Articles & Issues
- Language
- English
- Conflict of Interest
- In relation to this article, we declare that there is no conflict of interest.
- Publication history
-
Received January 11, 2011
Accepted July 6, 2011
- 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
The pinch technology combined with a heat pump applied in a three-effect evaporator and energy-saving performance assessment
Department of Environmental Science and Engineering, National Pingtung University of Science and Technology, Pingtung County, Taiwan 1Department of Civil Engineering, National Pingtung University of Science and Technology, Pingtung County, Taiwan 2Department of Applied Foreign Languages, Tainan University of Technology, Tainan City, Taiwan
chen5637@mail.npust.edu.tw
Korean Journal of Chemical Engineering, March 2012, 29(3), 341-348(8), 10.1007/s11814-011-0173-7
Download PDF
Abstract
This research investigated optimal energy utilization with pinch technology based on an actual gelatin production factory using a three-effect evaporator (TEE). A TEE is a well-known device used extensively when concentrating process fluid with large amounts of boiler steam. Under ideal energy use conditions, the exhaust heat can be recovered with the addition of a heat pump system. The study results showed that the original energy demand and discharge of the TEE were 1,736.2 and 1,733.2 kWh, respectively. Simulating the pinch technology use, the energy demand and discharge decreased to 1,531.5 and 1,527.7 kWh, respectively. When the heat pump was used to recover the exhaust heat, 324 kL per annum of fuel oil was saved, while electricity use increased 131 kWh. The total investment cost was 86,550 US$, but the total annual operation cost could save up to 166,421 US$. The net present value was estimated to be 544,316 US$ with a 5-year equipment operation. The investment expense could be completely recovered within a_x000D_
seven-month remuneration period.
References
Niesnfeld AE, Industrial evaporators, Instrument Society of America (1985)
Linnhoff B, Townsend DW, Boland D, Hewitt GF, Thomas BEA, Guy AR, Marsland RH, User guide on process integration for the efficient use of energy, 1st Ed., Institution of Chem. Eng., Rugby, UK (1982)
Linnhoff B, Hindmarsh E, Chem. Eng. Sci., 38, 745 (1983)
Linnhoff B, Ahmad S, Comp. Chem. Eng., 147, 729 (1990)
Ahmad S, Linnhoff B, Smith R, Comp. Chem. Eng., 14, 751 (1990)
Lee HP, Lee IY, Yoo KO, Korean J. Chem. Eng., 12(5), 589 (1995)
Tjoe TN, Linnhoff B, Chem. Eng., 28, 47 (1986)
Asante NDK, Zhu XY, Comp. Chem. Eng., 20, S7 (1996)
Phipps MA, Hoadley AFA, Korean J. Chem. Eng., 20(4), 642 (2003)
Salama AIA, Appl. Therm. Eng., 29, 2633 (2009)
Gundersen T, Naess L, Heat Recovery Systems & CHP., 10, 301 (1990)
Staine F, Favrat D, Appl. Therm. Eng., 16, 497 (1996)
LAZZARIN RM, Heat Recov. Syst. CHP, 14(6), 581 (1994)
LAZZARIN RM, Heat Recov. Syst. CHP, 15(3), 305 (1995)
Langley, Billy C, Heat pump technology, 1st Ed., Prentice Hall, New Jersey, USA (2001)
Kemp IC, Pinch analysis and process integration, 2nd Ed., Elsevier Ltd, UK (2007)
Eastop TD, Croft DR, Energy efficiency, 1st Ed., Longman Group Ltd., Malaysia, KPP (1995)
Fonyo Z, Benko N, Comp. Chem. Eng., 20, S85 (1996)
Wu C, Chen LG, Sun FR, Energy Conv. Manag., 39(5-6), 445 (1998)
Smith JM, Van Ness HC, Abbott MM, Introduction to chemical engineering thermodynamics, 7th Ed., McGraw-Hill, New York (2005)
Nguyen A, Kim Y, Shin Y, Int. J. Refriger., 28, 242 (2005)
Park KJ, Lee Y, Jung D, J. Mechanical Sci. Technol., 24, 879 (2010)
IEA, Heat Pump Centre, Heat pump performance, International Energy Agency (IEA) Heat Pump Centre, retrieved November 22, 2010 from: .
