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To design the micro-PrOx reactor, the effects of channel length, channel width, channel array, and O2 content in the reactant gas on the CO conversion and selectivity for CO were investigated.
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In the novel sonochemical reactor, the effect of frequency of irradiation on the rates of degradation has also been investigated.
Using a mathematical model of a terrace wall reactor, the effect of catalyst shape on performance of the reactor has been studied.
In the research and design of small modular reactor, the effect of ocean motions on the two phase flow instability should be evaluated.
In the developed reactor, the effect of four factors including initial phenol concentration, TiO2 concentration, turbidity, and pH on phenol removal efficiency is investigated using full factorial design.
For a single-zone autoclave reactor, the effect of imperfect mixing in the reactor is analyzed using both an imperfect mixing model and a perfect mixing model with temperature variant initiator-efficiency factor.
The predictions of the model are compared to experimental data for various gas and liquid flow rates to describe dynamic events, such as the start-up of the reactor and the effects of sudden changes in the operating conditions on the reactor behaviour and its thermal stability.
The decomposition activity of the designed reactor and the effects of a combination of ozone, UV, and TiO2 were examined.
For stirred multiphase reactors the effect of a dispersed (gas, liquid or solid) phase on the product distribution for a mixing sensitive reaction was tested.
The predicted reactor characteristics are shown to agree with large-scale reactor performance, and the effects of the most sensitive parameters are elucidated to provide a basis for reactor optimization.
Reactor configuration and addition of soil had the biggest effects on reactor performance, while the effects of organic loading rates and feed composition were less marked.
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Justyna Jupowicz-Kozak
CEO of Professional Science Editing for Scientists @ prosciediting.com