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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.
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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.
The membrane reactor model includes detailed treatments of the catalytic kinetics from the literature, accounts for reaction on the Pd membrane and hydrogen permeation inhibition by site blockage, among other features.
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.
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.
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CEO of Professional Science Editing for Scientists @ prosciediting.com