Summary
Verdict: Suspected serious data fabrication (red). An independent review of the published paper identified multiple internal inconsistencies that violate basic thermodynamics and the authors' own governing equations. The bulk-liquid temperature reportedly collapsed from an initial 323.13 K to 221-222 K in Section 5.1, well below the freezing point of methanol (179 K) and inconsistent with prior sections. Table 3 lists an experimental evaporation rate (3.61E-5 kg/s) that exceeds the explicitly stated thermodynamic maximum (3.58E-5 kg/s) at 53.5 °C. Table 6 percent changes in Section 4.4 do not match the underlying numbers. Table 5 shows a 50% rise in gas flow yielding an 86% rise in evaporation rate, contradicting the linear proportionality given in the authors' Eq (35). These cross-source contradictions strongly suggest fabricated or arbitrarily entered numerical data. Image-level reuse could not be assessed from text alone. AI-assisted review; final determination requires institutional investigation.
Verdict
🔴 Suspected serious data fabrication. Multiple physical and arithmetic contradictions across tables, text, and the authors' own equation indicate probable fabrication or severe negligence in numerical reporting.
Key findings
- Bulk liquid temperature drops from an initial 323.13 K to 221-222 K (Section 5.1), violating the freezing-point constraint of methanol (179 K) and contradicting prior sections, where temperatures only fall to ~321 K.
- Table 3 reports an experimental evaporation rate of 3.61×10⁻⁵ kg/s at 53.5 °C, exceeding the stated thermodynamic maximum of 3.58×10⁻⁵ kg/s for the same condition.
- Section 4.4 percentage changes (3%, 10%, 13%, 62%) do not match Table 6 values; recomputed values are 9.0%, 16.6%, 20.1%, 72.2% versus the 2.34 kg/s control.
- Table 5 shows a 50% gas-flow increase (1 → 1.5 L/min) raising evaporation rate from 2.68×10⁻⁵ to 4.99×10⁻⁵ kg/s (+86%), inconsistent with the linear proportionality in the authors' Eq (35) ($dm_{max}/dt = \rho Q Y/(1-p^*/p)$) and with the cooling-induced reduction of Y described in §4.3.1.
- Image-level reuse/duplication cannot be assessed (text-only review).
Evidence highlights
- DOI: 10.1016/j.ijheatmasstransfer.2021.122296
- Section 5.1 bulk-liquid temperatures: 221 K (3 g/s), 222 K (6 g/s), 321.4 K (15 g/s), against initial 323.13 K (Table 2).
- Table 3 (53.5 °C): Experimental 3.61×10⁻⁵ kg/s vs Predicted Thermodynamic Maximum 3.58×10⁻⁵ kg/s.
- Section 4.4 text vs Table 6: stated +3/+10/+13/+62% computed +9.0/+16.6/+20.1/+72.2%.
- Table 5: 1 L/min → 2.68×10⁻⁵ kg/s; 1.5 L/min → 4.99×10⁻⁵ kg/s (+86%) vs linear-proportionality prediction of +50%.
- Equation (35): $dm_{max}/dt = \frac{\rho Q Y}{1 - p^*/p}$ implies linear scaling in Q at fixed Y.
Notes
- Analysis is AI-assisted and text-only; final adjudication requires institutional review and raw-data audit.
- Recommended follow-ups: request original CFD input/output files and experimental logs from the authors; post technical concerns on PubPeer; notify the journal editorial office of the internal mathematical contradictions.
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