Complex thermodynamic analysis of the heat-technological complex of sugar production: analysis method
DOI:
https://doi.org/10.15587/2706-5448.2020.202026Keywords:
energy efficiency, irreversibility of processes, thermodynamic analysis, entropy method, resource-saving measuresAbstract
The object of research is the heat-technological systems of sugar production and the heat-technological complex as a whole. A modern sugar factory is a complex hierarchical system of inextricably interconnected elements, and its basis – a heat-technological complex – combines the elements of technological, heat transfer, and mechanical equipment, in which complex physicochemical processes are simultaneously realized, closely interacting. Given the complexity of the internal relationships of processes, their parameters and characteristics, it is necessary to systematically approach the analysis of real functioning, performance evaluation and the solution of optimization problems of the complex as a whole, as well as its individual subsystems and elements.
In this work, it is proposed a method for thermodynamic analysis of the heat-technological complex of sugar production as a single thermodynamic system, which allows to analyze the main factors influencing the energy efficiency of the complex regardless of the course of processes implemented within the system. The methodology is based on a joint analysis of the general synthetic and analytical balances of mass, energy and entropy. This model has a deep physical foundation, because the material balance equation is an integral form of the law of conservation of the quantity of matter, the energy balance equation is an integral form of the first law of thermodynamics, and the entropy balance equation is an integral form of the second law of thermodynamics. The main objective of the methodology is a quick assessment of the excellence of the heat-technological complex and its definition of “energy-saving potential”. Also, the application of the principle of energy compensation of irreversibility and entropy criteria allows to determine the sources and causes of system imperfections, and imperfections are compiled to help develop a system of measures to increase the efficiency of the optimal sequence complex. Therefore, the proposed methodology of thermodynamic analysis, in contrast to the methods based on exergy characteristics, provides a comprehensive analysis, operating only with the fundamental laws and principles of classical thermodynamics. It can also be used both to optimize the energy characteristics of existing ones and to design new sugar industry enterprises
References
- Kaushik, S. C., Reddy, V. S., Tyagi, S. K. (2011). Energy and exergy analyses of thermal power plants: A review. Renewable and Sustainable Energy Reviews, 15 (4), 1857–1872. doi: http://doi.org/10.1016/j.rser.2010.12.007
- Borsukiewicz-Gozdur, A. (2013). Exergy analysis for maximizing power of organic Rankine cycle power plant driven by open type energy source. Energy, 62, 73–81. doi: http://doi.org/10.1016/j.energy.2013.03.096
- Liao, G., E, J., Zhang, F., Chen, J., Leng, E. (2020). Advanced exergy analysis for Organic Rankine Cycle-based layout to recover waste heat of flue gas. Applied Energy, 266, 114891. doi: http://doi.org/10.1016/j.apenergy.2020.114891
- Karellas, S., Braimakis, K. (2016). Energy–exergy analysis and economic investigation of a cogeneration and trigeneration ORC–VCC hybrid system utilizing biomass fuel and solar power. Energy Conversion and Management, 107, 103–113. doi: http://doi.org/10.1016/j.enconman.2015.06.080
- Kamate, S. C., Gangavati, P. B. (2009). Exergy analysis of cogeneration power plants in sugar industries. Applied Thermal Engineering, 29 (5-6), 1187–1194. doi: http://doi.org/10.1016/j.applthermaleng.2008.06.016
- Taner, T., Sivrioglu, M. (2015). Energy–exergy analysis and optimisation of a model sugar factory in Turkey. Energy, 93, 641–654. doi: http://doi.org/10.1016/j.energy.2015.09.007
- Taner, T., Sivrioglu, M. (2015). Data on energy, exergy analysis and optimisation for a sugar factory. Data in Brief, 5, 408–410. doi: http://doi.org/10.1016/j.dib.2015.09.028
- Dogbe, E. S., Mandegari, M. A., Görgens, J. F. (2018). Exergetic diagnosis and performance analysis of a typical sugar mill based on Aspen Plus® simulation of the process. Energy, 145, 614–625. doi: http://doi.org/10.1016/j.energy.2017.12.134
- Tekin, T., Bayramoğlu, M. (1998). Exergy Loss Minimization Analysis of Sugar Production Process from Sugar Beet. Food and Bioproducts Processing, 76 (3), 149–154. doi: http://doi.org/10.1205/096030898531963
- Albdoor, A. K., Ma, Z., Cooper, P., Ren, H., Al-Ghazzawi, F. (2020). Thermodynamic analysis and design optimisation of a cross flow air to air membrane enthalpy exchanger. Energy, 117691. doi: http://doi.org/10.1016/j.energy.2020.117691
- Samiilenko, S. M., Vasylenko, S. M., Buliandra, O. F., Shtanheiev, K. O., Shutiuk, V. V. (2012). Metodolohichni zasady termodynamichnoho analizu teploobminnykh system tsukrovoho vyrobnytstva. Chastyna 2. Naukovi pratsi NUKhT, 45, 43–52.
Downloads
Published
How to Cite
Issue
Section
License
Copyright (c) 2020 Sergii Vasilenko, Sergii Samiilenko, Vоlоdymyr Bondar, Olena Bilyk
This work is licensed under a Creative Commons Attribution 4.0 International License.
The consolidation and conditions for the transfer of copyright (identification of authorship) is carried out in the License Agreement. In particular, the authors reserve the right to the authorship of their manuscript and transfer the first publication of this work to the journal under the terms of the Creative Commons CC BY license. At the same time, they have the right to conclude on their own additional agreements concerning the non-exclusive distribution of the work in the form in which it was published by this journal, but provided that the link to the first publication of the article in this journal is preserved.