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Gas distribution grid of a "cap" type is used to maximize the efficiency of the reactor of fluidized bed.
Product gases yield, gasification efficiency and exergy conversion efficiency of the reactor were analyzed.
However the different surface morphology of the TiO2 will influence the treatment efficiency of the reactor.
Furthermore, the configuration of reactor is an important factor in the PEC performance, and many researches have been carried on to improve the efficiency of the reactor [14].
The efficiency of the reactor was calculated for different thermal inputs, feed rates, rotational speeds and particle diameters.
The sludge digestion did not have any impact on COD and TP removal efficiency of the reactor.
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To increase the efficiency of the reactors final concentrators were used.
The efficiency of the reactors for volatile organic compound removal from high flow rates of air under Hg lamp irradiation using N F-TiO2 photocatalyst was iN F-TiO2ted.
When compared at an identical applied voltage of 20 kV (inlet ethylene: 200 ppm; adsorption time: 100 min; plasma oxidation time: 20 min), the mineralization efficiency of the hybrid reactor was greater than the sum of those of one- and two-stage reactors, i.e., 63, 42, and 10%, respectively.
The efficiency of the microchamber reactor was found to be one to two orders of magnitude higher than that of a batch reactor.
By comparing the ultraviolet visible (UV vis) absorbance of the original MO solution and the post-treatment sample, the reaction constants were calculated, representing the efficiencies of the reactors.
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Justyna Jupowicz-Kozak
CEO of Professional Science Editing for Scientists @ prosciediting.com