The severe slugging flow instability in flowline-riser systems is an upstream compressibility problem, where trapped gas upstream the riser base can be compressed and eventually cause blow out of the accumulated liquid in the riser. For the case of a very long riser, flow instabilities can be induced by gas expansion in the riser itself. Even small amounts of trapped gas can cause flow instabilities, as the accumulated gas is flushed through the bend at the riser base and into the riser. Small scale air-water experiments have been carried out to illustrate this phenomenon in an 8m long vertical riser with an internal diameter of 16mm. Constant inlet pressure is obtained by an overflow arrangement for the liquid. The gas is injected in a small undulation upstream the riser base. Unstable production has been observed both for continuous and non-continuous liquid production at the outlet, and the experiments have successfully been simulated by a Lagrangian slug tracking code.
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16th International Conference on Multiphase Production Technology
June 12–14, 2013
Cannes, France
Expansion Instabilities in Long Risers: Small Scale Experiments and Simulations
T.K. Kjeldby;
T.K. Kjeldby
Norwegian Universtiy of Science and Technology
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T. Arnult;
T. Arnult
Norwegian Universtiy of Science and Technology
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O.J. Nydal
O.J. Nydal
Norwegian Universtiy of Science and Technology
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Paper presented at the 16th International Conference on Multiphase Production Technology, Cannes, France, June 2013.
Paper Number:
BHR-2013-J2
Published:
June 12 2013
Citation
Kjeldby, T.K., Arnult, T., and O.J. Nydal. "Expansion Instabilities in Long Risers: Small Scale Experiments and Simulations." Paper presented at the 16th International Conference on Multiphase Production Technology, Cannes, France, June 2013.
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