Adsorption of As(III) from aqueous solutions by iron-impregnated quartz, lignite, and silica sand: kinetic study and equilibrium isotherm analysis

被引:3
作者
Gautam, Shashi B. [1 ]
Vaishya, R. C. [2 ]
Devnani, G. L. [1 ]
Mathur, Anil K. [3 ]
机构
[1] Harcourt Butler Technol Inst, Dept Chem Engn, Kanpur 208002, Uttar Pradesh, India
[2] Motilal Nehru Natl Inst Technol, Dept Civil Engn, Allahabad 211004, Uttar Pradesh, India
[3] Pollut Control Board, Lucknow 226010, Uttar Pradesh, India
关键词
As(III); Kinetics; IOCSS; Isotherms; IOCQS; IOCLS; Adsorption; ARSENIC REMOVAL; ELOVICH EQUATION; CONTAMINATED WATER; COATED SAND; SORPTION; GROUNDWATER; ADSORBENTS; MANGANESE; REACTOR; IONS;
D O I
10.1080/19443994.2013.797182
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this study, adsorption of As(III) removal on iron oxide-coated quartz, iron oxide-coated lignite sand, and iron oxide-coated silica sand were investigated. Batch studies were performed to evaluate the influences of various parameters like initial pH, adsorbent dose, and initial concentration for the removal of As(III). Optimum conditions for As(III) removal on the three adsorbents were found to be pH 7, adsorbent dose 20 g/l of solution, and equilibrium time 6 h. The kinetics study of As(III) removal have also been determined using a pseudo-first-order, pseudo-second-order, Weber and Morris, and Elovich model. Among the conventional models, the q(e,exp) and the q(e,calc) values from the pseudo-second-order kinetic model are very close to each other and followed by Weber-Morris and Elovich model for all adsorbents. In this system, the effective diffusion coefficient (D-e) value of As(III) is more than the order of 10(-9) cm(2)/s. This order shows in the literature that pore diffusion is the rate-limiting step for all the adsorbents. Equilibrium isotherms for the adsorption of As(III) on all the three adsorbents were analyzed by Langmuir, Freundlich, Redlich-Peterson (R-P), and Temkin isotherm models using nonlinear regression technique. R-P and Freundlich isotherm was found to be the best to represent the data for As(III) adsorption on all the adsorbents. The parameters obtained in this study for different kinetic and equilibrium models of all adsorbents are very comparable with other reported values for sand-based and other adsorbents.
引用
收藏
页码:3178 / 3190
页数:13
相关论文
共 46 条
  • [1] AHARONI C, 1979, J CHEM TECHNOL BIOT, V29, P404
  • [2] [Anonymous], 1975, BULLETIN
  • [3] [Anonymous], SOLIDS J PHYS CHEM A
  • [4] ELOVICH EQUATION FOR KINETICS OF ISOTOPIC EXCHANGE REACTIONS AT SOLID-LIQUID INTERFACES
    ATKINSON, RJ
    HINGSTON, FJ
    POSNER, AM
    QUIRK, JP
    [J]. NATURE, 1970, 226 (5241) : 148 - &
  • [5] THE EXCHANGE ADSORPTION OF IONS FROM AQUEOUS SOLUTIONS BY ORGANIC ZEOLITES .2.
    BOYD, GE
    ADAMSON, AW
    MYERS, LS
    [J]. JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1947, 69 (11) : 2836 - 2848
  • [6] Removal of As(III) in a column reactor packed with iron-coated sand and manganese-coated sand
    Chang, Yoon-Young
    Song, Ki-Hoon
    Yang, Jae-Kyu
    [J]. JOURNAL OF HAZARDOUS MATERIALS, 2008, 150 (03) : 565 - 572
  • [7] Arsenic removal by iron-modified activated carbon
    Chen, Weifang
    Parette, Robert
    Zou, Jiying
    Cannon, Fred S.
    Dempsey, Brian A.
    [J]. WATER RESEARCH, 2007, 41 (09) : 1851 - 1858
  • [8] APPLICATION OF ELOVICH EQUATION TO THE KINETICS OF PHOSPHATE RELEASE AND SORPTION IN SOILS
    CHIEN, SH
    CLAYTON, WR
    [J]. SOIL SCIENCE SOCIETY OF AMERICA JOURNAL, 1980, 44 (02) : 265 - 268
  • [9] Goel R, 2004, INDIAN J CHEM TECHN, V11, P518
  • [10] Preparation and evaluation of GAC-based iron-containing adsorbents for arsenic removal
    Gu, ZM
    Fang, J
    Deng, BL
    [J]. ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2005, 39 (10) : 3833 - 3843