RISS 학술연구정보서비스

검색
다국어 입력

http://chineseinput.net/에서 pinyin(병음)방식으로 중국어를 변환할 수 있습니다.

변환된 중국어를 복사하여 사용하시면 됩니다.

예시)
  • 中文 을 입력하시려면 zhongwen을 입력하시고 space를누르시면됩니다.
  • 北京 을 입력하시려면 beijing을 입력하시고 space를 누르시면 됩니다.
닫기
    인기검색어 순위 펼치기

    RISS 인기검색어

      SCOPUS KCI등재

      시멘트 분쇄에 포화 알코올이 미치는 영향 ( 2 ) = Effect of Saturated Alcohol on Cement Crushing ( 2 )

      한글로보기

      https://www.riss.kr/link?id=A3088605

      • 0

        상세조회
      • 0

        다운로드
      서지정보 열기
      • 내보내기
      • 내책장담기
      • 공유하기
      • 오류접수

      부가정보

      다국어 초록 (Multilingual Abstract)

      Use of iterative stepwise methods has been a common practice in designing multicomponent distillation columns, Sometimes, it is difficult to justify iterative calculations from the point of view of cost·effectiveness, particularly when the input information does not have precision or accuracy, or when one simply does not have sufficient information for the system under study. In this work a new method was proposed whereby quick and simple procedures give rise to values of 14 different parameters needed for the design of a column for a multicomponent distillation. Several simplifying assumptions are made in the course; the usual one of a quasi-binary in which the average relative volatility is represented by a geometric mean of relative volatilities of the light key referred to the heavy in the bottoms over the light key referred to the heavy in the distillate, Prater and Boyd`s approximation for column efficiency, approximations for expedience that arise in the actual mechanical fabrications of columns according to the common industrial practice, and other simplifications in the heat exchanger calculations. In order to validate the proposed method, comparisons are made with other popular methods such as Smith-Brinkly Short-Cut Method(SB), Fenske-Underwood-Erbar-Maddox Short-Cut Method(FUEM) and Step-by-Step Method(SBSM) by means of an actual design example. Departure from the results by the Step-by-Step method was about l096, the latter being the method yielding the highest accuracy as well as precision. Also, in this work procedures are presented for calculations of several hardware parameters of a distillation column and of heat exchangers annexed to the column.
      번역하기

      Use of iterative stepwise methods has been a common practice in designing multicomponent distillation columns, Sometimes, it is difficult to justify iterative calculations from the point of view of cost·effectiveness, particularly when the input info...

      Use of iterative stepwise methods has been a common practice in designing multicomponent distillation columns, Sometimes, it is difficult to justify iterative calculations from the point of view of cost·effectiveness, particularly when the input information does not have precision or accuracy, or when one simply does not have sufficient information for the system under study. In this work a new method was proposed whereby quick and simple procedures give rise to values of 14 different parameters needed for the design of a column for a multicomponent distillation. Several simplifying assumptions are made in the course; the usual one of a quasi-binary in which the average relative volatility is represented by a geometric mean of relative volatilities of the light key referred to the heavy in the bottoms over the light key referred to the heavy in the distillate, Prater and Boyd`s approximation for column efficiency, approximations for expedience that arise in the actual mechanical fabrications of columns according to the common industrial practice, and other simplifications in the heat exchanger calculations. In order to validate the proposed method, comparisons are made with other popular methods such as Smith-Brinkly Short-Cut Method(SB), Fenske-Underwood-Erbar-Maddox Short-Cut Method(FUEM) and Step-by-Step Method(SBSM) by means of an actual design example. Departure from the results by the Step-by-Step method was about l096, the latter being the method yielding the highest accuracy as well as precision. Also, in this work procedures are presented for calculations of several hardware parameters of a distillation column and of heat exchangers annexed to the column.

      더보기

      동일학술지(권/호) 다른 논문

      동일학술지 더보기

      더보기

      분석정보

      View

      상세정보조회

      0

      Usage

      원문다운로드

      0

      대출신청

      0

      복사신청

      0

      EDDS신청

      0

      동일 주제 내 활용도 TOP

      더보기

      주제

      연도별 연구동향

      연도별 활용동향

      연관논문

      연구자 네트워크맵

      공동연구자 (7)

      유사연구자 (20) 활용도상위20명

      이 자료와 함께 이용한 RISS 자료

      나만을 위한 추천자료

      해외이동버튼