A comprehensive analysis of uncertainty in thermal utilities: 3E case study of a sugar plant

被引:6
作者
Piri, Ahmad [1 ]
Hazervazifeh, Amin [2 ]
Nikbakht, Ali M. [1 ]
机构
[1] Urmia Univ, Dept Mech Engn Biosyst, Orumiyeh, Iran
[2] Univ Maragheh, Dept Mech Engn Biosyst, Maragheh, Iran
关键词
Exergy; Exergeo-economic; Heat loss; Thermography; Evaporation line; EXERGY ANALYSIS; INFRARED THERMOGRAPHY; ENERGY; OPTIMIZATION;
D O I
10.1016/j.seta.2022.102498
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Heat losses from the utilities are inevitable in industries which utilize heat in unit operations. Sugar processing plants are among the industries where energy is a considerable share of final product. Accurate thermodynamic and economic analyses in sugar industry depend strictly on estimation of heat losses from the surfaces of utilities. In this research, the evaporation line of a sugar plant was studied to investigate the error introduced by ignoring heat loss in the system performance. To this end, energy, exergy, and exergeo-economic (3E) analyses were performed. Mean temperature of the surfaces of all the evaporation line subsystems was measured using thermography and the heat losses from the surfaces were computed. The results of 3E analysis show that ignoring heat loss in the evaporation line, generates considerable deviations from actual values. Total energy loss, total exergy destruction, and total cost, had errors of 2.24%, 0.72%, and 0.90%, respectively. As for the case studied project, the 0.90% difference in the total cost is equal to 11.04 USD hr(-1) which is equivalent to 18.50% of the cost of natural gas consumption in the plant and accounts as a highly critical issue for industrialists.
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页数:8
相关论文
共 34 条
[1]   Introducing and 3E (energy, exergy, economic) analysis of an integrated transcritical CO2 Rankine cycle, Stirling power cycle and LNG regasification process [J].
Akbari, Nozar .
APPLIED THERMAL ENGINEERING, 2018, 140 :442-454
[2]   Exergy, exergoenvironmental and exergoeconomic evaluation of a heat pump-integrated wall heating system [J].
Akbulut, Ugur ;
Utlu, Zafer ;
Kincay, Olcay .
ENERGY, 2016, 107 :502-522
[3]  
Bapat S. M., 2016, International Journal of Renewable Energy Technology, V7, P46, DOI 10.1504/IJRET.2016.073401
[4]   Exergetic evaluation and comparison of quintuple effect evaporation units in Indian sugar industries [J].
Bapat, S. M. ;
Majali, V. S. ;
Ravindranath, G. .
INTERNATIONAL JOURNAL OF ENERGY RESEARCH, 2013, 37 (12) :1415-1427
[5]   Energy and exergy analyses of sugar production stages [J].
Bayrak, M ;
Midilli, A ;
Nurveren, K .
INTERNATIONAL JOURNAL OF ENERGY RESEARCH, 2003, 27 (11) :989-1001
[6]   Energy, exergy and advanced exergy analysis of a milk processing factory [J].
Buhler, Fabian ;
Tuong-Van Nguyen ;
Jensen, Jonas Kjaer ;
Holm, Fridolin Mueller ;
Elmegaard, Brian .
ENERGY, 2018, 162 :576-592
[7]   Heat Flux Sensors for Infrared Thermography in Convective Heat Transfer [J].
Carlomagno, Giovanni Maria ;
de Luca, Luigi ;
Cardone, Gennaro ;
Astarita, Tommaso .
SENSORS, 2014, 14 (11) :21065-21116
[8]   Infrared thermography for convective heat transfer measurements [J].
Carlomagno, Giovanni Maria ;
Cardone, Gennaro .
EXPERIMENTS IN FLUIDS, 2010, 49 (06) :1187-1218
[9]  
Cengel Y.A.A.J.G., 2015, Heat and Mass Transfer: Fundamentals & Applications
[10]  
Cengel Yu.A., 2011, Thermodynamics. An Engineering Approach, P1