Treatment of Flue Gas Desulfurization Wastewater by an Integrated Membrane-Based Process for Approaching Zero Liquid Discharge

被引:41
作者
Conidi, Carmela [1 ]
Macedonio, Francesca [1 ,2 ]
Ali, Aamer [1 ]
Cassano, Alfredo [1 ]
Criscuoli, Alessandra [1 ]
Argurio, Pietro [1 ]
Drioli, Enrico [1 ]
机构
[1] Univ Calabria, CNR, ITM, Inst Membrane Technol, Via P Bucci 17-C, I-87036 Arcavacata Di Rende, CS, Italy
[2] Univ Calabria, Dept Environm & Chem Engn, Via P Bucci 44-A, I-87036 Arcavacata Di Rende, CS, Italy
基金
欧盟地平线“2020”;
关键词
FGD wastewater; integrated membrane-based process; zero liquid-discharge; sustainability; HEAVY-METALS; VALENT IRON; DISTILLATION; REMOVAL; GROUNDWATER; REDUCTION; NITRATE; PLANTS;
D O I
10.3390/membranes8040117
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
An integrated membrane process for the treatment of wastewaters from a flue gas desulfurization (FGD) plant was implemented on a laboratory scale to reduce their salt content and to produce a water stream to be recycled in the power industry. The process is based on a preliminary pretreatment of FGD wastewaters, which includes chemical softening and ultrafiltration (UF) to remove Ca2+ and Mg2+ ions as well as organic compounds. The pretreated wastewaters were submitted to a reverse osmosis (RO) step to separate salts from water. The RO retentate was finally submitted to a membrane distillation (MD) step to extract more water, thus increasing the total water recovery factor while producing a high-purity permeate stream. The performance of RO and MD membranes was evaluated by calculating salts rejection, permeate flux, fouling index, and water recovery. The investigated integrated system allowed a total recovery factor of about 94% to be reached, with a consequent reduction of the volume of FGD wastewater to be disposed, and an MD permeate stream with an electrical conductivity of 80 S/cm, able to be reused in the power plant, with a saving in fresh water demand.
引用
收藏
页数:12
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