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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 />

29

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