4.6 Article

Performance, Reaction Pathway and Kinetics of the Enhanced Dechlorination Degradation of 2,4-Dichlorophenol by Fe/Ni Nanoparticles Supported on Attapulgite Disaggregated by a Ball Milling-Freezing Process

Journal

MATERIALS
Volume 15, Issue 11, Pages -

Publisher

MDPI
DOI: 10.3390/ma15113957

Keywords

disaggregated attapulgite; Fe/Ni bimetallic nanoparticles; 2,4-dichlorophenol; dechlorination degradation; reaction pathway; kinetics

Funding

  1. Key Project of Natural Science Foundation of China [41230638]
  2. Guiding Project of Science and Technology Research of Education Department of Hubei Province [B2020019]

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The ball milling-freezing-disaggregated attapulgite was used to disperse Fe/Ni nanoparticle clusters into single spherical particles, resulting in the formation of D-ATP-nFe/Ni composite material. This composite material exhibited improved dechlorination degradation of 2,4-dichlorophenol compared to ATP-nFe/Ni, with smaller particle size, larger specific surface area, higher degradation rate, and higher phenol yield. The main dechlorination pathway involved direct reduction to phenol, while the secondary pathway involved the removal of one chlorine atom to generate intermediate compounds.
Attapulgite (ATP) disaggregated by a ball milling-freezing process was used to support Fe/Ni bimetallic nanoparticles (nFe/Ni) to obtain a composite material of D-ATP-nFe/Ni for the dechlorination degradation of 2,4-dichlorophenol (2,4-DCP), thus improving the problem of agglomeration and oxidation passivation of nanoscale zero-valent iron (nFe) in the dechlorination degradation of chlorinated organic compounds. The results show that Fe/Ni nanoparticle clusters were dispersed into single spherical particles by the ball milling-freezing-disaggregated attapulgite, in which the average particle size decreased from 423.94 nm to 54.51 nm, and the specific surface area of D-ATP-nFe /Ni (97.10 m(2) / g) was 6.9 times greater than that of nFe/Ni (14.15 m(2) /g). Therefore, the degradation rate of 2,4-DCP increased from 81.9% during ATP-nFe/Ni application to 96.8% during D-ATP-nFe/Ni application within 120 min, and the yield of phenol increased from 57.2% to 86.1%. Meanwhile, the reaction rate K o b s of the degradation of 2,4-DCP by D-ATP-nFe/Ni was 0.0277 min(-1), which was higher than that of ATP-nFe/Ni (0.0135 min(-1)). In the dechlorination process of 2,4-DCP by D-ATP-nFe/Ni, the reaction rate for the direct dechlorination of 2,4-DCP of phenol (k(5) = 0.0156 min(-1)) was much higher than that of 4-chlorophenol (4-CP, k(2) = 0.0052 min(-1)) and 2-chlorophenol (2-CP, k(1) = 0.0070 min(-1)), which suggests that the main dechlorination degradation pathway for the removal of 2,4-DCP by D-ATP-nFe/Ni was directly reduced to phenol by the removal of two chlorine atoms. In the secondary pathway, the removal of one chlorine atom from 2,4-DCP to generate 2-CP or 4-CP as intermediate was the rate controlling step. The final dechlorination product (phenol) was obtained when the dechlorination rate accelerated with the progress of the reaction. This study contributes to the broad topic of organic pollutant treatment by the application of clay minerals.

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