Evidence map›Paper›PMID 32992563›Full record

ArticleMembranes2020

Performance Evaluation of Tight Ultrafiltration Membrane Systems at Pilot Scale for Agave Fructans Fractionation and Purification.

Noe Luiz-Santos, Rogelio Prado-Ramírez, Enrique Arriola-Guevara, Rosa-María Camacho-Ruiz, Lorena Moreno-Vilet

Abstract read
In one paragraph

Article in Membranes, 2020. 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. Review
  2. Physical Properties and Prebiotic Activities (Molecules (Basel, Switzerland) · 2022
    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

5 authors.

Noe Luiz-SantosCentro de Investigación y Asistencia en Tecnología y Diseño del Estado de Jalisco A.C. Camino arenero 1227. El Bajío, C.P. 45019 Zapopan, Jalisco, Mexico.
Rogelio Prado-RamírezCentro de Investigación y Asistencia en Tecnología y Diseño del Estado de Jalisco A.C. Camino arenero 1227. El Bajío, C.P. 45019 Zapopan, Jalisco, Mexico.
Enrique Arriola-GuevaraDepartamento de Ingeniería Química, CUCEI-Universidad de Guadalajara, Blvd. M. García Barragán 1421, C.P. 44430 Guadalajara, Jalisco, Mexico.
Rosa-María Camacho-RuizCentro de Investigación y Asistencia en Tecnología y Diseño del Estado de Jalisco A.C. Camino arenero 1227. El Bajío, C.P. 45019 Zapopan, Jalisco, Mexico.ORCID 0000-0001-9264-5655
Lorena Moreno-ViletCONACYT- Centro de Investigación y Asistencia en Tecnología y Diseño del Estado de Jalisco A.C. Av. Normalistas 800, Colinas de la Normal, C.P. 44270 Guadalajara, Jalisco, Mexico.ORCID 0000-0003-0020-0208

Funding

Consejo Nacional de Ciencia y Tecnología 287926
6 · The paper itself

Abstract

Ceramic and polymeric membrane systems were compared at the pilot scale for separating agave fructans into different molecular weight fractions that help to diversify them into more specific industrial applications. The effect of the transmembrane pressure of ultrafiltration performance was evaluated through hydraulic permeability, permeate flux and rejection coefficients, using the same operating conditions such as temperature, feed concentration and the molecular weight cut-off (MWCO) of membranes. The fouling phenomenon and the global yield of the process were evaluated in concentration mode. A size distribution analysis of agave fructans is presented and grouped by molecular weight in different fractions. Great differences were found between both systems, since rejection coefficients of 68.6% and 100% for fructans with degrees of polymerization (DP) > 10, 36.3% and 99.3% for fructooligosaccharides (FOS) and 21.4% and 34.2% for mono-disaccharides were obtained for ceramic and polymeric membrane systems, respectively. Thus, ceramic membranes are better for use in the fractionation process since they reached a purity of 42.2% of FOS with a yield of 40.1% in the permeate and 78.23% for fructans with DP > 10 and a yield of 70% in the retentate. Polymeric membranes make for an efficient fructan purification process, eliminating only mono-disaccharides, and reaching a 97.7% purity (considering both fructan fractions) with a yield of 64.3% in the retentate.

Indexed as

agave fructansceramic membranefine ultrafiltrationpolymeric membranerejection coefficient

Identifiers

PMID32992563
PMCPMC7601410

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Registered trials

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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.