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用于真空膜蒸馏的疏水性煤飞灰基陶瓷膜的研制

Development of Hydrophobic Coal-Fly-Ash-Based Ceramic Membrane for Vacuum Membrane Distillation.

作者信息

Zhang Zheng, Yang Jihao, Qi Run, Huang Jiguang, Chen Haiping, Zhang Heng

机构信息

School of Energy, Power and Mechanical Engineering, North China Electric Power University, Beijing 102206, China.

Beijing Key Laboratory of Pollutant Monitoring and Control in Thermoelectric Production Process, North China Electric Power University, Beijing 102206, China.

出版信息

Materials (Basel). 2023 Apr 17;16(8):3153. doi: 10.3390/ma16083153.

Abstract

Membrane distillation is an emerging separation technology with a high separation factor in water desalination. Ceramic membranes are increasingly used in membrane distillation because of high thermal and chemical stabilities. Coal fly ash is a promising ceramic membrane material with low thermal conductivity. In this study, three hydrophobic coal-fly-ash-based ceramic membranes were prepared for saline water desalination. The performances of different membranes in membrane distillation were compared. The effects of membrane pore size on permeate flux and salt rejection were researched. The coal-fly-ash-based membrane showed both a higher permeate flux and a higher salt rejection than the alumina membrane. As a result, using coal fly ash as the material for membrane fabrication can effectively increase the performance when applied to MD. Increasing the membrane pore size improved the permeate flux, but reduced the salt rejection. When the mean pore size increased from 0.15 μm to 1.57 μm, the water flux rose from 5.15 L·m·h to 19.72 L·m·h, but the initial salt rejection was reduced from 99.95% to 99.87%. The hydrophobic coal-fly-ash-based membrane with a mean pore size of 0.18 μm exhibited a water flux of 9.54 L·m·h and a salt rejection of higher than 98.36% in membrane distillation.

摘要

膜蒸馏是一种新兴的分离技术,在海水淡化方面具有较高的分离系数。陶瓷膜因其高热稳定性和化学稳定性而越来越多地用于膜蒸馏。粉煤灰是一种很有前景的低导热率陶瓷膜材料。在本研究中,制备了三种基于疏水性粉煤灰的陶瓷膜用于盐水淡化。比较了不同膜在膜蒸馏中的性能。研究了膜孔径对渗透通量和脱盐率的影响。基于粉煤灰的膜比氧化铝膜表现出更高的渗透通量和更高的脱盐率。因此,使用粉煤灰作为膜制造材料在应用于膜蒸馏时可以有效提高性能。增大膜孔径可提高渗透通量,但会降低脱盐率。当平均孔径从0.15μm增加到1.57μm时,水通量从5.15L·m⁻²·h上升到19.72L·m⁻²·h,但初始脱盐率从99.95%降至99.87%。平均孔径为0.18μm的疏水性粉煤灰基膜在膜蒸馏中表现出9.54L·m⁻²·h的水通量和高于98.36%的脱盐率。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/c6bc/10141027/456b602c7c0f/materials-16-03153-g001.jpg

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