Published Date
Solar Energy
August 2016, Vol.133:421–428, doi:10.1016/j.solener.2016.04.033
Author
Abstract
A hybrid photovoltaic–thermal (PVT) greenhouse solar dryer under mixed mode has been proposed and different parameters have been evaluated for climatic condition of Indian Institute of Technology, New Delhi (28_350N, 77_120E, 216 m above MSL), India. Further thermal modelling has been developed for the PVT greenhouse dryer by considering different parameter namely crop, greenhouse and solar cell temperatures, etc. Numerical computations have been done with the help of program made on MATLAB 2013a and the results are validated with experimental values. Characteristic curves have been developed for drying and system efficiency with experimental validation. Further, an overall thermal energy and exergy have been calculated. Theoretical and experimental values of overall thermal energy found to be 1.92 kW h and 2.03 kW h respectively. It can be seen that there is good agreement between theoretical and experimental value with r = 0.98 and e = 10.76. Further validation has also been done for energy and exergy of PVT dryer.
Keywords
Heat transfer coefficient
Overall thermal energy
Overall exergy
PVT greenhouse mixed mode dryer
For further details log on website :
http://www.sciencedirect.com/science/article/pii/S0038092X16300664
Solar Energy
August 2016, Vol.133:421–428, doi:10.1016/j.solener.2016.04.033
Author
Received 6 November 2015. Revised 3 March 2016. Accepted 20 April 2016. Available online 29 April 2016.
Highlights
- •Present system is designed for rural area in developing country where grid connectivity is not available everywhere.
- •Thermal modeling has been done with experimental validation.
- •Characteristic curve have been made for system and drying.
- •Overall thermal energy and overall exergy have been calculated with experimental validation.
A hybrid photovoltaic–thermal (PVT) greenhouse solar dryer under mixed mode has been proposed and different parameters have been evaluated for climatic condition of Indian Institute of Technology, New Delhi (28_350N, 77_120E, 216 m above MSL), India. Further thermal modelling has been developed for the PVT greenhouse dryer by considering different parameter namely crop, greenhouse and solar cell temperatures, etc. Numerical computations have been done with the help of program made on MATLAB 2013a and the results are validated with experimental values. Characteristic curves have been developed for drying and system efficiency with experimental validation. Further, an overall thermal energy and exergy have been calculated. Theoretical and experimental values of overall thermal energy found to be 1.92 kW h and 2.03 kW h respectively. It can be seen that there is good agreement between theoretical and experimental value with r = 0.98 and e = 10.76. Further validation has also been done for energy and exergy of PVT dryer.
Keywords
Nomenclature
- Ac
- area of crop surface (m2)
- Am
- area of module (m2)
- Ai
- area of all side wall of dryer (m2)
- Cf
- specific heat of air (J/kg K)
- Ccr
- specific heat of crop (J/kg K)
- C
- air conductance (W/m2 K)
- D
- diameter of fan (m)
- hi
- heat transfer coefficient (htc) inside solar drying chamber (W/m2 K)
- hcr
- total htc from crop surface to solar drying chamber (W/m2 K)
- hcrc
- convective htc from crop surface to solar drying chamber (W/m2 K)
- hcrew or hew
- evaporative htc from crop surface to solar drying chamber (W/m2 K)
- ho
- heat transfer coefficient from top of module to ambient (W/m2 K)
- h1
- heat transfer coefficient from wall of dryer to ambient (W/m2 K)
- It
- solar intensity (W/m2)
- I(i)
- solar intensity on the wall of drying chamber (W/m2)
- Ieff
- total radiation on the crop (W/m2)
- kg
- thermal conductivity of glass of module (W/m K)
- Kg
- thermal conductivity of glazing (W/m K)
- lg
- thickness of glass cover of module (m)
- Lg
- thickness of glazing (m)
- mass flow rate of air (kg/s)
- Mcr
- mass of crop (kg)
- N
- fan speed (RPM)
- Pfan
- power of fan (W)
- PTr
- partial pressure at green house chamber temperature (N/m2)
- PTcr
- partial pressure at crop temperature (N/m2)
- Ta
- ambient temperature (°C)
- To
- cell temperature for optimum cell efficiency i.e. 25 °C
- Tc
- cell temperature (°C)
- Tcr
- crop temperature (°C)
- Tcro
- initial crop temperature (°C)
- Tr
- drying chamber temperature (°C)
- Ubcr
- heat transfer coefficient from bottom of module to drying chamber (W/m2 K)
- Utca
- heat transfer coefficient from top of module to ambient air (W/m2 K)
- Qth,th,ov
- overall theoretical thermal energy
- Qth,exp,ov
- overall experimental thermal energy
- Qex,th,ov
- overall theoretical exergy
- Qex,exp,ov
- overall experimental exergy
- αc
- absorptivity of solar cell
- αcr
- absorptivity of crop
- β0
- temperature dependent efficiency factor
- βc
- packing factor of module
- γ
- relative humidity
- η0
- standard efficiency at standard condition
- ηc
- solar cell efficiency
- ηm
- module efficiency
- v
- wind velocity (m/s)
- v1
- air velocity in drying chamber (m/s)
- th
- thermal
- τg
- transmittivity of glass
- ⁎ Corresponding author.
For further details log on website :
http://www.sciencedirect.com/science/article/pii/S0038092X16300664
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