PENGARUH VARIASI SUHU REAKTOR TERHADAP HASIL
DESTILASI PLASTIK MENJADI BAHAN BAKAR MINYAK
DENGAN KONDENSOR 2 TINGKATAN
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Institusion
INSTITUT TEKNOLOGI DIRGANTARA ADISUTJIPTO
Author
ANDHIKA, MUHAMMAD
Subject
T Technology (General)
Datestamp
2024-06-27 07:41:25
Abstract :
The purpose of this study was to investigate the calorific value, density and viscosity of the distillate and to investigate the residual combustion in the reactor after the distillation process. The distillation was carried out with a maximum variation of reactor temperature of 380-390°C, 390-400°C and 400- 410°C using 2-stage Condensers. The material used in the distillation process was PET plastic (Polyethylene Terephthalate). The results obtained in this study were the highest calorific value obtained with the variation of the temperature of the reactor between 390-400°C in the Condenser 2, for 10513,027 cal/g. In addition, the temperature of the reactor in the condenser 1, between 400-410°C, had the lowest calorific value, for 9570,958 cal/g. In the density test, the highest value was obtained for the temperature variation of the reactor 380-390°C in the Condenser 2, for 683 kg/m3. In addition, the reactor temperature of 400-410°C in Condenser 1 had the lowest density value, for 648 kg/m3. In the viscosity test, the highest value obtained with the 380-390°C reactor temperature variation in condenser 2 had the highest viscosity value, 1,754 mm2 /s. In addition, the reactor temperature of 400-410°C in Condenser 2 had the lowest viscosity value, for 0,670 mm2 /s. In each experiment, there was residual combustion in the reactor. The results of the tests allowed to conclude that the variation of the temperature of the reactor with a condenser with 2 levels could also affect the calorific value, the density and the viscosity of the distilled fuel.
The purpose of this study was to investigate the calorific value, density and viscosity of the distillate and to investigate the residual combustion in the reactor after the distillation process. The distillation was carried out with a maximum variation of reactor temperature of 380-390°C, 390-400°C and 400- 410°C using 2-stage Condensers. The material used in the distillation process was PET plastic (Polyethylene Terephthalate). The results obtained in this study were the highest calorific value obtained with the variation of the temperature of the reactor between 390-400°C in the Condenser 2, for 10513,027 cal/g. In addition, the temperature of the reactor in the condenser 1, between 400-410°C, had the lowest calorific value, for 9570,958 cal/g. In the density test, the highest value was obtained for the temperature variation of the reactor 380-390°C in the Condenser 2, for 683 kg/m3. In addition, the reactor temperature of 400-410°C in Condenser 1 had the lowest density value, for 648 kg/m3. In the viscosity test, the highest value obtained with the 380-390°C reactor temperature variation in condenser 2 had the highest viscosity value, 1,754 mm2 /s. In addition, the reactor temperature of 400-410°C in Condenser 2 had the lowest viscosity value, for 0,670 mm2 /s. In each experiment, there was residual combustion in the reactor. The results of the tests allowed to conclude that the variation of the temperature of the reactor with a condenser with 2 levels could also affect the calorific value, the density and the viscosity of the distilled fuel.
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