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UWE Bristol Engineering showcase 2015

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Lawrence Dubey<br />

MEng Mechanical <strong>Engineering</strong><br />

Project Supervisor<br />

Rachel Szadziewska<br />

Increasing Heat Transfer by Pipe Roughening<br />

Experimental Study<br />

The primary aim of the proposed project was to<br />

investigate whether roughened tube had a<br />

significant impact on heat transfer, and whether it<br />

significantly affected the pressure drop and thus<br />

the pump power demand. Therefore the<br />

temperate and pressure values needed to<br />

measured over a length of smooth pipe and a<br />

length of roughened pipe.<br />

The experimental rig was set up as shown in the<br />

schematic diagram below. It consists of four main<br />

parts: water heating, temperature measurement,<br />

pressure measurement and flow rate<br />

measurement. The test pipes were made of<br />

copper, to represent common domestic water<br />

pipes. Both pipes were of the same dimensions,<br />

1m long and ID of 20mm, except that one of the<br />

pipes had been internally roughened by manual<br />

abrasion.<br />

Theoretical Analysis<br />

It was evident from the results, that the<br />

experiment produced unexpected and<br />

contradictory results. The rough pipe both felt and<br />

looked rougher. However the empirically<br />

calculated equivalent sand grain roughness‘<br />

conflicted with the reality of the pipes internal<br />

surface. This meant the heat transfer model could<br />

calculated, instead the focus changed to fluid flow.<br />

An analysis was conducted in Excel to determine<br />

the reason for this discrepancy. It was discovered<br />

that the pipe roughness ε was very small<br />

compared to the pipe diameter and the viscous<br />

sub layer completely submerged the effect of ε.<br />

This meant that the pipes acted as hydraulically<br />

smooth, so therefore smooth regime laws were<br />

applied. This showed again that the smooth pipe,<br />

had a higher friction factor as it had a slightly<br />

higher flow rate, due to error at the water valve.<br />

Filonenko<br />

correlation<br />

Blasius<br />

correlation<br />

Darcy-<br />

Weisbach<br />

equation<br />

Friction Factor Formula Comparison<br />

0.023179566<br />

0.022852982<br />

0.023624008<br />

0.023277335<br />

0.026230914<br />

0.02 0.022 0.024 0.026 0.028 0.03<br />

Friction Factor<br />

Friction<br />

Factor<br />

Smooth<br />

Pipe<br />

Friction<br />

Factor<br />

Rough<br />

Pipe<br />

0.029581001<br />

Pressure (Pa)<br />

Computational Fluid Dynamics (CFD)<br />

The aim was to use the ANSYS software to run a<br />

number of CFD simulations for the flow through a<br />

pipe. The parameters of the experiment were<br />

utilised as the inputs for the first series of CFD<br />

runs. This then meant that the empirical and CFD<br />

calculated pressure drops could be used for<br />

comparison purposes. Another set of runs were<br />

carried out with parameters that would produce<br />

the results expected of this investigation, the ideal<br />

results, which would help validate the theory<br />

The CFD results confirmed the hypothesis that the<br />

experimental pipes behaved hydraulically smooth.<br />

It also verified that increased roughness does lead<br />

to an increase in pressure loss.<br />

1600<br />

1400<br />

1200<br />

1000<br />

800<br />

600<br />

400<br />

200<br />

0<br />

Pressure (Pa)<br />

Comparing Rough Pipe vs Smooth Pipe<br />

1 1.2 1.4 1.6 1.8 2<br />

Distance (m)<br />

3000<br />

2500<br />

2000<br />

1500<br />

1000<br />

500<br />

0<br />

Pressure loss difference between a smooth and roughened pipe (idealised<br />

situation)<br />

1 1.2 1.4 1.6 1.8 2<br />

Distance (m)<br />

Smooth CFD<br />

Rough CFD<br />

Smooth<br />

Theoretical<br />

(Smooth Regime)<br />

Rough Theoretical<br />

(Smooth Regime)<br />

Smooth<br />

Experimental<br />

Rough<br />

Experimental<br />

Smooth Ideal<br />

Rough Ideal<br />

Project summary<br />

A wide variety of industrial processes involve the<br />

transfer of heat energy. These processes provide a<br />

source for energy efficiency increases. Enhanced heat<br />

transfer surfaces can be designed through a<br />

combination of factors that include: increasing fluid<br />

turbulence, generating secondary fluid flow patterns,<br />

reducing the thermal boundary layer thickness and<br />

increasing the heat transfer surface area.<br />

Project Objectives<br />

The project was an investigation into roughened pipe<br />

with the main objectives being the improvement of<br />

the heat transfer efficiency whilst minimising the<br />

pressure loss induced by turbulence. The paper<br />

discusses the theory behind the heat transfer and<br />

fluid mechanics and how this relates to heat transfer<br />

enhancement. A practical experiment,<br />

complemented by theoretical analysis and<br />

computational fluid dynamics, was conducted to the<br />

see how the theoretical results compared to the<br />

empirical data.<br />

Project Conclusion<br />

It was found that the experimental pipe had a relative<br />

roughness that when compared to the Reynolds<br />

number, resulted in the pipes acting hydraulically<br />

smooth, despite the fact that one pipe was in reality<br />

rougher than the other. This was because the<br />

boundary layer was thicker than the roughness<br />

height. This report details how these problems would<br />

be overcome in a revised experiment, so that the<br />

heat transfer could be analysed effectively. The CFD<br />

model was also employed to simulate an ideal<br />

experiment, in which the roughened pipe exhibited a<br />

rough regime, this verified that this does lead to an<br />

increased pressure loss.

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