An integrated CCHP system based on biomass and natural gas co-firing: Exergetic and thermo-economic assessments in the framework of energy nexus

被引:44
作者
Jalili, Mohammad [1 ]
Ghasempoura, Roghayeh [1 ]
Ahmadi, Mohammad Hossein [2 ]
Chitsazc, Ata [3 ]
Holagh, Shahriyar Ghazanfari [4 ]
机构
[1] Univ Tehran, Fac New Sci & Technol, Renewable energies & Environm Engn Dept, Tehran, Iran
[2] Shahrood Univ Technol, Fac Mech Engn, Shahrood, Iran
[3] Urmia Univ, Fac Engn, Mech Engn Dept, Orumiyeh, Iran
[4] Iran Univ Sci & Technol, Sch Mech Engn, Tehran, Iran
来源
ENERGY NEXUS | 2022年 / 5卷
关键词
Gasification; Thermo-economic analysis; Double effect absorption refrigeration cycle; Chemical exergy; Levelized cost of energy; OXIDE FUEL-CELL; WASTE-TO-ENERGY; MULTIOBJECTIVE OPTIMIZATION; PARTIAL GASIFICATION; POWER-PLANT; HEAT; PERFORMANCE; TURBINE; CYCLE; STEAM;
D O I
10.1016/j.nexus.2021.100016
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Agriculture and energy are inextricably connected; many energy systems can be driven by biomass supplied from agricultural waste products. In this study, a combined biomass/natural gas fed multi-generation system, prodcuing cooling, heating, and power is investigated from exergetic and thermo-economic standpoints. The system consists of four susbsystems, encompassing a gasification cycle, a gas cycle, a Rankine steam cycle, and a double effect absorption refrigeration cycle. To increase the lower heating value of the fuel injected into the combustion chamber, natural gas is mixed with syngas. Also, to exploit the exhaust gas from the stack of the gas turbine, the flue gas is divided into two streams by a spliter,providing the required heat for the Rankine steam and absorption refrigeration cycles. The effects of parameters such as the gas turbine inlet temperature , combustion chamber inlet pressure, the amount of natural gas mixed with syngas, and split ratio of the exhaust gas from the gas turbine on the thermodynamic and thermo-economic outputs are studied. The results show that the gas cycle with 61% and the double-effect absorption refrigeration cycle with 6% exergy destruction rates have the largest and lowest shares of the total exergy destruction rate, respectively. By changing the mixing ratio of the natural gas injected into the cycle from 0.5 to 1, the system's net work is seen to increase by 90.77%, while the modified ecological coefficient of the system performance boosts by 9.49%. In addition, such a change leads to 53.45% increase in the net present value of the total cost over the defined economic life, and also an increase of 90.25% in the net present value of the total output of the cycle equivalent to electricity over the economic life. Moreover, it brings about 19.36% decrease in the system's levelized cost of energy.
引用
收藏
页数:14
相关论文
共 62 条
[1]   Exergoeconomic analysis and multi-objective optimization of a novel combined flash-binary cycle for Sabalan geothermal power plant in Iran [J].
Aali, A. ;
Pourmahmoud, N. ;
Zare, V. .
ENERGY CONVERSION AND MANAGEMENT, 2017, 143 :377-390
[2]   Thermodynamic and economic analysis of performance evaluation of all the thermal power plants: A review [J].
Ahmadi, Mohammad H. ;
Nazari, Mohammad Alhuyi ;
Sadeghzadeh, Milad ;
Pourfayaz, Fathollah ;
Ghazvini, Mahyar ;
Ming, Tingzhen ;
Meyer, Josua P. ;
Sharifpur, Mohsen .
ENERGY SCIENCE & ENGINEERING, 2019, 7 (01) :30-65
[3]   Multi-objective optimization and exergetic-sustainability of an irreversible nano scale Braysson cycle operating with Maxwell-Boltzmann gas [J].
Ahmadi, Mohammad H. ;
Ahmadi, Mohammad-Ali ;
Pourfayaz, Fathollah ;
Bidi, Mokhtar ;
Acikkalp, Emin .
ALEXANDRIA ENGINEERING JOURNAL, 2016, 55 (02) :1785-1798
[4]   Development and assessment of an integrated biomass-based multi-generation energy system [J].
Ahmadi, Pouria ;
Dincer, Ibrahim ;
Rosen, Marc A. .
ENERGY, 2013, 56 :155-166
[5]   Exergy and and exergoeconomic assessment of hydrogen and cooling production from concentrated PVT equipped with PEM electrolyzer and LiBr-H2O absorption chiller [J].
Akrami, Ehsan ;
Nemati, Arash ;
Nami, Hossein ;
Ranjbar, Faramarz .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2018, 43 (02) :622-633
[6]   A techno-economic-environmental study evaluating the potential of oxygen-steam biomass gasification for the generation of value-added products [J].
AlNouss, Ahmed ;
McKay, Gordon ;
Al-Ansari, Tareq .
ENERGY CONVERSION AND MANAGEMENT, 2019, 196 :664-676
[7]   Economic feasibility analysis with the parametric dynamic simulation of a single effect solar absorption cooling system for various climatic regions in Turkey [J].
Altun, A. F. ;
Kilic, M. .
RENEWABLE ENERGY, 2020, 152 :75-93
[8]   Multi-objective optimization of a tri-generation system based on biomass gasification/digestion combined with S-CO2 cycle and absorption chiller [J].
Balafkandeh, S. ;
Zare, V. ;
Gholamian, E. .
ENERGY CONVERSION AND MANAGEMENT, 2019, 200
[9]   Multi-objective design optimization of a solar based system for electricity, cooling, and hydrogen production [J].
Behzadi, Amirmohammad ;
Habibollahzade, Ali ;
Ahmadi, Pouria ;
Gholamian, Ehsan ;
Houshfar, Ehsan .
ENERGY, 2019, 169 :696-709
[10]  
Bejan A., 1996, Thermal Design and Optimization