SPE Annual Technical Conference and Exhibition 1985
DOI: 10.2118/14283-ms
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Developments in the Simulation and Design of Multiphase Pipeline Systems

Abstract: Two-phase pipelines offer the potential for substantial cost savings in the offshore transport of hydrocarbons. Their design has been hampered by uncertainties in two-phase pressure drop relations, in flow regime determination, and in liquid slug length prediction. This uncertainty makes difficult the choice of pipe size and the design of downstream separation facilities. In order to reduce the uncertainty in two-phase flow pipeline design, Esso, Statoil, Mobil, Texaco, and Getty have sponsored the constructio… Show more

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Cited by 9 publications
(4 citation statements)
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“…The experimental facility described by Norris et al33 in which the test section encompasses a long horizontal pipeline culminating in a riser, has been modified to introduce the gas and liquid phases at the base of the vertical riser, to minimize upstream effects. The test fluids used were nitrogen and naphtha (a mixture of liquid hydrocarbons) at pressures of 20 and 90 bar and a nominal temperature of 30°C.…”
Section: Experimental Arrangementmentioning
confidence: 99%
“…The experimental facility described by Norris et al33 in which the test section encompasses a long horizontal pipeline culminating in a riser, has been modified to introduce the gas and liquid phases at the base of the vertical riser, to minimize upstream effects. The test fluids used were nitrogen and naphtha (a mixture of liquid hydrocarbons) at pressures of 20 and 90 bar and a nominal temperature of 30°C.…”
Section: Experimental Arrangementmentioning
confidence: 99%
“…In this study, OLGA 7 Licensed by Schlumberger group as a transient single phase and multiphase simulator was used to model the response of a pipeline system to leaks of different sizes and locations. OLGA is an Eulerian, transient, gas -liquid, pipe flow simulator developed in Norway (Norris III et al, 1985). A pvt file containing the fluid's compositional properties as defined in Table 1 was created using a PVTSIM software and this was used to model a single phase 100 m length pipe as described in Table 2.…”
Section: Leak Modelling Using Olga Simulatormentioning
confidence: 99%
“…In addition, the last 230 ft upstream of the riser inlet, starting at 1,083 ft from the mixing point, may be dipped 1º or 2º down to introduce terrain slugging in the riser. 19 All parts are made of carbon steel. The two-phase flow from the riser enters the top separator where the initial gasliquid separation takes place.…”
Section: Flow Loops Around the World -mentioning
confidence: 99%