Navegando por Assunto "Fluidization"

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Acesso aberto (Open Access)
Análise experimental e numérica da fluidização para aplicações industriais
(Universidade Federal do Pará, 2012-03) LOURENÇO, Reimar de Oliveira; MESQUITA, André Luiz Amarante; http://lattes.cnpq.br/1331279630816662; MACÊDO, Emanuel Negrão; http://lattes.cnpq.br/8718370108324505
The gas-particle fluidized beds have great importance in the processing industry, due to have a good effect of mixing between the phases, and high rates of heat and mass transfer, requiring it to lower power consumption. Some typical examples of industrial applications of this equipment can be found in processes involving catalytic reactions, catalyst regeneration, or the combustion and coal of gasification. The understanding of the fluid dynamic behavior of this equipment is of fundamental importance for the fluidized bed can be adapted to new conditions. The literature reports several studies of fluidized bed, reporting varied contributions already incorporated the knowledge of the operation. The CFD (Computational Fluid Dynamics) tool has proved a good alternative for understanding the operation of this equipment. The use of multiphase granular Eulerian model together with the conservation equations of mass, energy and momentum for each of the phases present, has shown success when applied to fluidized beds. Overall, this work is to study the behavior of the fluid dynamic flow of glass beads and alumina in conventional fluidized bed type gas-solid, varying models Gidaspow, Syamlal-O’Brien and Wen-Yu, as well as Turbulence Models K-ε and RSM. More specifically, the work seeks to study the behavior of the fluid-dynamic equipment, by monitoring the most important fluid-dynamic parameters, among which we highlight the minimum fluidization velocity of the same, the pressure drop at minimum fluidization equipment, its porosity and expansion of the bed particles, also at minimum fluidization. Experimental tests were compared with numerical simulations using CFD (Computational Fluid Dynamics) tool, in which good agreement of the simulated results compared to experimental results.
Acesso aberto (Open Access)
Caracterização, análise fluidodinâmica e secagem de sementes de painço em leito de jorro
(Universidade Federal do Pará, 2014-05-16) NASCIMENTO, Lidiane Diniz do; COSTA, Cristiane Maria Leal; http://lattes.cnpq.br/0581730621014796; FARIA, Lênio José Guerreiro de; http://lattes.cnpq.br/7428609361678173
S. italica seeds were analyzed in chemical, physical and qualitative aspects and then the fluidynamics was evaluated at ambient temperature, for different loads of material in two spouted bed configurations: conical (500, 800, 1100 and 1400 g ) and conventional ( 1300, 1700 and 2100 g). From the experimental data it was found that the particles were suitable for the system used, so the operating parameters of the spouted bed were collected , which were compared with their theoretical values calculated by empirical correlations available in literature. According to experimental conditions, it was necessary to choose only one of the configurations of spouted bed, so it was decided to operate the conventional spouted bed. For the seed drying kinetics only the optimal load (1700g) was utilized and the temperatures used were 44 , 65 and 86 °C, verifying the absence of constant drying rate, indicating that drying was controlled by diffusion mechanisms. The effective moisture diffusivity was estimated, resulting in the range from 0.7729x10-11 to 2.3189x10-11 and the relationship between the temperature and the effective moisture diffusivity was described by Arrhenius equation, providing an activation energy of 24,86 kJ/mol. The mathematical models that best described the drying curve were Diffusion Approximation, Page and Midilli et al. Furthermore, a rotational central composite design was applied with the objective of evaluating the influence of the independent variables time (X1) and temperature (X2) on the responses moisture ratio (XR), germination (G) and speed germination index (SGI) . The chosen answers are necessaries in the seeds quality control, as in the case of the moisture content during the storage. The G and SGI responses are indicative of the physiological state of the seeds, which are also important, in accordance with the purpose of the product. Through statistical analysis, for a confidence interval of 95%, it was found that XR and SGI were influenced only by X1, X2 and X22 , while G was statistically affected by X2 and X22 . The effects for all responses were negative , indicating that SGI and XR decrease with increasing of temperature and drying time. The answer G decreases with increasing of temperature. Quadratic models were proposed by the statistical analyzes, reaching good correlation coefficients (R2); 0.9632 (XR), 0.8998 (G) and 0.9724 (SGI). Then, the optimal value of the foxtail millet drying process was determined, using the concept of Desirability Function, which was corresponding to a drying time of 121 min at a temperature of 64 ° C, getting seeds with 82.99% of germination; speed germination index of 29.33 (dimensionless) and final moisture content of 11%.
