2018
DOI: 10.1007/s41742-018-0102-2
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Improvement of Carbamazepine Degradation by a Three-Dimensional Electrochemical (3-EC) Process

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Cited by 15 publications
(15 citation statements)
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“…Studies verify the performance of three-dimensional (3D) was much better, more cost-effective, and saved more energy than traditional two-dimensional (2D). The highest efficiency was recorded in the 3D process for removing carbamazepine compared to a 2D electrochemical process [68]. Furthermore, using a 3D electrode reactor to treat estriol, in batch mode, exhibited reaction rate per unit area was significantly higher and lower energy consumption than conventional 2D electrode…”
Section: Dsamentioning
confidence: 95%
“…Studies verify the performance of three-dimensional (3D) was much better, more cost-effective, and saved more energy than traditional two-dimensional (2D). The highest efficiency was recorded in the 3D process for removing carbamazepine compared to a 2D electrochemical process [68]. Furthermore, using a 3D electrode reactor to treat estriol, in batch mode, exhibited reaction rate per unit area was significantly higher and lower energy consumption than conventional 2D electrode…”
Section: Dsamentioning
confidence: 95%
“…Recently, biochars (waste biomass pyrolysis products) have drawn attention as alternative adsorbents to activated carbon due to their physicochemical properties and widespread availability [33]. Besides adsorption, electrochemical processes have gained increasing interest in recent years to treat polluted waters, and were applied by Alighardashi et al [34] to remove CBZ from wastewaters. Electrochemical systems offer several advantages, such as simple operation (at ambient temperature and pressure), robust performance, the capability to adjust to variations in the influent composition and flow rate [35], and viability in degrading nonbiodegradable pollutants [36].…”
Section: Introductionmentioning
confidence: 99%
“…The removal of pollutants in 3D systems is 10-50% higher than in 2D systems, while simultaneously reducing energy consumption [35]. Alighardashi et al [34] applied a 3D electrochemical process for CBZ degradation employing two aluminum electrodes, as both anode and cathode, and powdered activated carbon as the particulate electrode, achieving a removal efficiency of 89.8%.…”
Section: Introductionmentioning
confidence: 99%
“…The traditional 2D electrochemical reactor, including cathodes and anodes, has the mass transfer limitation and the low area-volume ratio [20][21][22]. On the other hand, 3D electrochemical reactor promotes the mass transfer efficiency, current efficiency, and decreases the energy consumption, whereas relatively low cyclic stability is still an issue [23][24][25].During the process of pollutants oxidization in the 2D reactor, the DSA electrode became inactive due to corrosion and the coatings dispersed in solution that also cannot be recycled, which result in serious material waste [26]. In our previous work [27,28], a new electrolytic cell type named 2.5D electrode system was proposed, as shown in Scheme 1.…”
mentioning
confidence: 99%
“…The traditional 2D electrochemical reactor, including cathodes and anodes, has the mass transfer limitation and the low area-volume ratio [20][21][22]. On the other hand, 3D electrochemical reactor promotes the mass transfer efficiency, current efficiency, and decreases the energy consumption, whereas relatively low cyclic stability is still an issue [23][24][25].…”
mentioning
confidence: 99%