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A 250 mL membrane reactor system was constructed as shown in Fig. 1.
For the operability analysis, a nonlinear model that describes the membrane reactor system is derived.
In this paper we report an analysis of performance data from a catalytic membrane reactor system published by Pashkova et al. in 2010 [1].
A technical solution and development of a method for on-line HPLC monitoring of bioreactor processes in a membrane reactor system are presented.
The design represents a first step to a compact and efficient microchannel membrane reactor system for production and separation of hydrogen.
The workability of the prototype was validated by comparing the process data at microscale to those obtained using a lab-scale membrane reactor system.
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The National Science Foundation got a bit more down to the point in its appeal for "reactor engineering applications" (including, but not limited to, membrane reactor systems and supercritical fluid applications).
Anodic alumina membranes exhibit pore structure and gas permeability characteristics useful in designing integrated gas separation and catalytic membrane reactor systems.
One method that has been shown to decrease product inhibition and/or increase water availability is the utilisation of membrane reactor systems which remove monomeric sugars after they are produced [ 21, 22].
Isothermal, two-dimensional models are employed to compare performance of a CCP membrane system against (i) an un-modified permselective film in a gas purification membrane (GPM) system, and (ii) an equivalent packed-bed membrane reactor (PBMR) system, for coupling water gas-shift reaction water gas-shiftation freactionpical heavy hydrocarbon reformate mixture (9%CO, 28%H2, 15%H2O, 3%CO2).
The obtained results were in line with those of Jabornig and Favero (2013) who used Moving Bed Biofilm Membrane Reactor (MBBMR) system for treatment of greywater, while their reported TSS removal efficiency was 98%.
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