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Study on concentrating primary reverse osmosis retentate by direct contact membrane distillation

机译:直接接触膜蒸馏浓缩一次反渗透保留物的研究

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The direct contact membrane distillation (DCMD) applied for the concentration of the primary reverse osmosis (PRO) retentate was presented in the paper. All the experiments were carried out using the self-made hydrophobic polyvinylidene fluoride (PVDF) membranes. The DCMD process (permeate flux and conductivity) and membrane fouling phenomenon were investigated. Three kinds of PRO retentate (direct PRO retentate, silica bearing PRO retentate, and iron and manganese bearing PRO retentate) were used in the experiments. During the whole period of investigation, the membranes were found to be thermally stable and good separation characteristics. The RO was fed with the tap water with the recovery of 50%. After DCMD process, the whole water recovery can be significantly enhanced to 98.8%. Membrane fouling was observed during the process. Membrane clogging caused by the formed deposit (CaCO3, CaSO4, and silicate) was the main reason of the membrane efficiency reduction. It was found that CaCO3 formed at first during the process, and can be alleviated even eliminated by acidification. When the PRO retentate was concentrated a high level, CaSO4 formed and caused a sharp decline of module efficiency. During the DCMD process of silica bearing PRO retentate, silica may co-precipitate with soluble metals to form silicate at alkaline solutions while colloid silica may form at acidic solutions. The influence of iron and manganese is not significant.
机译:本文介绍了用于浓缩初级反渗透(PRO)截留液的直接接触膜蒸馏(DCMD)。所有实验均使用自制的疏水性聚偏二氟乙烯(PVDF)膜进行。研究了DCMD工艺(渗透通量和电导率)和膜污染现象。实验中使用了三种PRO保留物(直接PRO保留物,带有二氧化硅的PRO保留物以及带有铁和锰的PRO保留物)。在整个研究过程中,发现这些膜具有热稳定性和良好的分离特性。 RO注入自来水,回收率为50%。经过DCMD处理后,整个水回收率可以显着提高到98.8%。在此过程中观察到膜结垢。由形成的沉积物(CaCO3,CaSO4和硅酸盐)引起的膜堵塞是膜效率降低的主要原因。发现在该过程中首先形成CaCO 3,并且甚至可以通过酸化消除CaCO 3。当PRO截留液高浓度浓缩时,形成CaSO4并导致组件效率急剧下降。在带有PRO渗余物的二氧化硅的DCMD过程中,二氧化硅可能与可溶性金属共沉淀,从而在碱性溶液中形成硅酸盐,而胶体二氧化硅可能在酸性溶液中形成。铁和锰的影响不大。

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