-Bi Ping Pong mathematical process model is not suitable for the description of the lipase catalysed biodiesel production in a microreactor. Therefore, three additional mathematical process models were proposed. Prior to transport model development, the reaction rates were described with double substrate Michaelis- Menten kinetics, Bi-Bi Ping-Pong kinetics, and Hill kinetics. The Hill kinetic model was proposed as the best kinetic model based on the model selection criterion. In order to validate the proposed mathematical process models, biodiesel synthesis in a microreactor was performed at four different initial process conditions. In all validation experiments, free fatty acid concentration and enzyme concentration were kept constant and the oil to methanol ratio in the inlet streams was altered. An increase of biodiesel yield was observed for the higher methanol concentration in the system. If a large excess of methanol was used (oil to methanol ratio 1:90) the yield was higher than 90% for the residence time of only 40 min. In comparison to the batch process, where the yield of 96% was achieved for 48 h, this was a significant improvement. Two out of three proposed mathematical process models described experimental data very well for all analysed residence times. Considering the level of complexity and accuracy, a mathematical process model of steady-state two parallel plug flow reactors was proposed as the optimum solution for the mathematical description of enzymatic biodiesel synthesis performed in a microreactor.
Izvorni jezik
Engleski
Znanstvena područja
Kemijsko inženjerstvo, Interdisciplinarne tehničke znanosti, Biotehnologija
Napomena
Glavni autor: Martin Gojun
POVEZANOST RADA
Projekti:
HRZZ-IP-2016-06-7993 - Razvoj integriranog mikrosustava za biokatalitičku proizvodnju biodizela (DeMSy(BioPro)2) (Zelić, Bruno, HRZZ - 2016-06) ( CroRIS)
Ustanove:
Prehrambeno-biotehnološki fakultet, Zagreb,
Fakultet kemijskog inženjerstva i tehnologije, Zagreb
Citiraj ovu publikaciju:
Časopis indeksira:
- Current Contents Connect (CCC)
- Web of Science Core Collection (WoSCC)
- Science Citation Index Expanded (SCI-EXP)
- SCI-EXP, SSCI i/ili A&HCI
- Scopus
Uključenost u ostale bibliografske baze podataka::
- CA Search (Chemical Abstracts)