Investigations on arsenic(V) removal by modified calcined bauxite

被引:70
作者
Bhakat, P. B. [1 ]
Gupta, A. K. [1 ]
Ayoob, S. [1 ]
Kundu, S. [1 ]
机构
[1] Indian Inst Technol, Dept Civil Engn, Environm Engn Div, Kharagpur 721302, W Bengal, India
关键词
As(V) removal; modified calcined bauxite; kinetics; isotherms; breakthrough curve;
D O I
10.1016/j.colsurfa.2006.02.045
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The present study suggests a solution to the real life problem of arsenic poisoning of potable ground water by examining the use of calcined bauxite, a locally available adsorbent in a modified form, for arsenic(V) scavenging. This adsorbent (modified calcined bauxite, MCB) exhibited excellent As(V) removal (99-100%) over a wide range of pH similar to 2-8 in batch studies. In the neutral pH range (pH similar to 7), the intensity of adsorption increased from 0.099 to 1.37 mg g(-1) corresponding to initial As(V) concentrations of 0.5-8 mg l(-1) with a dose of 5 g I-1 within 3 h. The sorption kinetics was found to follow the pseudo-second order model. The Langmuir, Freundlich and Dubinin-Radushkevich models were tried to represent the equilibrium data of As(V) adsorption. The removal of As(V) can be best modeled using Langmuir isotherm which renders the maximum adsorption capacity as 1.566 mg g(-1). The sorption process was almost unaffected by temperature variations.. During sorption, no appreciable ionic effects except from SO42- and EDTA complex were observed from the background ions Ca2+, Fe3+, Cl-, NO3-, PO43- and F-. The most distinguishing characteristic was the pH of the effluent within the drinking water range of 6-7.5. The column study results show that at a sorbent bed depth of 10 cm and feed flow rate of 8 ml min(-1), the MCB media was capable of treating 8.161 (260 bed volumes) of As(V) spiked water (C-0 = 2 mg l(-1)) before breakthrough. The values of adsorption rate coefficient (K) and adsorption capacity coefficient (N) are calculated using Logit method of column design and were found to be 0.24671 mg(-1) h(-1) and 865.85 mg l(-1), respectively. The XRD data analysis describes chemical combinations of the sorption mechanism. The consistency in arsenic sorption over a wide pH range, availability and adaptability in the local environment, excellent sorption potential, least interference from most of the anions, negligible temperature effects and quality of the treated water makes it an ideal choice for arsenic removal. (c) 2006 Elsevier B.V. All rights reserved.
引用
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页码:237 / 245
页数:9
相关论文
共 37 条
  • [1] ADAK A, 2003, INTERDISCIPL ENV REV, V5, P230
  • [2] Arsenic adsorption from aqueous solutions by activated red mud
    Altundogan, HS
    Altundogan, S
    Tümen, F
    Bildik, M
    [J]. WASTE MANAGEMENT, 2002, 22 (03) : 357 - 363
  • [3] [Anonymous], 1989, STANDARD METHODS EXA
  • [4] Removal of arsenic from water by zero-valent iron
    Bang, S
    Korfiatis, GP
    Meng, XG
    [J]. JOURNAL OF HAZARDOUS MATERIALS, 2005, 121 (1-3) : 61 - 67
  • [5] Benefield L.D., 1982, Process Chemistry for Water and Wastewater Treatment
  • [6] Sorption and filtration of metals using iron-oxide-coated sand
    Benjamin, MM
    Sletten, RS
    Bailey, RP
    Bennett, T
    [J]. WATER RESEARCH, 1996, 30 (11) : 2609 - 2620
  • [7] BGS, 2001, Tech. Rep. WC/00/19
  • [8] Ceyhan Ö, 2001, TURK J CHEM, V25, P193
  • [9] Arsenic calamity in the Indian subcontinent - What lessons have been learned?
    Chakraborti, D
    Rahman, MM
    Paul, K
    Chowdhury, UK
    Sengupta, MK
    Lodh, D
    Chanda, CR
    Saha, KC
    Mukherjee, SC
    [J]. TALANTA, 2002, 58 (01) : 3 - 22
  • [10] Chowdhury U.K., 2001, ENVIRON SCI-TOKYO, V8, P393