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Client Citation Analysis

Membrane performance evaluation and residual fouling characterization in a thermophilic submerged AnMBR treating pulp and paper primary sludge at varying solids retention times

This study evaluated thermophilic submerged AnMBR treatment of pulp-and-paper primary sludge and used Dropometer-based contact angle measurements to relate sludge surface-property changes to membrane fouling across varying solids retention times.

At-a-Glance Summary

Primary surface measurement reported

The paper measured contact angle of mixed liquor suspended solids (MLSS) and membranes, using pure water as the probe fluid under different solids retention time conditions.

Dropometer attribution in the paper

The authors state that “The contact angle of MLSS and membranes was measured by Dropometer M-3 (Droplet Smart Tech Inc. Canada).”

How the surface-tension / contact-angle data were used in the study

The contact-angle data were used alongside zeta potential, dewaterability, particle-size distribution, membrane resistance and permeability, SEM-EDX, FTIR, and XPS to interpret how sludge surface properties shifted with solids retention time and how those changes related to membrane fouling behavior.

Paper Details

Title
Membrane performance evaluation and residual fouling characterization in a thermophilic submerged AnMBR treating pulp and paper primary sludge at varying solids retention times
Authors
Alnour Bokhary; Mathew Leitch; Baoqiang Liao
Journal
Separation and Purification Technology
Year
2025
Volume
358
Pages / Article
130438

Journal context

What it is
Journal-level metrics for the publication venue (not a rating of this specific article).
How to read it
Compare metrics within category; updates are annual and lag current-year publications.

Scopus metrics (Elsevier / Scopus rating 2024)

CiteScore 2024

15.1

CiteScore subject ranks (CiteScore 2024)
  • Q1 - Chemistry, Analytical Chemistry (7/160)
  • Q1 - Chemical Engineering, Filtration and Separation (3/19)
SNIP 2024

1.383

SJR 2024

1.697

Journal Impact Factor (Clarivate JCR)

Journal Impact Factor (JCR 2024)

8.2

5-Year Impact Factor

8.1

What Was Measured

Primary surface / interfacial measurement

The paper measured contact angle of MLSS and membranes. Reported phase-wise contact-angle values are given for MLSS, with ranges of 49.3–62.4° at 32 d SRT, 28.2–42.3° at 45 d SRT, and 19.1–26.7° at 55 d SRT.

Supporting measurements

The contact-angle results were interpreted with zeta potential, dewaterability, particle size distributions of reactor mixed liquor and loose gel layer, soluble microbial products, and membrane resistance and permeability. Broader fouling characterization also included SEM-EDX, FTIR, and XPS analyses of virgin and used PVDF membranes.

Role of the Dropometer

The Dropometer was used to measure the contact angle of MLSS and membranes during thermophilic submerged AnMBR treatment of pulp-and-paper primary sludge. Pure water was used as the probe fluid, about 3 μL of water was dispensed with a micropipette onto the specimen surface, and an average contact angle value was calculated for each tested specimen.

In the study workflow, the contact-angle data served as a comparative surface-property readout that the authors used together with zeta potential, dewaterability, solids concentration, particle-size distribution, and residual fouling characterization to interpret SRT-dependent changes in membrane fouling behavior.

Method Snapshot

Method Snapshot Table

Phase / condition SRT HRT Temperature System / substrate Dropometer-related specimens Dropometer conditions eported contact-angle output Related fouling context Instruments / notes
Phase I 32 d 5 d 50±1°C Thermophilic submerged AnMBR treating primary sludge from a thermomechanical pulping mill MLSS and membranes Dropometer M-3; pure water probe fluid; about 3 μL droplet; average contact angle calculated for each tested specimen MLSS contact angle: 49.3–62.4° Zeta potential: -20.098±1.71 mV; dewaterability: 29.48±1.98 s; MLSS: 16.55–23.02 g/L 6.5 L reactor; PVDF flat-plate MF membrane; 0.03 m² area; 0.1 μm pore size; biogas sparging 3.76±0.08 L/min
Phase II 45 d 5 d 50±1°C Same system MLSS and membranes Same Dropometer workflow MLSS contact angle: 28.2–42.3° Zeta potential: -27.65±1.56 mV; dewaterability: 33.48±0.38 s; MLSS: 20.38–26.18 g/L Same operating platform
Phase III 55 d 5 d 50±1°C Same system MLSS and membranes Same Dropometer workflow MLSS contact angle: 19.1–26.7° Zeta potential: -29.00±2.18 mV; dewaterability: 48.57±2.39 s; MLSS: 26.36–28.96 g/L Same operating platform
Common analytical set used with the contact-angle results 32-55 d 5 d 50±1°C Same system MLSS, membranes, gel layer Contact angle interpreted with zeta potential, CST, PSD, SEM-EDX, FTIR, XPS, SMP, membrane resistance, and permeability Comparative hydrophobicity across SRT conditions Gel layer identified as predominant fouling mechanism; total hydraulic resistance increased with increasing SRT Surface-property analysis located in Chapter V, Sections 3.5-3.6

