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

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

Jason Price (JAPR)<br />

<strong>CAPEC</strong>-<strong>PROCESS</strong><br />

Alberto Quaglia (AQ)<br />

important in chemical process-product design. However, due to<br />

the increased complexity of the molecular structures of<br />

chemicals, their wider applications, and demands for greater<br />

accuracy, extension and analysis of the current prediction<br />

methods as well as development of new models are necessary.<br />

Therefore, the combination of group-contribution (GC) and<br />

atom connectivity (CI) (the GC Plus approach) that is able to<br />

extend the application range of the host property model has been<br />

developed and extended to predict the UNIFAC GC-model<br />

parameters (see PEC09-17). The objectives of this PhD-project<br />

is to analyze the performance of the GC Plus approach in VLE and<br />

SLE calculations and based on it, to extend and further develop<br />

the GC Plus approach for other versions of the UNIFAC models<br />

and to apply the models for chemical process synthesis and<br />

design.<br />

Supervisors: RaG, GK<br />

Start: 01-04-2009; End: 31-09-2012<br />

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

Operation and Control of Enzymatic Biodiesel Production<br />

This work explores the control of biodiesel production via an<br />

enzymatic catalyst. Currently enzymatic catalysts are not in<br />

widespread use for commercial-scale biodiesel production. This<br />

is mainly due to non-optimized process designs. Furthermore is<br />

it unclear what process variables need to be monitored and<br />

controlled to ensure optimal economics. Critical to the project is<br />

to develop a control methodology to optimize the productivity<br />

of biodiesel production. The implementation of a control system<br />

to handle changes in the feed composition and the correct<br />

dosing of alcohol can potentially lead to very large energy<br />

savings and at the same time provide a more consistent product<br />

quality. However given most conversion and quality analyses of<br />

biodiesel are commonly done by chromatographic methods,<br />

suitable measurement techniques will need to be investigated to<br />

obtain real-time information on the states of the system.<br />

The main deliverable is a steady state and dynamic simulation<br />

model of the process including a strategy for monitoring and<br />

process control. This model and the proposed strategies will be<br />

validated experimentally on the department’s pilot facilities.<br />

Supervisors: JW, JKH, MAN<br />

Start: 01-09-2011; End: 01-10-2014<br />

Research area: B, D<br />

Incremental refinement of process design<br />

Process Simulation is not common in the food and biofuels<br />

industries, mainly due to the complexity of thermodynamics and<br />

transport properties of the species involved.<br />

37

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