2022
DOI: 10.1039/d2nj02313j
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Enhanced Cr(vi) removal by hierarchical CoFe2O4@SiO2–NH2via reduction and adsorption processes

Abstract: In order to highly effective removal of toxicity Cr (VI), 3D porous CoFe2O4@SiO2-NH2 has been successfully fabricated. As expected, the saturated adsorption capacity of the resulting CoFe2O4@SiO2-NH2 composite toward Cr...

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Cited by 5 publications
(3 citation statements)
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“…utilized mesoporous carbon for the removal of lead and copper, 10 while Zhou et al employed hierarchical magnetic CoFe 2 O 4 @SiO 2 –NH 2 as a promising adsorbent for Cr( vi ) removal. 12 Despite the use of commercial adsorbents, there is an increasing need for developing highly efficient and economical materials for metal adsorption. A sustainable remediation method should exhibit high pollutant removal performance, economical, simple operation, and environment-friendly processes.…”
Section: Introductionmentioning
confidence: 99%
“…utilized mesoporous carbon for the removal of lead and copper, 10 while Zhou et al employed hierarchical magnetic CoFe 2 O 4 @SiO 2 –NH 2 as a promising adsorbent for Cr( vi ) removal. 12 Despite the use of commercial adsorbents, there is an increasing need for developing highly efficient and economical materials for metal adsorption. A sustainable remediation method should exhibit high pollutant removal performance, economical, simple operation, and environment-friendly processes.…”
Section: Introductionmentioning
confidence: 99%
“…The Cr(VI)-removal performance could be promoted by combining the excellent adsorption effects and the reduction properties. Fe-ethylene glycol complex microspheres [136], mesoporous amino-group-functionalized iron/silica hollow spheres (Fe/SiO2-NH2 HSs) [137] and 3D porous CoFe2O4@SiO2-NH2 [138] have been applied in Cr(VI)-contaminated-water remediation. To realize the resourceful utilization of industrial waste, the Fe-P slag was employed as a reductive agent for Cr(VI) removal by a simplified industrial procedure, providing some new and feasible thoughts for the resourceful utilization of industrial waste in Cr wastewater treatment [139].…”
Section: Reductive Adsorbentsmentioning
confidence: 99%
“…FeMnOx/MWCNTs C0 = 50 mg/L; adsorbent dose: 1 g/L; contact time: 60 min; pH: 2.0 47.25 mg/g [34] Cr(III) GO@CZ C0 = 30 mg/L; adsorbent dose: 300 mg/L; contact time: 60 min; pH = 7.0 285.71 mg/g [43] Cr(VI) Gr-Si-PPy C0 = 100 mg/L; adsorbent dose: 400 mg/L; T = 25 °C; contact time: 60 min; pH: 2.0 429.2 mg/g [47] Cr(VI) GO@SiO2@C@Ni-400 C0 = 20 mg/L; T = 25 °C; adsorbent dose: 0.15 g/L; pH = 3.0 299.20 mg/g [50] Cr(VI) GO-NiFe LDH C0 = 20 mg/L; T = 30 °C; contact time: 280 min; adsorbent dose: 80 mg/L 53.6 mg/g [51] Cr(VI) Fe3O4-GO C0 = 600 mg/L; T = 25 °C; adsorbent dose: 125 mg/L; pH = 6.0 280.6 mg/g [55] Cr(VI) TSGA C0 = 50 mg/L; T = 25 °C; adsorbent dose: 800 mg/L; contact time: 40 min; pH = 2.0 100% removal [60] Cr(VI) APTES-NPSi C0 = 200 mg/L; T = 25 °C; adsorbent dose: 5 mg; contact time: 180 min; pH = 2.0 103.75 mg/g [64] Cr(VI) MnFe-LDH/MnFe2O3@3DNF C0 = 300 mg/L; T = 25 °C; contact time: 120 min; adsorbent dose: 5 mg; pH = 2.0 564.88 mg/g [121] Cr(VI) 3D porous CoFe2O4@SiO2-NH2 C0 = 150 mg/L; contact time: 600 min; adsorbent dose: 1 g/L; T = 25 °C; pH = 2.0 126.8 mg/g [138] Cr(VI) TCMR C0 = 150 mg/L; contact time: 360 min; adsorbent dose: 2 g/L; T = 25 °C; pH = 5.0 27.04 mg/g [150] Cr(VI) Rice husk C0 = 100 mg/L; contact time: 60 min; adsorbent dose: 50 g/L; T = 25 °C; pH = 5.0-6.0 30 mg/g [158] Cr(VI) BCS and BCW C0 = 320 mg/L; contact time: 24 h; adsorbent dose: 4 g/L; T = 25 °C; pH = 2.0 24.6 mg/g for BCS, 23.6 mg/g for BCW [159] Cr(VI) SDBC C0 = 100 mg/L; contact time: 24 h; adsorbent dose: 1 g/L; T = 25 °C; pH = 5.0 688~738 μmol/g [161] Cr(VI) ZBC C0 = 100 mg/L; contact time: 600 min; adsorbent dose: 4 g/L; T = 25 °C; pH = 1.0 33.87 mg/g [175] Cr Cr(VI) Co/Zn-based ZIF C0 = 15.0 mg/L; contact time: 30 min; adsorbent dose: 33 mg; T = 25 °C; pH = 6.5 69.4 mg/g [191] Cr(VI) NH2-SBA-15 C0 = 25.0 mg/L; contact time: 4 h; adsorbent dose: 100 mg; T = 30 °C; pH = 2.0 Removal efficiency of 88% [192] Cr(VI) Ficus carica bast fiber C0 = 350.0 mg/L; contact time: 210 min; adsorbent dose: 0.5 g; T = 25 °C; pH = 3.0 19.68 mg/g [193] Cr(VI) and Cr(III)…”
Section: Cr(vi)mentioning
confidence: 99%