TY - JOUR
T1 - A two-stage desalination process for zero liquid discharge of flue gas desulfurization wastewater by chloride precipitation
AU - Xin, Yi
AU - Zhou, Zhen
AU - Ming, Qiang
AU - Sun, Dongqi
AU - Han, Jun
AU - Ye, Xiaofang
AU - Dai, Shifeng
AU - Jiang, Lu Man
AU - Zhao, Xiaodan
AU - An, Ying
N1 - Publisher Copyright:
© 2020 Elsevier B.V.
PY - 2020/10/5
Y1 - 2020/10/5
N2 - A two-stage desalination process was developed to achieve zero liquid discharge (ZLD) of flue gas desulfurization (FGD) wastewater by precipitating chloride as Friedel's salt. Influential factors for Friedel's salt precipitation, including dosage, reaction time, concentration of sulfate, were investigate by batch tests. Batch results showed that at calcium to aluminum molar ratio of 3.0, the optimal chloride removal and the highest crystallinity of Friedel's salt were obtained. Sulfate impeded Friedel's salt precipitation by competitive inhibition mechanism, and thus calcium sulfate removal was designed in advance of chloride removal. Batch results and long-term results of bench-scale experiments showed that magnesium and part of sulfate were effectively removed by lime addition in Stage I of the proposed process, and then the remaining sulfate and 48.1 % of chloride were precipitated as ettringite and Friedel's salt in Stage II. The effluent of the two-stage process was alkaline with low turbidity, and had considerable desulfurization capacity. Techno-economic evaluation showed that the two-stage process is technically feasible, economically viable and environmentally friendly technology for ZLD of FGD wastewater.
AB - A two-stage desalination process was developed to achieve zero liquid discharge (ZLD) of flue gas desulfurization (FGD) wastewater by precipitating chloride as Friedel's salt. Influential factors for Friedel's salt precipitation, including dosage, reaction time, concentration of sulfate, were investigate by batch tests. Batch results showed that at calcium to aluminum molar ratio of 3.0, the optimal chloride removal and the highest crystallinity of Friedel's salt were obtained. Sulfate impeded Friedel's salt precipitation by competitive inhibition mechanism, and thus calcium sulfate removal was designed in advance of chloride removal. Batch results and long-term results of bench-scale experiments showed that magnesium and part of sulfate were effectively removed by lime addition in Stage I of the proposed process, and then the remaining sulfate and 48.1 % of chloride were precipitated as ettringite and Friedel's salt in Stage II. The effluent of the two-stage process was alkaline with low turbidity, and had considerable desulfurization capacity. Techno-economic evaluation showed that the two-stage process is technically feasible, economically viable and environmentally friendly technology for ZLD of FGD wastewater.
KW - Chloride removal
KW - Flue gas desulfurization wastewater
KW - Friedel's salt
KW - Layered double hydroxides
KW - Wastewater
UR - https://www.scopus.com/pages/publications/85083781273
U2 - 10.1016/j.jhazmat.2020.122744
DO - 10.1016/j.jhazmat.2020.122744
M3 - 文章
C2 - 32361139
AN - SCOPUS:85083781273
SN - 0304-3894
VL - 397
JO - Journal of Hazardous Materials
JF - Journal of Hazardous Materials
M1 - 122744
ER -