Abstract
This chapter includes environment feasibility of solar hybrid systems. In this regard, drying system with PVT air collector has been studied in details. It is seen that the market has different types of PV modules (a-Si, CdTe p-Si, c-Si, and CIGS) are available in the market. Further, thermal modeling has been explored to calculate the thermal energy (TE). Weather-related data has been taken from IMD, Pune, for yearly analysis. Various temperatures, namely outlet air from collector, cell, drying chamber, and crop surface have been calculated through thermal modeling developed for the system. Further, energy payback time (EPBT) for 100% PV area with different PV technologies used on flat plate air collector-integrated drying system found between 3.2 and 1.59 years. Environmental feasibility has also been evaluated for various solar PV cell technologies integrated with the system.
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Abbreviations
- A c :
-
Area of the crop surface (m2)
- A cf :
-
Opening area of fan (m2)
- A c1 :
-
Cross-sectional area of duct of air collector (m2)
- A m :
-
Area of the PV module (m2)
- A w :
-
Area of side walls of dryer (m2)
- A t :
-
Area of the tray (m2)
- C f :
-
Specific heat of air (J/kg K)
- C cr :
-
Specific heat of crop (J/kg K)
- d :
-
Diameter of DC fan (m)
- E el :
-
Electrical energy (kWh)
- hi :
-
Heat transfer coefficient inside PVT air collector and solar drying system (W/m2K)
- h crr :
-
Total heat transfer coefficient from crop surface to drying chamber (W/m2K)
- h crc :
-
Convective heat transfer coefficient from crop surface to drying chamber (W/m2K)
- h crew or h ew :
-
Evaporative heat transfer coefficient from crop surface to drying chamber (W/m2K)
- h o :
-
Heat transfer coefficient from top of module to ambient air (W/m2K)
- h pf :
-
Heat transfer coefficient from absorbing plate to working fluid (W/m2K)
- I t :
-
Solar intensity (W/m2)
- I w :
-
Total solar intensity on the walls of drying chamber (W/m2)
- K g :
-
Thermal conductivity of glazing (W/mK)
- L g :
-
Thickness of the glass (m)
- \( \dot{M}_{f} \) :
-
Mass flow rate of working fluid (air) (kg/s)
- M cr :
-
Mass of crop (kg)
- P Tr :
-
Partial pressure at greenhouse chamber temperature (N/m2)
- P Tcr :
-
Partial pressure at crop temperature (N/m2)
- T a :
-
Ambient temperature (°C)
- T o :
-
Cell temperature for optimum cell efficiency
- T c :
-
Cell temperature (°C)
- T cr :
-
Crop temperature (°C)
- T cro :
-
Initial crop temperature (°C)
- T r :
-
Drying chamber temperature (°C)
- T foN :
-
Air temperature at outlet of Nth PVT air collector (°C)
- U bcf :
-
Heat transfer coefficient from bottom of module to working fluid (W/m2K)
- U tca :
-
Heat transfer coefficient from top of module to ambient air (W/m2K)
- U bpa :
-
Heat transfer coefficient from bottom of absorbing plate to ambient air (W/m2K)
- Q th :
-
Thermal energy (kWh)
- Q eq,th :
-
Equivalent thermal energy (kWh)
- Q th,ex :
-
Thermal exergy (kWh)
- α c :
-
Absorptivity of solar cell
- α cr :
-
Absorptivity of crop
- β 0 :
-
Temperature-dependent efficiency factor
- β c :
-
Packing factor of module
- γ :
-
Relative humidity
- η 0 :
-
Standard efficiency at standard condition
- η c :
-
Solar cell efficiency
- η m :
-
Module efficiency
- η th :
-
Thermal efficiency
- η el :
-
Electrical efficiency
- η eq,th :
-
Equivalent thermal efficiency
- η ex :
-
Exergy efficiency
- η eq,ex :
-
Equivalent exergy efficiency
- v :
-
Wind velocity in ambient (m/s)
- v 1 :
-
Air velocity in duct of air collector (m/s)
- v 2 :
-
Air velocity from fan (m/s)
- v 3 :
-
Air velocity in drying chamber (m/s)
- τ g :
-
Transmittivity of glass
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Appendices
Appendix I
Formulae used to compute various heat transfer coefficient are as follows:
\( A_{cf} = (\pi /4) \times d^{2} \) | \( v_{2} = \dot{M}_{f} /(\rho \times A_{cf} ) \) |
\( v_{1} = ((\pi /4) \times d^{2} \times v_{2} )/A_{c1} \) | \( v_{3} = ((\pi /4) \times d^{2} \times v_{2} )/A_{t} \) |
\( h_{i} = 2.8 + 3v_{1} \) | \( h_{o} = 5.7 + 3.8v \) |
\( h_{{{\text{cr}}r}} = h_{{{\text{cr}}c}} + h_{\text{crew}} \) | \( h_{crc} = 2.8 + 3v_{3} \) |
\( h_{\text{crew}} = \frac{{0.01667h_{{{\text{cr}}c}} (P_{Tcr} - \gamma P_{Tr} )}}{{T_{\text{cr}} - T_{r} }} \) | \( P_{Tcr} = \exp (25.317 - (5144/(273 + T_{cr} ))) \)\( U_{bpa} = 1/((L_{p} /K_{p} ) + (1/h_{i} )) \) |
\( P_{Tr} = \exp (25.317 - (5144/(273 + T_{r} ))) \) | \( U_{bcf} = 1/((L_{g} /K_{g} ) + (1/h_{i} )) \) |
\( U_{tca} = 1/((L_{g} /K_{g} ) + (1/h_{o} )) \) | \( U_{wra} = 1/((L_{g} /K_{g} ) + (1/h_{o} )) \) |
\( UA = A_{w} U_{wra} \) |
Appendix II
Various design parameters taken for the calculation of different temperatures
αc = 0.85 | τg = 0.9 | βc = 0.83 |
ηo = 0.15 | αcr = 0.4 | Mcr = 2 kg |
Ccr = 3900 J/kg K | γ = 0.4 | v = 2 m/s |
Am = 0.358 m2 | Aw = 0.390 m2 | Ac = 1.073 m2 |
Cf = 1005 J/kg K | Kg = 1.1 W/mK | d = 0.01 m |
Lg = 0.003 m | Lp = 0.002 m | Kp = 0.8 W/mK |
ρ = 1.17 kg/m3 | T0 = 25 °C | At = 0.169 m2 |
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Tiwari, S., Tiwari, P., Dwivedi, V.K., Tiwari, G.N. (2021). Environmental Feasibility of Solar Hybrid Systems. In: Singh, S.N., Tiwari, P., Tiwari, S. (eds) Fundamentals and Innovations in Solar Energy. Energy Systems in Electrical Engineering. Springer, Singapore. https://doi.org/10.1007/978-981-33-6456-1_15
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