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.