Key Findings

Lower hydrophobicity at longer SRT

The MLSS contact-angle range decreased from 49.3–62.4° at 32 d SRT to 28.2–42.3° at 45 d and 19.1–26.7° at 55 d. The authors interpreted sludge at higher SRT as less hydrophobic than sludge at lower SRT.

MLSS buildup aligned with fouling severity

MLSS concentration increased across the SRT phases from 16.55–23.02 g/L to 26.36–28.96 g/L. The paper identifies MLSS concentration as the predominant factor affecting membrane performance, with higher solids levels accompanying higher hydraulic resistance and more foulant deposition.

Gel layer dominated the resistance profile

Resistance analysis showed gel-layer resistance accounted for about 98.6–98.8% of total resistance during primary-sludge treatment. The authors therefore identified loose gel-layer formation as the predominant membrane-fouling mechanism in this operating window.

Smaller particles showed stronger deposition tendency

The paper reports that most MLSS and loose-gel-layer particles were larger than membrane pores, while smaller particles showed the greater tendency to deposit on the membrane surface. This supported the broader fouling interpretation used alongside the surface-property data.

Residual foulants remained after cleaning

EDX, FTIR, and XPS all indicated that used membranes still carried foulant signatures after cleaning. The authors linked these residuals to both organic and inorganic materials and to increased solids accumulation at longer SRT.

Figures & Visuals

Figure 5.3 — Links surface-property shifts to operating response

What it shows

This figure shows permeate flux and transmembrane pressure over time across the 32, 45, and 55 d SRT phases.

Figure 5.4 — Quantifies the fouling mechanism

What it shows

This figure breaks membrane resistance into components and shows the dominance of gel-layer resistance during treatment.

Figure 5.5 — Shows membrane morphology changes across SRT

What it shows

SEM images compare virgin and used PVDF membranes after operation at the three tested solids retention times.

Figure 5.8 — Adds particle-size context to the contact-angle results

What it shows

This figure shows the particle-size distributions of reactor mixed liquor and membrane loose gel layer used to interpret fouling behavior alongside the contact-angle data.

Why It Matters

This paper sits in a membrane-performance context where stable sludge treatment and stable methane-generating operation depend on how solids behave at the membrane surface. In that workflow, the Dropometer-derived contact-angle measurements gave the authors a direct way to compare surface-property changes in the mixed liquor as SRT increased.

By combining contact angle with zeta potential, dewaterability, particle-size distributions, and post-run foulant characterization, the study used surface-property data as part of a broader fouling diagnosis rather than as a standalone metric. That made the contact-angle results practically useful for understanding why longer SRT operation coincided with higher MLSS concentration, stronger fouling signatures, and gel-layer-dominated resistance.

Practical Takeaways

Comparative hydrophobicity tracking

The authors used Dropometer contact-angle measurements to compare how MLSS surface behavior changed across 32, 45, and 55 d SRT operation, giving a direct surface-property readout within the fouling study.

Use contact angle with companion metrics

In this paper, contact angle was interpreted together with zeta potential, dewaterability, PSD, SMP, and membrane-resistance data, which is how the authors turned a wetting measurement into a fouling interpretation.

Longer SRT shifted the surface-property profile

Lower contact-angle ranges at longer SRT coincided with higher MLSS concentrations and more severe fouling indicators, making the Dropometer data useful for phase-to-phase comparison rather than a single-point measurement.

Surface data supported mechanism identification

The Dropometer results supported the paper’s broader conclusion that gel-layer formation, rather than pore blocking, was the dominant fouling pathway under the tested conditions.

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