Exergy analysis of Naphtha Hydrotreating Unit (NHU)

被引:3
作者
Agbo, A. F. [1 ]
Aboje, A. A. [1 ]
Obayomi, K. S. [2 ]
机构
[1] Fed Univ Technol Minna Niger State, Dept Chem Engn, Minna, Nigeria
[2] Univ Omu Aran Kwara State Landmark, Dept Chem Engn, Coll Engn, Omu Aran, Nigeria
来源
3RD INTERNATIONAL CONFERENCE ON SCIENCE AND SUSTAINABLE DEVELOPMENT (ICSSD 2019): SCIENCE, TECHNOLOGY AND RESEARCH: KEYS TO SUSTAINABLE DEVELOPMENT | 2019年 / 1299卷
关键词
Exergy; Aspen Hysys; Heater; NHU; Column; ENERGY; CONSUMPTION; SECTOR;
D O I
10.1088/1742-6596/1299/1/012025
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The aim of this research work is to develop an exergy analysis of Naphtha Hydrotreating Unit of the Kaduna Refinery and Petrochemical Company (KRPC). This was achieved through extraction of data from the Laboratory operating manual and the process flow diagram of the naphtha hydrotreating unit of the refinery which is used in the simulation; the site of primary exergy destruction was also determined. The major components of exergy efficiencies of the major component were determine. Also the potential for process improvement through revamp was determined. Exergy analysis of Naphtha Hydrotreating Unit (NHU) of the Kaduna Refining and Petrochemical Company was successfully simulated using Aspen HYSYS. Exergy efficiencies were found to be very low in Heaters 11H01 and 11H02 at 23.9% and 50.0% respectively. Similarly low efficiencies were respectively observed in Columns 11C02 and 11C01 at 48.7% and 52.8%. The major contributors to exergy destructions were found to be Column 11C01 and Heater 11H01 with percentage contribution of 21.6% and 14.6% respectively, totaling 36.2% of the total irreversibility recorded in the NHU process. Heat recovery from flue gas in the furnace and boilers was considered and found to be economically viable with a payback period of less than one year.
引用
收藏
页数:8
相关论文
共 21 条
[1]  
Agha M. H., 2009, INTEGRATED MANAGEMEN
[2]   A new exergy method for process analysis and optimization [J].
Chang, H ;
Li, JW .
CHEMICAL ENGINEERING SCIENCE, 2005, 60 (10) :2771-2784
[3]   Exergy as a potential tool for sustainable drying systems [J].
Dincer, Ibrahim .
SUSTAINABLE CITIES AND SOCIETY, 2011, 1 (02) :91-96
[4]   Heat Integration of an Oxy-Combustion Process for Coal-Fired Power Plants with CO2 Capture by Pinch Analysis [J].
Fu, Chao ;
Gundersen, Truls .
PRES 2010: 13TH INTERNATIONAL CONFERENCE ON PROCESS INTEGRATION, MODELLING AND OPTIMISATION FOR ENERGY SAVING AND POLLUTION REDUCTION, 2010, 21 :181-186
[5]  
Ghannadzadeh A., 2012, Exergetic Balances and Analysis in a Process Simulator: A Way to Enhance Process Energy Integration
[6]  
Hart Resources Limited, 2012, NIG EXTR IND TRANSP
[7]   Energy savings and emissions reductions for rewinding and replacement of industrial motor [J].
Hasanuzzaman, M. ;
Rahim, N. A. ;
Saidur, R. ;
Kazi, S. N. .
ENERGY, 2011, 36 (01) :233-240
[8]   Effects of operating variables on heat transfer and energy consumption of a household refrigerator-freezer during closed door operation [J].
Hasanuzzaman, M. ;
Saidur, R. ;
Masjuki, H. H. .
ENERGY, 2009, 34 (02) :196-198
[9]  
Kinsey JL, 2010, AIR RECUPERATOR COMB
[10]  
Nuhu M, 2012, Int. J. Chem. Eng. Appl., P441, DOI [10.7763/ijcea.2012.v3.239, DOI 10.7763/IJCEA.2012.V3.239]