Evidence map›Paper›PMID 36005657›Full record

ArticleMembranes2022

Membrane Water Treatment for Drinking Water Production from an Industrial Effluent Used in the Manufacturing of Food Additives.

Karina Hernández, Claudia Muro, Oscar Monroy, Vianney Diaz-Blancas, Yolanda Alvarado, María Del Carmen Diaz

Abstract read
In one paragraph

Article in Membranes, 2022. The graph could read no effect estimate from its abstract, so it casts no vote on the map. Cited by 3 papers.

0numbers the graph read from it
0cells of the map it votes in
3citing papers in PubMed
–field-weighted citation impact
1 · What the graph read from it

What it found

Each row is one number read from the abstract, on the scale the paper reported it, with its interval. Left of the dashed line favours the treatment, right favours the comparator. Under each row is the sentence it came from. New to these charts? A ten-minute tutorial.

The abstract states no effect estimate the extractor could read, or names no intervention and outcome on the map, so this paper lights no cell and moves no belief. It is still indexed, cited and linked below.

2 · The registry

The trial behind it

Trials whose registry record cites this paper, or whose number appears in the abstract. A trial that started after this paper was published is citing it as background, not reporting it.

Neither the registry nor the abstract names a trial number. If this is a trial report, that itself is worth knowing.

3 · Its place in the literature

Who cites it

3 citing papers in PubMed.

  1. Article
  2. Article
  3. Article
4 · The record

Corrections and comments

PubMed lists nothing against this paper. Absence here is not a guarantee, only a check that was made.

5 · Who and what money

Authors and funding

6 authors.

Karina HernándezTecnológico Nacional de México/Instituto Tecnológico de Toluca, Avenida Tecnológico S/N Colonia Agrícola Bellavista, Metepec, Ciudad de México 52140, Mexico.
Claudia MuroTecnológico Nacional de México/Instituto Tecnológico de Toluca, Avenida Tecnológico S/N Colonia Agrícola Bellavista, Metepec, Ciudad de México 52140, Mexico.ORCID 0000-0002-4394-5851
Oscar MonroyDepartamento de Biotecnología, Universidad Autónoma Metropolitana, Avenida San Rafael Atlixco 186, Colonia Vicentina, Iztapalapa, Ciudad de México 09340, Mexico.
Vianney Diaz-BlancasTecnológico Nacional de México/Instituto Tecnológico de Toluca, Avenida Tecnológico S/N Colonia Agrícola Bellavista, Metepec, Ciudad de México 52140, Mexico.
Yolanda AlvaradoTecnológico Nacional de México/Instituto Tecnológico de Toluca, Avenida Tecnológico S/N Colonia Agrícola Bellavista, Metepec, Ciudad de México 52140, Mexico.
María Del Carmen DiazTecnológico Nacional de México/Instituto Tecnológico de Toluca, Avenida Tecnológico S/N Colonia Agrícola Bellavista, Metepec, Ciudad de México 52140, Mexico.ORCID 0000-0001-9786-8014

Funding

Consejo Mexiquense de Ciencia y Tecnología FICDTEM-2021-028Consejo Nacional de Ciencia y Tecnología 788926
6 · The paper itself

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/m

Indexed as

dye removalfood effluentsmembrane treatmentpotable watersaline effluentswater recovery

Identifiers

PMID36005657
PMCPMC9412253

What OpenQuestion holds

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LicenceCC BY
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Registered trials

None linked

Read under generation 80e0d062 · epoch 390. Bibliography from PubMed, PubMed Central and OpenAlex; grants from NIH RePORTER; trial links from ClinicalTrials.gov; estimates, votes and beliefs from the OpenQuestion graph.