Induced crystallization techniques for fluoride removal from wastewater: Current developments and applications

被引:0
作者
Gao, Xilan [1 ,2 ]
Liu, Jiuchen [2 ]
Gai, Nan [2 ]
Wang, Jihong [3 ]
Yuan, Zhimin [4 ]
Zhou, Beihai [1 ]
Hou, Rongrong [5 ]
Yuan, Rongfang [1 ]
Chen, Huilun [1 ]
机构
[1] Univ Sci & Technol Beijing, Sch Energy & Environm Engn, Beijing Key Lab Resource Oriented Treatment Ind Po, Beijing 100083, Peoples R China
[2] Minist Nat Resources China, Natl Res Ctr Geoanal NRCGA, Key Lab Ecogeochem, Beijing 100037, Peoples R China
[3] China lPPR Int Engn Co Ltd, Beijing 100089, Peoples R China
[4] Natl Inst Clean & Low Carbon Energy, Beijing 102209, Peoples R China
[5] CCCC First Harbor Engn Co Ltd, Tianjin Port Engn Inst Co Ltd, Tianjin 300222, Peoples R China
来源
JOURNAL OF ENVIRONMENTAL CHEMICAL ENGINEERING | 2025年 / 13卷 / 05期
关键词
Induced crystallization; Cryolite; Fluidized bed crystallization; Resource recovery; Actual wastewater treatment; FLUIDIZED-BED REACTOR; CALCIUM-FLUORIDE; CRYOLITE NA3ALF6; FINES PRODUCTION; GROWTH-KINETICS; RECOVERY; PRECIPITATION; ADSORPTION; CAF2; PH;
D O I
10.1016/j.jece.2025.117653
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Excessive fluoride in wastewater poses significant risks to ecosystems and human health. Crystallization methods, including cryolite, calcium fluoride, and fluorapatite, demonstrate high fluoride removal efficiency (>90 %) under optimized conditions and offer the added benefit of resource recovery. Maintaining an optimal pH range (5-7) after chemical dosing enhances removal efficiency, though sulfate interference remains a limiting factor. CaF2 and FAP typically crystallize at ambient temperature, with molar ratios of Ca/F= 0.6-0.7 and Ca:P:F= 10:4:1, respectively. In contrast, Na3AlF6 crystallization performs best at 20-50 degrees C with an Al/F ratio of 1:6. While the small-scale research on the crystallization methods of the three products is in full swing, only the CaF2 crystallization has been comprehensively applied in pilot-scale trials and full-scale engineering. Na3AlF6 crystallization is currently at the pilot-scale stage, whereas FAP crystallization has made no progress during the small-scale stage. Each method faces specific challenges. CaF2 crystallization requires improvements in product purity and effluent quality. FAP crystallization needs effective phosphate control and cost-efficient reactor design. Na3AlF6 must balance product purity with fluoride removal efficiency. Future research should prioritize the optimization of operational parameters, cost reduction, and the development of practical applications for novel approaches to facilitate large-scale implementation.
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页数:18
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