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The model elucidates the complex spatiotemporal processes occurring within the washcoat and along the reactor length.
New results are obtained for reactor length and optimal cost of reactor.
By solving this optimization problem, it has been shown that an optimal reactor length exists.
Control is accomplished using secondary measurements of temperature along the reactor length.
The model predicts liquid phase chemical conversions and the interfacial temperatures along the reactor length.
The effects of reactor length and outer wall thickness are also explored.
A much higher reactor length of a tubular MR is necessary to achieve the same conversion.
Simple algebraic equations are derived to predict the temperature rise along the reactor length.
This is drastically affected by the liquid viscosity and in some extent by the reactor length and the foam thickness.
Implicit finite difference method solved the equations on the considered reactor length (50 cm) and diameter (20 cm).
The optimisation parameters studied were: the carrier flow rate, the lengths of the sample and reagent loops, and reactor length.
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