Ammonia removal from aqueous solution using natural Chinese clinoptilolite

被引:256
作者
Du, Q [1 ]
Liu, SJ [1 ]
Cao, ZH [1 ]
Wang, YQ [1 ]
机构
[1] Nankai Univ, Coll Environm Sci & Engn, Tianjin 300071, Peoples R China
关键词
ammonia removal; capacity; clinoptilolite; ion exchange; zeolite;
D O I
10.1016/j.seppur.2004.04.011
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper assesses the potential of natural Chinese clinoptilolite for ammonia removal from aqueous solution. In batch study, the effects of relevant parameters, such as contact time, pH and initial ammonia concentration were examined, respectively. The results show that although contact time needs at least 4 h in order to attain exchange equilibrium, ammonia removal by clinoptilolite occurs rapidly within the first 15 min of contact time; the pH has an effect on ammonia removal efficiency as it can influence both the character of the exchanging ions and the clinoptilolite itself; the ammonia removal capacity of clinoptilolite increases with the increase of initial ammonia concentration. In column study, clinoptilolite bed was exhausted at different flow velocities and ammonia breakthrough capacity of clinoptilolite bed was calculated. Furthermore, the optimum regeneration conditions were considered. The results show that flow velocity can affect breakthrough capacity of clinoptilolite by changing hydraulic retention time and the volume of 15-20 BV of 0.5 mol/L sodium chloride solution at pH 11-12 is sufficient for complete regeneration of clinoptilolite in column. (C) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:229 / 234
页数:6
相关论文
共 14 条
[1]   Ammonia removal from sewage using natural Australian zeolite [J].
Booker, NA ;
Cooney, EL ;
Priestly, AJ .
WATER SCIENCE AND TECHNOLOGY, 1996, 34 (09) :17-24
[2]   Sardinian natural clinoptilolites for heavy metals and ammonium removal:: experimental and modeling [J].
Cincotti, A ;
Lai, N ;
Orrù, R ;
Cao, G .
CHEMICAL ENGINEERING JOURNAL, 2001, 84 (03) :275-282
[3]   Ammonia removal from wastewaters using natural Australian zeolite. I. Characterization of the zeolite [J].
Cooney, EL ;
Booker, NA ;
Shallcross, DC ;
Stevens, GW .
SEPARATION SCIENCE AND TECHNOLOGY, 1999, 34 (12) :2307-2327
[4]   Combined filter for ammonia removal - Part I: Minimal zeolite contact time and requirements for desorption [J].
Dimova, G ;
Mihailov, G ;
Tzankov, T .
WATER SCIENCE AND TECHNOLOGY, 1999, 39 (08) :123-129
[5]   SORPTION OF CHROMATE AND OTHER INORGANIC ANIONS BY ORGANO-ZEOLITE [J].
HAGGERTY, GM ;
BOWMAN, RS .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 1994, 28 (03) :452-458
[6]   THE USE OF ZEOLITE FOR AMMONIUM UPTAKE [J].
HARALAMBOUS, A ;
MALIOU, E ;
MALAMIS, M .
WATER SCIENCE AND TECHNOLOGY, 1992, 25 (01) :139-145
[7]   INVESTIGATIONS ON NATURAL HUNGARIAN ZEOLITE FOR AMMONIA REMOVAL [J].
HLAVAY, J ;
VIGH, G ;
OLASZI, V ;
INCZEDY, J .
WATER RESEARCH, 1982, 16 (04) :417-420
[8]  
JORGENSEN SE, 1976, WATER RES, V10, P213, DOI 10.1016/0043-1354(76)90130-5
[9]   EQUILIBRIUM AND CAPACITY DATA OF CLINOPTILOLITE [J].
JORGENSEN, SE ;
LIBOR, O ;
BARKACS, K ;
KUNA, L .
WATER RESEARCH, 1979, 13 (02) :159-165
[10]   Ammonia removal from wastewater by ion exchange in the presence of organic contaminants [J].
Jorgensen, TC ;
Weatherley, LR .
WATER RESEARCH, 2003, 37 (08) :1723-1728