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A general catalytic packed bed membrane reactor model is also presented.
A fluidized bed membrane reactor model for ethanol reforming has been developed and validated with the obtained experimental results.
Our membrane reactor model utilizes one-dimensional, explicit oxygen permeation and five tubular reaction chamber with three kinetic expressions.
A two-dimensional pseudo-homogeneous packed bed membrane reactor model was developed that solves the continuity and momentum equations and the component mass and energy balances.
These differences are shown to be a function of the intrinsic reaction kinetics with the aid of an isothermal membrane reactor model.
A simple membrane reactor model has been employed to investigate the performance of C5/C6 hydroisomerization process on zeolites and compare it to a state-of-the-art total isomerization (TIP) process.
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A model library for spatially distributed membrane reactor models is presented.
Two different membrane reactor models were developed: a 1D phenomenological model and a quasi-lumped model inside the overall system implemented in Aspen Plus.
The membrane reactor has been modelled using a 2D mathematical model, capable of modelling the non-ideal flow pattern formed in this type of reactors.
The immobilisation of an ionically tagged Hoveyda catalyst in an ionic liquid previously supported on a solvent-resistant polyimide membrane (Starmem 228) was prepared leading to an original catalytic membrane successfully used in a membrane reactor for a model metathesis reaction.
of a selective membrane reactor requires a kinetic model (or rate expression) for transport through the membrane and the effects of various co-adsorbates.
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