Stoecker WF, Jones JW, Refrigeration and air conditioning, 2nd Ed., McGraw-Hill, Taipei, Taiwan (1982)
Tan CM, Metal extraction in refrigerant R134a, Master’s Thesis, National Chiao Tung University, Hsinchu, Taiwan (2002)
Lee MY, Choi DW, Kim YH, Korean J. Chem. Eng., 26(3), 631 (2009)
Yoo C, Lee TY, Kim J, Moon I, Jung JH, Han C, Oh JM, Lee IB, Korean J. Chem. Eng., 24(4), 567 (2007)
Linnhoff B, Townsend DW, Boland D, Hewitt GF, Thomas BEA, Guy AR, Marsland RH, User guide on process integration for the efficient use of energy, 1st Ed., Institution of Chem. Eng., Rugby, UK (1982)
Linnhoff B, Hindmarsh E, Chem. Eng. Sci., 38, 745 (1983)
Linnhoff B, Ahmad S, Comp. Chem. Eng., 147, 729 (1990)
Ahmad S, Linnhoff B, Smith R, Comp. Chem. Eng., 14, 751 (1990)
Lee HP, Lee IY, Yoo KO, Korean J. Chem. Eng., 12(5), 589 (1995)
Tjoe TN, Linnhoff B, Chem. Eng., 28, 47 (1986)
Asante NDK, Zhu XY, Comp. Chem. Eng., 20, S7 (1996)
Phipps MA, Hoadley AFA, Korean J. Chem. Eng., 20(4), 642 (2003)
Salama AIA, Appl. Therm. Eng., 29, 2633 (2009)
Gundersen T, Naess L, Heat Recovery Systems & CHP., 10, 301 (1990)
Staine F, Favrat D, Appl. Therm. Eng., 16, 497 (1996)
LAZZARIN RM, Heat Recov. Syst. CHP, 14(6), 581 (1994)
LAZZARIN RM, Heat Recov. Syst. CHP, 15(3), 305 (1995)
Langley, Billy C, Heat pump technology, 1st Ed., Prentice Hall, New Jersey, USA (2001)
Kemp IC, Pinch analysis and process integration, 2nd Ed., Elsevier Ltd, UK (2007)
Eastop TD, Croft DR, Energy efficiency, 1st Ed., Longman Group Ltd., Malaysia, KPP (1995)
Fonyo Z, Benko N, Comp. Chem. Eng., 20, S85 (1996)
Wu C, Chen LG, Sun FR, Energy Conv. Manag., 39(5-6), 445 (1998)
Smith JM, Van Ness HC, Abbott MM, Introduction to chemical engineering thermodynamics, 7th Ed., McGraw-Hill, New York (2005)
Nguyen A, Kim Y, Shin Y, Int. J. Refriger., 28, 242 (2005)
Park KJ, Lee Y, Jung D, J. Mechanical Sci. Technol., 24, 879 (2010)
IEA, Heat Pump Centre, Heat pump performance, International Energy Agency (IEA) Heat Pump Centre, retrieved November 22, 2010 from: .
Stoecker WF, Jones JW, Refrigeration and air conditioning, 2nd Ed., McGraw-Hill, Taipei, Taiwan (1982)
Tan CM, Metal extraction in refrigerant R134a, Master’s Thesis, National Chiao Tung University, Hsinchu, Taiwan (2002)
Lee MY, Choi DW, Kim YH, Korean J. Chem. Eng., 26(3), 631 (2009)
Yoo C, Lee TY, Kim J, Moon I, Jung JH, Han C, Oh JM, Lee IB, Korean J. Chem. Eng., 24(4), 567 (2007)