2013 Volume 7 Issue 4
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Ding Hui, Peng Zhaoyang, Li Yi, Wen Qinxue, Chen Zhiqiang. Treatment of oilfield produced water by inorganic ceramic membrane[J]. Chinese Journal of Environmental Engineering, 2013, 7(4): 1399-1404.
Citation: Ding Hui, Peng Zhaoyang, Li Yi, Wen Qinxue, Chen Zhiqiang. Treatment of oilfield produced water by inorganic ceramic membrane[J]. Chinese Journal of Environmental Engineering, 2013, 7(4): 1399-1404.
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Treatment of oilfield produced water by inorganic ceramic membrane

  • 1.

    Shengli Engineering & Consulting Co. Ltd., Shengli Oil Field, Dongying 257026, China

  • 2.

    State Key Laboratory of Urban Water Resource and Environment, Harbin Institute of Technology, Harbin 150090, China

  • Received Date: 21/06/2012
    Accepted Date: 05/04/2012
    Available Online: 09/04/2013
    Fund Project:
  • The operation parameters and fouling mechanism of ceramic membrane used for treating oilfield produced water were discussed. The field test analyzed the effects of different operation parameters on membrane flux, oil and suspended solid removal efficiency by ceramic membrane, the constituent of membrane resistance and the cleaning method of membrane fouling. Experimental results show that the optimal operation condition are transmembrane pressure of 0.16 MPa, temperature of 50℃ and cross-flow velocity of 5.0 m/s when the quality of the effluent is achieved with A1 standard. Results also show that NaOH combined with HNO3 is helpful to recover membrane flux.
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Treatment of oilfield produced water by inorganic ceramic membrane

  • Received Date: 21/06/2012
  • Accepted Date: 05/04/2012
  • Available Online: 09/04/2013
Fund Project:

Abstract: The operation parameters and fouling mechanism of ceramic membrane used for treating oilfield produced water were discussed. The field test analyzed the effects of different operation parameters on membrane flux, oil and suspended solid removal efficiency by ceramic membrane, the constituent of membrane resistance and the cleaning method of membrane fouling. Experimental results show that the optimal operation condition are transmembrane pressure of 0.16 MPa, temperature of 50℃ and cross-flow velocity of 5.0 m/s when the quality of the effluent is achieved with A1 standard. Results also show that NaOH combined with HNO3 is helpful to recover membrane flux.

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