Acesso aberto (Open Access)
Recobrimento de sementes de linhaça (Linum usitatissimum L.) com suspensão biopolimérica em leito de jorro
(Universidade Federal do Pará, 2016-12-14) SANTANA, Elza Brandão; FARIA, Lênio José Guerreiro de; http://lattes.cnpq.br/7428609361678173; COSTA, Cristiane Maria Leal; http://lattes.cnpq.br/0581730621014796
It was studied application of starch in natura come from manioc starch (Manihot esculenta Crantz) in obtaining a biopolymer suspension in the coating of linseed (Linum usitatissimum L.), using as coating equipment a conventional spouted bed. We analyzed the physical and chemical characteristics of cassava starch and seeds, as well as the physiological characteristics of the seeds in natura and covered. Tests were carried out to obtain the biopolymer suspension including preliminary immersion coating tests, to evaluate the acceptance of the seed structure by the polymer matrix, based on physical data (angle of repose). For the execution of the coating process, tests were performed to define the coating operation, which included adjustments in the operating system from the study of fluid dynamics to the pumping of the suspension to make it possible to define the conditions of operation of the spouted bed. Fluid dynamics curves were constructed with different charges and atomization pressures, obtaining the fluid dynamic parameters ΔPM, ΔPje, ΔPmj and Umj. From the fluid dynamics results, the operating conditions were determined for a load of 1000 g of seeds, spray pressure of 5 psi, distance of the spray nozzle of 14 cm above the fixed seed bed and air velocity in the range of 1,9 to 1,29Umj. To analyze the coating process used an experimental design type PCCR considering the input variables, air temperature (Tar) and flow rate of the suspension (Qs), and efficiency responses (η), growt of the particle (δ), loss grip (Pad), process evaporation rate (Ėp), germination (G) and germination speed index (GSI). To estimate an optimal point of this operation was applied to define desirability function, wherein the generated optimum for the overall desirability was 0.9630 with the seed bed operating at 51 °C and 12 mL/min, respectively. The obtained results show that the coating process was efficient in relation to the values obtained for the responses and also to maintain the physiological qualities of the seeds. In addition, to open precedents for application in foods since the seeds covered had water activity of 0,34, in front of an initial activity of 0,62 for the seeds in natura.
Acesso aberto (Open Access)
Transporte pneumático fluidizado: estudos de casos aplicados à indústria do alumínio primário
(Universidade Federal do Pará, 2011-08) VASCONCELOS, Paulo Douglas Santos; MESQUITA, André Luiz Amarante; http://lattes.cnpq.br/1331279630816662
This work is a contribution to science and applied technology developed to fluidized bed and fluidized motion conveying used in the powder handling of the industrial processes. In the case of fluidized bed it is proposed an empirical equation to predict the minimum fluidization velocity for the fluoride alumina, crust powder and others powders used in the industrial processes with good results compared with the experiments and the equations available in the literature. It was also studied the constitutive equations to predict the behavior of the angle of repose and interparticles friction as a function of the superficial velocity of fluidization. In a second step it is proposed an equation to predict the capacity of the Air Pneumatic Fluidized Conveyor with good results compared with the experiments for fluoride alumina. The Air Fluidized Conveyor is a contribution to applied technology reducing the consumption of energy, it operates even in upward direction, and so, decreasing the rate kWh/ton in the powder handling of the industrial processes.