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Using tertiary-treated municipal wastewater as makeup water by reverse osmosis membrane

机译:用三级反渗透膜处理城市污水作为补充水

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The objective of this research was to study the possibility of using reclaimed municipal wastewater in cooling tower by treating the water using reverse osmosis (RO) membrane. In this study, RO membrane was operated at initial flow rate of 6.3 m(3)/d, whereas the initial transmembrane pressure (TMP) was at 116 psi. During the operating period, permeate flux slightly decreased to 4.8 m(3)/day with the increase of TMP up to 127 psi and membrane fouling resistance of 3.34E + 12 m(-1). Major membrane fouling mechanism was complete blocking followed by standard blocking and cake layer formation. Average permeate characteristics were 36.3 mu S/cm of conductivity, 42.3 mg/L of TDS, 4.4 mg/L of hardness, 22.7 mg/L as CaCO3 of alkalinity, 0.002 mg/L of iron, 0.05 mg/L as CaCO3, 1.5 mg/L of chloride, 2.1 mg/L of silica, and there was no phosphate passing through RO membrane. Percent rejections compared to UF treated wastewater were in the range of 90.2-99.9% except for silica where rejection was only 85.1%. Scaling and corrosion index was studied in terms of Langelier saturation index (LSI) and Ryznar stability index (RSI). Without RO membrane, LSI value was -0.59 and RSI value was 8.5. With RO membrane, LSI value was -5.0 and RSI value was 17.0. From calculation of cycles of blowdown, it was found that when using the membrane, the cycles increased from 2.3 to 44 cycles. This, then, resulted in reduction of makeup water from 379.0 to 221.2 m(3)/d, a decrease by 41.6%. Payback period of installation and operation of RO membrane system was 14 months.
机译:这项研究的目的是通过使用反渗透(RO)膜处理水来研究在冷却塔中使用再生市政废水的可能性。在这项研究中,反渗透膜的初始流速为6.3 m(3)/ d,而初始跨膜压力(TMP)为116 psi。在运行期间,渗透物通量略有下降,降至4.8 m(3)/天,而TMP最高可达127 psi,膜防污性能为3.34E + 12 m(-1)。膜的主要结垢机理是完全阻塞,然后是标准阻塞和滤饼层形成。平均渗透特性为36.3μS/ cm的电导率,42.3 mg / L的TDS,4.4 mg / L的硬度,22.7 mg / L的碱度(CaCO3),0.002 mg / L的铁,0.05 mg / L的CaCO3、1.5毫克/升的氯化物,2.1毫克/升的二氧化硅,并且没有磷酸盐通过反渗透膜。与超滤处理后的废水相比,废品率在90.2-99.9%范围内,但二氧化硅的废品率仅为85.1%。根据朗格里尔饱和指数(LSI)和Ryznar稳定性指数(RSI)研究了结垢和腐蚀指数。没有RO膜的情况下,LSI值为-0.59,RSI值为8.5。对于RO膜,LSI值为-5.0,RSI值为17.0。通过排污循环的计算,发现使用膜时,循环从2.3增加到44个循环。然后,这导致补充水从379.0减少到221.2 m(3)/ d,减少了41.6%。反渗透膜系统安装和运行的投资回收期为14个月。

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