Thermodynamic and economic evaluation of a novel configuration for sustainable production of power and freshwater based on biomass gasification

被引:8
作者
Rahimi, M. J. [1 ]
Hamedi, M. H. [1 ]
Amidpour, M. [2 ]
机构
[1] KN Toosi Univ Technol, Fac Mech Engn, Energy Convers Div, POB 19395-1999,19 Pardis Str,Mollasadra Ave, Tehran 1999143344, Iran
[2] KN Toosi Univ Technol, Fac Mech Engn, Energy Syst Div, POB 19395-1999,19 Pardis Str,Mollasadra Ave, Tehran 1999143344, Iran
来源
ENERGY SYSTEMS-OPTIMIZATION MODELING SIMULATION AND ECONOMIC ASPECTS | 2021年 / 12卷 / 01期
关键词
Biomass gasification; Combined production; Economic analysis; C# programming; RENEWABLE ENERGY-SOURCES; DOWNDRAFT GASIFIER; EQUILIBRIUM-MODEL; SUPERFICIAL VELOCITY; COMPUTER-SIMULATION; EXERGY ANALYSIS; REDUCTION ZONE; COMBINED-CYCLE; GAS-ENGINE; DESALINATION;
D O I
10.1007/s12667-019-00346-y
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
This paper presents a novel thermal cycle for renewable production of power and freshwater with the use of biomass gasification technology. For this purpose, a realistic simulation program is developed (in C# programming language) to predict the composition of synthesis gas produced in the gasifier. Using the proposed system, both power and water demand of a small city with 3000 people can be met without any fossil fuel consumption. So, the proposed system can help in reaching a sustainable future. This novel system is then compared with two conventional systems for the production of power and water. The first one is a conventional natural gas-based system without any heat integration and the second one is a natural gas-based system with heat integration. It is concluded that the novel proposed system will result in 5,267,800 m(3) of natural gas saving per annum in comparison to the conventional system without heat integration. On the other hand, 4,211,300 m(3) of natural gas per year is saved in comparison to the conventional system with heat integration. Economic results show that the levelized cost of produced power and water for the novel system are 0.11 $/kWh and 1.25 $/m(3) respectively, and the period of return is 13.6. Additionally, a sensitivity analysis is performed to specify the impact of various thermodynamic and economic variables of the system on the final outputs. This research makes it possible to compare this renewable combined system with other conventional systems from thermodynamic and economic points of view.
引用
收藏
页码:61 / 106
页数:46
相关论文
共 70 条
  • [1] 48Perry JH., 1950, Chemical Engineers Handbook, V3rd
  • [2] Recent progress in the use of renewable energy sources to power water desalination plants
    Abdelkareem, Mohammad Ali
    Assad, M. El Haj
    Sayed, Enas Taha
    Soudan, Bassel
    [J]. DESALINATION, 2018, 435 : 97 - 113
  • [3] Biomass gasification cogeneration - A review of state of the art technology and near future perspectives
    Ahrenfeldt, Jesper
    Thomsen, Tobias P.
    Henriksen, Ulrik
    Clausen, Lasse R.
    [J]. APPLIED THERMAL ENGINEERING, 2013, 50 (02) : 1407 - 1417
  • [4] Performance analysis of a MSF desalination unit
    Al-Hengari, S
    El-Bousiffi, M
    El-Mudir, W
    [J]. DESALINATION, 2005, 182 (1-3) : 73 - 85
  • [5] Energy consumption and water production cost of conventional and renewable-energy-powered desalination processes
    Al-Karaghouli, Ali
    Kazmerski, Lawrence L.
    [J]. RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2013, 24 : 343 - 356
  • [6] Thermal analysis of ME-TVC plus MEE desalination systems
    Alasfour, FN
    Darwish, MA
    Bin Amer, AO
    [J]. DESALINATION, 2005, 174 (01) : 39 - 61
  • [7] Energetic and exergetic analysis of cogeneration power combined cycle and ME-TVC-MED water desalination plant: Part-1 operation and performance
    Almutairi, Abdulrahman
    Pilidis, Pericles
    Al-Mutawa, Nawaf
    Al-Weshahi, Mohammed
    [J]. APPLIED THERMAL ENGINEERING, 2016, 103 : 77 - 91
  • [8] [Anonymous], 2002, IND BOILERS HEAT REC
  • [9] Modelling of a downdraft gasifier fed by agricultural residues
    Antonopoulos, I-S.
    Karagiannidis, A.
    Gkouletsos, A.
    Perkoulidis, G.
    [J]. WASTE MANAGEMENT, 2012, 32 (04) : 710 - 718
  • [10] Development of an equilibrium model for the simulation of thermochemical gasification and application to agricultural residues
    Azzone, Emanuele
    Morini, Mirko
    Pinelli, Michele
    [J]. RENEWABLE ENERGY, 2012, 46 : 248 - 254