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Submerged membrane coagulation hybrid system as pretreatment to organic matter removal from seawater

机译:浸没膜混凝混合系统作为海水中有机物去除的预处理

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摘要

In this study, a commonly used ferric chloride was utilised as coagulant for removing organic compounds from seawater. More than 57% of dissolved organic carbon (DOC) was removed at optimum dosage of 3 mg Fe~(+3)/L The coagulation by FeCI_3 at optimum dosage could remove a majority (95%) of hydrophobic compounds. The results from Liquid Chromatography - Organic Carbon Detector showed that only <0.02 mg/L of hydrophobic compounds was found after coagulation. In addition, the modified fouling index decreased considerably from 15,848 s/L~2 with raw seawater to 3,025 s/L~2 with seawater after coagulation. In-line coagulation coupled with submerged membrane system (ICSMS) was also trialled. It is observed that critical flux was increased from 20 L/m~2·h in the conventional submerged membrane system to 55 L/m~2 h in ICSMS. The ICSMS could remain the high DOC removal efficiency (more than 70%) at filtration rate of 20 L/m~2 h when keeping the development of trans-membrane pressure was significant lower than that of conventional submerged membrane system.
机译:在这项研究中,常用的氯化铁被用作凝结剂,用于从海水中去除有机化合物。在3 mg Fe〜(+3)/ L的最佳剂量下,去除了超过57%的溶解有机碳(DOC)。以FeCI_3的最佳剂量进行凝结可以去除大部分(95%)疏水性化合物。液相色谱-有机碳检测器的结果显示,凝结后仅发现<0.02 mg / L的疏水性化合物。此外,凝结后的修正污垢指数从原海水的15848 s / L〜2显着降低至原海水的3025 s / L〜2。还尝试了在线混凝与浸没膜系统(ICSMS)。观察到临界通量从常规浸没膜系统中的20 L / m〜2·h增加到ICSMS中的55 L / m〜2 h。当保持跨膜压力的发展明显低于传统的浸没式膜系统时,ICSMS可以在20 L / m〜2 h的过滤速率下保持较高的DOC去除效率(超过70%)。

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