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      소규모 해수담수화시설 물 생산량 제고 방안 - 전라남도 해수담수화시설을 중심으로 - = A Study on the Improvement of Water Production in Small-Scale Desalination Plants

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      https://www.riss.kr/link?id=A109043229

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      다국어 초록 (Multilingual Abstract) kakao i 다국어 번역

      Desalination was a water treatment process that involved converting saline water to fresh water. Desalination generated an estimated 0.03 hundred million ㎥/day of fresh water in Korea. But, water shortage problems in the island area were not solved regarding the low capacity of desalination plants, the low amount of available salinity groundwater, etc. Furthermore, the low recovery rate of freshwater, lack of expertise of local operators, water leakage and contamination by old pipelines needed to be improved. This study used a reverse osmosis system projection program to compare compared desalination processes to improve water production and decrease electricity consumption.
      It was investigated that over 80 % of small-scale desalination plants in Jeollanam-do produced 50 ㎥/day. The total dissolved solids of feed water were at least 115 mg/L, up to 28,273 mg/L, an average of 5,676 mg/L, and the water temperature of raw water was at least 5.2 ℃, up to 28.1 ℃, and the average of 17.0 ℃. Based on the investigation results, plant capacity and the total dissolved solids of the final freshwater for performance simulation were set at 50 ㎥/day, 500 mg/L, and the total dissolved solids and temperature of raw water were set at 6,500 mg/L, and 17 ℃. The process compared and analyzed changes in the quality and quantity of freshwater by designing the ‘1st RO’ process, the ‘1st RO + ERD’ process with an energy recovery device added, the ‘1st RO + Recirculation’ process, and the ‘2nd RO + Recirculation’ process.
      In the ‘1st RO’ process, 200 ㎥/day of feed water was required to produce 50 ㎥/day of fresh water, but in the ‘1st RO + Recirculation’ process and the ‘2nd RO + Recirculation’ process, the amount of feed water required could be reduced to 83.3 ㎥/day and 66.7 ㎥/day. The ‘1st RO’ process consumed 1.47 kWh/㎥. However, in the ‘1st RO + ERD’ process, it is lowered to 0.45 kWh/㎥. The recovery rate was increased by 75 % in the ‘2nd RO + Recirculation’ process. Finally, reducing the electric energy consumed in freshwater production in summer was possible.
      When replacing old desalination plants or installing new ones, the ‘1st RO + ERD’ process, which can lower electricity consumption, should be considered rather than the ‘1st RO’ process, the ‘1st RO + Recirculation’ process and the ‘2nd RO + Recirculation’ process, which could increase waster production.
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      Desalination was a water treatment process that involved converting saline water to fresh water. Desalination generated an estimated 0.03 hundred million ㎥/day of fresh water in Korea. But, water shortage problems in the island area were not solved ...

      Desalination was a water treatment process that involved converting saline water to fresh water. Desalination generated an estimated 0.03 hundred million ㎥/day of fresh water in Korea. But, water shortage problems in the island area were not solved regarding the low capacity of desalination plants, the low amount of available salinity groundwater, etc. Furthermore, the low recovery rate of freshwater, lack of expertise of local operators, water leakage and contamination by old pipelines needed to be improved. This study used a reverse osmosis system projection program to compare compared desalination processes to improve water production and decrease electricity consumption.
      It was investigated that over 80 % of small-scale desalination plants in Jeollanam-do produced 50 ㎥/day. The total dissolved solids of feed water were at least 115 mg/L, up to 28,273 mg/L, an average of 5,676 mg/L, and the water temperature of raw water was at least 5.2 ℃, up to 28.1 ℃, and the average of 17.0 ℃. Based on the investigation results, plant capacity and the total dissolved solids of the final freshwater for performance simulation were set at 50 ㎥/day, 500 mg/L, and the total dissolved solids and temperature of raw water were set at 6,500 mg/L, and 17 ℃. The process compared and analyzed changes in the quality and quantity of freshwater by designing the ‘1st RO’ process, the ‘1st RO + ERD’ process with an energy recovery device added, the ‘1st RO + Recirculation’ process, and the ‘2nd RO + Recirculation’ process.
      In the ‘1st RO’ process, 200 ㎥/day of feed water was required to produce 50 ㎥/day of fresh water, but in the ‘1st RO + Recirculation’ process and the ‘2nd RO + Recirculation’ process, the amount of feed water required could be reduced to 83.3 ㎥/day and 66.7 ㎥/day. The ‘1st RO’ process consumed 1.47 kWh/㎥. However, in the ‘1st RO + ERD’ process, it is lowered to 0.45 kWh/㎥. The recovery rate was increased by 75 % in the ‘2nd RO + Recirculation’ process. Finally, reducing the electric energy consumed in freshwater production in summer was possible.
      When replacing old desalination plants or installing new ones, the ‘1st RO + ERD’ process, which can lower electricity consumption, should be considered rather than the ‘1st RO’ process, the ‘1st RO + Recirculation’ process and the ‘2nd RO + Recirculation’ process, which could increase waster production.

