气隙膜蒸馏脱盐海水和高盐产出水

Prashan M. Rodrigo , Sana Fatima , Raghava R. Kommalapati , Shankararaman Chellam
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引用次数: 0

摘要

气隙膜蒸馏(AGMD)为解决全球淡水短缺问题提供了一种很有前途的方法。它通过有效地淡化海水和处理石油和天然气部门的复杂采出水来实现这一目标。AGMD利用热梯度将水蒸气输送到疏水膜上,而气隙通过最小化导热损失来提高分离效率。咸淡水、海水和采出水的含盐量各不相同,德克萨斯州二叠纪盆地的采出水含盐量最高,咸淡水最低。处理高盐采出水具有挑战性。本研究系统地评估了商用聚四氟乙烯(PTFE)膜在各种操作条件下的性能,包括进料温度(40-60°C)、流速(1 - 3 L min−1)和孔径(0.1 µm vs. 0.45 µm),以优化微咸水、海水、实验室过滤PW和预处理PW的脱盐效果。本研究跟踪了三种不同含盐量水基质的实时通量减少情况,并评估了渗透水质。与去离子水相比,在流量为2 L min - 1、热进料温度为50°C、冷却剂温度为27.3°C时,盐水、海水、采出水(A)和(B)的平均通量分别降低了1 - 7 %、23-28 %、45-50 %和48-53 %。所有水基质的结果都显示出非凡的盐去除率(> 99% %),导致渗透物的总溶解固体(TDS)浓度低于500 mg L−1,这适用于农业和其他有益的再利用应用。对于孔径为0.45 μm的盐水、海水、采出水(A)和(B),能耗分别为~ 6.4、~ 8.2、~ 11.0和~ 11.4 kWh L−1。膜后特性显示最小的结构退化,强调PTFE即使暴露于高强度采出水后的耐久性。AGMD通过解决传统海水淡化技术的缺点提供了一个有希望的替代方案,例如与热方法相关的高能耗以及在处理高盐源时反渗透的高压力需求。它适用于可扩展和节能的应用。该研究证明了AGMD是一种可持续的全球水安全技术,在具有挑战性的环境和操作可行性之间取得了平衡。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Air-gap membrane distillation to desalinate seawater and hypersaline-produced water
Air gap membrane distillation (AGMD) offers a promising approach to tackling global freshwater shortages. It achieves this by effectively desalinating seawater and treating complex-produced water from the oil and gas sector. AGMD utilizes a thermal gradient to transport water vapor across a hydrophobic membrane, while an air gap improves separation efficiency by minimizing conductive heat loss. Salinity levels in brackish water, seawater, and produced water vary, with produced water from the Permian Basin in Texas having the maximum salinity and brackish water having the lowest. Treating hypersaline-produced water is challenging. This study systematically assesses the performance of commercial polytetrafluoroethylene (PTFE) membranes under a variety of operational conditions, including feed temperature (40–60°C), flow rate (1–3 L min−1), and pore size (0.1 µm vs. 0.45 µm) to optimize the desalination of brackish water, seawater, laboratory-filtered PW, and pretreated PW. This research tracked the real-time flux reduction with three distinct saline-level water matrices and assessed the permeate water quality. The average flux reduced by 1–7 %, 23–28 %, 45–50 %, and 48–53 %, respectively, for saline water, seawater, produced water (A) and (B) compared to deionized water at a flow rate of 2 L min−1, a 50°C hot feed temperature, and a 27.3°C coolant temperature. The results of all water matrices demonstrated extraordinary salt rejection (>99 %), resulting in a permeate with a total dissolved solids (TDS) concentration of less than 500 mg L−1, which is applicable for agriculture and other beneficial reuse applications. The energy consumptions were ∼6.4, ∼8.2, ∼11.0, and ∼11.4 kWh L−1, respectively, for saline water, seawater, produced water (A), and (B) with a 0.45 μm pore size membrane. Post-membrane characteristics revealed minimal structural degradation, underscoring the durability of PTFE even after exposure to high-strength produced waters. AGMD offers a promising alternative by addressing the drawbacks of traditional desalination techniques, such as the high energy consumption associated with thermal methods and the intense pressure demands of reverse osmosis when dealing with hypersaline sources. It is suitable for scalable and energy-efficient applications. This research proved AGMD to be a sustainable global water security technology, balancing high performance in challenging environments and operational feasibility.
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