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      중공사막 접촉기를 이용한 암모니아 물질전달 모델링 = Modeling of Ammonia Mass Transfer Using a Hollow Fiber Membrane Contactor

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      https://www.riss.kr/link?id=A104796695

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      다국어 초록 (Multilingual Abstract)

      Ammonia in water which is toxic to human, its concentration is regulated below 0.5 mg/L in drinking water. Current study aimed to develop appropriate models for ammonia stripping using hollow fiber membrane contactor. Two different models were developed during the study. Model 1 was assumed only free ammonia (NH_3) transfer in stripping process, whereas the Model 2 was assumed with total ammonia (NH_3^+NH_4^+) transfer. Ammonium chloride (NH_4Cl), sodium hydroxide(NaOH) were used to make ammonia solution, which was concentration of 25 mg as N/L at a pH of 10.5. The experimental conditions were such that, the liquid flow was in tube-side in upward direction and the gas flow was on shell-side in downward direction at room temperature. The experimental and modeling results showed that marginal difference were observed at low gas flux. However the difference between the both models and experimental value were increased when the gas flux was increased. The study concludes that the Model 1 with free ammonia is more appropriate when both models were compared and useful in ammonia stripping process at low gas flux.
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      Ammonia in water which is toxic to human, its concentration is regulated below 0.5 mg/L in drinking water. Current study aimed to develop appropriate models for ammonia stripping using hollow fiber membrane contactor. Two different models were develop...

      Ammonia in water which is toxic to human, its concentration is regulated below 0.5 mg/L in drinking water. Current study aimed to develop appropriate models for ammonia stripping using hollow fiber membrane contactor. Two different models were developed during the study. Model 1 was assumed only free ammonia (NH_3) transfer in stripping process, whereas the Model 2 was assumed with total ammonia (NH_3^+NH_4^+) transfer. Ammonium chloride (NH_4Cl), sodium hydroxide(NaOH) were used to make ammonia solution, which was concentration of 25 mg as N/L at a pH of 10.5. The experimental conditions were such that, the liquid flow was in tube-side in upward direction and the gas flow was on shell-side in downward direction at room temperature. The experimental and modeling results showed that marginal difference were observed at low gas flux. However the difference between the both models and experimental value were increased when the gas flux was increased. The study concludes that the Model 1 with free ammonia is more appropriate when both models were compared and useful in ammonia stripping process at low gas flux.

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      참고문헌 (Reference)

      1 신대운, "폐수의 감압 암모니아 탈기에 관한 연구" 27 (27): 93-99, 2001

      2 정주영, "영가철 충진 회분식 복극전해조에 의한 질산성 질소 제거" 대한토목학회 31 (31): 187-192, 2011

      3 김인원, "다공성 중공사막 기액 접촉기를 이용한 SO2 제거에서 막재질과 흡수제의 영향" 한국가스학회 10 (10): 14-21, 2006

      4 李華永, "水溶液中 암모니아 Recycling을 위한 Air Stripping 特性에 관한 硏究" 한국자원리싸이클링학회 12 (12): 31-37, 2003

      5 P.H. Liao, "Removal of nitrogen from swine manure wastewaters by ammonia stripping" 54 : 17-20, 1995

      6 W. J. Weber, "Process Dynamics in Environmental Systems" Wiley-Interscience 719-725, 1996

      7 X. Tan, "Polyvinylidene fluoride (PVDF) hollow fibre membranes for ammonia removal from water" 271 (271): 59-68, 2006

      8 Z. Qi, "Microporous Hollow Fibers for Gas Absorption: II. Mass Transfer Across The Membrane" 23 : 333-345, 1985

      9 Z. Qi, "Microporous Hollow Fibers for Gas Absorption: I. Mass Transfer in the Liquid" 23 : 321-332, 1985

      10 H. Mahmud, "Mass transport in the membrane air-stripping process using microporous polypropylene hollw fibers: effect of toluene in aqueous feed" 209 : 207-219, 2002

      1 신대운, "폐수의 감압 암모니아 탈기에 관한 연구" 27 (27): 93-99, 2001

      2 정주영, "영가철 충진 회분식 복극전해조에 의한 질산성 질소 제거" 대한토목학회 31 (31): 187-192, 2011

      3 김인원, "다공성 중공사막 기액 접촉기를 이용한 SO2 제거에서 막재질과 흡수제의 영향" 한국가스학회 10 (10): 14-21, 2006

      4 李華永, "水溶液中 암모니아 Recycling을 위한 Air Stripping 特性에 관한 硏究" 한국자원리싸이클링학회 12 (12): 31-37, 2003

      5 P.H. Liao, "Removal of nitrogen from swine manure wastewaters by ammonia stripping" 54 : 17-20, 1995

      6 W. J. Weber, "Process Dynamics in Environmental Systems" Wiley-Interscience 719-725, 1996

      7 X. Tan, "Polyvinylidene fluoride (PVDF) hollow fibre membranes for ammonia removal from water" 271 (271): 59-68, 2006

      8 Z. Qi, "Microporous Hollow Fibers for Gas Absorption: II. Mass Transfer Across The Membrane" 23 : 333-345, 1985

      9 Z. Qi, "Microporous Hollow Fibers for Gas Absorption: I. Mass Transfer in the Liquid" 23 : 321-332, 1985

      10 H. Mahmud, "Mass transport in the membrane air-stripping process using microporous polypropylene hollw fibers: effect of toluene in aqueous feed" 209 : 207-219, 2002

      11 S. Atchariyawut, "Mass transfer study and modeling of gas-liquid membrane contacting process by multistage cascade model for CO2 absorption" 63 : 15-22, 2008

      12 M.A. Lévêque, "Les lois de la transmission de chaleur par convection" 13 : 201-299, 1928

      13 A. Gabelman, "Hollow fiber membrane contactors" 159 : 61-106, 1999

      14 R. Prasad, "Dispersion-free solvent extraction with microporous hollow-fiber modules" 34 : 177-188, 1988

      15 M.C. Yang, "Designing hollow-fiber contactors" 32 : 1910-1915, 1986

      16 M.J. Semmens, "Ammonia Removal From Water Usinig Microporous Hollow Fibers" 51 : 127-140, 1990

      17 X. Quan, "Air stripping of ammonia in a water-sparged aerocyclone reactor" 170 : 983-988, 2009

      18 A. Bonmati, "Air stripping of ammonia from pig slurry: characteristics and feasibility as a pre- or post-treatment to mesophilic anaerobic digestion" 23 (23): 261-272, 2003

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      2026 평가예정 재인증평가 신청대상 (재인증)
      2020-12-28 학술지명변경 외국어명 : Journal of the Korean Society of Water and Wastewater -> Journal of Korean Society of Water and Wastewater KCI등재
      2020-01-01 평가 등재학술지 유지 (재인증) KCI등재
      2017-01-01 평가 등재학술지 유지 (계속평가) KCI등재
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      2000-07-01 평가 등재후보학술지 선정 (신규평가) KCI등재후보
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      기준연도 WOS-KCI 통합IF(2년) KCIF(2년) KCIF(3년)
      2016 0.2 0.2 0.21
      KCIF(4년) KCIF(5년) 중심성지수(3년) 즉시성지수
      0.19 0.15 0.342 0.01
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