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Membrane distillation and membrane electrolysis of coal seam gas reverse osmosis brine for clean water extraction and NaOH production

机译:煤层气反渗透盐水的膜蒸馏和膜电解用于净水萃取和NaOH生产

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摘要

Membrane distillation (MD) and membrane electrolysis (ME) were evaluated for simultaneous fresh water extraction and NaOH production from a mixture of NaCl and NaHCO3 to simulate the composition of coal seam gas (CSG) reverse osmosis (RO) brine. Experimental results demonstrate the potential of MD for producing fresh water and simultaneously concentrating CSG RO brine prior to the ME process. MD water flux was slightly reduced by the increased feed salinity and the decomposition of bicarbonate to CO2 during the concentration of CSG RO brine. MD operation of CSG RO brine at a concentration factor of 10 (90% water recovery) was achieved with distillate conductivity as low as 18 mu S/cm, and without any observable membrane scaling. Exceeding the concentration factor of 10 could lead to deterioration in both water flux and distillate quality due to the precipitation of NaCl, NaHCO3, and Na2CO3 on the membrane. With respect to ME, current density and water circulation rates exerted strong influences on the ME process performance. Combining ME with MD reduced the thermal energy requirement of ME by 3 MJ per kg of NaOH produced and the thermal energy consumption of MD by 22 MJ per m(3) of clean water extracted. Crown Copyright (C) 2016 Published by Elsevier B.V. All rights reserved.
机译:评估膜蒸馏(MD)和膜电解(ME)的同时从NaCl和NaHCO3的混合物中提取淡水和生产NaOH,以模拟煤层气(CSG)反渗透(RO)盐水的组成。实验结果证明了MD在生产ME工艺之前生产淡水并同时浓缩CSG RO盐水的潜力。在CSG RO盐水浓缩过程中,进料盐度的增加和碳酸氢盐分解为CO2会稍微降低MD的水通量。在馏出物电导率低至18μS / cm且没有任何可观察到的膜结垢的情况下,实现了CSG RO盐水在浓度因子10(水回收率90%)下的MD操作。超过10的浓缩系数可能会由于NaCl,NaHCO3和Na2CO3在膜上的沉淀而导致水通量和馏出液质量下降。对于ME,电流密度和水循环速率对ME工艺性能产生很大影响。将ME与MD结合使用可将ME的热能需求降低3 MJ / kg所产生的NaOH,将MD的热能消耗降低22 MJ / m(3)所抽取的清洁水。官方版权(C)2016,由Elsevier B.V.保留所有权利。

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