Boosting vapor flux in osmotic distillation: A comprehensive evaluation of operating conditions and membrane properties

IF 5.5 Q1 ENGINEERING, CHEMICAL
Longxi Zhou, Di He, Zhangxin Wang, Yuanmiaoliang Chen
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Abstract

Osmotic distillation (OD) presents a promising technique for desalination in seawater electrolysis, but its effectiveness is hindered by low vapor flux and limited operational efficiency. This study employs a theoretical model to evaluate how operating conditions and membrane properties impact OD vapor flux. For conventional membranes, optimizing parameters mitigates concentration and temperature polarization but provides only modest increase in vapor flux, as the membrane contributes the majority of mass transfer resistance. With 0.6 M NaCl/3.5 M K2CO3 as feed/draw solutions, regardless of operating condition, the vapor flux of conventional membranes cannot exceed 0.94 kg m-2 h-1. In contrast, improving membrane properties, which leads to vapor permeability (Bm) enhancement, offers significantly more potential for increasing vapor flux. However, this improvement must be paired with an increased thermal conduction coefficient (Km,d) to avoid severe temperature polarization. Furthermore, our modeling results further indicate that operating condition optimization has a markedly larger impact on advanced membranes with improved Bm and Km,d than conventional membranes (60.7 % vs. 8.3 % vapor flux increase). These findings underscore the necessity for research efforts to prioritize the advancement of membrane design, while subsequent studies can focus on optimizing operating conditions alongside these improved membranes. This approach will significantly improve OD vapor flux and provide critical insights for the future development of OD technology, thereby facilitating its application in seawater electrolysis.

Abstract Image

提高渗透蒸馏中的蒸汽通量:操作条件和膜性能的综合评价
渗透蒸馏(OD)是一种很有前途的海水电解脱盐技术,但由于蒸汽通量低和操作效率有限,影响了其效果。本研究采用理论模型来评估操作条件和膜性能对OD蒸气通量的影响。对于传统膜,优化参数可以减轻浓度和温度极化,但只提供适度的蒸汽通量增加,因为膜贡献了大部分传质阻力。以0.6 M NaCl/3.5 M K2CO3为进料/提取液,无论在何种工况下,常规膜的汽通量都不能超过0.94 kg M -2 h-1。相反,改善膜的性能,导致蒸汽渗透性(Bm)增强,为增加蒸汽通量提供了更大的潜力。然而,这种改进必须与增加的热传导系数(Km,d)相结合,以避免严重的温度极化。此外,我们的建模结果进一步表明,与传统膜相比,操作条件优化对改善Bm和Km,d的先进膜的影响明显更大(蒸汽通量增加60.7%比8.3%)。这些发现强调了研究工作优先考虑膜设计的必要性,而后续的研究可以集中在优化操作条件以及这些改进的膜上。该方法将显著提高OD蒸汽通量,为OD技术的未来发展提供重要见解,从而促进其在海水电解中的应用。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
Chemical Engineering Journal Advances
Chemical Engineering Journal Advances Engineering-Industrial and Manufacturing Engineering
CiteScore
8.30
自引率
0.00%
发文量
213
审稿时长
26 days
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