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

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Rita Lencastre Fernandes<br />

(RLF)<br />

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

Amol S Hukkerikar (AMH)<br />

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

Population balance models and computational fluid dynamics:<br />

a model framework to describe heterogeneity in fermentors<br />

The project focuses on the development of models that can<br />

predict the growth and behaviour of heterogeneous microbial<br />

populations. Experimental data is used to formulate Matlab<br />

based models that can predict changes in the microbial<br />

distributed properties (e.g. single cell protein content, growth<br />

and productivity) due to varying environmental conditions in the<br />

fermentor. In a later stage, the population model will be<br />

integrated with a fluid dynamics model for a stirred reactor,<br />

allowing for predicting process behavior under different<br />

environmental conditions. The project is partly funded by the<br />

Danish Council for Strategic Research in the frame of the<br />

project "Towards robust fermentation processes by targeting<br />

population heterogeneity at microscale", and developed in tight<br />

collaboration with the ERA-NET Industry Biotechnology<br />

project "Targeting population heterogeneity at microscale for<br />

robust fermentation processes".<br />

Supervisors: KVG, AJ, Ingmar Nopens (Ghent Univ)<br />

Started: 01-11-2009; Finish: 07-12-2012<br />

Research area: Process-product modelling/design<br />

Model based integrated process-product design - retrofitting<br />

and optimisation<br />

The main objective of this project is to develop a systematic<br />

framework for model based design and optimisation of the<br />

principal unit operations involved in edible oil/bio-fuel industry<br />

and apply the developed methodology for improvement in the<br />

performance of existing installations for edible oil/bio-fuel<br />

processes. Although the oleo-chemical industry is mature and<br />

based on well established processes, the complex systems that<br />

lipids compounds form, and the lack of accurate unit operation<br />

models have limited a wide application of computer aided<br />

methods and tools for process synthesis, modeling and<br />

simulation within this industry. In consequence, the first part of<br />

this project will be the development of unit operations model<br />

library consisting of a collection of new and adopted models<br />

that are not available in existing process simulation tools. The<br />

second part of the work will focus on application of developed<br />

models for optimisation of existing processes with respect to<br />

performance indicators such as minimum operational cost,<br />

product yield improvement and sustainability index.<br />

Supervisors: RaG, GSI, Bent Sarup (Alfa Laval).<br />

Started: 01-07-2010; Finish: 30-06-2013<br />

Research area: A, B, C, E<br />

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