A grain dryer consists of a long semicircular duct of radius R = 1 m . One-half of the base surface consists of an electrically heated plate of emissivity ε p = 0.8 , while the other half supports the grain to be dried, which has an emissivity of ε g = 0.9 . In a batch drying process for which the temperature of the grain is T g = 330 K , 2.50 kg of Water are to be removed per meter of duct length over a 1-h period. (a) Neglecting convection heat transfer, determine the required temperature T p of the heater plate. (b) If the water vapor is swept from the duct by the flow of dry air, what convection mass transfer coefficient h m must be maintained by the flow? (c) If the air is at 300 K, is the assumption of negligible convection justified?
A grain dryer consists of a long semicircular duct of radius R = 1 m . One-half of the base surface consists of an electrically heated plate of emissivity ε p = 0.8 , while the other half supports the grain to be dried, which has an emissivity of ε g = 0.9 . In a batch drying process for which the temperature of the grain is T g = 330 K , 2.50 kg of Water are to be removed per meter of duct length over a 1-h period. (a) Neglecting convection heat transfer, determine the required temperature T p of the heater plate. (b) If the water vapor is swept from the duct by the flow of dry air, what convection mass transfer coefficient h m must be maintained by the flow? (c) If the air is at 300 K, is the assumption of negligible convection justified?
Solution Summary: The author explains the temperature of the heater required for specified drying rate.
A grain dryer consists of a long semicircular duct of radius
R
=
1
m
. One-half of the base surface consists of an electrically heated plate of emissivity
ε
p
=
0.8
, while the other half supports the grain to be dried, which has an emissivity of
ε
g
=
0.9
. In a batch drying process for which the temperature of the grain is
T
g
=
330
K
, 2.50 kg of Water are to be removed per meter of duct length over a 1-h period.
(a) Neglecting convection heat transfer, determine the required temperature Tpof the heater plate. (b) If the water vapor is swept from the duct by the flow of dry air, what convection mass transfer coefficient hmmust be maintained by the flow? (c) If the air is at 300 K, is the assumption of negligible convection justified?
Net movement of mass from one location, usually meaning stream, phase, fraction, or component, to another. Mass transfer occurs in many processes, such as absorption, evaporation, drying, precipitation, membrane filtration, and distillation.
A spherical instrumentation device with a diameter of 102.16 mm has an emissivity of 0.32. It is
contained in a large space simulation chamber whose temperature is preserved at 64.1 K. If its
daily operation is restricted to the temperature range 50.6
A furnace is of cylindrical shape with a diameter of 1.2 m and a length of 1.2 m. The top surface has an emissivity of 0.70 and is maintained at 500 K. The bottom surface has an emissivity of 0.50 and is maintained at 650 K. The side surface has an emissivity of 0.40. Heat is supplied from the base surface at a net rate of 1400 W. Determine the temperature of the side surface and the net rates of heat transfer between the top and the bottom surfaces, and between the bottom and side surfaces.
2_5190874259647370...
A cylindrical shape is with diameter of 1.2m and length of 1.2m. The top surface has an emissivity of 0.7
and temperature 500 K. The bottom surface has an emissivity of o.5 and temperature 650 K. The side
surface has an emissivity of 0.4. Determine the shape factors for all surfaces.
E 0.0
L=650 K
II
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