막 증발법(Membrane Distillation)을 이용한 고농도 하･폐수처리 가능성 연구

서지정보

ㆍ발행기관 : 대한상하수도학회 ㆍ수록지정보 : 상하수도학회지 / 29권 / 2호
ㆍ저자명 : 김세운, 이동우, 민경진, 조진우

영어 초록

In this study, we applied a membrane distillation process to investigate a feasibility of treating a wastewater with high concentration of organic matters including nitrogen and phosphorus. The laboratory scale experiment was performed by using a hydrophobic PVDF membrane with the pore size of 0.22 m and porosity of 75%. The installation was direct contact type where the temperature difference between a feed and permeate side was controlled to have a range from 20 to 60C. We observed a flux variation and a concentration changes of COD, PO4 3-－P, NH4 + -N and conductivity of feed side as well as permeate side with various temperature differences (20 to 60C), cross flow velocities (0.09 to 0.27 m/s) through the module, and pH (6.6 to 12.0) of the feed that has the initial concentration of COD about 1,000 mg/L, total nitrogen 390 mg/L, total phosphorus 10 mg/L, conductivity of 7,000 s/cm. The results showed that the average flux was ranged from 4 to 40 L/m2/hr which was almost similar with the flux of NaCl and deionized water used as a feed solution. The lowest flux was obtained at the operating condition with the temperature difference of 20C and cross flow velocity of 0.09 m/s while the highest one was measured with 60C and 0.27 m/s. Above 99% of COD and PO4 3- -P in the feed could be rejected regardless of an operating condition. However, the removal rate of ammonium nitrogen was varied from 64 to 99% depending on the pH of feed solution.

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