Utilizing Blast Furnace gas to run a supercritical CO2 cycle to meet part of the internal consumption of the iron plant and to produce fresh water through a multi-effect desalination unit

Document Type : Research Paper

Authors

Department of Mechanical Engineering, Faculty of Mechanical Engineering, University of Tabriz, Tabriz, Iran

Abstract

Iron furnace gases, a byproduct of the steel and iron industries, have been the subject of research on employing them to power some of the factory's internal needs. The rise in fuel costs and focus on energy system sustainability have created distinct frameworks for heat loss sources and low-value fuels. In this study, iron furnace gas produced in steel and iron factories has been used to produce additional power to provide part of the domestic power consumption of these factories. Supercritical carbon dioxide cycle has been used to generate power. The results show that at the optimal point, the system has emissions of 0.52 and a net power output of 22100 kWh. Also, the efficiency of the system is 38.56% and the emission of carbon dioxide is 0.510 ton/MWh. Also, by increasing the temperature of the exhaust gas by 150 degrees, it is clear that 2 MW of recycled heat can be obtained. Also, in this regard, the output work of the turbine has increased by 0.8 kW and increases the efficiency of the whole cycle by 31.5% to 37%.

Keywords


[1] Zetterholm J, Ji X, Sundelin B, Martin PM, Wang C. Dynamic modelling for the hot blast stove. Appl Energy 2017;185:2142–50. https://doi.org/10.1016/J.APENERGY.2016.02.128.
[2] Açikkalp E, Aras H, Hepbasli A. Advanced exergy analysis of an electricity-generating facility using natural gas. Energy Convers Manag 2014;82:146–53. https://doi.org/10.1016/J.ENCONMAN.2014.03.006.
[3] Boyaghchi FA, Molaie H. Sensitivity analysis of exergy destruction in a real combined cycle power plant based on advanced exergy method. Energy Convers Manag 2015;99:374–86. https://doi.org/10.1016/J.ENCONMAN.2015.04.048.
[4] Anvari S, Khoshbakhti Saray R, Bahlouli K. Employing a new optimization strategy based on advanced exergy concept for improvement of a tri-generation system. Appl Therm Eng 2017;113:1452–63. https://doi.org/10.1016/J.APPLTHERMALENG.2016.11.146.
[5] Dostal V, Hejzlar P, Driscoll MJ. The Supercritical Carbon Dioxide Power Cycle: Comparison to Other Advanced Power Cycles. Http://DxDoiOrg/1013182/NT06-A3734 2017;154:283–301. https://doi.org/10.13182/NT06-A3734.
[6] Milani D, Luu MT, McNaughton R, Abbas A. Optimizing an advanced hybrid of solar-assisted supercritical CO2 Brayton cycle: A vital transition for low-carbon power generation industry. Energy Convers Manag 2017;148:1317–31. https://doi.org/10.1016/J.ENCONMAN.2017.06.017.
[7] Zhao D, Xue J, Li S, Sun H, Zhang Q dong. Theoretical analyses of thermal and economical aspects of multi-effect distillation desalination dealing with high-salinity wastewater. Desalination 2011;273:292–8. https://doi.org/10.1016/J.DESAL.2011.01.048.
[8] Chen Q, Burhan M, Shahzad MW, Ybyraiymkul D, Akhtar FH, Li Y, et al. A zero liquid discharge system integrating multi-effect distillation and evaporative crystallization for desalination brine treatment. Desalination 2021;502:114928. https://doi.org/10.1016/J.DESAL.2020.114928.
[9] Tahir F, Al-Ghamdi SG. Integrated MED and HDH desalination systems for an energy-efficient zero-liquid discharge (ZLD) system. Energy Reports 2022;8:29–34. https://doi.org/10.1016/J.EGYR.2022.01.028.
[10] Tahir F, Al-Ghamdi SG. CFD analysis of evaporation heat transfer for falling films application. Energy Reports 2022;8:216–23. https://doi.org/10.1016/J.EGYR.2021.11.096.
[11] Chitgar N, Emadi MA. Development and exergoeconomic evaluation of a SOFC-GT driven multi-generation system to supply residential demands: Electricity, fresh water, and hydrogen. Int J Hydrogen Energy 2021;46:17932–54. https://doi.org/10.1016/J.IJHYDENE.2021.02.191.
[12] Aguilar-Jiménez JA, Velázquez N, López-Zavala R, Beltrán R, Hernández-Callejo L, González-Uribe LA, et al. Low-temperature multiple-effect desalination/organic Rankine cycle system with a novel integration for fresh water and electrical energy production. Desalination 2020;477:114269. https://doi.org/10.1016/J.DESAL.2019.114269
[13] Marques JGO, Costa AL, Pereira C. Thermodynamic study of a novel trigeneration process of hydrogen, electricity, and desalinated water: The case of Na-O-H thermochemical cycle, SCWR nuclear power plant, and MED desalination installation. Energy Convers Manag 2020;209:112648. https://doi.org/10.1016/J.ENCONMAN.2020.112648.
[14] Bejan A, Tsatsaronis G. Thermal design and optimization. John Wiley & Sons; 1996.
[15] Sarkar J, Bhattacharyya S. Optimization of recompression S-CO2 power cycle with reheating. Energy Convers Manag 2009;50:1939–45. https://doi.org/10.1016/j.enconman.2009.04.015.
[16] Banik S, Ray S, De S. Thermodynamic modeling of a recompression CO2 power cycle for low-temperature waste heat recovery. Appl Therm Eng 2016;107:441–52. https://doi.org/10.1016/j.applthermaleng.2016.06.179.
[17] Moghimi M, Emadi M, Akbarpoor AM, Mollaei M. Energy and exergy investigation of a combined cooling, heating, power generation, and seawater desalination system. Appl Therm Eng 2018. https://doi.org/10.1016/j.applthermaleng.2018.05.092.