Evidence map›Paper›PMID 38343923›Full record

ArticleACS omega2024

Nanofiltration PVP Membrane with Gradient Cross-Linking for Efficient Polycyclic Aromatic Hydrocarbons Removal.

Abdulnoor Ali Jazem Ghanim, Sharjeel Waqas, Muhammad Hamad Zeeshan, Javed Akbar Khan, Syed Ali Ghalib, Muhammad Irfan, Saifur Rahman, Salim Nasar Faraj Mursal, Mohammed Jalalah, Abdulkarem H M Almawgani

Abstract read
In one paragraph

Article in ACS omega, 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

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

2 citing papers in PubMed.

  1. Article
  2. Efficient COACS omega · 2025
    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

10 authors.

Abdulnoor Ali Jazem GhanimCivil Engineering Department, College of Engineering, Najran University, Najran 61441, Saudi Arabia.
Sharjeel WaqasSchool of Chemical Engineering, The University of Faisalabad, Faisalabad 37610, Pakistan.ORCID https://orcid.org/0000-0003-1426-7016
Muhammad Hamad ZeeshanChemical Engineering Department, Universiti Teknologi PETRONAS, Bandar Seri Iskandar, 32610 Perak, Malaysia.
Javed Akbar KhanMechanical and Electrical Engineering Department, University of China Petroleum (East China), Dongying 257061, Shandong, China.
Syed Ali GhalibInstitute of Chemical Engineering and Technology, University of the Punjab, Quaid-e-Azam Campus, Lahore 54590, Pakistan.ORCID https://orcid.org/0009-0004-2273-5873
Muhammad IrfanElectrical Engineering Department, College of Engineering, Najran University, Najran 61441, Saudi Arabia.ORCID https://orcid.org/0000-0003-4161-6875
Saifur RahmanElectrical Engineering Department, College of Engineering, Najran University, Najran 61441, Saudi Arabia.
Salim Nasar Faraj MursalElectrical Engineering Department, College of Engineering, Najran University, Najran 61441, Saudi Arabia.
Mohammed JalalahElectrical Engineering Department, College of Engineering, Najran University, Najran 61441, Saudi Arabia.
Abdulkarem H M AlmawganiElectrical Engineering Department, College of Engineering, Najran University, Najran 61441, Saudi Arabia.

Funding

No grant is acknowledged in the PubMed record.

6 · The paper itself

Abstract

Polycyclic aromatic hydrocarbons (PAHs) are persistent organic pollutants that may contaminate various water sources and pose serious dangers to human health and the environment. Due to their capacity for size-based separation, nanofiltration membranes have become efficient instruments for PAH removal. However, issues such as membrane fouling and ineffective rejection still exist. To improve PAH rejection while reducing fouling problems, this work created a new gradient cross-linking poly(vinylpyrrolidone) (PVP) nanofiltration membrane. The gradient cross-linking technique enhanced the rejection performance and antifouling characteristics of the membrane. The results demonstrated that the highest membrane flow was achieved at a 0.15% SDS-PVP membrane. There is a trade-off between membrane flux and salt rejection since salt rejection increases with SDS owing to the growth of big pores. The membrane flux was reduced for the 0.25% SDS-PVP membrane owing to poor SDS dispersion. The prepared membrane showed enhanced removal efficiencies for the removal of the PAH compounds. The PVP membrane has the potential to be used in several water treatment applications, improving water quality, and preserving the environment.

Identifiers

PMID38343923
PMCPMC10851246

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LicenceCC BY-NC-ND
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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.