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      철 석출장치가 결합된 무산소.호기공정에 의한 인 제거 특성 = Phosphorus Removal (Characteristics by Anoxic Oxic Process) by Anoxic and Oxic Processed Combined with Iron Electrolysis

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      https://www.riss.kr/link?id=A103755069

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      다국어 초록 (Multilingual Abstract)

      In this study, the (phosphorous removal) the characteristics of phosphorous removal due to (the iron compound precipitated) iron compound precipitation by iron electrolysis in (the anoxic. oxic process) anoxic and oxic processes (equipped with the) in an iron precipitation device were analyzed. During the device operation period, the average concentration of BOD, T-N, and T-P were 219.9 mg/l, 54.6 mg/l and 6.71 mg/l, respectively. The BOD/$COD_{Cr}$ ratio was 0.74, and the BOD/T-N and BOD/T-P ratios were 4.0 and 32.8, respectively. The removal rate of (the organic matters) organic matter (BOD and $COD_{Cr}$) was very high at 91.6% or higher, and that of nitrogen was 80.5%. The phosphorous concentration (of the final) in the treated water was 0.43 mg/l (0.05-0.74 mg/l) on average, and the removal efficiency was high at 90.8%. The soluble T-P concentrations in (an) the anoxic reactor, oxic reactor (II) and final treated water were 1.99 mg/l, 0.79 mg/l and 0.43 mg/l, respectively, which indicated that the phosphorous concentration in the treated water was very low. Regardless of the changes in the concentrations of (organic matters) organic matter, nitrogen and phosphorous in the influent, the quality of the treated water was relatively stable and high. The removal rate of T-P somewhat increased with the increase in the F/M ratio in the influent, and it also linearly increased in proportion to the T-P loading rate in the influent. In the treatment process used in this study, phosphorous was removed (using) by the precipitated iron oxide. Therefore, the consumption of organic (matters) matter for biological phosphorus removal was minimized and (most of the organic matters were) was mostly used as the organic carbon source for the denitrification in the anoxic reactor. This (can be an economic) treatment process (without the need for the supply of additional organic matters) is economic and does not require the supply of additional organic matter.
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      In this study, the (phosphorous removal) the characteristics of phosphorous removal due to (the iron compound precipitated) iron compound precipitation by iron electrolysis in (the anoxic. oxic process) anoxic and oxic processes (equipped with the) in...

      In this study, the (phosphorous removal) the characteristics of phosphorous removal due to (the iron compound precipitated) iron compound precipitation by iron electrolysis in (the anoxic. oxic process) anoxic and oxic processes (equipped with the) in an iron precipitation device were analyzed. During the device operation period, the average concentration of BOD, T-N, and T-P were 219.9 mg/l, 54.6 mg/l and 6.71 mg/l, respectively. The BOD/$COD_{Cr}$ ratio was 0.74, and the BOD/T-N and BOD/T-P ratios were 4.0 and 32.8, respectively. The removal rate of (the organic matters) organic matter (BOD and $COD_{Cr}$) was very high at 91.6% or higher, and that of nitrogen was 80.5%. The phosphorous concentration (of the final) in the treated water was 0.43 mg/l (0.05-0.74 mg/l) on average, and the removal efficiency was high at 90.8%. The soluble T-P concentrations in (an) the anoxic reactor, oxic reactor (II) and final treated water were 1.99 mg/l, 0.79 mg/l and 0.43 mg/l, respectively, which indicated that the phosphorous concentration in the treated water was very low. Regardless of the changes in the concentrations of (organic matters) organic matter, nitrogen and phosphorous in the influent, the quality of the treated water was relatively stable and high. The removal rate of T-P somewhat increased with the increase in the F/M ratio in the influent, and it also linearly increased in proportion to the T-P loading rate in the influent. In the treatment process used in this study, phosphorous was removed (using) by the precipitated iron oxide. Therefore, the consumption of organic (matters) matter for biological phosphorus removal was minimized and (most of the organic matters were) was mostly used as the organic carbon source for the denitrification in the anoxic reactor. This (can be an economic) treatment process (without the need for the supply of additional organic matters) is economic and does not require the supply of additional organic matter.

