Heterogeneous kinetics of the reduction of chromium (VI) by elemental iron

被引:60
作者
Fiuza, Antonio [1 ]
Silva, Aurora [2 ]
Carvalho, Goreti [2 ]
de la Fuente, Antonio V. [1 ]
Delerue-Matos, Cristina [2 ]
机构
[1] Univ Porto, CIGAR, Fac Engn, P-4200465 Oporto, Portugal
[2] Inst Politecn Porto, REQUIMTE, Inst Super Engn, P-4200072 Oporto, Portugal
关键词
Chromium reduction; Reactive permeable barriers; Heterogeneous kinetics; ZERO-VALENT IRON; AQUEOUS-SOLUTION; CR(VI) REMOVAL; WATER; GROUNDWATER; NANOPARTICLES; CHROMATE; WASTE;
D O I
10.1016/j.jhazmat.2009.10.116
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Zero valent iron (ZVI) has been extensively used as a reactive medium for the reduction of Cr(VI) to Cr(III) in reactive permeable barriers. The kinetic rate depends strongly on the superficial oxidation of the iron particles used and the preliminary washing of ZVI increases the rate. The reaction has been primarily modelled using a pseudo-first-order kinetics which is inappropriate for a heterogeneous reaction. We assumed a shrinking particle type model where the kinetic rate is proportional to the available iron surface area, to the initial volume of solution and to the chromium concentration raised to a power a which is the order of the chemical reaction occurring at surface. We assumed alpha = 2/3 based on the likeness to the shrinking particle models with spherical symmetry. Kinetics studies were performed in order to evaluate the suitability of this approach. The influence of the following parameters was experimentally studied: initial available surface area, chromium concentration, temperature and pH. The assumed order for the reaction was confirmed. In addition, the rate constant was calculated from data obtained in different operating conditions. Digital pictures of iron balls were periodically taken and the image treatment allowed for establishing the time evolution of their size distribution. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:1042 / 1047
页数:6
相关论文
共 16 条
[1]   Cr(VI) removal from aqueous solution by iron (III) hydroxide-loaded sugar beet pulp [J].
Altundogan, HS .
PROCESS BIOCHEMISTRY, 2005, 40 (3-4) :1443-1452
[2]   In-situ remediation of Cr(VI)-contaminated groundwater using permeable reactive walls: Laboratory studies [J].
Blowes, DW ;
Ptacek, CJ ;
Jambor, JL .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 1997, 31 (12) :3348-3357
[3]  
BLOWES DW, 1996, DESIGN INSTALLATION, V1
[4]   Chromate reduction in wastewater at different pH levels using thin iron wires - A laboratory study [J].
Chang, LY .
ENVIRONMENTAL PROGRESS, 2005, 24 (03) :305-316
[5]   Hexavalent chromium removal by ferrochromium slag [J].
Erdem, M ;
Altundogan, HS ;
Turan, MD ;
Tümen, F .
JOURNAL OF HAZARDOUS MATERIALS, 2005, 126 (1-3) :176-182
[6]   Chromium removal from aqueous solution by ferrite process [J].
Erdem, M ;
Tumen, F .
JOURNAL OF HAZARDOUS MATERIALS, 2004, 109 (1-3) :71-77
[7]   Kinetics of hexavalent chromium reduction by scrap iron [J].
Gheju, M. ;
Iovi, A. .
JOURNAL OF HAZARDOUS MATERIALS, 2006, 135 (1-3) :66-73
[8]   THE KINETICS OF HEXAVALENT CHROMIUM REDUCTION BY METALLIC IRON [J].
GOULD, JP .
WATER RESEARCH, 1982, 16 (06) :871-877
[9]   Removal of chromium from synthetic plating waste by zero-valent iron and sulfate-reducing bacteria [J].
Guha, S ;
Bhargava, P .
WATER ENVIRONMENT RESEARCH, 2005, 77 (04) :411-416
[10]   Comparative study of various magnetic nanoparticles for Cr(VI) removal [J].
Hu, Jing ;
Lo, Irene M. C. ;
Chen, Guohua .
SEPARATION AND PURIFICATION TECHNOLOGY, 2007, 56 (03) :249-256