Performance Evaluation of Heat Exchangers in a Polyethylene Plant

This paper evaluates the performance of three heat exchanger units (2-E-2301, 3-E-901 and 3-E-401) in a polyethylene plant. Steady state monitoring and direct collection of data from the equipment in the plant were performed and the data were analyzed by using energy equations to determine the ove...

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Main Authors: Barinaadaa Thaddeus Lebele-Alawa, Innocent Okpara Ohia
Format: Article
Language:English
Published: Taiwan Association of Engineering and Technology Innovation 2013-01-01
Series:International Journal of Engineering and Technology Innovation
Subjects:
Online Access:http://sparc.nfu.edu.tw/~ijeti/download/V3-no1-49-57.pdf
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spelling doaj-d8f09a897c9347128861f04fc79b3bd02020-11-25T01:06:33ZengTaiwan Association of Engineering and Technology InnovationInternational Journal of Engineering and Technology Innovation2223-53292226-809X2013-01-01314957Performance Evaluation of Heat Exchangers in a Polyethylene Plant Barinaadaa Thaddeus Lebele-Alawa0Innocent Okpara Ohia1Rivers State University of Science and TechnologyRivers State University of Science and TechnologyThis paper evaluates the performance of three heat exchanger units (2-E-2301, 3-E-901 and 3-E-401) in a polyethylene plant. Steady state monitoring and direct collection of data from the equipment in the plant were performed and the data were analyzed by using energy equations to determine the overall heat transfer coefficient, heat duty, temperature and pressure range of hot and cold fluids, capacity ratio and effectiveness. The results show that for 2-E-2301, the overall heat transfer coefficient is over 50 percent less than the design figure and the heat duty is over 75 percent than the design figure. For the 3-E-901 the heat duty and the overall heat transfer are over 75 percent less than the design figure which was traceable to fouling. This affected the effectiveness, capacity ratio and temperature range of the hot and cold fluid. For the 3-E-401, the heat duty was found to be within the limit of design figure. The temperature difference in the hot fluid side and the capacity ratio were within the limits of the design figure. Thus, the results show qualitative performance evaluation of the heat exchangers. http://sparc.nfu.edu.tw/~ijeti/download/V3-no1-49-57.pdfheat-exchangerheatperformanceenergy
collection DOAJ
language English
format Article
sources DOAJ
author Barinaadaa Thaddeus Lebele-Alawa
Innocent Okpara Ohia
spellingShingle Barinaadaa Thaddeus Lebele-Alawa
Innocent Okpara Ohia
Performance Evaluation of Heat Exchangers in a Polyethylene Plant
International Journal of Engineering and Technology Innovation
heat-exchanger
heat
performance
energy
author_facet Barinaadaa Thaddeus Lebele-Alawa
Innocent Okpara Ohia
author_sort Barinaadaa Thaddeus Lebele-Alawa
title Performance Evaluation of Heat Exchangers in a Polyethylene Plant
title_short Performance Evaluation of Heat Exchangers in a Polyethylene Plant
title_full Performance Evaluation of Heat Exchangers in a Polyethylene Plant
title_fullStr Performance Evaluation of Heat Exchangers in a Polyethylene Plant
title_full_unstemmed Performance Evaluation of Heat Exchangers in a Polyethylene Plant
title_sort performance evaluation of heat exchangers in a polyethylene plant
publisher Taiwan Association of Engineering and Technology Innovation
series International Journal of Engineering and Technology Innovation
issn 2223-5329
2226-809X
publishDate 2013-01-01
description This paper evaluates the performance of three heat exchanger units (2-E-2301, 3-E-901 and 3-E-401) in a polyethylene plant. Steady state monitoring and direct collection of data from the equipment in the plant were performed and the data were analyzed by using energy equations to determine the overall heat transfer coefficient, heat duty, temperature and pressure range of hot and cold fluids, capacity ratio and effectiveness. The results show that for 2-E-2301, the overall heat transfer coefficient is over 50 percent less than the design figure and the heat duty is over 75 percent than the design figure. For the 3-E-901 the heat duty and the overall heat transfer are over 75 percent less than the design figure which was traceable to fouling. This affected the effectiveness, capacity ratio and temperature range of the hot and cold fluid. For the 3-E-401, the heat duty was found to be within the limit of design figure. The temperature difference in the hot fluid side and the capacity ratio were within the limits of the design figure. Thus, the results show qualitative performance evaluation of the heat exchangers.
topic heat-exchanger
heat
performance
energy
url http://sparc.nfu.edu.tw/~ijeti/download/V3-no1-49-57.pdf
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