Ammonia-Ca-K Competitive Ion-Exchange on Zeolites in Mining Wastewater Treatment: Batch Regeneration and Column Performance

被引:9
作者
Narbaitz, Roberto Martin [1 ]
Chartrand, Zachary G. [1 ]
Sartaj, Majid [1 ]
Downey, Jason [2 ]
机构
[1] Univ Ottawa, Dept Civil Engn, 161 Louis Pasteur Pvt, Ottawa, ON K1N 6N5, Canada
[2] Dowclear Inc, 627 South Isl Pk Dr, Manotick, ON K4M 1J2, Canada
来源
JOURNAL OF SUSTAINABLE MINING | 2020年 / 19卷 / 02期
基金
加拿大自然科学与工程研究理事会;
关键词
ion exchange; ammonia; clinoptilolite; mining wastewater; competitive ion exchange; potassium;
D O I
10.46873/2300-3960.1006
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This manuscript addresses the treatment of explosives-impacted mining wastewaters (EIMWW) using ion-exchange to remove elevated levels of ammonia. Repeated batch loading-regeneration cycles were conducted for two commercially available zeolite media used in the treatment of ammonia-laden EIMWW to establish the effects of competing ions and regeneration solution composition. The Northern Ontario EIMWW tested contained 3.87 meq/L total ammonia (TA) as well as 2.85 mg/L K+ and 3.9 meq/L Ca2+. The media studied were a natural clinoptilolite and a modified clinoptilolite (SIR-600). Five regenerant solutions with different NaCl and KCl concentrations were evaluated using batch tests. The presence of potassium in the regenerant was found to hinder the TA exchange capacity of both zeolites. The SIR-600 and the natural clinoptilolite used in conjunction with the 10% NaCl solution featured the best TA exchange capacities, 0.46 +/- 0.02 meq TA/g and 0.36 +/- 0.05 meq TA/g, respectively. The batch tests showed that both media had a slight preference for K+ over TA. The continuous flow column tests performed using SIR-600 media greatly accentuated the selectivity of K+ over TA. In reaching the same 0.55 meq TA/L breakthrough level, the same modified zeolite column was able to treat five times more volume of a synthetic TA solution than EIMWW.
引用
收藏
页码:58 / 71
页数:14
相关论文
共 34 条
  • [1] Intensification of ammonia removal from waste water in biologically active zeolitic ion exchange columns
    Almutairi, Azel
    Weatherley, Laurence R.
    [J]. JOURNAL OF ENVIRONMENTAL MANAGEMENT, 2015, 160 : 128 - 138
  • [2] AMES LL, 1960, AM MINERAL, V45, P689
  • [3] [Anonymous], 2006, ADSORPTION ION EXCHA, DOI DOI 10.1016/B978-0-444-52783-7.X5000-9
  • [4] APHA, 2005, Standard Methods for the Examination of Water and Wastewater
  • [5] The Diavik Waste Rock Project: Persistence of contaminants from blasting agents in waste rock effluent
    Bailey, Brenda L.
    Smith, Lianna J. D.
    Blowes, David W.
    Ptacek, Carol J.
    Smith, Leslie
    Sego, David C.
    [J]. APPLIED GEOCHEMISTRY, 2013, 36 : 256 - 270
  • [6] Biological nitrogen removal of high-strength ammonium industrial wastewater with two-sludge system
    Carrera, J
    Baeza, JA
    Vicent, T
    Lafuente, J
    [J]. WATER RESEARCH, 2003, 37 (17) : 4211 - 4221
  • [7] Clinoptilolite-based mixed matrix membranes for the selective recovery of potassium and ammonium
    Casadella, A.
    Kuntke, P.
    Schaetzle, O.
    Loos, K.
    [J]. WATER RESEARCH, 2016, 90 : 62 - 70
  • [8] Chartrand ZG, 2018, THESIS U OTTAWA CANA
  • [9] Chen JP, 2002, WASTE MANAGE, V22, P711
  • [10] Optimization of ammonia removal by ion-exchange resin using response surface methodology
    Ding, Y.
    Sartaj, M.
    [J]. INTERNATIONAL JOURNAL OF ENVIRONMENTAL SCIENCE AND TECHNOLOGY, 2016, 13 (04) : 985 - 994