Crisman Annual Report 2009 - Harold Vance Department of ...
Crisman Annual Report 2009 - Harold Vance Department of ...
Crisman Annual Report 2009 - Harold Vance Department of ...
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Investigation <strong>of</strong> Swirl Flows Applied to the Oil and Gas Industry<br />
Introduction<br />
Swirl flow (or vortex flow) is a fluid stream which has<br />
a rotational velocity as well as a linear velocity (Fig.<br />
1). It typically occurs in cyclones, hydrocyclones,<br />
spray dryers, heat exchangers with twisted-tape<br />
inserts, and vortex burners. It is also the basic<br />
principle behind foam-breaking or de-foaming<br />
separators, which have received significant industrial<br />
attention in recent years. Current research at Texas<br />
A&M University is studying the various applications<br />
<strong>of</strong> swirl flow to help mitigate particular problems<br />
in the oil and gas industry. Among the swirl flow<br />
applications under investigation are liquid unloading<br />
in gas wells and wet gas metering.<br />
Swirling Flow<br />
For the purpose <strong>of</strong> the analysis presented here, the<br />
expansion/contraction section and the venturi were<br />
excluded from the simulations in order to allow focus<br />
on the effects <strong>of</strong> the swirling device.<br />
In prior described experiments (Falcone et al.,<br />
2003), the actual length <strong>of</strong> straight pipe upstream<br />
<strong>of</strong> the swirler was about 10 m. This resulted in fully<br />
developed annular flow prior to the fluid reaching<br />
the swirler. To simulate this correctly with the CFD<br />
model while minimizing the mesh requirements<br />
(and hence the running times), a sensitivity analysis<br />
was performed on the length <strong>of</strong> pipe to be modeled<br />
before the swirler. It was found that a length <strong>of</strong> 2<br />
m in the model yielded annular flow upstream the<br />
swirler. The final model used for the CFD simulations<br />
is shown in Fig. 2.<br />
(continued on next page)<br />
Axial Flow<br />
Direction<br />
Fig. 1. Schematic <strong>of</strong> a swirl flow, showing a particle’s helical path.<br />
Objectives<br />
A commercial CFD s<strong>of</strong>tware package will be used<br />
in this study, with the objective <strong>of</strong> investigating<br />
the efficiency <strong>of</strong> the liquid separation at high gas<br />
fraction and evaluating the persistence <strong>of</strong> the swirl<br />
downstream <strong>of</strong> the flow conditioning device. These<br />
features are essential to understand not only the<br />
efficiency <strong>of</strong> in-line separation devices used for wet<br />
gas metering purposes, but also that <strong>of</strong> downhole<br />
tools for liquid unloading in gas wells.<br />
Approach<br />
A commercial CFD s<strong>of</strong>tware package was used.<br />
A model <strong>of</strong> the ANUMET meter was built and<br />
simulations were run using the input data from the<br />
reported experiments (Falcone, 2006). The pipe<br />
diameter was increased from 31.8 mm to 32.1 mm,<br />
which provided a 0.15 mm thick inflation boundary<br />
on the pipe walls that helped to capture the film<br />
thickness more efficiently than tetrahedral elements.<br />
Project Information<br />
2.4.17 Investigation <strong>of</strong> Swirl Flows Applied to the Oil and<br />
Gas Industry<br />
Related Publications<br />
Falcone, G., Hewitt, G.F., Lao, L., Richardson, S.M. ANUMET:<br />
A Novel Wet Gas Flowmeter. Paper SPE 84504 presented at<br />
the 2003 SPE <strong>Annual</strong> Technical Conference and Exhibition,<br />
Denver, Colorado, 5-8 October.<br />
Surendra, M., Falcone, G., Teodoriu, C. Investigation <strong>of</strong><br />
Swirl Flows Applied to the Oil and Gas Industry. Paper<br />
SPE 115938 presented at the 2008 SPE <strong>Annual</strong> Technical<br />
Conference and Exhibition, Denver, Colorado, 21-24<br />
September.<br />
Contacts<br />
Gioia Falcone<br />
979.847.8912<br />
gioia.falcone@pe.tamu.edu<br />
Catalin Teodoriu<br />
catalin.teodoriu@pe.tamu.edu<br />
Meher Surendra<br />
CRISMAN INSTITUTE<br />
<strong>Crisman</strong> <strong>Annual</strong> <strong>Report</strong> <strong>2009</strong><br />
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