scispace - formally typeset
Open AccessJournal ArticleDOI

Numerical investigation on heat transfer performance and flow characteristics in a roughened vortex chamber

Reads0
Chats0
TLDR
In this paper, the effects on flow and heat transfer rates when the inside surface of the vortex chamber was roughened by adding flow turbulators to its wall were discussed.
About
This article is published in Applied Thermal Engineering.The article was published on 2019-05-05 and is currently open access. It has received 13 citations till now. The article focuses on the topics: Vortex & Nusselt number.

read more

Citations
More filters
Journal ArticleDOI

Numerical study on swirl cooling flow, heat transfer and stress characteristics based on fluid-structure coupling method under different swirl chamber heights and Reynolds numbers

TL;DR: In this paper, a three-dimensional swirl cooling model coupled with high temperature mainstream cascade channel and blade leading edge solid region is established to simulate the flow, heat transfer and stress characteristics.
Journal ArticleDOI

Influence of Bingham fluid viscosity on energy performances of a vortex chamber pump

TL;DR: In this paper, the authors evaluated the performance of vortex chamber pumps for coal-water and Bingham fluids with different rheological parameters and determined the dependence of the pump efficiency on the Bingham viscosity and the yield stress.
Journal ArticleDOI

Numerical investigation on the flow and heat transfer in swirl chambers with distributed multi exit slots and dimple/protrusion structure

TL;DR: In this paper, a novel swirl chamber with distributed multi-exit slots is proposed, for which different outlet configurations are considered, and flow and heat transfer characteristics are numerically investigated and compared with those of conventional chamber.
Journal ArticleDOI

A hybrid multiphase flow model for the prediction of both low and high void fraction nucleate boiling regimes

TL;DR: In this article, a turbulent rough wall function model is implemented in the hybrid multiphase flow solver for the numerical prediction of high and low void fraction flow boiling regimes in nuclear power plant.
Journal ArticleDOI

Numerical evaluation on the decaying swirling flow in a multi-lobed swirl generator

TL;DR: In this paper, decaying swirling flow character was predicted in the multi-lobed swirl generator (MLSG) for specific engineering applications, such as energy minimization and energy minimisation.
References
More filters
Journal ArticleDOI

Numerical Study of the Turbulent Flow Past an Airfoil with Trailing Edge Separation

TL;DR: In this paper, a methode numerique par volume fini pour the resolution des equations de Navier-Stokes bidimensionnelles, incompressible, and stationnaires, en coordonnees generales curvilignes, is presented.
Journal ArticleDOI

A hybrid RANS-LES approach with delayed-DES and wall-modelled LES capabilities

TL;DR: In this article, a CFD strategy is proposed that combines delayed detached-eddy simulation (DDES) with an improved RANS-LES hybrid model aimed at wall modelling in LES (WMLES).
Journal ArticleDOI

Development of DDES and IDDES Formulations for the k-ω Shear Stress Transport Model

TL;DR: In this paper, the authors proposed modifications of two recently developed hybrid CFD strategies, Delayed Detached Eddy Simulation (DDES) and DDES with Improved wall-modeling capability (IDDES), aimed at fine-tuning of these approaches to the k-ω SST background RANS model.
Journal ArticleDOI

Local entropy production in turbulent shear flows: a high-Reynolds number model with wall functions

TL;DR: In this article, entropy production in incompressible turbulent shear flows of Newtonian fluids is analyzed systematically and incorporated into a CFD code, based on asymptotic considerations wall functions for the four production terms are developed.
Related Papers (5)
Frequently Asked Questions (19)
Q1. What is the entropy generation in the proposed model?

The entropy generation in the proposed model is divided into two parts: fluid entropygeneration, Sgen,fluid, which is directly related to irreversibility owing to friction and turbulent dissipation, and thermal entropy generation, Sgen,heat, which is associated with heat transfer irreversibility. 

In this study, an investigation of a vortex chamber was carried out to gain a full understanding of the nature of the vortex flow and the cooling capability inside the chamber. The paper discusses the effects on flow and heat transfer rates when the inside surface of the vortex chamber was roughened by adding flow turbulators to its wall. The paper also presents the results of a comparative investigation of jet impingement and vortex cooling on a concave wall using different parameters, such as the total pressure loss coefficient, Nusselt number and thermal performance factor, to evaluate the cooling effectiveness and flow dynamics. Furthermore, the entropy generation in swirl flow with the roughened wall was assessed over a wide range of Reynolds numbers. Further increase in rib height has an adverse impact on thermal performance. 

In the jet impingement cooling technique, the relatively high-pressure drop may be attributed to the kinetic energy loss after leaving the nozzle and frictional losses near the wall. 

when the Reynolds number exceeds 50000, the ribs have a negative effect on the heat transfer compared to the smooth case 6- In a smooth chamber, the impact of heat transfer contributes significantly to the total entropygeneration over the range tested of Reynolds numbers. 

When the rib height reaches 2.00 mm, the ribs divert the flow further from the wall towards the core, resulting in a circulation region near the heated wall between the first three ribs and decreasing the size of the core vortex. 

Four square cross-section ribs of heights 0.25, 0.50, 1.00 and 2.00 mm were used, with a range of Reynolds number from 10000 to 100000.1- Numerical simulations were compared with experimental results for flow and heat transfer ina smooth vortex chamber. 

2- The study indicates that the flow inside the vortex chamber is steady for a smooth wall andrib heights smaller than 0.25 mm, but as either the rib height or the Reynolds number increases the flow become quasi-steady. 

In order to analyse the effects of the flow with maximum efficiency, the same configuration with the same boundary conditions should be used for all flow rates. 

The RNG kε model was adopted for all the following calculations, not only because of its ability to predict the heat transfer and velocity profiles more accurately, but also its low computational cost. 

As the flow advances to the following ribs, the peak from the reattachment decreases considerably until the last (fourth) rib, when the peak starts to fade away. 

the value of Nu/Nuo for a rib height of 2.00 mm shows a 26% decrease in heat transfer at high values of Reynolds number compared to the smooth chamber. 

5- The rib roughened wall produces superior thermal performance and heat transfer when theReynolds number is less the 50000 for rib height of 0.25 mm compared to the smooth case. 

At Reynolds number of 100000, the vortex chamber with rib heights of 2.00 mm and 1.00 mm has pressure loss coefficients higher by about twice and 1.6 times, respectively, than for the smooth vortex chamber. 

For the smooth chamber, the normalised Nusselt number is high at the beginning of the chamber owing to the high tangential flow velocity entering the chamber and the beginning of the concave wall, which reduces the thermal boundary layer in that region. 

At low Reynolds number, the region of maximum Nusselt number is near the inlet anddecreases towards the outlet for all ribs, except the rib of height 2.00 mm, where the heat transfer near the centre of the heated wall is greatest, primarily owing to the separation created by the first rib, which results in two large vortices being formed before and after the second rib. 

Increasing the Reynolds number to 20000 results in a heat transfer reduction for all cases, the maximum reduction being for the rib of height 2.00 mm, likely owing to the main flow being shifted away from the heated wall, as shown in Figure 8. 

The normalised Nusselt number shows that heat transfer for low Reynolds numbers is higher in the vortex chamber and, as the Reynolds number increases, jet impingement rises compared to the vortex chamber at Re > 50000. 

The highest Nu/Nuo peak occurs for a rib of height 0.50 mm and Reynolds number 10000;thereafter, for this height of rib, the initial peak progressively decreases with an increase in Reynolds number. 

as the Reynolds number increases, so the maximum normalised Nusselt number at the beginning of the chamber increases.