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For complex reactions, the choice of reactor type is important for attaining optimum product yields.
A decision tree to aid the choice of reactor design features is provided.
A decision to proceed might be made in 2007, followed by a commercial choice of reactor and supplier, a safety licensing process, a public inquiry and a period for construction and commissioning.
The literature gives little guidance on the factors (e.g. choice of reactor, sequence of adding reagents, imperfect mixing) determining the product distribution of parallel reactors.
The drawability and the uniformity of the resultant fibres and films are sensitively affected by the drawing temperatures and rates, and also by the choice of reactor powder.
The rationale for the choice of reactor is discussed and a CuO/Al2O3 based oxygen carrier has been selected for the initial reactor evaluation.
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The choice of reactors was based on experimental temperature: 15 mL passivated HIP® Titanium 64 tube reactors (200°C); 20 mL I-Chem® borosilicate vials with PTFE/Si septum caps (70°C) and 15 mL BD HDPE Falcon® tubes (22°C).
The state-of-the-art in paraffin oxidation and the main features that affect the choice of the reactor and the process configuration are discussed.
Utilization of the produced heat is crucial and the choice of the reactor should be done with respect to the catalyst stability properties.
When the enzyme stabilization is not fully successful, the optimal choice of the reactor type and operation mode is depending on the process and enzyme deactivation characteristics.
One essential engineering problem when developing an industrial enzymatic process concerns the choice of the reactor operating alternative based on à-priori knowledge of the process kinetics and enzyme inactivation characteristics.
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