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The basic reactor set up was the same as described by van den Berg et al. (2015).
Two kinds of reactors are considered: a basic reactor and constructal reactors with different scales, from 1 to i scales.
The continuous cyclic operation of a packed-bed chemical looping combustion process is described using a basic reactor model.
The next two sections set forth basic reactor models for commonly used reactor types, including mechanically agitated reactors and bubble column reactors.
Basic reactor models and assumptions based on an ideal plug flow pattern have been used in all the reactors during the chemical reactions and the heat transfer operations.
Optimal design for a basic reactor module with one lamp was accomplished for lamp-diameter-to-plate-height ratio of 0.7, while the plate-spacing-to-plate-height ratio was correlated by [αoptimum = 0.191 β2 − 0.5597 β + 0.3854].
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Each basic unit reactor consists of microchannel patterned stainless sheets.
Traditionally, design of low-temperature processes begins with the basic process (reactors and separators).
Kinetics model which describes intrinsic characteristics of reactions involved in Chemical Looping Combustion (CLC) can be used as a basic tool for reactor design and reactor modeling.
A brief introduction to the basic objectives of reactor design and the various types of reactors used in the chemical industry is given.
An overview of cavitational reactors in the specific area of water disinfection, in terms of the basic mechanism, different reactor designs including recommendations for optimum operating parameters and applicability of the cavitation phenomena for disinfection of different micro-organisms have been presented.
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