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Fabrication of high-performance pervaporation desalination composite membranes with study of its acid-base stability
被引:0
|作者:
Yang, Menghan
[1
]
Niu, Chenghao
[1
]
Guo, Yifei
[2
]
Cao, Bing
[2
]
Zhang, Rui
[2
]
机构:
[1] Beijing Univ Chem Technol, Coll Mat Sci & Engn, Beijing 100029, Peoples R China
[2] Beijing Univ Chem Technol, Coll Chem Engn, Beijing 100029, Peoples R China
关键词:
Perfluorosulfonic acid;
High performance pervaporation membrane;
Membrane forming structure and mechanism;
Concentration of acid and base solutions;
WASTE-WATER;
PERFLUOROSULFONIC IONOMER;
ELECTRODIALYSIS;
SEPARATION;
IMPACT;
D O I:
10.1016/j.seppur.2024.129277
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
In the process of industrial production will produce a lot of acid and alkaline waste liquid, how to effectively treat acid and alkali waste liquid is an important topic at present. At present, there are some problems about the treatment of acid and alkali waste liquid, such as large investment, complicated process and low efficiency. Pervaporation has the characteristics of mild operating conditions and no influence of osmotic pressure threshold, so it has great application potential in the concentration, reuse and reduction of acid and alkali waste liquid. However, at present, conventional pervaporation dense membrane materials cannot maintain long-term stability in strong acid and alkali environment, in order to achieve this performance, we use perfluorosulfonic acid resin with good acid and alkali resistance as the dense layer substrate. PFSA/PTFE/PP composite membrane was prepared by spraying process, and the final prepared composite membrane had a pure water flux of 45 +/- 1.2 kg/(m2 center dot h) 2 center dot h) at 70 degree celsius. The acid and alkali resistance of the intrinsic membrane and the composite membrane was evaluated, and it was found that the feed liquid was concentrated to 20 wt% after 19 h long concentration operation at 70degree celsius and starting liquid was 5 wt% H2SO4 2 SO 4 and 5 wt% NaOH. The retention rate of acid and alkali can be maintained above 99.9 %. During the concentration of H2SO4 2 SO 4 solution, the dense layer structure is affected, and the pure water flux of the composite membrane is reduced, eventually maintaining around 32 kg/ (m2 center dot h). 2 center dot h). In the process of concentrating NaOH solution, the pure water flux of the composite membrane increased first and then decreased, and the final pure water flux of the membrane remained near 40 kg/(m2 center dot h). 2 center dot h).
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页数:17
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