ABSTRACT
The main objective of this paper is to establish a mathematical framework to analyze the complex thermal economic performance of the calcination process. To find the factors affecting exergy efficiency loss, different exergy destruction is investigated in detail. Furthermore, the exergy flow cost model for exergy cost saving has also been developed. The results show that the vertical shaft furnace is a self-sufficiency equipment without additional fuel required, but the overall exergy destruction accounts for 54.11% of the total exergy input. In addition, the energy efficiency of the waste heat recovery boiler and thermal deaerator are 83.52% and 96.40%, whereas the exergy efficiency of the two equipment are 65.98% and 94.27%. Furthermore, the import exergy flow cost of vertical shaft furnace, waste heat recovery boiler and thermal deaerator are 366.5197 RMB per MJ, 0.1426 RMB per MJ, and 0.0020 RMB per MJ, respectively. Based on the result, several suggestions were proposed to improve the exergoeconomic performance. Assessing the performance of suggested improvements, the total exergy destruction of vertical shaft furnace is reduced to 134.34 GJ per hours and the exergy efficiency of waste heat recovery boiler is raised up to 66.02%. Moreover, the import exergy flow cost of the three different equipment is reduced to 0.0329 RMB per MJ, 0.1304 RMB per MJ, and 0.0002 RMB per MJ, respectively.
KEYWORDS
PAPER SUBMITTED: 2021-06-09
PAPER REVISED: 2021-08-14
PAPER ACCEPTED: 2021-08-17
PUBLISHED ONLINE: 2021-10-10
THERMAL SCIENCE YEAR
2022, VOLUME
26, ISSUE
Issue 2, PAGES [1999 - 2012]
- Bamas, R., Presence and Control of Polycyclic Aromatic Hydrocarbons in Petroleum Coke Drying and Calcination Plants, Fuel Processing Technology, 60 (1999), 2, pp. 111-18
- Zhan, X., et al., Catalytic Effect of Black Liquor on the Gasification Reactivity of Petroleum Coke, Applied Energy, 87 (2010), 5, pp. 1710-15
- Azari, K., et al., Mixing Variables for Prebaked Anodes Used in Aluminum Production, Powder Technology, 235 (2013), pp. 341-48
- Martins, M. A., et al., Modeling and Simulation of Petroleum Coke Calcination in Rotary Kilns, Fuel, 80 (2001), 11, pp. 1611-22
- Bui, R.T., et al., Model-based Optimization of the Operation of the Coke Calcining Kiln. Carbon, 31 (1993), 7, pp. 1139-47
- Yue, Q., et al., Resources Saving and Emissions Reduction of the Aluminum Industry in China, Resources, Conservation and Recycling. 104 (2015), pp. 68-75
- Xiao, J., et al., A Real-Time Mathematical Model for the Two-Dimensional Temperature Field of Petroleum Coke Calcination in Vertical Shaft Calciner, Jom, 68 (2016), 8, pp. 2149-59
- Shan, Y., et al., Rapid Growth of Petroleum Coke Consumption and its Related Emissions in China, Applied Energy, 226 (2018), SEP.15, pp. 494-502
- Xiao, J. et al., Modeling and Simulation of Petroleum Coke Calcination in Pot Calciner Using Two-Fluid Model, Jom, 68 (2015), 2, pp. 643-55
- Elkanzi, E. M., Simulation of the Coke Calcining Processes in Rotary Kilns, Chemical Product and Process Modeling,2 (2007), 3, pp. 1-14
- Filkoski, R., et al., Energy Optimisation of Vertical Shaft Kiln Operation in the Process of Dolomite Calcination, Thermal Science, 22 (2018), 5, pp. 2123-35
- Dolianitis, I. et al., Waste Heat Recovery at the Glass Industry with the Intervention of Batch and Cullet Preheating, Thermal Science, 20 (2016), 4, pp. 1245-58
- Wei, Y. M., et al., An Empirical Analysis of Energy Efficiency in China‘s Iron and Steel Sector, Energy, 32 (2007), 12, pp. 2262-70
- Guo, Z. C., Fu, Z. X., Current Situation of Energy Consumption and Measures Taken for Energy Saving in the Iron and Steel Industry in China, Energy, 35 (2010), 11, pp. 4356-60
- Rodriguez, M. T. T., et al., Combining LCT Tools for the Optimization of an Industrial Process: Material and Energy Flow Analysis and Best Available Techniques, Journal of Hazardous Materials, 192 (2011), 3, pp. 1705-19
- Stefanovic, G., et al., CO2 Reduction Options in Cement Industry: The Novi Popovac Case, Thermal Science, 14 (2010), 3, pp. 671-79
- Bejan, A., Exergy Analysis of Thermal, Chemical, and Metallurgical Processes, International Journal of Heat & Fluid Flow, 10 (1988), 1, pp. 87-88
- Çamdali, Ü., et al., Second Law Analysis of Thermodynamics in the Electric Arc Furnace at a Steel Producing Company, Energy Conversion and Management, 44 (2003), 6, pp. 961-73
- Domínguez, A., et al., Exergy Accounting Applied to Metallurgical Systems: The case of Nickel Processing, Energy, 62 (2013), dec.1, pp. 37-45
- Lazzaretto, A., Tsatsaronis, G., SPECO: A Systematic and General Methodology for Calculating Efficiencies and Costs in Thermal Systems, Energy, 31 (2006), 8-9, pp. 1257-89
- Gaggioli, R. A., Wepfer, W. J., Exergy Economics: I. Cost Accounting Applications, Energy, 5 (1980), 8-9, pp. 823-37
- Regulagadda P., et al., Exergy Analysis of a Thermal Power Plant with Measured Boiler and Turbine Losses, Applied Thermal Engineering, 30 (2010), 8-9, pp. 970-76
- Rong, W., et al., Exergy Assessment of a Rotary Kiln-electric Furnace Smelting of Ferronickel Alloy, Energy, 138 (2017), nov.1, pp. 942-53
- Rong, W., et al., Cheung SCP. Energy and Exergy Analysis of an Annular Shaft Kiln with Opposite Burners, Applied Thermal Engineering, 119 (2017), pp. 629-38
- Michaelis, P., et al., Exergy Analysis of the Life Cycle of Steel, Energy, 23 (1998), 3, pp, 213-20
- Morris, D. R., Szargut, J., Standard Chemical Exergy of Some Elements and Compounds on the Planet Earth, Energy, 11 (1986), 8, pp. 733-55