Crina Muscalu on Muck Rack

Crina Muscalu

As seen in: MDPI
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Articles

The In-Silico Optimization of a Batch Reactor for D-Fructose Production by Using the Cetus Process with In-Situ Cofactor Quick Regeneration

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By Gheorghe Maria, Daniela Gheorghe, Crina Muscalu, Andreea Scoban
| preprints.org
This version is not peer-reviewed. Gheorghe Maria  *,Daniela Gheorghe,Crina Muscalu,Andreea Scoban Gheorghe Maria  *,Daniela Gheorghe,Crina Muscalu,Andreea Scoban This version is not peer-reviewed. Currently D-fructose (DF) is produced by enzymatic isomerization of beta-D-glucose (DG) under disadvantageous conditions (equilibrium conversion of 50%, costly fructose separation, glucose isomerase poor stability vs. impurities from preliminary starch saccharification).
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The In Silico Optimization of a Fed-Batch Reactor Used for the Enzymatic Hydrolysis of Chicory Inulin to Fructose by Employing a Dynamic Approach

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By Daniela Gheorghe, Gheorghe Maria, Laura Renea, Crina Muscalu
| MDPI
All articles published by MDPI are made immediately available worldwide under an open access license. No special permission is required to reuse all or part of the article published by MDPI, including figures and tables. For articles published under an open access Creative Common CC BY license, any part of the article may be reused without permission provided that the original article is clearly cited. For more information, please refer to https://www.mdpi.com/openaccess.
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In-Silico Optimization of a FBR Used for the Enzymatic Hydrolysis of Chicory Inulin to Fructose by Employing a Dynamic Approach and Various Numerical Algorithms

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By Daniela Gheorghe, Gheorghe Maria, Laura Renea, Crina Muscalu
| preprints.org
Submitted: 17 February 2025 You are already at the latest version Inulin enzymatic hydrolysis becomes in the last years a very promising alternative to produce fructose on a large scale. Genetically modified chicory was used to extract inulin of industrial quality. By using an adequate kinetic model from literature, the present paper is aiming at determining the optimal operating alternatives of a batch (BR), or a fed-batch (FBR) reactor used for the inulin hydrolysis to fructose.
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