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Pressure-driven membrane and ion exchange hybrid system for the treatment of wastewater containing sulfite and nitrite

机译:压力驱动膜与离子交换混合系统处理含亚硫酸盐和亚硝酸盐的废水

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Denitrification of flue gas can generate a large amount of wastewater. Depending on the denitrification technology used, the water could contain a fair amount of sulfite and nitrite that need to be removed for water reuse or discharge. An integrated pressure-driven membrane and ion exchange (IX) process is therefore designed and tested for this purpose in this work. The process contains a combination of nanofiltration (NF), reverse osmosis (RO), and a mixed bed IX. NF was performed on a DL1812 membrane module at 2.0MPa using a simulated wastewater containing 63.0g/L Na2SO3 and 49.5g/L NaNO2. Sulfite was separated from nitrite with a retention rate of 92.0%, and its overall recovery efficiency achieved 91.09%. The recovery rate of nitrite in the permeate of NF was 71.06%, which was further elevated by RO using a SG1812 membrane module. A four-pass RO process was shown to be capable of recovering 98.15% of NaNO2 in the final retention. Finally, it was demonstrated that followed by IX treatment, sulfite and nitrite were successfully removed to meet the water surface discharge criteria, proving the feasibility of the hybrid NF-RO-IX system as a viable alternative for treating and reusing denitrification wastewater.
机译:烟气的反硝化会产生大量废水。根据所使用的反硝化技术的不同,水中可能含有大量的亚硫酸盐和亚硝酸盐,需要将其去除后再用于水的再利用或排放。因此,在这项工作中为此目的设计并测试了集成的压力驱动膜和离子交换(IX)工艺。该工艺包含纳滤(NF),反渗透(RO)和混合床IX的组合。使用包含63.0g / L Na2SO3和49.5g / L NaNO2的模拟废水在2.0MPa的DL1812膜组件上进行NF。从亚硝酸盐中分离出亚硫酸盐,保留率为92.0%,总回收效率达到91.09%。 NF透过物中亚硝酸盐的回收率为71.06%,使用SG1812膜组件通过RO进一步提高了该回收率。结果表明,四遍反渗透工艺能够回收最终保留物中的98.15%的NaNO2。最后,证明了通过IX处理后,亚硫酸盐和亚硝酸盐被成功去除以满足水表面排放标准,证明了混合NF-RO-IX系统作为处理和再利用反硝化废水的可行替代方案的可行性。

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