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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 />

55

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