TY - JOUR
T1 - Towards thermal design optimization of tubular digesters in cold climates
T2 - A heat transfer model
AU - Perrigault, Thibault
AU - Weatherford, Vergil
AU - Martí-Herrero, Jaime
AU - Poggio, Davide
PY - 2012/11
Y1 - 2012/11
N2 - A cold climate, low cost, tubular digester is monitored and temperatures from different parts of the slurry, greenhouse, and adobe walls are presented, discussing the thermal performance of the digester. The slurry exhibits a vertical gradient of 6. °C, with a mean value of 24.5. °C, while the ambient temperature varies from 10. °C to 30. °C, showing the efficiency of the system as a solar heat collector with thermal inertia. A simple time-dependent thermal model is developed using inputs of solar radiation, wind velocity, ambient temperature, and digester geometry. The model outputs include temperatures of the slurry, the biogas, its holding membrane and the greenhouse air, wall and cover. Radiative, convective and conductive heat transfer phenomena are considered between all system elements. The model has 0.47. °C (2%) standard error for the average slurry temperature. This model can be used to predict the influence of geometry and materials on the performance of the digester.
AB - A cold climate, low cost, tubular digester is monitored and temperatures from different parts of the slurry, greenhouse, and adobe walls are presented, discussing the thermal performance of the digester. The slurry exhibits a vertical gradient of 6. °C, with a mean value of 24.5. °C, while the ambient temperature varies from 10. °C to 30. °C, showing the efficiency of the system as a solar heat collector with thermal inertia. A simple time-dependent thermal model is developed using inputs of solar radiation, wind velocity, ambient temperature, and digester geometry. The model outputs include temperatures of the slurry, the biogas, its holding membrane and the greenhouse air, wall and cover. Radiative, convective and conductive heat transfer phenomena are considered between all system elements. The model has 0.47. °C (2%) standard error for the average slurry temperature. This model can be used to predict the influence of geometry and materials on the performance of the digester.
KW - Anaerobic digestion
KW - Heat transfer
KW - Low-cost tubular digester
KW - Plug flow
KW - Thermal performance
UR - http://www.scopus.com/inward/record.url?scp=84866153666&partnerID=8YFLogxK
U2 - 10.1016/j.biortech.2012.08.019
DO - 10.1016/j.biortech.2012.08.019
M3 - Artículo
C2 - 22989653
AN - SCOPUS:84866153666
SN - 0960-8524
VL - 124
SP - 259
EP - 268
JO - Bioresource Technology
JF - Bioresource Technology
ER -