La eliminación de metales tóxicos presentes en efluentes líquidos mediante resinas de cambio iónico. Parte VIII: Arsénico(III))/OH-/Dowex 1x8

Autores/as

DOI:

https://doi.org/10.3989/revmetalm.132

Palabras clave:

Arsénico(III), Dowex 1x8, Efluentes líquidos, Eliminación, Nanotubos de carbono de pared múltiple

Resumen


En el presente trabajo se utiliza la resina de intercambio aniónico para la eliminación de arsénico(III) de medios acuosos. Esta eliminación se ha investigado teniendo en cuenta diversas variables experimentales como son: la velocidad de agitación del sistema, la temperatura, el pH de la disolución y la dosificación de resina al sistema. El equilibrio de intercambio aniónico tiene un carácter endotérmico y no espontaneo, en el rango de temperaturas comprendido entre 20 °C y 60 °C, la cinética del proceso responde al modelo de pseudo-segundo orden, sin embargo, el mecanismo de carga del arsénico en la resina cambia en el rango de temperaturas comprendido entre 20 °C y 40 °C. La isoterma de carga del metal en la resina responde al modelo linearizado de Freundlich. Se comparan los resultados de carga de arsénico en la resina Dowex 1x8 con los obtenidos con otras resinas y con nanotubos de carbono de pared multiple. La elución del arsénico se puede realizar con disoluciones acidas, por ejemplo 1 M HCl.

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Publicado

2018-12-30

Cómo citar

Alguacil, F. J., & Escudero, E. (2018). La eliminación de metales tóxicos presentes en efluentes líquidos mediante resinas de cambio iónico. Parte VIII: Arsénico(III))/OH-/Dowex 1x8. Revista De Metalurgia, 54(4), e132. https://doi.org/10.3989/revmetalm.132

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