Two general models for batch simultaneous enzymatic and microbial reaction (SEMR) processes are presented, the second derived from and simpler than the first and accounting for enzyme denaturation. Using the second model and parameter values from the literature, simulation was used to examine a range of enzyme addition rate strategies (in which the rate was a linear function of time) for a relatively fast ethanol fermentation and for a longer duration citric acid fermentation, both using cellulose as the substrate. For the ethanol process it is optimal (for a specific objective function which accounts for product value and enzyme cost) to add all the enzyme at the beginning of the process. But for the citric acid process a linearly decreasing enzyme addition rate, coupled with the addition of a small fraction of the enzyme at time zero, is better than pure batch operation or operation with the best constant enzyme feed rate.
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Shandong Inst Business & Technol, Sch Math & Informat Sci, Yantai, Peoples R China
Curtin Univ, Dept Math & Stat, Perth, WA, AustraliaShandong Inst Business & Technol, Sch Math & Informat Sci, Yantai, Peoples R China
Liu, Chongyang
Gong, Zhaohua
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Shandong Inst Business & Technol, Sch Math & Informat Sci, Yantai, Peoples R ChinaShandong Inst Business & Technol, Sch Math & Informat Sci, Yantai, Peoples R China
Gong, Zhaohua
Teo, Kok Lay
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Curtin Univ, Dept Math & Stat, Perth, WA, AustraliaShandong Inst Business & Technol, Sch Math & Informat Sci, Yantai, Peoples R China
Teo, Kok Lay
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Loxton, Ryan
Feng, Enmin
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Dalian Univ Technol, Sch Math Sci, Dalian, Peoples R ChinaShandong Inst Business & Technol, Sch Math & Informat Sci, Yantai, Peoples R China
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Univ Syiah Kuala, Fac Engn, Dept Chem Engn, Banda Aceh 23111, Indonesia
Univ Malaya, Fac Engn, Dept Chem Engn, Kuala Lumpur 50603, MalaysiaUniv Syiah Kuala, Fac Engn, Dept Chem Engn, Banda Aceh 23111, Indonesia
Yahya, Azwar Muhammad
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Hussain, Mohd Azlan
Wahab, Ahmad Khairi Abdul
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Univ Malaya, Fac Engn, Biomed Engn Dept, Kuala Lumpur 50603, MalaysiaUniv Syiah Kuala, Fac Engn, Dept Chem Engn, Banda Aceh 23111, Indonesia
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IFP Energies Nouvelles, Rond Point Echangeur Solaize BP 3, F-69360 Solaize, FranceIFP Energies Nouvelles, Rond Point Echangeur Solaize BP 3, F-69360 Solaize, France
Battista, Federico
Almendros, Melanie Gomez
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IFP Energies Nouvelles, Rond Point Echangeur Solaize BP 3, F-69360 Solaize, FranceIFP Energies Nouvelles, Rond Point Echangeur Solaize BP 3, F-69360 Solaize, France
Almendros, Melanie Gomez
Rousset, Romain
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IFP Energies Nouvelles, Rond Point Echangeur Solaize BP 3, F-69360 Solaize, FranceIFP Energies Nouvelles, Rond Point Echangeur Solaize BP 3, F-69360 Solaize, France
Rousset, Romain
Bouillon, Pierre-Antoine
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IFP Energies Nouvelles, Rond Point Echangeur Solaize BP 3, F-69360 Solaize, FranceIFP Energies Nouvelles, Rond Point Echangeur Solaize BP 3, F-69360 Solaize, France