Bibliographic citations
Reaño, L., Rengifo, C. (2015). Evaluar la eficiencia energética del caldero para estandarizar datos de variables termodinámicas y su uso en la planta piloto de la FIQ – UNAP [Tesis, Universidad Nacional de la Amazonía Peruana]. http://repositorio.unapiquitos.edu.pe/handle/20.500.12737/4157
Reaño, L., Rengifo, C. Evaluar la eficiencia energética del caldero para estandarizar datos de variables termodinámicas y su uso en la planta piloto de la FIQ – UNAP [Tesis]. : Universidad Nacional de la Amazonía Peruana; 2015. http://repositorio.unapiquitos.edu.pe/handle/20.500.12737/4157
@misc{renati/969215,
title = "Evaluar la eficiencia energética del caldero para estandarizar datos de variables termodinámicas y su uso en la planta piloto de la FIQ – UNAP",
author = "Rengifo Calderón, Cesar Augusto",
publisher = "Universidad Nacional de la Amazonía Peruana",
year = "2015"
}
This research was performed taking into account that the pilots of the plants college beer and alcohol do not have experimental data; Variable referred to measurable such as PTV and other thermodynamic properties. During the evaluation of the cauldron, as a source of energy, it was found that the parameters of pressure and temperature are indicated starting in theory, to a cauldron that capacity. Currently, the control parameters in the power line, are not as reliable, because they need maintenance or replacement of equipment parts. We worked with a temperature of 160 ° C, saturation pressure of 6.2 bar; the same as those calculated using steam tables, and from which other thermodynamic variables are calculated as the value of produced steam heat coming out of the kettle (2846.4 kJ) heat provided by the fuel (3617.33 kJ), the energy efficiency of the ladle (78.6%), volume of saturated liquid (1.1029 cm3 / g), the volume of saturated steam (307.14 cm3 / g), the specific volume of water in the pot (41.55 cm3 / g), the quality of steam reaching the pilot plant (13.22%), the enthalpy input to the cereal cooker (963.66 kJ / kg), the internal energy specified in the entry of the cooker (925.48 kJ / kg), the specific internal energy in the cooker outlet (927.06 kJ / kg), the total heat (94.8 kJ), the variation of entropy (0.1226 kJ/ kg. ° K) and the production of entropy (7.356 kJ / K). According to the calculations, you can set the values found as indicated are not close to the theoretical data. This means no loss of internal energy to flow and lost steam in line and going to the environment. The data obtained in the calculations for steam are entirely practical information.
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