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At least elements to calculate the cost of the plant, for both reactors are given.
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Finally, brief concluding remarks on porous ceramic membrane reactors are given and possible future research interests are also outlined.
Comprehensive overviews of the available literature data for glucose removal by membranes and for cellulose enzyme stability in membrane reactors are given.
Brief review of the design, specific features of thermal hydraulics of reactor cores and circulation loops of pool-type research reactors is given.
A survey of recently published research work on solid electrolyte (SE) membrane reactors is given, with focus on high-temperature oxygen ion conductors, high-temperature proton conductors and low-temperature proton conductors.
Main parameters of EAST reactor are given in Table 1 [9].
In this case, recommendations for the design of the reactor are given.
Empirically obtained deposition models for the used symmetrical plasma reactor are given.
The example of calculation of activation reactor is given below.
A design procedure for the reverse flow reactor is given.
The schematic diagram of the subcritical reactor is given in Fig. 1.
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