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Commenced in January 2007 Frequency: Monthly Edition: International Publications Count: 30123

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Hydrodynamic Analysis with Heat Transfer in Solid Gas Fluidized Bed Reactor for Solar Thermal Applications
Fluidized bed reactors are known as highly exothermic and endothermic according to uniformity in temperature as a safe and effective mean for catalytic reactors. In these reactors, a wide range of catalyst particles can be used and by using a continuous operation proceed to produce in succession. Providing optimal conditions for the operation of these types of reactors will prevent the exorbitant costs necessary to carry out laboratory work. In this regard, a hydrodynamic analysis was carried out with heat transfer in the solid-gas fluidized bed reactor for solar thermal applications. The results showed that in the fluid flow the input of the reactor has a lower temperature than the outlet, and when the fluid is passing from the reactor, the heat transfer happens between cylinder and solar panel and fluid. It increases the fluid temperature in the outlet pump and also the kinetic energy of the fluid has been raised in the outlet areas.
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[1] F. Bazdidi Tehrani, M. Sedaghat nejad, Ekrami, I. Naeem, Vaasefi, “Single and double phases analysis of mixed nano-fluid transfer in vertical rectangular channel under the heat asymmetric boundary conditions”, Elmosannat University, Iran, 2014.
[2] S. Pahlavani, H. Hashem Abadi, A. Heidari, “CFC simulation of bubble slurry backmix Terephthalic acid producer reactor hydrodynamic”, Elmosannat University, Iran, 2014.
[3] E. Mehrabi Gohari, “Hydrodynamic simulation of a solid-gas fluidized bed by using Boltzman network and uniform profile”, 2016.
[4] A. Khaamesi, R. Abdollah Poursorkhi, M. Pourfalah, “Review of the fluidized bed heat exchangers operation with solar power supply”, Mazandaran University of Science and Technology, 2017.
[5] A. A. Jamali, Sh. Shah Hosseini, “Experimental Investigation and Numerical Simulation of a Three-Phase fluidized bed using Particle Image Tracing”, scientific journal of Fluid Mechanics, no. 1, pp.1 -, 2014.
[6] H. Hosseini, R. Rahimi, M. Zivdar, A. Samimi, “unstable simulation of B kind particles”, 2010.
[7] Y. Behjat, S. Shahhosseini, S. H. Hashemabadi, “CFD modeling of hydrodynamic and heat transfer in fluidized bed reactors”, International Communications in Heat and Mass Transfer, 35(3), 357-368, 2008.
[8] A. Ghaemi, N. Ismail-Zadeh, Sh. Shahhosseini, Y. Behjat, “Simulation of carbon dioxide absorption in a reactor reactor”, Faculty of Chemical Engineering, Iran University of Science and Technology, Tehran.
[9] Q. Wang, Y. Feng, J. Lu, W. Yin, H. Yang, P. J. Witt, M. Zhang, “Numerical study of particle segregation in a coal beneficiation fluidized bed by a TFM–DEM hybrid model: influence of coal particle size and density”, Chemical Engineering Journal. 260 (2015) 240–257.
[10] L. Lu, A. Morris, T. Li, S. Benyahia, Extension of a coarse-grained particle method to simulate heat transfer in fluidized beds, Int. J. Heat Mass Transf. 111 (2017) 723–735.
[11] J. R. Van Ommen, R. F. Mudde, Measuring the gas-solids distribution in fluidized beds – a review, Int. J. Chem. React. Eng. 6 (2008) 1542–6580.
[12] Y. Tsuji, T. Kawaguchi, T. Tanaka, Discrete particle simulation of twodimensional fluidized bed, Powder Technol. 77 (1993) 79–87.
[13] H. Zhang, A. Yu, W. Zhong, Y. Tan, A combined TLBM–IBM–DEM scheme for simulating isothermal particulate flow in fluid, Int. J. Heat Mass Transf. 91 (2015) 178–189.
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