TY - JOUR
T1 - Investigation of Thin-Layer Drying of Coffee Beans Using a Double-Condenser Compression Refrigeration System
T2 - Effects of Air Mass Flux, Specific Humidity and Drying Temperature
AU - Dzaky, Muhammad Irfan
AU - Kosasih, Engkos Achmad
AU - Hakim, Imansyah Ibnu
AU - Zikri, Ahmad
N1 - Publisher Copyright:
© 2023, Semarak Ilmu Publishing. All rights reserved.
PY - 2023/6
Y1 - 2023/6
N2 - The drying process is the key to the quality of the coffee produced. The allowable moisture content of coffee beans is 12%. The air mass flux, specific humidity, and the drying temperature are varied using a bed dryer drying system combined with a double condenser refrigeration system. Robusta coffee beans are used in this research to obtain the characterization of coffee beans. The highest drying rate constant is obtained by 2.44 X 10-4 s-1 directly proportional to the increased air mass flux and drying air temperature, with a value of 1.701 kg/s m2 and 80°C, but inversely proportional to the specific humidity, with a value of 7.01 g/kg D.A. The lowest activation energy value was 31.88 kJ/mol when the air mass flux was 1.701 kg/s m2, the drying air temperature was 80 °C, and the average specific humidity was 7.01 g/kg D.A. In this work, the developed correlation is proposed to practically predict the activation energy (EA) and the pre-exponential factor (A) with equation Ea=24.767 Øam-0.244 w0.225 and A=0.380 Øam-2.796 w2.766 respectively. Based on Ea and A correlation equation, it can be used for designing a bed dryer type coffee drying system for a larger scale.
AB - The drying process is the key to the quality of the coffee produced. The allowable moisture content of coffee beans is 12%. The air mass flux, specific humidity, and the drying temperature are varied using a bed dryer drying system combined with a double condenser refrigeration system. Robusta coffee beans are used in this research to obtain the characterization of coffee beans. The highest drying rate constant is obtained by 2.44 X 10-4 s-1 directly proportional to the increased air mass flux and drying air temperature, with a value of 1.701 kg/s m2 and 80°C, but inversely proportional to the specific humidity, with a value of 7.01 g/kg D.A. The lowest activation energy value was 31.88 kJ/mol when the air mass flux was 1.701 kg/s m2, the drying air temperature was 80 °C, and the average specific humidity was 7.01 g/kg D.A. In this work, the developed correlation is proposed to practically predict the activation energy (EA) and the pre-exponential factor (A) with equation Ea=24.767 Øam-0.244 w0.225 and A=0.380 Øam-2.796 w2.766 respectively. Based on Ea and A correlation equation, it can be used for designing a bed dryer type coffee drying system for a larger scale.
KW - activation energy
KW - coffee beans
KW - drying rate constant
KW - parchment coffee
KW - refrigeration
KW - Robusta
UR - http://www.scopus.com/inward/record.url?scp=85171499809&partnerID=8YFLogxK
U2 - 10.37934/arfmts.106.1.90103
DO - 10.37934/arfmts.106.1.90103
M3 - Article
AN - SCOPUS:85171499809
SN - 2289-7879
VL - 106
SP - 90
EP - 103
JO - Journal of Advanced Research in Fluid Mechanics and Thermal Sciences
JF - Journal of Advanced Research in Fluid Mechanics and Thermal Sciences
IS - 1
ER -