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Received April 20, 2011
Accepted May 31, 2011
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열복합 증류탑의 에너지 절감과 엑서지 비교

Energy Conservation and Exergy Comparison of a Fully Thermally Coupled Distillation Column

동아대학교 화학공학과, 604-714 부산시 사하구 하단동 840번지
Department of Chemical Engineering, Dong-A University, 840 Hadan-dong, Saha-gu, Busan 604-714, Korea
Korean Chemical Engineering Research, February 2012, 50(1), 55-60(6), NONE Epub 2 February 2012
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Abstract

분리벽형 증류탑으로 상용화된 열복합 증류 시스템의 에너지 절약효과와 엑서지 손실을 기존의 3성분 분리 시스템인 2 탑 증류탑의 에너지 사용량 및 엑서지 손실과 비교하였다. 비교에 사용한 예제공정으로 석유화학 공장에서 보편적으로 사용하는 벤젠-톨루엔-m-자일렌 분리 공정을 대상으로 하였다. 본 연구에서는 열복합 증류탑의 설계방법을 제시하고 HYSYS를 이용하여 계산된 에너지 사용량을 비교하였다. 동일한 증류단수를 사용하였을 때 열복합 증류 시스템이 에너지 사용량을 28.2% 절감할 수 있음을 알았으며, 엑서지 손실은 10.4% 더 많았다. 엑서지 손실의 증가는 열복합 증류탑의 양방향 연결 흐름에 의한 증류단 내에서의 추가적인 혼합과 주탑 하부에서의 압력상승에 의한 재비기에서의 온도 상승이 주요 원인이다.
The energy conservation and exergy loss of a fully thermally coupled distillation commercialized as the divided wall column are compared with those of a conventional two-column system for ternary separation. The used example for the comparison is the benzene-toluene-m-xylene separation process widely used in a petrochemical plant. The design procedure of the fully thermally coupled distillation column is explained, and the energy requirement is compared_x000D_ using the HYSYS. When the same numbers of trays are utilized, the fully thermally coupled distillation column uses 28.2% less energy and 10.4% more exergy loss. The increase of the exergy loss is due to the additional mixing from the bidirectional inter-linking and the temperature elevation in the reboiler from the increased pressure at the bottom of the main column.

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