Articles & Issues
- Language
- korean
- Conflict of Interest
- In relation to this article, we declare that there is no conflict of interest.
- Publication history
-
Received November 16, 2006
Accepted December 13, 2006
Available online March 5, 2007
-
This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits
unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
Copyright © KIChE. All rights reserved.
All issues
석유화학단지 수소 재활용 최적 네트워크 설계
Optimal Hydrogen Recycling Network Design of Petrochemical Complex
서울대학교 화학생물공학부, 151-742 서울시 관악구 신림동 산56-1
School of Chemical and Biological Engineering, Seoul National Universty, San 56-1, Shinlim-dong, Gwanak-gu, Seoul 151-742, Korea
chhan@snu.ac.kr
Korean Chemical Engineering Research, February 2007, 45(1), 25-31(7)
https://doi.org/NONE
https://doi.org/NONE
Download PDF
Abstract
석유화학단지내에서 석유화학공장과 정유공장과 같은 산업현장에서는 상당량의 수소가 부산물로 발생되고 있으나, 이는 대부분 자체적으로 연료로 사용되고 있다. 그러나 연료로 사용되는 상당량의 수소를 에너지원의 원료나 기타 공정의 원료로 재활용할 경우, 현재보다 수소의 가치를 높여서 사용할 수 있다. 본 연구에서는 석유화학단지내 공장간 수소 재활용 네트워크를 설계하였다. 수소 핀치 분석을 통하여 교환망 구성에 필요한 최소의 수소 요구 및 정제량을 파악하고, 네트워크 구성에 필요한 비용과 기타 제약 조건으로 최적화 문제를 구성하여 공급처(source)와 수요처(sink) 공장간에 최적으로 수소를 재활용하기 위한 네트워크를 설계하였다.
In a petrochemical complex, large amount of hydrogen is produced as a by-product and used as a fuel in petrochemical and oil refinery plants. By recycling this byproduct hydrogen as a raw material, the value of hydrogen can be greatly improved. This paper proposes a design methodology for optimal hydrogen recycle network between plants in petrochemical complex by analyzing the hydrogen pinch, required cost and constraints.
References
Linhoff B, Townsend DW, Boland D, Hewitt GF, Thomas BEA, Gut AR, Marsland RH, User Guide on Process Integration for the Efficient Use of Energy, Ins. Chem. Eng., Rugby, UK (1982)
Linhoff B, Chem. Eng. Res. Des., 71, 503 (1993)
Shenoy UV, “Heat Exchanger Network Synthesis: Process Optimization by Energy and Resource Analysis, Gulf Publishing Company,” Houston (1995)
Smith R, Chemical Process Design, McGraw-Hill, NY (1995)
Towler GP, Mann R, Serriere AJ, Gabaude CM, Ind. Eng. Chem. Res., 35(7), 2378 (1996)
Alves JJ, Towler GP, Ind. Eng. Chem. Res., 41(23), 5759 (2002)
Hallale N, Liu F, Adv. Environ. Res., 6, 81 (2001)
Liu F, Zhang N, Chem. Eng. Res. Des., 82(A10), 1315 (2004)
Ruthven D, Farooq S, Knaebel K, “Pressure Swing Adsorption,” VCH, NY (1994)
Peters M, Timmerhaus K, Plant Design and Economics for Chemical Engineers, McGraw-Hill, NY (1991)
Parker N, Using Natural Gas Transmission Pipeline Costs to Estimate Hydrogen Pipeline Costs, Oil & Gas Journal’s annual Pipeline Economics Report(1991-2003)
Linhoff B, Chem. Eng. Res. Des., 71, 503 (1993)
Shenoy UV, “Heat Exchanger Network Synthesis: Process Optimization by Energy and Resource Analysis, Gulf Publishing Company,” Houston (1995)
Smith R, Chemical Process Design, McGraw-Hill, NY (1995)
Towler GP, Mann R, Serriere AJ, Gabaude CM, Ind. Eng. Chem. Res., 35(7), 2378 (1996)
Alves JJ, Towler GP, Ind. Eng. Chem. Res., 41(23), 5759 (2002)
Hallale N, Liu F, Adv. Environ. Res., 6, 81 (2001)
Liu F, Zhang N, Chem. Eng. Res. Des., 82(A10), 1315 (2004)
Ruthven D, Farooq S, Knaebel K, “Pressure Swing Adsorption,” VCH, NY (1994)
Peters M, Timmerhaus K, Plant Design and Economics for Chemical Engineers, McGraw-Hill, NY (1991)
Parker N, Using Natural Gas Transmission Pipeline Costs to Estimate Hydrogen Pipeline Costs, Oil & Gas Journal’s annual Pipeline Economics Report(1991-2003)
