混合膜法处理合成采出水

N. Chin, S. Lai, K. C. Chong, S. S. Lee, C. Koo, H. S. Thiam
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引用次数: 0

摘要

采用微滤和超滤混合工艺处理水罐脱水采出水。采用聚醚砜(PES)、n-甲基-2-吡咯烷酮(NMP)和聚乙烯吡咯烷酮(PVP)制备了预处理MF膜。同时,超滤膜含有额外的成分,即二氧化钛(TiO2)纳米颗粒,含量在0 ~ 1.0 wt.%之间。从渗透通量、除油率和通量回收率等方面分析了膜的性能。由于亲水性的改善,TiO2纳米颗粒的增加增强了孔隙的形成、孔隙度和纯水的渗透性。超滤膜的渗透通量随着TiO2纳米颗粒的增加和压力的增加而增加。MF法的除油率仅为52.35%,UF法的除油率为82.34% ~ 95.71%。值得注意的是,整体除油率可达97.96%。结果表明,在3 bar的跨膜压力下,掺量为1.0 wt.% TiO2的PES膜是最有前途的膜。虽然使用1.0 M NaOH溶液作为清洗剂可以回收膜水通量,但效果并不理想,回收率仅为52.18%。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Treatment of Synthetic Produced Water using Hybrid Membrane Processes
The study was concerned with the treatment of tank dewatering produced water using hybrid microfiltration (MF) and ultrafiltration (UF) processes. The pre-treatment MF membrane was fabricated with polyethersulfone (PES), n-methyl-2-pyrrolidone (NMP) and polyvinylpyrrolidone (PVP). The UF membranes meanwhile contained additional component, i.e., titanium dioxide (TiO2) nanoparticles in the range of zero to 1.0 wt.%. The membrane performances were analysed with respect to permeate flux, oil removal and flux recovery ratio. An increase in TiO2 nanoparticles enhanced the pore formation, porosity and pure water permeability due to improved hydrophilicity. The permeate flux of UF membranes increased with the increase of TiO2 nanoparticles and pressure. The oil removal rate by MF process was only 52.35%, whereas the oil rejection efficiency was between 82.34% and 95.71% for UF process. It should be highlighted that the overall oil removal rate could achieve as high as 97.96%. Based on the results, the PES membrane incorporated with 1.0 wt.% TiO2 was proved to be the most promising membrane at a transmembrane pressure of 3 bar. Although 1.0 M NaOH solution could be used as cleaning agent to recover membrane water flux, it is not capable of achieving good results as only 52.18% recovery rate was obtained.
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