Membrane and Water Treatment

  • 제10권5호
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  • Pages.321-330
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  • 2019
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  • 2005-8624(pISSN)
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  • 2092-7037(eISSN)
테크노프레스 (Techno-Press)
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DOI QR코드

DOI QR Code

Membrane distillation of power plant cooling tower blowdown water

  • Ince, Elif (Gebze Technical University, Department of Environmental Engineering) ;
  • Uslu, Yasin Abdullah (Gebze Technical University, Department of Environmental Engineering)
  • 투고 : 2018.10.06
  • 심사 : 2019.04.09
  • 발행 : 2019.09.25
⟨ 이전 논문 다음 논문 ⟩

초록

The objective of this study was to examine the recovery of the power plant cooling tower blowdown water (CTBD) by membrane distillation. The experiments were carried out using a flat plate poly vinylidene fluoride (PVDF) membrane with a pore diameter of $0.22{\mu}m$ by a direct contact membrane distillation unit (DCMD). The effects of operating parameters such as transmembrane temperature difference (${\Delta}T$), circulation rate and operating time on permeate flux and membrane fouling have been investigated. The results indicated that permeate flux increased with increasing ${\Delta}T$ and circulation rate. Whereas maximum permeate flux was determined as $47.4L/m^2{\cdot}h$ at ${\Delta}T$ of $50^{\circ}C$ for all short term experiments, minimum permeate flux was determined as $7.7L/m^2{\cdot}h$ at ${\Delta}T$ of $20^{\circ}C$. While $40^{\circ}C$ was determined as the optimum ${\Delta}T$ in long term experiments. Inorganic and non-volatile substances caused fouling in the membranes.

키워드

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