Scenario analysis of gasification process application in electrical energy-freshwater generation from heavy fuel oil, thermodynamic, economic and environmental assessment

被引:49
作者
Meratizaman, Mousa [1 ]
Monadizadeh, Sina [2 ]
Ebrahimi, Armin [1 ]
Akbarpour, Hamed [1 ]
Amidpour, Majid [1 ]
机构
[1] KN Toosi Univ Technol, Fac Mech Engn, Dept Energy Syst Engn, Tehran, Iran
[2] Islamic Azad Univ, North Tehran Branch, Fac Ind Engn, Tehran, Iran
关键词
Integrated gasification combined cycle; Solid oxide fuel cell-gas turbine; Electrical energy-freshwater generation system; Annualized cost of system; Environmental analysis; GAS-TURBINE; COAL-GASIFICATION; CO2; CAPTURE; CHP SYSTEM; MODEL; OPTIMIZATION; PERFORMANCE; CELL; DESALINATION; SIMULATION;
D O I
10.1016/j.ijhydene.2014.12.072
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Today heavy fuel oil is still produced and plays an important role in providing required energy. However, there could be environmental problems as a result of burning these utilized fuel oils. Also, the heavy fuel oil cannot be used in high efficiency power plants same as combined cycle because of physical characteristics. Partial oxidation (Gasification) process is introduced as a solution to reduce the emission production in the power generation cycle from heavy fuel oil. In this process, the heavy fuel oil is converted into the syngas (mainly consist of CO and H-2). The chemical energy content of syngas can be converted into the electrical energy with high efficiency and low emission production through high efficient cycle like combined cycle and Solid oxide fuel cell-gas turbine. To improve the efficiency of high temperature power generation system, a thermal desalination unit is coupled with them during the scenario analysis. Thermodynamic simulation, economic and environmental assessment are performed to investigate the feasibility of introduced power generation system. Results show that the suggested scenarios are not economic in the current condition. Applying the emission penalty cost and producing the more valuable product same as freshwater can improve the system feasibility. Copyright (C) 2014, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:2578 / 2600
页数:23
相关论文
共 49 条
[31]   Optimal coupling of site utility steam network with MED-RO desalination through total site analysis and exergoeconomic optimization [J].
Manesh, M. H. Khoshgoftar ;
Ghalami, H. ;
Amidpour, Majid ;
Hamedi, M. H. .
DESALINATION, 2013, 316 :42-52
[32]   Introduction of an efficient small-scale freshwater-power generation cycle (SOFC-GT-MED), simulation, parametric study and economic assessment [J].
Meratizaman, Mousa ;
Monadizadeh, Sina ;
Amidpour, Majid .
DESALINATION, 2014, 351 :43-58
[33]   Exergy based performance analysis of a solid oxide fuel cell and steam injected gas turbine hybrid power system [J].
Motahar, Sadegh ;
Alemrajabi, Ali Akbar .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2009, 34 (05) :2396-2407
[34]  
Netherlands Institute for social research, 2014, STAT
[35]   Assessment of economic viability for PV/wind/diesel hybrid energy system in southern Peninsular Malaysia [J].
Ngan, Mei Shan ;
Tan, Chee Wei .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2012, 16 (01) :634-647
[36]   Electrochemical and thermodynamic modeling of a CHP system using tubular solid oxide fuel cell (SOFC-CHP) [J].
Pirkandi, Jamasb ;
Ghassemi, Majid ;
Hamedi, Mohammad Hossein ;
Mohammadi, Rafat .
JOURNAL OF CLEANER PRODUCTION, 2012, 29-30 :151-162
[37]  
Ragland KW, 1901, J BIORESOUR TECHNOL, V37, P161
[38]   A review of recent advances on process technologies for upgrading of heavy oils and residua [J].
Rana, Mohan S. ;
Sámano, Vicente ;
Ancheyta, Jorge ;
Diaz, J. A. I. .
FUEL, 2007, 86 (09) :1216-1231
[39]   Modeling and optimizing a CHP system for natural gas pressure reduction plant [J].
Sanaye, Sepehr ;
Nasab, Amir Mohammadi .
ENERGY, 2012, 40 (01) :358-369
[40]  
Saravelou F, 1991, MODEL FLUIDIZED BED