Experimental study of heat transfer in an in-line tube bundle under reciprocating pulsating cross-flow: effects of Prandtl number and waveform asymmetry

Published: 29 May 2026| Version 1 | DOI: 10.17632/sy625fznsn.1
Contributors:
Aidar Hayrullin,
,
,
,

Description

This dataset contains operating parameters, similarity criteria, and measurement uncertainties for 180 pulsating-flow experimental regimes conducted on an 8×8 in-line tube bundle (D = 10 mm, S_L/D = S_T/D = 1.3) with water as the working fluid. Experiments cover the parameter ranges Re = 1200-3400, Pr = 3.5-5.0, A/D = 5-15, f = 0.18-0.45 Hz, and duty cycle psi = 0.2-0.5. The dataset includes the Nusselt number under pulsating flow (Nu_p), the heat transfer enhancement ratio (Nu_p/Nu_st), derived similarity parameters (Strouhal number, Fourier number, combined parameter (A/D)St), and expanded measurement uncertainties at the 95% confidence level evaluated in accordance with the GUM framework. Full description of the experimental methodology and data reduction procedure is provided in the associated manuscript.

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Steps to reproduce

Experiments were conducted on a purpose-built physical model of a tubular heat exchanger with an 8x8 in-line tube bundle (D = 10 mm, S_L/D = S_T/D = 1.3) and a rectangular channel cross-section of 107x107 mm, using water as the working fluid. Flow pulsations were generated by a double-acting hydraulic cylinder controlled by a PLC-based pneumatic system. The Reynolds number, Prandtl number, pulsation frequency, amplitude, and duty cycle were maintained at target values by a closed-loop control algorithm. Heat transfer coefficients were determined from overall heat transfer coefficients measured using pre-calibrated Pt1000 RTDs. Full details of the experimental setup, instrumentation, and data reduction procedure are provided in the associated manuscript.

Institutions

Categories

Heat Transfer, Thermal Engineering, Heat Exchanger, Heat Transfer Analysis

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