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PEC12-25 CAPEC-PROCESS Industrial Consortium ... - DTU Orbit

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3.3 Post-Doctoral Research Project Overview<br />

Miguel Mauricio Iglesias<br />

(MMI)<br />

<strong>CAPEC</strong><br />

Supervisors: GSI<br />

Start: 01-01-2012; End: 30-09-2012<br />

Mathias Nordblad (MAN)<br />

<strong>PROCESS</strong><br />

Supervisors: JW<br />

Start: 01-12-2008; End: 31-11-2012<br />

Model-based scale-up of bioprocesses<br />

Scale-up is an important step in the development and<br />

commercialization of new process technologies in many<br />

industries, for production of chemicals such enzymes,<br />

antibiotics or materials such as bioplastics. Moving a<br />

fermentation process from a lab-scale to a commercial/<br />

production scale remains still challenging due to a number of<br />

factors that affects biological response of cells to changing<br />

conditions from cultivation. Scale-up problems may arise<br />

then due to inadequate interphase mass transfer, heat removal<br />

and non-uniform temperature and concentration gradients in<br />

the reactor. As a result, many large-scale fermentation<br />

processes give a lower yield than achieved in the laboratory.<br />

This project conducted as part of DSF funded EcoDesign<br />

aims at developing a framework for scale-up of bioreactors<br />

based on data and information translated into quantitative<br />

knowledge using models. The framework allows using<br />

multiobjective scale-up principles and various degree of<br />

models, from first-principles to empirical (e.g. response<br />

surface type models based on experimental data) to hybrid<br />

models.<br />

Research area: B, D<br />

Process design and evaluation for enzymatic biodiesel<br />

production<br />

Biodiesel is one of the more established renewable fuel<br />

alternatives. It is traditionally produced using alkaline<br />

catalysis, which comes with certain limitations.<br />

The use of enzymatic catalysis promises several advantages<br />

over traditional production method, including higher yields,<br />

compatibility with a wider range of oil feedstocks and a safer<br />

process. Additionally, the mild reaction conditions also<br />

reduce the need for product purification and increase the<br />

value of the by-product glycerol. However, the process<br />

requires development and optimization to meet criteria for<br />

performance and operating costs.<br />

The focus of this project is the reaction and process design<br />

for enzymatic biodiesel production, based on evaluation of<br />

the performance of individual unit operations and overall<br />

process economics. The project is part of, and supported by, a<br />

larger collaboration looking into catalyst and reactor<br />

performance in enzyme-catalyzed biodiesel reactions, as well<br />

as system thermodynamics and sustainability issues.<br />

Collaborators: Emmelev; Novozymes; Aarhus University;<br />

<strong>DTU</strong> Management

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