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Black odorous water concentrating by forward osmosis (FO) with aquaporin biomimetic membranes: Pollutants concentrating and membrane fouling characteristics

机译:用前渗透(FO)浓缩的黑色渗透水(FO)与水素仿生膜:污染物浓缩和膜污染特性

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This study aimed to investigate pollutant concentration and membrane fouling characteristics of a forward osmosis (FO) process using aquaporin biomimetic membrane (ABM) for concentrating black odorous water. The membrane cells were operated in active layer facing feed solution (ALFS) mode with 2 M NaCl solution as the draw solution. The system was continuously performed for 64 batch cycles, and each cycle duration was 24 h. At the end of each cycle, physical cleaning with deionized water was employed as the membrane recovery strategy. The results showed that the rejection ratios of chemical oxygen demand (COD), total phosphorus (TP) and nitrate (NO3-N) could reached 97.2%, 98.0%, and 85.0%, respectively, while most NH4+-N penetrated into the draw solution due to cation exchange. The total nitrogen (TN) rejection ratio was largely dependent upon the NH4+-N/TN ratio. At high NH4+-N/TN ratio, the successions of ammonia oxidizing bacteria (AOB) communities enriched in the biofouling layer in different experimental stages would affect the transformation degree of NH4+-N, and thus lead to much fluctuations of TN rejection. The average initial water flux reached 9.84 L/(m(2).h), and the average water flux of each cycle kept stable especially in the later stage of the experiment. In the biofouling layer, polysaccharides enhanced while proteins decreased in the later period. P, Mn, Fe and Na also accumulated on the surface. Noranki Reyranellaceae, Erythrobacter, SM1A02, Pirellula, and Hydrogenophaga were the predominant genera enriched in the fouling layer, which would lead to complex pollutants transformations, especially nitrogen transformation, during the FO process.
机译:本研究旨在研究使用Aquaporin仿生膜(ABM)浓缩黑色气味水的前渗透(FO)工艺的污染物浓度和膜污染特性。膜细胞在面向饲料溶液(ALF)模式的有源层中操作,用2M NaCl溶液作为拉伸溶液。持续进行64个分批循环的系统,每个循环持续时间为24小时。在每个循环结束时,使用与去离子水的物理清洁作为膜回收策略。结果表明,化学需氧量(COD),总磷(TP)和硝酸盐(NO3-N)的排斥比分别可分别达到97.2%,98.0%和85.0%,而大多数NH4 + -N渗透到绘图中解决方案由于阳离子交换。总氮气(TN)排斥比在很大程度上取决于NH 4 + -N / TN比率。在高NH4 + -N / TN比率下,在不同实验阶段中富含生物污垢层的氨氧化细菌(AOB)群落的阶段将影响NH4 + -N的转化度,从而导致TN排斥的波动。平均初始水通量达到9.84升/(m(2).h),每个循环的平均水通量保持稳定,特别是在实验的后期阶段。在生物污垢层中,多糖增强,而蛋白质在后期减少。 P,Mn,Fe和Na也积聚在表面上。 Noranki葡萄腊丹细胞,红斑狼杆菌,SM1A02,染色层和氢气是富含污染层的主要属,这将导致复杂的污染物转化,尤其是氮转化在FO过程中。

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