Abstract:This paper discusses the turbulent flow and heat transfer from a uniform air flow with high temperature to the outside through a 90° curved square pipe. Both conjugate heat transfer (CHT) simulation and experiments of temperature field measurements at cross sections of the pipe are performed. A straight pipe is investigated and compared with the 90° curved pipe. The temperature of the air flow at the inlet of the pipe is set at 402 K, and the corresponding Reynolds number is approximately 6 × 104. To obtain th… Show more
“…The large amount of heat dissipated to the pipe wall at the first bend is transferred upstream and downstream through the inside of the pipe by thermal conduction. The tendency for heat transfer enhancement to occur at the first bend is consistent with previous results by Guo [23] and Liberto et al [29].…”
supporting
confidence: 92%
“…Figure 9b shows that for the double-bend pipe, the high-temperature core, which is at the center of the first bend entrance (z = 40 D), shifts to the outside (−x side) at the first bend exit (z = 42.4 D). This shift may be due to compressive heating of the fluid on the outside of the bend by centrifugal forces, as suggested by Guo et al for their single-bend pipe [23]. The distribution after the entrance to the second bend (z = 47.4 D ~53.7 D) shows that the hot core, which was biased toward the −x side, gradually shifts toward the +x side.…”
Section: Resultsmentioning
confidence: 67%
“…From the middle of the second bend, the local Nu number decreases significantly, indicating that the heat transfer enhancement is not significant. Figure 19 also shows the experimental results of Guo et al [23], who evaluated the heat transfer characteristics of a single-bend pipe under the same flow conditions. In the experiment of Guo et al, the local Nusselt number also increased in the middle of the first bend, a trend that is consistent with the simulation in the present study.…”
Section: Evaluation Of Heat Transfer Characteristicsmentioning
confidence: 98%
“…They found that the heat transfer was mostly greater on the outside of the bend than on the inside of the bend, and that the difference decreased with an increasing Reynolds number. Guo et al [23] measured the cross-sectional temperature profile of a pipe with a 90 • bend, finding that the heat flux was higher on the outside of the bend as the hot core of the fluid was biased outward by the bend. Other studies on bend geometries have mainly investigated coil-type and U-shaped pipes.…”
Section: Introductionmentioning
confidence: 99%
“…As described above, various studies have investigated the heat transfer characteristics of bent pipes, but few studies [23] have experimentally evaluated heat transfer characteristics by measuring the in-plane temperature distribution. The heat transfer characteristics of pipes with single bends and U-shaped bends and coil-type piping have been actively studied for applications such as heat exchangers, but there has been a lack of research on the heat transfer characteristics of turbulent flow in S-shaped double bends.…”
This study evaluates the heat dissipation and Nusselt number for an S-shaped double-bend pipe, for which an experimental evaluation is lacking. In terms of the velocity field, the mean velocity and turbulent kinetic energy were measured through particle image velocimetry. Heat transfer characteristics were evaluated in validated conjugate heat transfer simulations, and a k-ω SST turbulence model was used for flow simulation inside the pipe. Heat transfer enhancement was observed at the first bend, as observed in previous studies on single-bend and U-shaped bends, whereas no heat transfer enhancement was observed at the second bend. This result was due to higher turbulent heat flux at the first bend because of higher eddy diffusion on the outside of the bend, whereas eddy diffusion was lower on the outside of the second bend owing to the history of the first bend. The heat transfer characteristics of the S-shaped double-bend pipe elucidated in this study provide valuable insight for devising strategies to reduce heat loss in automotive exhaust pipes with multiple bends. Furthermore, the conjugate heat transfer simulation model used in this study provides a benchmark for heat transfer calculations for multi-bend pipes.
