PEC12-25 CAPEC-PROCESS Industrial Consortium ... - DTU Orbit
PEC12-25 CAPEC-PROCESS Industrial Consortium ... - DTU Orbit
PEC12-25 CAPEC-PROCESS Industrial Consortium ... - DTU Orbit
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<strong>PROCESS</strong><br />
Supervisor: JW<br />
Start: 10-01-2011; End: 09-01-2013<br />
Paloma Andrade Santacoloma<br />
(PSA)<br />
<strong>PROCESS</strong><br />
Supervisors: JW, KVG, GSI<br />
Start: 01-11-2008; End: 31-10-2011<br />
placed on the process, such as oxidation reactions. In this<br />
project, oxidation reactions catalyzed by oxidases and/or<br />
Baeyer-Villiger monooxygenases will be used as model<br />
reactions to develop a standardized methodology, a “process<br />
discovery platform”, which will guide researchers in the<br />
establishment of cost-efficient and environmentally friendly<br />
industrial bioprocesses.<br />
In the first instance, scale-down laboratory reactors and<br />
processes will be used to assess new configurations and<br />
modes of operation. In the latter stages of the project, pilotplant<br />
trials will serve as an assessment and a demonstration of<br />
the new process technology on selected targets. After<br />
collection of kinetic, stability and thermodynamic data, these<br />
will be used for process modelling from a technical and<br />
economic perspective. In order to evaluate also the<br />
environmental benefits, simplified life cycle assessments of<br />
the developed technologies will be performed.<br />
Collaborators: UCL-London, Slovak Univ of Tech, CLEA<br />
Technologies B.V., LentiKat´s a.s.<br />
Multi-enzyme process modelling<br />
Nowadays multi-enzyme processes are seen as an alternative<br />
to assist in the synthesis of complex compounds of industrial<br />
interest. In general, a multi-enzyme in-pot process is<br />
characterized by the mixture of enzymes that catalyze several<br />
reactions in a single pot. Therefore, the individual enzyme<br />
contributes with its specific action driving thus a given<br />
transformation to the subsequent one until the desired product<br />
is obtain. In this manner, purification steps of intermediate<br />
products may be eliminated. Consequently, it potentially<br />
leads to considerable process improvements like increases in<br />
the process yield and reduction in downstream processing and<br />
operating costs.<br />
Reliable mathematical models of such multi-catalytic<br />
schemes can improve the potential benefit of this technology.<br />
In that manner, the best outcome of the process can be<br />
obtained on the basis of a thorough understanding of what<br />
modifications in the system are required to optimize the use<br />
of enzymes. In order to do this evaluation effectively, a<br />
methodological framework is developed for the mathematical<br />
modeling of these processes, integrated with a computeraided<br />
methodology which enable the analysis of models,<br />
simulations, parameter estimation, sensitivity analysis, multiobjective<br />
criteria evaluation and the like. The idea is to use<br />
the models to find either promising configurations for<br />
experimental validation, or, evaluate and analyze an existing<br />
process under different conditions by simulation, to identify<br />
opportunities for improvement.<br />
Research area: Process technology and units operations<br />
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