用于石油天然气行业可持续采出水处理和减少危险废物量的预试验正渗透-膜蒸馏混合系统

IF 6.3 2区 工程技术 Q1 ENGINEERING, CHEMICAL
Hyuk Soo Son , Alla Alpatova , Muhammad Saqib Nawaz , Sofiane Soukane , Sandra C. Medina , Veerabhadraiah Gudideni , Ali Al-Qahtani , Dalaver H. Anjum , Noreddine Ghaffour
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The MD permeate production was doubled and comprised 0.4 L/h for 7:1 MD/FO area ratio (0.105 m<sup>2</sup> and 0.015 m<sup>2</sup>, respectively) compared to permeate production that was observed with equal MD and FO membrane area (0.015 m<sup>2</sup> each). The conductivity of the final product water was 364.9 ± 2.7 μS/cm, comparable to the typical potable water conductivity, implying its potential for reuse applications and minimizing volume of hazardous waste. Analysis of MD permeate quality showed that concentration of major ions was reduced by &gt;99 % and chemical oxygen demand was removed by 90.1 %. Continuous operation with real produced streams led to partial pore wetting on the MD active layer. The microscopy showed organic fouling caused by oil and grease deposition and NaCl/CaSO<sub>4</sub> scaling was found on both sides of FO membrane. These results suggest that PW pretreatment should be implemented to alleviate membrane fouling and pore wetting. 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引用次数: 0

摘要

本研究介绍了预试验规模的混合正渗透-膜蒸馏(FO-MD)模块,该模块设计用于同时处理来自石油和天然气行业的不同挑战性采出水(PW)流。在该模块中,热汲取溶液同时作为 MD 进料溶液。该模块的性能通过长时间的合成和实际压采水流进行了评估。在 MD/FO 面积比为 7:1(分别为 0.105 m2 和 0.015 m2)的情况下,MD 的渗透产量是原来的两倍,达到 0.4 L/h,而在 MD 和 FO 膜面积相同(各为 0.015 m2)的情况下,渗透产量是原来的两倍。最终产品水的电导率为 364.9 ± 2.7 μS/cm,与典型的饮用水电导率相当,这意味着其具有再利用的潜力,并能最大限度地减少有害废物的数量。MD 渗透水质分析表明,主要离子浓度降低了 99%,化学需氧量降低了 90.1%。利用实际产生的液流进行的连续操作导致 MD 活性层上出现部分孔隙湿润。显微镜检查显示,油脂沉积和 NaCl/CaSO4 在 FO 膜两侧结垢造成了有机污垢。这些结果表明,应采用 PW 预处理来减轻膜污垢和孔隙湿润。在利用真实的 DE 和 WO 流进行的实验中,我们还观察到 7.07 g/m2 h 的反向溶质通量。这项研究的结果有助于确定系统放大过程中出现的挑战,并为整合 FO-MD 混合技术从油气设施中回收水提供依据。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Pre-pilot forward osmosis – Membrane distillation hybrid system for sustainable produced water treatment and reducing volume of hazardous waste in oil and gas industry

Pre-pilot forward osmosis – Membrane distillation hybrid system for sustainable produced water treatment and reducing volume of hazardous waste in oil and gas industry
This study introduces pre-pilot scale hybrid forward osmosis - membrane distillation (FO-MD) module, designed for the simultaneous treatment of different challenging produced water (PW) streams from Oil &Gas Industry. In this module, hot draw solution simultaneously serves as MD feed solution. The performance of this module was assessed with synthetic and real PW streams for extended operating times. The MD permeate production was doubled and comprised 0.4 L/h for 7:1 MD/FO area ratio (0.105 m2 and 0.015 m2, respectively) compared to permeate production that was observed with equal MD and FO membrane area (0.015 m2 each). The conductivity of the final product water was 364.9 ± 2.7 μS/cm, comparable to the typical potable water conductivity, implying its potential for reuse applications and minimizing volume of hazardous waste. Analysis of MD permeate quality showed that concentration of major ions was reduced by >99 % and chemical oxygen demand was removed by 90.1 %. Continuous operation with real produced streams led to partial pore wetting on the MD active layer. The microscopy showed organic fouling caused by oil and grease deposition and NaCl/CaSO4 scaling was found on both sides of FO membrane. These results suggest that PW pretreatment should be implemented to alleviate membrane fouling and pore wetting. We also observed reverse solute flux of 7.07 g/m2 h in experiments utilizing real DE and WO streams. The results of this study helped to identify challenges arising from the system scale-up and provide grounds for integrating hybrid FO-MD technology to recover water from oil and gas facilities.
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来源期刊
Journal of water process engineering
Journal of water process engineering Biochemistry, Genetics and Molecular Biology-Biotechnology
CiteScore
10.70
自引率
8.60%
发文量
846
审稿时长
24 days
期刊介绍: The Journal of Water Process Engineering aims to publish refereed, high-quality research papers with significant novelty and impact in all areas of the engineering of water and wastewater processing . Papers on advanced and novel treatment processes and technologies are particularly welcome. The Journal considers papers in areas such as nanotechnology and biotechnology applications in water, novel oxidation and separation processes, membrane processes (except those for desalination) , catalytic processes for the removal of water contaminants, sustainable processes, water reuse and recycling, water use and wastewater minimization, integrated/hybrid technology, process modeling of water treatment and novel treatment processes. Submissions on the subject of adsorbents, including standard measurements of adsorption kinetics and equilibrium will only be considered if there is a genuine case for novelty and contribution, for example highly novel, sustainable adsorbents and their use: papers on activated carbon-type materials derived from natural matter, or surfactant-modified clays and related minerals, would not fulfil this criterion. The Journal particularly welcomes contributions involving environmentally, economically and socially sustainable technology for water treatment, including those which are energy-efficient, with minimal or no chemical consumption, and capable of water recycling and reuse that minimizes the direct disposal of wastewater to the aquatic environment. Papers that describe novel ideas for solving issues related to water quality and availability are also welcome, as are those that show the transfer of techniques from other disciplines. The Journal will consider papers dealing with processes for various water matrices including drinking water (except desalination), domestic, urban and industrial wastewaters, in addition to their residues. It is expected that the journal will be of particular relevance to chemical and process engineers working in the field. The Journal welcomes Full Text papers, Short Communications, State-of-the-Art Reviews and Letters to Editors and Case Studies
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