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      참고문헌 (Reference)

      1 한국수자원공사, "해수담수화 사업"

      2 이현경, "해수담수화" 한국과학기술기획평가원 12-16, 2021

      3 전종민 ; 김수한, "하수재이용 및 해수담수화를 위한 정삼투-역삼투 융합공정의 탄소배출량 분석" 대한토목학회 42 (42): 351-357, 2022

      4 김택승, "태양에너지 시스템과 해수담수화 공정의 최적 조합 모델 선정을 위한 설계 플랫폼 개발" 한국태양에너지학회 10 : 75-, 2019

      5 손진식, "차세대 해수담수화 플랜트 산업 및 기술동향 브리프" 국토해양지식정보센터 8-10, 2013

      6 홍승관, "중동 시장 진출을 위한 현지맞춤형 저에너지 해수담수화 기술 개발" 대한토목학회 67 (67): 26-37, 2019

      7 윤승현 ; 우달식, "원수 특성 변화 및 공정운영 조건에 따른 해수담수화 에너지 소비량 분석" 대한상하수도학회 33 (33): 286-288, 2019

      8 정재학 ; 김누리 ; 전종민 ; 김수한, "역삼투 공정 설계 프로그램의 신뢰성 평가" 대한환경공학회 41 (41): 42-47, 2019

      9 김지혜 ; 이경혁 ; 임재림, "에너지 소모를 고려한 역삼투 해수담수화 플랜트 주요 성능인자 영향 분석" 한국막학회 29 (29): 314-322, 2019

      10 국가통계포탈, "수도요금 현황"

      1 한국수자원공사, "해수담수화 사업"

      2 이현경, "해수담수화" 한국과학기술기획평가원 12-16, 2021

      3 전종민 ; 김수한, "하수재이용 및 해수담수화를 위한 정삼투-역삼투 융합공정의 탄소배출량 분석" 대한토목학회 42 (42): 351-357, 2022

      4 김택승, "태양에너지 시스템과 해수담수화 공정의 최적 조합 모델 선정을 위한 설계 플랫폼 개발" 한국태양에너지학회 10 : 75-, 2019

      5 손진식, "차세대 해수담수화 플랜트 산업 및 기술동향 브리프" 국토해양지식정보센터 8-10, 2013

      6 홍승관, "중동 시장 진출을 위한 현지맞춤형 저에너지 해수담수화 기술 개발" 대한토목학회 67 (67): 26-37, 2019

      7 윤승현 ; 우달식, "원수 특성 변화 및 공정운영 조건에 따른 해수담수화 에너지 소비량 분석" 대한상하수도학회 33 (33): 286-288, 2019

      8 정재학 ; 김누리 ; 전종민 ; 김수한, "역삼투 공정 설계 프로그램의 신뢰성 평가" 대한환경공학회 41 (41): 42-47, 2019

      9 김지혜 ; 이경혁 ; 임재림, "에너지 소모를 고려한 역삼투 해수담수화 플랜트 주요 성능인자 영향 분석" 한국막학회 29 (29): 314-322, 2019

      10 국가통계포탈, "수도요금 현황"

      11 김정빈 ; 홍승관, "미래 그린 해수담수화 기술" 대한상하수도학회 34 (34): 403-410, 2020

      12 법제처, "먹는물관리법"

      13 최인수, "도서지역 해수담수화시설의 효율적인 운영방안 연구" 한국지방행정연구원 50-63, 2015

      14 최창규 ; 김창민 ; 임주환 ; 김동호 ; 김인수, "국내 역삼투 방식 해수담수화 플랜트 시설 용량별 에너지 사용량 기반 경제성 분석" 대한환경공학회 41 (41): 389-398, 2019

      15 황문현 ; 김인수, "국내 및 해외의 해수담수화 기술 비교분석" 대한환경공학회 38 (38): 255-268, 2016

      16 "국가물관리위원회"

      17 "국가물관리위원회"

      18 Mark W., "The Guidebook to Membrane Desalination Technology" Balaban Desalination Publications 5-20, 2006

      19 박경태 ; 이상현, "LNG 냉열 기반 해수담수화 공정의 설계 및 분석" 한국화학공학회 60 (60): 371-376, 2022

      20 환경부, "2024년 주요업무 추진계획"

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