2015
DOI: 10.1016/j.electacta.2015.05.135
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Characterization of hydrodynamics and mass transfer in two types of tubular electrochemical reactors

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Cited by 51 publications
(25 citation statements)
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“…Other parameters, such as temperature (T), pH value, and electricity can be obtained when the influent quality and flow rate are held constant in the electrolytic cell. The kinetic constant K is only related to current density ( j ) under the conditions of the original pH of 3 and Na 2 SO 4 concentration of 0.10 mol L −1 [11].…”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…Other parameters, such as temperature (T), pH value, and electricity can be obtained when the influent quality and flow rate are held constant in the electrolytic cell. The kinetic constant K is only related to current density ( j ) under the conditions of the original pH of 3 and Na 2 SO 4 concentration of 0.10 mol L −1 [11].…”
Section: Resultsmentioning
confidence: 99%
“…Conventional mathematical or mechanistic models can be used to predict the final state of the system only under given circumstances [10]. Wang et al [11] calculated the velocity distribution and turbulence distribution of a new type of tubular plunger flow reactor by CFD. CFD can reveal the mass transfer process and mechanism of an electrochemical reactor, but it is still affected by grid mass, transfer mode, and calculation [12,13].…”
Section: Introductionmentioning
confidence: 99%
“…Besides the acquisition of numerical data, the visual representation of a wide variety of parameters facilitates the understanding of the system. In the last decade, different research groups have made use of this type of software to improve and understand systems such as AO, EC and EF, for example, Figure 3a shows the mixing comparison of a vertical-flow tubular and a concentric tubular electrochemical reactors, as can be seen the turbulent intensity of wastewater was higher around the electrodes in the former reactor, which translates as a better mass transfer of the active substances towards the electrodes surface (Wang et al, 2015), Figure 3b illustrates the current distribution in the electrodes of an EC reactor (Villalobos-Lara et al, 2020) and Figure 3c shows the generation of Fe 2+ that takes place in the cathode due to the reduction of Fe 3+ after different time intervals during the EF process (Reza et al, 2015).…”
Section: Computational Fluid Dynamics In Electrochemical Reactorsmentioning
confidence: 99%
“…Compilation of representative publications on stand-alone electrochemical processes applied to the treatment of highly polluted wastewater. [Adapted with permission from: (Wang, Li et al 2015) (Villalobos-Lara et al, 2020 and (Reza, Masoud et al 2015)]. Copyright Elsevier.…”
Section: Declaration Of Interest Statementmentioning
confidence: 99%
“…As a result, the mass transfer coefficient of the ow cell strongly affects its oxidation performance. 29,30 Although a surface-modied BDD electrode has an effective surface area that is several times larger, its lower mass transfer rate leads to a bulky double-layer charge region, resulting in a net negative effect. Therefore, a more precise design of the electrode surface that considers the effect on mass transport is required for electrochemical oxidation applications.…”
Section: 2728mentioning
confidence: 99%