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      참고문헌 (Reference)

      1 조일형, "철 석출장치에 의한 폐수 중의 인 제거 특성" 한국환경보건학회 32 (32): 89-95, 2006

      2 Rabinowitz, B, "Upgrading wastewater treatmentplants for biological nutrient removal" 22 (22): 53-60, 1990

      3 "U.S. EPA : Process Design Manual for PhosphorusControl"

      4 Nicholls, H. A, "The readily biodegradable fraction of sewage ; itsinflunence of phosphorus removal and measurement" 17 : 73-87, 1985

      5 Goncalves, R. F, "Primary fermentation of soluble and particulateorganic matter for wastewater treatment" 30 (30): 53-62, 1994

      6 Groterud O, "Phosphorusremoval from water by means of electrolysis" 20 (20): 667-669, 1986

      7 James, B. R, "Phosphorus sorption by peat and sand amended withiron oxiders or steel wool" 64 (64): 699-705, 1967

      8 Kavanaugh, M. C, "Phosphorus removal by postprecipitationwith Fe(III)" 50 : 216-233, 1978

      9 Gangol,N, "Phosphate adsorptionstudies" 45 (45): 842-849, 1973

      10 NIER, "NIER, HRERC : Feasibility study on the applicationof physicochemical process for phosphorous removalin environmental facilities located in upper reaches ofthe watershed lake" GOVP1200947842 160-169, 2009

      1 조일형, "철 석출장치에 의한 폐수 중의 인 제거 특성" 한국환경보건학회 32 (32): 89-95, 2006

      2 Rabinowitz, B, "Upgrading wastewater treatmentplants for biological nutrient removal" 22 (22): 53-60, 1990

      3 "U.S. EPA : Process Design Manual for PhosphorusControl"

      4 Nicholls, H. A, "The readily biodegradable fraction of sewage ; itsinflunence of phosphorus removal and measurement" 17 : 73-87, 1985

      5 Goncalves, R. F, "Primary fermentation of soluble and particulateorganic matter for wastewater treatment" 30 (30): 53-62, 1994

      6 Groterud O, "Phosphorusremoval from water by means of electrolysis" 20 (20): 667-669, 1986

      7 James, B. R, "Phosphorus sorption by peat and sand amended withiron oxiders or steel wool" 64 (64): 699-705, 1967

      8 Kavanaugh, M. C, "Phosphorus removal by postprecipitationwith Fe(III)" 50 : 216-233, 1978

      9 Gangol,N, "Phosphate adsorptionstudies" 45 (45): 842-849, 1973

      10 NIER, "NIER, HRERC : Feasibility study on the applicationof physicochemical process for phosphorous removalin environmental facilities located in upper reaches ofthe watershed lake" GOVP1200947842 160-169, 2009

      11 류홍덕, "Expanded polystylene(EPS) 여재를 이용한 BNR(Biological Nutrient Removal) 공정 개발" 대한환경공학회 28 (28): 1-6, 2006

      12 "Environmental Protection Agency"

      13 "Envinet. Co. Ltd., Gakuyng Cosmo, Daejin Environment: Phosphorus Removal by Anoxic · Oxic Pilot-Plant adding ferrous compound by Iron Electrolysis"

      14 Bard, A. T, "Encyclopedia of electrochemistry of theelements" 4 : 230-360, 1982

      15 "EPA : Phosphorus Removal Design Manual" EnvironmtalProtection Agency 1-87, 1987

      16 "APHA-AWWA-WPCF : Standard methods for theexamination of water and wastewater" American PublicHealth Association 2002

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      학술지 이력

      학술지 이력
      연월일 이력구분 이력상세 등재구분
      2022 평가예정 계속평가 신청대상 (등재유지)
      2017-01-01 평가 우수등재학술지 선정 (계속평가)
      2013-01-01 평가 등재 1차 FAIL (등재유지) KCI등재
      2010-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2008-02-15 학술지명변경 외국어명 : Korean Journal of Environmental Health -> JOURNAL OF ENVIRONMENTAL HEALTH SCIENCES KCI등재
      2008-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2006-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2005-09-13 학술지등록 한글명 : 한국환경보건학회지
      외국어명 : Korean Journal Of Environmental Health
      KCI등재
      2005-06-02 학술지등록 한글명 : 한국환경보건학회지
      외국어명 : Korean Journal of Environmental Health
      KCI등재
      2005-01-27 학회명변경 한글명 : 한국환경위생학회 -> 한국환경보건학회
      영문명 : Korean Society Of Environmental Health -> Korean Society of Environmental Health
      KCI등재
      2003-01-01 평가 등재학술지 선정 (등재후보2차) KCI등재
      2002-01-01 평가 등재후보 1차 PASS (등재후보1차) KCI등재후보
      1999-01-01 평가 등재후보학술지 선정 (신규평가) KCI등재후보
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      학술지 인용정보

      학술지 인용정보
      기준연도 WOS-KCI 통합IF(2년) KCIF(2년) KCIF(3년)
      2016 0.44 0.44 0.4
      KCIF(4년) KCIF(5년) 중심성지수(3년) 즉시성지수
      0.42 0.4 0.605 0.21
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