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Membrane Water Treatment for Drinking Water Production from an Industrial Effluent Used in the Manufacturing of Food Additives.
Hernández, Karina; Muro, Claudia; Monroy, Oscar; Diaz-Blancas, Vianney; Alvarado, Yolanda; Diaz, María Del Carmen.
Afiliación
  • Hernández K; Tecnológico Nacional de México/Instituto Tecnológico de Toluca, Avenida Tecnológico S/N Colonia Agrícola Bellavista, Metepec, Ciudad de México 52140, Mexico.
  • Muro C; Tecnológico Nacional de México/Instituto Tecnológico de Toluca, Avenida Tecnológico S/N Colonia Agrícola Bellavista, Metepec, Ciudad de México 52140, Mexico.
  • Monroy O; Departamento de Biotecnología, Universidad Autónoma Metropolitana, Avenida San Rafael Atlixco 186, Colonia Vicentina, Iztapalapa, Ciudad de México 09340, Mexico.
  • Diaz-Blancas V; Tecnológico Nacional de México/Instituto Tecnológico de Toluca, Avenida Tecnológico S/N Colonia Agrícola Bellavista, Metepec, Ciudad de México 52140, Mexico.
  • Alvarado Y; Tecnológico Nacional de México/Instituto Tecnológico de Toluca, Avenida Tecnológico S/N Colonia Agrícola Bellavista, Metepec, Ciudad de México 52140, Mexico.
  • Diaz MDC; Tecnológico Nacional de México/Instituto Tecnológico de Toluca, Avenida Tecnológico S/N Colonia Agrícola Bellavista, Metepec, Ciudad de México 52140, Mexico.
Membranes (Basel) ; 12(8)2022 Jul 29.
Article en En | MEDLINE | ID: mdl-36005657
ABSTRACT
An integrated membrane process for treatment of effluents from food additive manufacturing was designed and evaluated on a laboratory scale. The principal focus was water recovery with the possibility of its reuse as potable water. The industrial effluent presented high content of dyes and salts. It was red in color and presented brine characteristics. The whole effluent was fed into the integrated process in continuous flow. The steps of the process are as follows sedimentation (S), adsorption by activated carbon (AC), ion exchange using resins (IEXR), and reverse osmosis (RO) (S-AC-IEXR-RO). The effect of previous operations was evaluated by stress-rupture curves in packaged columns of AC and IEXR, membrane flux, and fouling dominance in RO. Fouling was evaluated by way of the Silt Density Index and membrane resistance examination during effluent treatment. The integrated membrane process provided reclaimed water with sufficiently high standards of quality for reuse as potable water. AC showed a high efficiency for color elimination, reaching its rupture point at 20 h and after 5L of effluent treatment. IEXR showed capacity for salt removal, providing 2.2-2.5 L of effluent treatment, reaching its rupture point at 11-15 h. As a result of these previous operations and operating conditions, the fouling of the RO membrane was alleviated, displaying high flux of water 20-18 L/h/m2 and maintaining reversible fouling dominance at a feed flow rate of 0.5-0.7 L/h. The characteristics of the reclaimed water showed drinking water standards.
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Texto completo: 1 Colección: 01-internacional Base de datos: MEDLINE Tipo de estudio: Guideline Idioma: En Revista: Membranes (Basel) Año: 2022 Tipo del documento: Article País de afiliación: México

Texto completo: 1 Colección: 01-internacional Base de datos: MEDLINE Tipo de estudio: Guideline Idioma: En Revista: Membranes (Basel) Año: 2022 Tipo del documento: Article País de afiliación: México