Evidence map›Paper›PMID 39062966›Full record

ArticleInternational journal of molecular sciences2024

Pervaporation Dehydration Mechanism and Performance of High-Aluminum ZSM-5 Zeolite Membranes for Organic Solvents.

Qing Wang, Cheng Qian, Changxu Guo, Nong Xu, Qiao Liu, Bin Wang, Long Fan, Kunhong Hu

Abstract read
In one paragraph

Article in International journal of molecular sciences, 2024. The graph could read no effect estimate from its abstract, so it casts no vote on the map. Cited by 2 papers.

0numbers the graph read from it
0cells of the map it votes in
2citing papers in PubMed
–field-weighted citation impact
1 · What the graph read from it

What it found

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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

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3 · Its place in the literature

Who cites it

2 citing papers in PubMed.

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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

8 authors.

Qing WangSchool of Energy, Materials and Chemical Engineering, Hefei University, Hefei 230601, China.ORCID 0000-0002-4551-6866
Cheng QianSchool of Energy, Materials and Chemical Engineering, Hefei University, Hefei 230601, China.ORCID 0009-0000-9468-6864
Changxu GuoSchool of Energy, Materials and Chemical Engineering, Hefei University, Hefei 230601, China.
Nong XuSchool of Energy, Materials and Chemical Engineering, Hefei University, Hefei 230601, China.
Qiao LiuSchool of Energy, Materials and Chemical Engineering, Hefei University, Hefei 230601, China.
Bin WangState Key Laboratory of Materials-Oriented Chemical Engineering, College of Chemical Engineering, Nanjing Tech University, Nanjing 210009, China.ORCID 0000-0002-6601-2544
Long FanSchool of Energy, Materials and Chemical Engineering, Hefei University, Hefei 230601, China.
Kunhong HuSchool of Energy, Materials and Chemical Engineering, Hefei University, Hefei 230601, China.

Funding

Anhui Province Excellent Research and Innovation Team Project for Universities 2022AH010096Anhui Province Excellent Research and Innovation Team Project for Universities 2023AH010050Anhui Provincial Natural Science Foundation 2308085QB65Key Research and Development Project of Anhui Province 2022a05020041National Natural Science Foundation of China 22208146National Natural Science Foundation of China 22308076National State Key Laboratory of Materials-Oriented Chemical Engineering KL21-04University Natural Sciences Research Project of Anhui Province 2023AH040305
6 · The paper itself

Abstract

Membrane-based pervaporation (PV) for organic solvent dehydration is of great significance in the chemical and petrochemical industries. In this work, high-aluminum ZSM-5 zeolite membranes were synthesized by a fluoride-assisted secondary growth on α-alumina tubular supports using mordenite framework inverted (MFI) nanoseeds (~110 nm) and a template-free synthesis solution with a low Si/Al ratio of 10. Characterization by XRD, EDX, and SEM revealed that the prepared membrane was a pure-phase ZSM-5 zeolite membrane with a Si/Al ratio of 3.8 and a thickness of 2.8 µm. Subsequently, two categories of PV performance parameters (i.e., flux versus separation factor and permeance versus selectivity) were used to systematically examine the effects of operating conditions on the PV dehydration performance of different organic solvents (methanol, ethanol, n-propanol, and isopropanol), and their PV mechanisms were explored. Employing permeance and selectivity effectively disentangles the influence of operating conditions on PV performance, thereby elucidating the inherent contribution of membranes to separation performance. The results show that the mass transfer during PV dehydration of organic solvents was mainly dominated by the adsorption-diffusion mechanism. Furthermore, the diffusion of highly polar water and methanol molecules within membrane pores had a strong mutual slowing-down effect, resulting in significantly lower permeance than other binary systems. However, the mass transfer process for water/low-polar organic solvent (ethanol, n-propanol, and isopropanol) mixtures was mainly controlled by competitive adsorption caused by affinity differences. In addition, the high-aluminum ZSM-5 zeolite membrane exhibited superior PV dehydration performance for water/isopropanol mixtures.

Indexed as

Membranes, ArtificialSolventsZeolites2-PropanolAluminumEthanolWater2-PropanolAluminumEthanolMembranes, ArtificialSolventsWaterZeolitesZSM-5 zeoliteadsorption–diffusion mechanismorganic solvent dehydrationpervaporationsecondary growthZSM-5 zeolite membrane

Identifiers

PMID39062966
PMCPMC11277172

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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.