It should be noted that the spread is entirely due to the dynamic conditions of the fluidized bed and not due to the instrumentation which was found to gwe reproducible results in runs performed in air. Experimental results are reported for the heat transfer between a high-temperature fluidized bed and an immersed horizontal tube array. (2) There is an optimum height of the ice-cube-packed bed to maximize the amount of cold energy release. In this chapter the heat transfer in solid-solid-fluid systems with thermal nonequilibrium between the phase pairs will be examined. The measured performance of heat transfer is excellent and that of fluidization is satisfactory, in spite of the static bed height being as small as 13 mm. Learn about our remote access options, School of Chemical Engineering, Chungnam National University, Daeduk Science Town, Daejeon 305‐764, Korea, Dept. SOLID HOLDUP AND CIRCULATION RATE IN A LIQUID-SOLID CIRCULATING FLUIDIZED BED WITH VISCOUS LIQUID MEDIUM. Khan, T. and Turton, R., 1992, " The Measurement of Heat balance for a control volume of length ∆ ∆ ∆ ∆x. Experiments were carried out in order to verify the influence of solid particle flow rate and distance between baffles immersed in a shallow fluidized bed. Reviews on heat transfer process in different types of FBC. Measurements of these coefficients in beds of 559 and 751 μm sand particles at temperatures up to 1,175 K have been made using this probe. Heat Mass Transfer, Vol. The effects of various parameters such as water flow rates, particle geometries, materials, and corrugated tube geometries, The Present work is carried out to investigate the thermal behavior of cross flow plate fin heat exchanger having offset strip fin. Results showed that the heat transfer coefficient increases with the solid flow rate and with the presence of baffles inside the bed, Efeito da Temperatura no Coeficiente de Transferência de Calor entre um Leito Fluidizado e Objetos Imersos. Figure 7.1(a) is for an internal particulate flow and heat transfer, where the net flow of particles and fluid is upward against the gravity vector. (4) A nondimensional correlation equation for predicting the time taken for the ice-cube-packed bed to completely melt is derived. The thermal design for fluidized bed cooler revealed to the installation of a heat exchanger consists of (65) horizontal tubes with (33.4) mm diameter and (4) m length inside the bed trough. Heat transfer in three-phase (G/L/S) circulating fluidized beds with low surface tension media. Packed-fluidized beds with horizontal, slanted, and vertical tubes are Experimental studies of local and total heat-transfer when passed through the heat exchanger, and the absolute humidity of the outlet air is reduced to about a quarter of that of the inlet air. For the identification of the dominating heat transfer mechanisms an approach with Computational Fluid Dynamics (CFD) simulations is chosen. and you may need to create a new Wiley Online Library account. Mainly two regimes namely packed bed and fluidized bed regimes will be considered for the analysis. They found that both the ash tempera- ture and ash-side heat transfer coefficient decease gradually along the ash-flow direction, while, the effects of operation parameters cannot be predicted by this model. © 2008-2020 ResearchGate GmbH. Learn more. On the contrary, the leading sphere can reduce the drag and heat transfer rate of the trailing sphere by more than 20% even when the two spheres are separated by six diameters. Bed temperature measurements along the length of the heat exchanger were experimentally obtained and heat balances for differential control volumes of the heat exchanger were made in order to obtain the axial profile of the bed-to-tube heat transfer coefficient. Experimental Methods for Engineers Fundamentals of Heat and Mass Transfer The Measurement of Instantaneous Heat Transfer Coefficients Around the Circumference of a Tube Immersed in a High Temperature Fluidized Bed. Access options Buy single article. The experimental results also showed that the suspension-wall heat transfer coefficient increased considerably with the solid flow rate and also when the particle diameter decreased. Some correlations are given for evaluating heat-exchanger The case of the fluidization of 1204 spheres by a jet flow has also been studied and compared against the case of the fluidization by a uniform flow. The modified Nu'=f(Re) equation exhibits a proper correlation between the results of the experiments in the literature and those of our experiments. In desert climates cooling greenhouses are needed to protect crops from extremely high temperature. The solver is validated against an existing model as well as own experimental results. Holdup and Flow Behavior of Fluidized Solid Particles in a Liquid-Solid Circulating Fluidized Bed. All rights reserved. Particles are tracked individually and their velocities and positions are solved based on the equations of linear and angular motions; particle temperature is assumed to be a constant. Germany, Poland, Greece, USA, and Australia). This approach uses a direct numerical simulation combined with the immersed boundary method (DNS-IB). 169-192) studied the fluidization of 1204 spheres by a uniform flow without heat transfer using a fictitious domain-based DNS. Lowell and Co. Inc. (Lowell and Co.) and Jay S. Dweck, Consultant, Inc., (JSD) to enhance the capability of ASPEN in simulating coal gasification and oil shale processing plants. Results show that the trailing sphere has an insignificant effect on the leading sphere when it comes to the drag and heat transfer rate. <> So, this work was trying to overcome this situation and to examine the feasibility of greenhouse cooling using groundwater in the indirect-direct evaporative cooling (IDEC) unit. The flexibility of the fluidized bed in managing the heat of chemical reaction has perhaps been its main virtue in the eyes of the chemical process engineer. The population balance model is validated with physically measured data taken from the literature . By exploring the rich data generated from the DNS-IB simulations, we are able to obtain statistically averaged fluid and particle velocity as well as particle heat transfer rate in a fluidized bed. With this background, the utilization of lignite for energy production is expected to remain a common practice in the decades to come since the availability of lignite is considerable in many countries of Europe and the world (e.g. Of specific interest in this study was the effect of bed temperature. 45% of the total global coal reserves consist of low-rank coals (LRCs) such as lignite. Figure 3 presents the bed temperature profiles for 9 cells comparing the model data with the measured ones. At each temperature, measurements were taken to evaluate both local and average values of the total heat transfer coefficient and the radiation contribution. Effect of pressure fluctuations on the heat transfer characteristics in a pressurized slurry bubble column. The experiments were carried out with and without vertical baffles in a fluidized bed with immersed horizontal tubes filled with water, in a counter flow arrangement. Sets of experiments had conducted to determine the thermal performance of the given heat exchanger. In the fluidized bed with small (< 0.1 mm) particles, convection by particles account for 90% of the overall heat transfer, while in the beds of large particles (> 1 mm) only 20% of the heat transfer is done by particle convection.
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