“…The large amount of heat dissipated to the pipe wall at the first bend is transferred upstream and downstream through the inside of the pipe by thermal conduction. The tendency for heat transfer enhancement to occur at the first bend is consistent with previous results by Guo [23] and Liberto et al [29].…”
supporting
confidence: 92%
“…Figure 9b shows that for the double-bend pipe, the high-temperature core, which is at the center of the first bend entrance (z = 40 D), shifts to the outside (−x side) at the first bend exit (z = 42.4 D). This shift may be due to compressive heating of the fluid on the outside of the bend by centrifugal forces, as suggested by Guo et al for their single-bend pipe [23]. The distribution after the entrance to the second bend (z = 47.4 D ~53.7 D) shows that the hot core, which was biased toward the −x side, gradually shifts toward the +x side.…”
Section: Resultsmentioning
confidence: 67%
“…From the middle of the second bend, the local Nu number decreases significantly, indicating that the heat transfer enhancement is not significant. Figure 19 also shows the experimental results of Guo et al [23], who evaluated the heat transfer characteristics of a single-bend pipe under the same flow conditions. In the experiment of Guo et al, the local Nusselt number also increased in the middle of the first bend, a trend that is consistent with the simulation in the present study.…”
Section: Evaluation Of Heat Transfer Characteristicsmentioning
confidence: 98%
“…They found that the heat transfer was mostly greater on the outside of the bend than on the inside of the bend, and that the difference decreased with an increasing Reynolds number. Guo et al [23] measured the cross-sectional temperature profile of a pipe with a 90 • bend, finding that the heat flux was higher on the outside of the bend as the hot core of the fluid was biased outward by the bend. Other studies on bend geometries have mainly investigated coil-type and U-shaped pipes.…”
Section: Introductionmentioning
confidence: 99%
“…As described above, various studies have investigated the heat transfer characteristics of bent pipes, but few studies [23] have experimentally evaluated heat transfer characteristics by measuring the in-plane temperature distribution. The heat transfer characteristics of pipes with single bends and U-shaped bends and coil-type piping have been actively studied for applications such as heat exchangers, but there has been a lack of research on the heat transfer characteristics of turbulent flow in S-shaped double bends.…”
This study evaluates the heat dissipation and Nusselt number for an S-shaped double-bend pipe, for which an experimental evaluation is lacking. In terms of the velocity field, the mean velocity and turbulent kinetic energy were measured through particle image velocimetry. Heat transfer characteristics were evaluated in validated conjugate heat transfer simulations, and a k-ω SST turbulence model was used for flow simulation inside the pipe. Heat transfer enhancement was observed at the first bend, as observed in previous studies on single-bend and U-shaped bends, whereas no heat transfer enhancement was observed at the second bend. This result was due to higher turbulent heat flux at the first bend because of higher eddy diffusion on the outside of the bend, whereas eddy diffusion was lower on the outside of the second bend owing to the history of the first bend. The heat transfer characteristics of the S-shaped double-bend pipe elucidated in this study provide valuable insight for devising strategies to reduce heat loss in automotive exhaust pipes with multiple bends. Furthermore, the conjugate heat transfer simulation model used in this study provides a benchmark for heat transfer calculations for multi-bend pipes.
In order to have a precise knowledge on how pressure gradients and buoyancy force affect fluid flow and energy distribution in a bending channel, it is important to perform a comprehensive study on flow characteristics and heat transfer mechanisms that trigger out the transition of fluids into a turbulent state, subject to a sustained pressure gradient. The present paper explores a computational modeling on two-dimensional fluid flow and thermal characteristics in a bent square channel of strong curvature. The Newton–Raphson (N-R) iteration method is applied to obtain a bifurcation structure depending on the pressure-driven force, the Dean number (De), covering 0 < De ≤ 5000. As a consequence, four branches of asymmetric steady solutions are identified for each of the cases of the Grashof number, Gn (=1000, 1500, and 2000), where only the first branch is found to exhibit asymmetric two-vortex solutions while the remaining branches encompass two- to four-vortex solutions. The similarity and disparity in the branching structure are also demonstrated. Then, adopting the Adam–Bashforth (A-B) method together with Crank–Nicholson (C-N) formula, the unsteady solutions (US) have been explored, validated by power spectrum density (PSD) and phase space Within the realm of US, two- and three-vortex solutions are found and these solutions exhibit transitions from steady to chaotic behavior profoundly. Effects of the Grashof number with convective heat transfer (CHT) are also compared. By analyzing the Nusselt number (Nu), it is observed that in case of highly chaotic flow, CHT experiences substantial enhancement. This intensified CHT arises from increased turbulence and mixing, facilitating more efficient thermal energy exchange under such chaotic flow conditions.
The turbulent pulsating flow and heat transfer in straight and 90° curved square pipes are investigated in this study. Both experimental temperature field measurements at the cross-sections of the pipes and conjugate heat transfer (CHT) simulation were performed. The steady turbulent flow was investigated and compared to the pulsating flow under the same time-averaged Reynolds number. The time-averaged Reynolds number of the pulsating flow, as well as the steady flow, was approximately 60,000. The Womersley number of the pulsating flow was 43.1, corresponding to a 30 Hz pulsating frequency. Meanwhile, the Dean number in the curved pipe was approximately 31,000. The results showed that the local heat flux of the pulsating flow was greater than that of the steady flow when the location was closer to the upstream pulsation generator. However, the total heat flux of the pulsating flow was less than that of the steady flow. Moreover, the instantaneous velocity and temperature fields of the simulation were used to demonstrate the heat transfer mechanism of the pulsating flow. The behaviors, such as the obvious separation between the air and pipe wall, the low-temperature core impingement, and the reverse flow, suppress the heat transfer.
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