The Pinch Design Method for Heat Exchanger Networks Considering the Heat Capacity Flowrate of a Stream with Variation in Temperature

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Abstract:

A novel method of locating the pinch is presented for the design of heat exchanger networks. The method is based on the pinch design method for heat exchanger networks which was first introduced by Linnhoff. The method first consider the heat capacity flowrate of a stream with variation in temperature. This is because heat capacity flowrate of a stream with variation in temperature not only affect minimum utility requirement for heat exchanger network but also affect the pinch location, choice ofΔTmin.

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Advanced Materials Research (Volumes 396-398)

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1048-1054

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November 2011

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© 2012 Trans Tech Publications Ltd. All Rights Reserved

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[1] Gundersen, T., & Naess, L. The synthesis of cost optimal heat exchanger networks: An industrial review of the state of the art. Computers & Chemical Engineering, Vol.12, issue6, 503-530, (1988)

DOI: 10.1016/0098-1354(88)87002-9

Google Scholar

[2] Ahmad, S., & Linnhoff, B.. Overall cost targets for heat exchanger networks. In Proceedings of the 11th IChem E annual research meeting on heat transfer. (1984)

Google Scholar

[3] Hall, S. G., Ahmad, S., & Smith, R. . Capital cost targets for heat exchanger networks comprising mixed materials of construction, pressure ratings and exchanger types. Computers & Chemical Engineering, Vol.14, issue3, 319-335, (1990)

DOI: 10.1016/0098-1354(90)87069-2

Google Scholar

[4] Trivedi K K, O'Neill B K, Roach J R , Wood R M. Systematic energy relaxation in MER heat exchanger works. Computers and Chemical Engineering , Vol.14, 601-611, (1990)

DOI: 10.1016/0098-1354(90)87030-s

Google Scholar

[5] Polley, G. T.,&Panjeh Shahi, M. H. . Interfacing heat exchanger network synthesis and detailed heat exchanger design. Transactions of the Institute of Chemical Engineers, Vol.69, 445-457, (1991)

Google Scholar

[6] Hojjati, M. R., Omidkhah, M. R., & Panjeh Shahi, M. H. . Cost effective heat exchanger network design with mixed materials of construction. Iranian Journal of Chemistry & Chemical Engineering, Vol.23, issue2, 89-100, (2004)

Google Scholar

[7] A. Akbari, M.R. Omidkhah, M.R. Hojjati. Heat exchanger network area targeting considering stream allocation to shell or tubes[J]. Computers and Chemical Engineering, Vol.32, issue12, 3143-3152, (2008)

DOI: 10.1016/j.compchemeng.2008.05.009

Google Scholar

[8] F. Pettersson. Heat exchanger network design using geometric mean temperature difference[J]. Computers & Chemical Engineering, Vol.32, issue8, 1726-1734, (2008)

DOI: 10.1016/j.compchemeng.2007.08.015

Google Scholar

[9] Jos´e M. Ponce-Ortega , Arturo Jim´enez-Guti´errez, Ignacio E. Grossmann. Optimal synthesis of heat exchanger networks involving isothermal process streams[J]. Computers & Chemical Engineering, Vol.32, issue8, 1918-1942, (2008)

DOI: 10.1016/j.compchemeng.2007.10.007

Google Scholar

[10] M. Akbarnia, M. Amidpour, A. Shadaram. A new approach in pinch technology considering piping costs in total cost targeting for heat for heat exchanger network[J]. Chemical Engineering Research and Design, Vol.87, issue3, 357-365, (2009)

DOI: 10.1016/j.cherd.2008.09.001

Google Scholar

[11] R. Mohammadhasani Khorasany, M. Fesanghary. A novel approach for synthesis of cost-optimal heat exchanger networks[J]. Computers & Chemical Engineering, Vol.33, issue8, 1363-1370, (2009)

DOI: 10.1016/j.compchemeng.2008.12.004

Google Scholar

[12] Xiurong Nie and Yourun Li. Simultaneous optimization of technological processes and heat exchanger networks[J]. Journal of Chemical Industry and Engineering(In Chinese), Vol.43, issue5, 609-614, (1992)

Google Scholar

[13] Li Zhou, Wanli Hu and Guocong Yu. A simple NLP method of making a stiff heat exchanger network resilient[J]. Journal of Chemical Industry and Engineering(In Chinese), Vol.42, issue1, 96-102, (1993)

Google Scholar

[14] Hui Li, Li Wang and Pingjing Yao. HEN design using pseudo- temperature approach [J]. Journal of Chemical Engineering of Chinese Universities(In Chinese), Vol.11, issue1, 99-103, (1997)

Google Scholar

[15] Weiping Gao and Ying Yang.Retrofit and control of heat exchanger networks[J]. Journal of Chemical Industry and Engineering(In Chinese), Vol.54, issue7, 965-971, (2003)

Google Scholar

[16] Xionglin Luo, Lin Sun, Chuanfang Wang, et al. Operating pinch point analysis and bypass optimal control of heat exchanger networks [J]. Journal of Chemical Industry and Engineering(In Chinese), Vol.59, issue5, 1020-6021, (2008)

Google Scholar

[17] Kang Cai, Xin Guan, Xing Luo, et al. Optimization of large-scale heat exchanger networks by evolution of sub-networks [J]. Journal of Chemical Industry and Engineering(In Chinese), Vol.60, issue6, 2265-2270, (2009)

Google Scholar