DEFINICIÓN FLUJO MULTIFÁSICO Y APLICACIONES .. Hasta ahora, se han diseñado tuberías capaces de manejar flujos multifásicos pero no se sabe con. Resumen. Durante los últimos 60 años numerosos autores se han dedicado al estudio del comportamiento de flujo multifásico en tuberías. Grupo i no considera resbalamiento entre las fases. Flujo multifasico tuberias horizontales download as powerpoint presentation. Flujo multifasico tuberias.

Author: Mikall Vuzuru
Country: Denmark
Language: English (Spanish)
Genre: Technology
Published (Last): 18 December 2017
Pages: 141
PDF File Size: 10.9 Mb
ePub File Size: 6.64 Mb
ISBN: 619-9-14317-438-5
Downloads: 43110
Price: Free* [*Free Regsitration Required]
Uploader: Zulrajas

The momentum conservation equation 6 [38] in the right hand side contains: Dukler, “A model for predicting flow regime transitions multifasco horizontal and near horizontal gas-liquid flow,” AIChE Journalvol. There is an intermediate period of time between 10 minutes sec and 40 minutes secwhen both mechanisms are present.

They also suggested that gas bubbles are stabilized due to the rearrangement of water droplets dispersed in oil Figure 2surrounding the interface and increasing the superficial viscosity and elasticity associated to smaller droplet sizes in the emulsion. Raithby, “A transient two-fluid model for the simulation of slug flow in pipelines – i. Some works are focused on a specific flow pattern [50].

flujo de niebla – Schlumberger Oilfield Glossary

On the other hand, unsteady state models have to calculate the outflow in the pipe. Two-Flow Regimes and its Implications. In this work, formulation and notation used in [38] have been selected, and it is used in what follows.

Fluid properties and flow pattern prediction specially at high pressure and high temperature HPHT are two of tuherias. The dispersion morphology was analyzed using optical microscopy. The foamability and foam stability studies of the system were conducted in two different ways: Universidad de Los Andes.

Moreover, some researchers noticed flow patterns in two-phase flows and slippage between phases. Foams from Non-Aqueous Systems. They found that the increment in the total pressure drop is directly proportional to the superficial gas velocity in the pipeline and proposed a pressure drop model based on Lockhart-Martinelli model obtaining a good fitting. O pedalN. M arcanoL. Nicklin, “Two-phase bubble flow,” Chemical Engineering Nultifasicovol.


Universidad de los Andes. Transportation of foamy oil through pipelines is a challenge in Venezuelan fields due to the relatively mmultifasico gas volumes produced with oil. Belandria studied the effect of solids in non-aqueous foam with mineral oil viscosity up to 0.

Some authors assume isothermal analysis [51],[46],[52] or adiabatic conditions [50] from the wall of the pipe, other authors used only one mixture energy conservative equation in spite of develop an hydraulic two fluid model [54].

Teodoriu, “Hydraulic analysis of gasoil- sand flow in horizontal wells,” in Society of Petroleum Engineers This method is used for vertical flow multifasicl it has been selected several times by different authors as starting point for new models.

The pressure gradient is calculated as a combination of friction, gravity, wall inflow 4 and expansion pressure drop. They found that there is an optimum concentration of water at which the stability of the foam increases, and small quantities of water and surfactants produce a drastic change in the foaminess of the oil.

Similar results were presented by Bogdanovic et al. S chmidtD. Finally, the model was compared with well cases from several origins and 7 methods. Ishii and Hibiki coincide with Shoham saying that developing the constitutive equations required to specify the thermodynamic, transport and chemical properties of the multiphase streams are considerably more complicated in comparison to single-phase flow due to the complex nature of two or more phases flowing together with a mobile and deformable interface, in which different flow patterns can be present.


Some other methods are flow pattern independent, most of them present a mathematical advantage of being continuous. In these experiments, the drainage stage took less than ten minutes Figure Foam samples were taken under dynamic conditions and foamability and foam stability were studied. A comparison of 8 correlations for vertical and deviated pipes was made by [8].

flujo de burbujas

multifaasico Lao, “High viscosity effects on characteristics of oil and gas two-phase flow in horizontal pipes,” Chemical Engineering Sciencevol. A review of several models to predict the pressure drop and heat transfer in pipelines is presented in [29]. Foamy oil transport as a multiphase flow system. The first mechanistic model was developed by [23], since then, several methods have been published, i.

Pressure Drop Measurement and Prediction. F ribergS. A new dynamic approach uses an interfacial area transport equation IATE [38]. In this work a review about the most relevant methods found in the literature to model the multiphase flow in pipelines is presented. The size of the bubbles increases as coalescence progresses, 15 minutes later the shape of the bubbles in the foam were mostly spherical, mu,tifasico by a liquid film, with bubble size in the order of several millimeters and it was possible to differentiate two zones: The large scale models are based on space averaging.

The continuity equation 5 is formed by a transient term temporal derivativea convective term spatial derivative and a change of phase term. The first mechanism is dominated by gravitational drainage, multigasico occurs in the first ten minutes.