The Effect of Supported Liquid Membrane and Liquid Membrane Phase on the Extraction Efficiency of Coal Gasification Wastewater

Authors

  • Yao Jie School of Municipal and Environmental Engineering, Harbin Institute of Technology, Harbin150090, P.R. China
  • Du Ziwei National Engineering Centre of Urban Water Resources, 202 Hehai Road, Harbin150090, P.R. China
  • You Hong School of Municipal and Environmental Engineering, Harbin Institute of Technology, Harbin150090, P.R. China
  • Yang Shuren National Engineering Centre of Urban Water Resources, 202 Hehai Road, Harbin150090, P.R. China
  • Li Biaoming Municipal Planning and Designing Institute of Changchun, No.8888, Ziyou Road Changchun130000, P.R. China
  • Wang Zhongwei National Engineering Centre of Urban Water Resources
  • Sjack van Agtmaal Evides Industriewater B.V. Schaardijk 150, 3063 NH Rotterdam, The Netherlands
  • Feng Chunhui Evides Industriewater B.V. Schaardijk 150
  • Han Bangjun School of Civil Engineering, Heilongjiang University, Xuefu Road, Harbin150090, P.R. China

DOI:

https://doi.org/10.6000/1929-6037.2013.02.03.4

Keywords:

Supported liquid membrane, extracting agent, coal gasification wastewater, phenol recovery

Abstract

The extraction and recovery of phenol from high concentration coal gasification wastewater has been investigated using polypropylene (PP) hollow fiber membranes and polyvinylidene fluoride (PVDF) hollow fiber membranes as supported liquid membrane and the mixture of extraction agent and paraffin as liquid membrane phase, with sodium hydroxide as stripping agent. The effect of the composition of the liquid membrane phase made of N-503-kerosene, tributyl phosphate (TBP)-kerosene or trialkyl phosphine oxide (TRPO)-kerosene on extraction efficiency has been studied. The supported liquid membrane give novel extraction result for the extraction of phenol from high concentration coal gasification wastewater when proper liquid membrane phases and liquid membrane support body materials are used in supported liquid membrane system. Under the operating conditions of waste water temperature at 20 ˚C pH at 8.4, waste water and stripping phase flow rate at 5 L/h, the supported liquid membrane using PP as supported liquid membrane and the extraction agent of TBP with volume proportion of 20% could operate continuously and stablely more than 24 hours and the extraction efficiency be 4% higher than that of PVDF-TBP supported liquid membrane systems.

References

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Jie Y, Zhi-Ru H, An-Guo L, et al. Supported liquid membrane extraction to treat coal gasification wastewater containing high concentrations phenol [J]. J Harbin Instit Technol 2012; 19(1). http://d.wanfangdata.com.cn/periodical_hebgydxxb-e201201011.aspx

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Published

2013-08-31

How to Cite

Jie, Y., Ziwei, D., Hong, Y., Shuren, Y., Biaoming, L., Zhongwei, W., Agtmaal, S. van, Chunhui, F., & Bangjun, H. (2013). The Effect of Supported Liquid Membrane and Liquid Membrane Phase on the Extraction Efficiency of Coal Gasification Wastewater. Journal of Membrane and Separation Technology, 2(3), 191–197. https://doi.org/10.6000/1929-6037.2013.02.03.4

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