Ammonia nitrogen removal from coking wastewater and high quality gypsum recovery by struvite recycling by using calcium hydroxide as decomposer

被引:18
作者
Huang, Haiming [1 ]
Li, Bing [1 ,3 ]
Dai, Jiankun [2 ]
Wang, Wenjun [2 ]
Zhang, Minge [1 ]
Ou, Yangzhu [1 ]
机构
[1] Dongguan Univ Technol, Sch Environm & Civil Engn, Dongguan 523808, Peoples R China
[2] Chinese Acad Environm Sci, Ctr Environm Engn Design, Beijing 100012, Peoples R China
[3] Tsinghua Univ, Shenzhen Int Grad Sch, Shenzhen 518055, Peoples R China
关键词
Coking wastewater; Struvite; Ammonia nitrogen; Gypsum; Recycling; BREAKPOINT CHLORINATION; EFFLUENTS; DENITRIFICATION; PRECIPITATION; PHOSPHATE; NUTRIENTS; MAGNESIUM; PHENOL; GROWTH;
D O I
10.1016/j.jenvman.2021.112712
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This study deals with the highly significant and cost-effective pretreatment of the high concentration of the Total Ammonia Nitrogen (TAN) in coking wastewater to improve the biodegradability. Struvite crystallization is a promising process for TAN removal, but the high operating cost hinders its application. To solve this problem, a novel struvite recycling process was proposed for pre-treating TAN present in the coking wastewater, within which struvite was decomposed in the solid-liquid system using Ca(OH)(2) as the decomposer. The results indicates that 91% of ammonium in struvite could be stripped out from the decomposition solution, with Ca(OH)(2):NH4+ in the molar ratio of 2:1, temperature at 35 degrees C and a gas to liquid volume ratio of 3500. The resulting solution, post the escape of the ammonia, was dissolved by sulfuric acid. Approximately 100% of the phosphate and magnesium were observed to be released from the insoluble phosphate compounds, resulting in the formation of high-purity gypsum. A TAN removal efficiency of 89% could be achieved by reusing the supernatant after the dissolution of the decomposition product, at pH 9.5 and the Mg:TAN:PO4-P molar ratio of 1.2:1:1. The pilot-scale test demonstrated that approximately 86% TAN was removed from the coking wastewater and the purity of recovered could reach over 99%. Further economic analysis proves that the operation cost of the proposed process is 0.55$ per m(3) of coking wastewater, showing a 73% cost reduction when compared to struvite crystallization without recycling.
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页数:9
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