2013
DOI: 10.1016/j.jenvman.2013.01.041
|View full text |Cite
|
Sign up to set email alerts
|

Photoelectrocatalytic degradation of acid dye using Ni–TiO2 with the energy supplied by solar cell: Mechanism and economical studies

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

1
14
0
1

Year Published

2014
2014
2019
2019

Publication Types

Select...
8

Relationship

0
8

Authors

Journals

citations
Cited by 38 publications
(16 citation statements)
references
References 51 publications
1
14
0
1
Order By: Relevance
“…The increase in conversion level due to the increase of catalyst loading can be explained by an increase in the number of active sites available for photocatalytic reaction on the N,S co‐doped TiO 2 . Consequently, this results in an increase in the number of absorbed photons and adsorbed IBP and this in turn raises the number of oxidative species . The geometry and working conditions of the reactor are the most important factors affecting the threshold value of catalyst loading .…”
Section: Resultsmentioning
confidence: 99%
“…The increase in conversion level due to the increase of catalyst loading can be explained by an increase in the number of active sites available for photocatalytic reaction on the N,S co‐doped TiO 2 . Consequently, this results in an increase in the number of absorbed photons and adsorbed IBP and this in turn raises the number of oxidative species . The geometry and working conditions of the reactor are the most important factors affecting the threshold value of catalyst loading .…”
Section: Resultsmentioning
confidence: 99%
“…Hence commercially available micro-TiO 2 is used in the study as photocatalyst. Olya et al [42] reported the cost per m 3 for treatment of textile wastewater by solar photocatalytic degradation process using Ni-TiO 2 to be around $9.42.…”
Section: Comparison With Nano-tiomentioning
confidence: 99%
“…When the particle electrode reaches a certain amount in the reaction system, the oxidative degradation efficiency of chloramphenicol sharply declines with the continuous increase in the particle filling ratio. The reasons mainly include the following aspects: (a) The current density under a constant condition is not enough to excite polarization of excess particle electrode, and the excess particle electrode will become a high‐impedance material, reducing the mass transfer efficiency of the electron to some extent (Yan et al., ); (b) when the particle electrode is overfilled, excessive particle electrodes may be in contact with each other, leading to short‐circuiting current generation and side reactions (Zhao et al., ); (c) with the further increase in the number of particle electrodes, the 3‐D particle electrode tends to form a whole electrode, continuously decreasing electrocatalytic oxidation reaction area (Olya, Pirkarami, Soleimani, & Bahmaei, ). So, the optimal packing ratio is 50.0%.…”
Section: Resultsmentioning
confidence: 99%