Balance de energía y exergía de un horno de cuba vertical para la producción de cal

Energy balance and exergy of a vertical cell furnace for lime production

dc.creatorSagastume, Alexis
dc.creatorCogollos Martínez, Juan Bautista
dc.date2020-07-21T22:02:42Z
dc.date2020-07-21T22:02:42Z
dc.date2019-09-25
dc.date.accessioned2023-10-03T19:11:41Z
dc.date.available2023-10-03T19:11:41Z
dc.identifierSagastume Gutiérrez and J. Cogollos Martínez “Balance de energía y exergía de un horno de cuba vertical para la producción de cal”, IJMSOR, vol. 4, no. 1, 2019. https://doi. org/10.17981/ijmsor.04.01.08
dc.identifier2539-5416 electrónico
dc.identifierhttps://hdl.handle.net/11323/6786
dc.identifierhttps://doi.org/10.17981/ijmsor.04.01.08
dc.identifier10.17981/ijmsor.04.01.08
dc.identifier2539-5416
dc.identifierCorporación Universidad de la Costa
dc.identifierREDICUC - Repositorio CUC
dc.identifierhttps://repositorio.cuc.edu.co/
dc.identifier.urihttps://repositorioslatinoamericanos.uchile.cl/handle/2250/9168742
dc.descriptionThis paper aims with methodologies and indicators for evaluating the impacts of freshwater use, the existing methods fundamentally analyze the amount of water used in relation to the impacts caused. Taking into account that there is a recognized need to consider the impacts, specifically on life cycle bases, the problem is that the data is considered insufficient or unreliable in the life cycle databases of water use, in addition not The method for evaluating the impact of the life cycle coincides with regard to the estimated impacts on the use of fresh water. These difficulties are highlighted and the advantages, limitations, differences in the results between different methods are analyzed, and the need for an improved methodology for evaluating the impacts of water use on life cycle bases. Quicklime production is a high energy consumer that is also characterized by high CO2 emissions. This work sets out to develop the energetic and exergetic balance of the limestone calcination process in order to identify the most influential factors in fuel consumption. The results show that the destruction of exergy during due to the combustion of the fuel and the transfer of heat and moment of the process are the most irreversible processes. The results also show that the energy and the exergy contained in the exhaust gases represent the main loss of the process. The combination of these factors represents more than 50% of the energy supplied to the process.
dc.descriptionEl trabajo trata las metodologías y los indicadores para la evaluación de los impactos de uso del agua dulce, los métodos existentes analizan fundamentalmente la cantidad de agua usada con relación a los impactos ocasionados. Teniendo en cuenta que hay una necesidad reconocida para considerar los impactos, específicamente sobre bases del ciclo de vida, la problemática es que se consideran insuficientes los datos o no son confiables en las bases de datos del ciclo de vida del uso del agua, además no coincide el método de valoración del impacto del ciclo de vida para lo relacionado con los impactos estimados en el uso del agua dulce, se resaltan estas dificultades y se analizan las ventajas, limitaciones, diferencias en los resultados entre diversos métodos y se observa la necesidad de una metodología perfeccionada para la evaluación de los impactos del uso del agua sobre bases del ciclo de vida. La producción de cal viva es un alto consumidor de energía que además se caracteriza por elevadas emisiones de CO2. Este trabajo se propone desarrollar el balance energético y exergético del proceso de calcinación de calizas con el objetivo de identificar los factores más influyentes en el consumo de combustible. Los resultados muestran que la destrucción de exergía durante debido a la combustión del combustible y a la transferencia de calor y momento del proceso son los procesos más irreversibles. Los resultados además muestran que la energía y la exergía contenida en los gases de escape representan la principal pérdida del proceso. La combinación de estos factores representa más del 50% de la energía suministrada al proceso.
dc.formatapplication/pdf
dc.formatapplication/pdf
dc.languagespa
dc.publisherCorporación Universidad de la Costa
dc.relationIJMSOR; Vol. 4, Núm. 1 (2019)
dc.relationIJMSOR: International Journal of Management Science & Operation Research
dc.relationIJMSOR: International Journal of Management Science & Operation Research
dc.relation[1] A. Sagastume, J. Van Caneghem, J. B. Cogollos and C. Vandecasteele, “Evaluation of the environmental performance of lime production in Cuba”, J Clean Prod, vol. 31, no. 1, pp. 126–136, Aug. 2012. https://doi.org/10.1016/j. jclepro.2012.02.035
dc.relation[2] P. A. Ochoa, A. Sagastume, J. B. Cogollos and C. Vandecasteele, “Cleaner production in a small lime factory by means of process control”, J Clean Prod, vol. 18, no. 12, pp. 1171–1176, Aug. 2010. https://doi.org/10.1016/j.jclepro.2010.03.019
