Adsorption of As(III) from aqueous solution onto iron oxide impregnated activated alumina

被引:87
作者
Kuriakose, S [1 ]
Singh, TS [1 ]
Pant, KK [1 ]
机构
[1] Indian Inst Technol, Dept Chem Engn, New Delhi 110016, India
来源
WATER QUALITY RESEARCH JOURNAL OF CANADA | 2004年 / 39卷 / 03期
关键词
activated alumina; iron oxide; adsorption; arsenite; breakthrough curve;
D O I
10.2166/wqrj.2004.036
中图分类号
TV21 [水资源调查与水利规划];
学科分类号
081501 ;
摘要
The optimal parameters. affecting the adsorption of arsenic ions As(III) on iron oxide impregnated activated alumina (IOIAA) were determined by conducting batch and column experiments. The adsorption of As(Ill) was strongly dependent on pH, temperature and initial adsorbate concentration. The adsorption process satisfied the Langmuir and Freundlich isotherms. Equilibrium studies were conducted to obtain the thermodynamic parameters and data showed the endothermic nature of adsorption. Kinetics studies showed that a pseudo first-order rate equation successfully described the adsorption process. Equilibrium was attained within 10 h and the time taken to attain equilibrium was independent of initial arsenite concentration. Column studies showed that adsorption was strongly dependent on empty bed contact time. Column design parameters such as the time taken for the establishment of primary adsorption zone, fractional capacity, length of primary adsorption zone and the percentage saturation at breakpoint were calculated to be in the range of 18.3 to 70.4 h, 0.39 to 0.63, 3.0 to 3.85 cm and 69.6 to 81.5%, respectively. The observations mentioned above provide a direct relationship between the length of the adsorption zone (8) and percent saturation at break point.
引用
收藏
页码:258 / 266
页数:9
相关论文
共 32 条
[1]   Adsorption of phenol using different types of activated bentonites [J].
Al-Asheh, S ;
Banat, F ;
Abu-Aitah, L .
SEPARATION AND PURIFICATION TECHNOLOGY, 2003, 33 (01) :1-10
[2]  
Altundogan HS, 2000, WASTE MANAGE, V20, P761
[3]  
[Anonymous], J INDIAN WATER WORKS
[4]   Removal of arsenic from ground water by manganese dioxide-coated sand [J].
Bajpai, S ;
Chaudhuri, M .
JOURNAL OF ENVIRONMENTAL ENGINEERING-ASCE, 1999, 125 (08) :782-784
[5]   Removal of arsenic from groundwater using low cost ferruginous manganese ore [J].
Chakravarty, S ;
Dureja, V ;
Bhattacharyya, G ;
Maity, S ;
Bhattacharjee, S .
WATER RESEARCH, 2002, 36 (03) :625-632
[6]   Kinetics of the arsenite oxidation in seepage water from a tin mill tailings pond [J].
Daus, B ;
Mattusch, J ;
Paschke, A ;
Wennrich, R ;
Weiss, H .
TALANTA, 2000, 51 (06) :1087-1095
[7]   OXIDATION OF ARSENATE(III) WITH MANGANESE OXIDES IN WATER-TREATMENT [J].
DRIEHAUS, W ;
SEITH, R ;
JEKEL, M .
WATER RESEARCH, 1995, 29 (01) :297-305
[8]   Granular ferric hydroxide - a new adsorbent for the removal of arsenic from natural water [J].
Driehaus, W ;
Jekel, M ;
Hildebrandt, U .
JOURNAL OF WATER SERVICES RESEARCH AND TECHNOLOGY-AQUA, 1998, 47 (01) :30-35
[9]   Arsenate and chromate retention mechanisms on goethite .1. Surface structure [J].
Fendorf, S ;
Eick, MJ ;
Grossl, P ;
Sparks, DL .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 1997, 31 (02) :315-320
[10]   Arsenate and chromate retention mechanisms on goethite .2. Kinetic evaluation using a pressure-jump relaxation technique [J].
Grossl, PR ;
Eick, M ;
Sparks, DL ;
Goldberg, S ;
Ainsworth, CC .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 1997, 31 (02) :321-326