ABSTRACT
RESUMO Neste estudo, foram obtidas as cinéticas e isotermas de adsorção do fenol presentes em efluentes sintéticos em reator batelada e coluna de leito fixo, utilizando como adsorvente carvão ativado de casca de coco. O objetivo foi a obtenção dos parâmetros cinéticos e de equilíbrio do processo para simular diferentes condições operacionais em uma coluna de adsorção em leito fixo. Foram avaliadas a influência do pH, a massa de adsorvente, a concentração inicial de fenol e três diferentes temperaturas para os testes em reator batelada. Foi possível trabalhar no pH natural da solução e o aumento da temperatura indicou adsorção exotérmica, favorável e espontânea. Os dois modelos de isoterma (Langmuir e Freundlich) representaram bem os dados experimentais (R2 ≈ 0,9). Valores aproximados de capacidade máxima de adsorção foram encontrados para o reator batelada e para a coluna de leito fixo (qmáx = 41,69 mg.g-1 para o reator batelada e qmáx = 41,98 mg.g-1 para a coluna de leito fixo). O método de Volumes Finitos foi utilizado na discretização das equações matemáticas e um algoritmo computacional foi implementado em linguagem FORTRAN. O código computacional foi validado com dados experimentais deste trabalho (erro médio de 13%), podendo-se assim simular diferentes condições operacionais do sistema de adsorção em coluna de leito fixo com vista a futuras aplicações industriais.
ABSTRACT In this study, the kinetics and adsorption isotherms of phenol present in synthetic effluents were obtained in a batch reactor and fixed bed column, using adsorbent coconut shell activated carbon. The objective was to obtain the kinetic and equilibrium parameters of the process to simulate different operating conditions in a fixed bed adsorption column. The influence of the pH, adsorbent mass, initial phenol concentration, and three different temperatures for the batch reactor tests were evaluated. It was possible to work on the natural pH of the solution and the temperature increase indicated exothermic, favorable, and spontaneous adsorption. Both isotherm models (Langmuir and Freundlich) represented the experimental data (R2 ≈ 0.9). Approximate values of maximum adsorption capacity were found for the batch reactor and for the fixed bed column (qmax = 41.69 mg g-1 for the batch reactor and qmax = 41.98 mg g-1 for the fixed bed column). The Finite Volume method was used in the discretization of the mathematical equations and a computational algorithm was implemented in FORTRAN programming language. The computational code was validated with experimental data of this work (mean error of 13%) and it was possible to simulate different operational conditions of the fixed bed column adsorption system for future industrial applications.
ABSTRACT
RESUMEN El objetivo de la presente investigación fue evaluar la cáscara de la mazorca cacao (Theobroma cacao L.) para su uso en la adsorción de cromo hexavalente en solución acuosa, usando columna de lecho empacado, aplicando el método de superficie de respuesta (MSR), con el fin de determinar los valores óptimos de las variables incidentes en el proceso y, posteriormente, con estos valores, realizar los ensayos de adsorción. Se utilizó un diseño de experimentos compuesto central con puntos estrellas. La biomasa, se lavó, se secó, se disminuyó tamaño y se tamizó; los experimentos, se llevaron a cabo a 25°C, a diferentes tamaños de partícula, de caudal y de cantidad de biomasa, en columnas en sistema en continuo, obteniéndose un porcentaje de remoción de 39,16%, de Cr(VI). Al realizar los experimentos en sistema por lotes, se obtuvo que a tamaño de partícula 0,355mm, se favorece la adsorción. De los ensayos de adsorción en columna, utilizando los parámetros óptimos arrojados obtenidos por el MSR, se obtuvo un porcentaje de remoción de 62,65%, encontrando que los modelos de Yoon-Nelson y Thomas fueron los que ajustaron los datos experimentales de la curva de ruptura, con R2= 0,98. Se concluye que la cáscara de cacao es un buen precursor de bioadsorbentes y que las variables más influyentes en la adsorción de Cr(VI) en sistema por lotes y continuo son el tamaño de partícula y la altura del lecho.
SUMMARY The aim of the present investigation was to evaluate the cocoa shell (Theobroma cacao L.) for its use in the adsorption of hexavalent chromium in aqueous solution using packed bed column, applying the surface response method (SRM) in order to determine the optimum values of the variables involved in the process. The adsorption tests were carried out with these values. Was used a central composite experiment design with star points. The biomass was washed, dried, decreased size and sieved; the experiments were carried out at 25°C, at different particle sizes, flow rate and amount of biomass, in columns in continuous system; obtaining a percentage of removal of 39.16% of C (VI). Was obtained when performing the experiments in batch system that at a size of 0.355mm particle favors the adsorption. From the adsorption tests in the column using the optimum parameters obtained by the MSR, was obtained a removal percentage of 62.65%; finding that the models of Yoon-Nelson and Thomas were those that adjusted the experimental data of the rupture curve, with R2 =0.98. It's concluded that the cocoa shell is a good precursor of bioadsorbents and that the most influential variables in Cr (VI) adsorption in batch and continuous systems are particle size and bed height.