dc.relation[3] R. S. Boynton, Chemistry and Technology of Lime and Limestone, New york: John Wiley & Sons, 1980.
dc.relation[4] H. Ruch, “The theoretical limits of heat consumption in lime burning due to the physical and chemical laws”, ZKG Int, vol. 34, no. 1, pp. 20–26, Jan, 1981.
dc.relation[5] Y. De la Peña, G. Bordeth, H. Campo, y U. Murillo, Clean Energies: An Opportunity to save the Planet, IJMSOR, vol. 3, n.º 1, pp. 21-25, dic. 2018.
dc.relation[6] Duarte Forero, J., Guillín Estrada, W., & Sánchez Guerrero, J. (2018). Desarrollo de una metodología para la predicción del volumen real en la cámara de combustión de motores diésel utilizando elementos finitos. INGE CUC, 14(1), 122-132. https://doi.org/10.17981/ingecuc.14.1.2018.11.
dc.relation[7] A. Sagastume and C. Vandecasteele, “Exergy-based indicators to evaluate the possibilities to reduce fuel consumption in lime production”, Energy, vol. 36, no. 5, pp. 2820–2827, May. 2011. https://doi.org/10.1016/j.energy.2011.02.023
dc.relation[8] D. Sheng-xiang, x. Qing-song and Z. Jie-min, “A lime shaft kiln diagnostic expert system based on holographic monitoring and real-time simulation,” Expert Syst Apl, vol. 38, no. 12, pp. 15400–15408, Nov. 2011. https://doi. org/10.1016/j.eswa.2011.06.021
dc.relation[9] M.Z. Sogut, Z. Oktay and A. Hepbasli, “Energetic and exergetic assessment of a trass mill process in a cement plant,” Energy Convers Manag, vol. 50, no. 9, pp. 2316–2323, Sep. 2009. https://doi.org/10.1016/j.enconman.2009.05.013
dc.relation[10] P. Regulagadda, I. Dincer and G. F. Naterer, “Exergy analysis of a thermal power plant with measured boiler and turbine losses”, Appl Therm Eng, vol. 30, no. 8-9, pp. 970–976, Jun. 2010. https://doi.org/10.1016/j.applthermaleng.2010.01.008
dc.relation[11] Z. Utlu, Z Sogut, A. Hepbasli and Z. Oktay, “Energy and exergy analyses of a raw mill in a cement production”, Appl Therm Eng, vol. 26, no. 17-18, pp. 2479–2489, Dec. 2006. https://doi.org/10.1016/j.applthermaleng.2005.11.016
dc.relation[12] I. H. Aljundi, “Energy and exergy analysis of a steam power plant in Jordan”, Appl Therm Eng, vol. 29, no. 2-3, pp. 324–328, Feb. 2009. https://doi.org/10.1016/j.applthermaleng.2008.02.029
dc.relation[13] A. Senegacnik, J. Oman and B. Sirok, “Analysis of calcination parameters and the temperature profile in an annular shaft kiln. Part 1: Theoretical survey”, Appl Therm Eng, vol. 27, no. 8-9, pp. 1473–1482, Jun. 2007. https://doi. org/10.1016/j.applthermaleng.2006.09.026
dc.relation[14] P. L. Zuideveld and P. J. van den Berg, “Design of lime shaft kilns”, Chem Eng Sci, vol. 26, no. 6, pp. 875–883, Jun. 1971. https://doi.org/10.1016/0009-2509(71)83048-8
dc.relation[15] y. A. Çengel and M. A. Boles, Thermodynamics: An Engineering Approach, 5th ed. Boston, MA, USA; McGrawHill, 2006.
dc.relation[16] A. Bejan, G. Tsatsaronis and M. J. Moran, Thermal design and optimization. New york: John Wiley & Sons, 1996.
dc.relation[17] C. Koroneos, G. Roumbas and N. Moussiopoulos, “Exergy analysis of cement production”, IJEX, vol. 2, no. 1, pp. 55– 68, Jan. 2005. https://doi.org/10.1504/IJEx.2005.006433
dc.relation[18] H. Piringer and W. Werner, “Conversion of large-diameter single shaft kilns to lignite dust firing successfully concluded”, ZKG Int, vol. 61, no. 1, pp. 46–52, Jan. 2008.
dc.relation[19] A. Bes, “Dynamic Process Simulation of Limestone Calcination in Normal Shaft Kilns”, Doctoral Thesis, ISUT, Magdeburg, de, 2006. Available: www.uni-magdeburg.de/ isut/TV/English/Research/Project/Bes.pdf
dc.relation[20] A. Bes, E. Specht and G. Kehse, “Calculation of the cooling zone length and the lime discharge temperature of lime shaft kilns”, ZKG Int, vol. 60, no. 4, pp. 63–73, Jan. 2007.
dc.relation[21] T. Kotas, The exergy method of thermal plant analysis, 2th ed., Krieger Publishing Company, Fla, USA, 1995.
dc.relation[22] C. Chen, E. Specht and J. Kehse, “Influences of origin and material property of limestone upon its decomposition behavior in shaft kilns”, ZKG Int, vol. 60, no. 1, pp. 51–60, Jan. 2007
dc.relation1
dc.relation4
dc.relationIJMSOR
dc.rightshttp://creativecommons.org/publicdomain/zero/1.0/
dc.rightsinfo:eu-repo/semantics/openAccess
dc.rightshttp://purl.org/coar/access_right/c_abf2
dc.sourceIJMSOR: International Journal of Management Science & Operation Research
dc.sourcehttp://ijmsoridi.com/index.php/ijmsor/article/view/110
dc.subjectEnergy
dc.subjectExergy
dc.subjectEfficiency
dc.subjectEnergía
dc.subjectExergía
dc.subjectEficiencia
dc.titleBalance de energía y exergía de un horno de cuba vertical para la producción de cal
dc.titleEnergy balance and exergy of a vertical cell furnace for lime production
dc.typeArtículo de revista
dc.typehttp://purl.org/coar/resource_type/c_6501
dc.typeText
dc.typeinfo:eu-repo/semantics/article
dc.typeinfo:eu-repo/semantics/publishedVersion
dc.typehttp://purl.org/redcol/resource_type/ART
dc.typeinfo:eu-repo/semantics/acceptedVersion
dc.typehttp://purl.org/coar/version/c_ab4af688f83e57aa


Este ítem pertenece a la siguiente institución