Advances in Concentrated Solar Power: A Perspective of Heat Transfer

Author(s):  
Fadi Alnaimat ◽  
Yasir Rashid
Solar Energy ◽  
2014 ◽  
Vol 105 ◽  
pp. 468-478 ◽  
Author(s):  
Dileep Singh ◽  
Elena V. Timofeeva ◽  
Michael R. Moravek ◽  
Sreeram Cingarapu ◽  
Wenhua Yu ◽  
...  

2005 ◽  
Vol 127 (3) ◽  
pp. 425-429 ◽  
Author(s):  
C. Wieckert

A high-temperature solar chemical reactor for the processing of solids is scaled up from a laboratory scale (5kW concentrated solar power input) to a pilot scale (200kW). The chosen design features two cavities in series: An upper cavity has a small aperture to let in concentrated solar power coming from the top. It serves as the solar receiver, radiant absorber, and radiant emitter to a lower cavity. The lower cavity is a well-insulated enclosure. It is subjected to thermal radiation from the upper cavity and serves in our application as the reaction chamber for a mixture of ZnO and carbon. Important insight for the definition of the geometrical parameters of the pilot reactor has been generated by a radiation heat transfer analysis based on the radiosity enclosure theory. The steady-state model accounts for radiation heat transfer within the solar reactor including reradiation losses through the reactor aperture, wall losses due to thermal conduction and heat consumption by the endothermic chemical reaction. Key results include temperatures of the different reactor walls and the thermal efficiency of the reactor as a function of the major geometrical and physical parameters. The model, hence, allows for a fast estimate of the influence of these parameters on the reactor performance.


2019 ◽  
Vol 140 (1) ◽  
pp. 33-51 ◽  
Author(s):  
Duraisamy Ramalingam Rajendran ◽  
Esakkimuthu Ganapathy Sundaram ◽  
Paulraj Jawahar ◽  
Vaithilingam Sivakumar ◽  
Omid Mahian ◽  
...  

Solar Energy ◽  
2018 ◽  
Vol 164 ◽  
pp. 47-57 ◽  
Author(s):  
Yunshu Zhang ◽  
Ye Cai ◽  
SungHwan Hwang ◽  
Gregory Wilk ◽  
Freddy DeAngelis ◽  
...  

2015 ◽  
Vol 69 ◽  
pp. 663-671 ◽  
Author(s):  
C. Jung ◽  
J. Dersch ◽  
A. Nietsch ◽  
M. Senholdt

2011 ◽  
Vol 133 (3) ◽  
Author(s):  
Franziska Schaube ◽  
Antje Wörner ◽  
Rainer Tamme

High temperature thermal storage technologies that can be easily integrated into future concentrated solar power plants are a key factor for increasing the market potential of solar power production. Storing thermal energy by reversible gas–solid reactions has the potential of achieving high storage densities while being adjustable to various plant configurations. In this paper the Ca(OH)2/CaO reaction system is investigated theoretically. It can achieve storage densities above 300 kWh/m3 while operating in a temperature range between 400 and 600°C. Reactor concepts with indirect and direct heat transfer are being evaluated. The low thermal conductivity of the fixed bed of solid reactants turned out to considerably limit the performance of a storage tank with indirect heat input through the reactor walls. A one-dimensional model for the storage reactor is established and solved with the Finite Element Method. The reactor concept with direct heat transfer by flowing the gaseous reactant plus additional inert gas through the solid reactants did not show any limitation due to heat transfer. If reaction kinetics are fast enough, the reactor performance in case of the Ca(OH)2/CaO reaction system is limited by the thermal capacity of the gaseous stream to take-up heat of reaction. However, to limit pressure drop and the according losses for compression of the gas stream, the size of the storage system is restricted in a fixed bed configuration.


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