Experiment Research of Phase Inversion in Mineral Oil-Water Two-Phase Flow in Horizontal Pipe

2009 ◽  
Vol 131 (4) ◽  
Author(s):  
Wei Wang ◽  
Jing Gong

In oil-water two-phase dispersed flow, phase inversion may occur when the continuous phase becomes dispersed. This phenomenon, which controls the nature of the phase in contact with the pipe, has a great importance on the corrosion and on the pressure drop, which dramatically affects the delivery ability and operational modality. It is therefore imperative for the phase inversion research to be taken into consideration. However, most of the knowledge on phase inversion is for light mineral oil with low viscosity, few research focuses on high viscosity oil-water phase inversion. Arirachakaran et al. (1989, “An Analysis of Oil/Water Flow Phenomena in Horizontal Pipes,” SPE Professional Product Operating Symposium, Oklahoma, SPE Paper No. 18836) found that critical water fraction when inversion occurred was dramatically reduced with the increment of oil viscosity, and the existing phase inversion models are invalidated. In this paper, an experimental study has been made of high viscosity mineral oil-water flow through a horizontal pipe loop. Results indicate that phase inversion for oil phase with high viscosity occurs much earlier than low viscosity oil, and phase inversion tends to be delayed, with the increment in experimental temperature. The influence of mixture velocities on the inversion process could be neglected in the range of mixture velocities that we studied. As well, inversion point obtain by our experiment are best predicted by the correlation of Arirachakaran et al. (1989, “An Analysis of Oil/Water Flow Phenomena in Horizontal Pipes,” SPE Professional Product Operating Symposium, Oklahoma, SPE Paper No. 18836). Models of Decarre and Fabre (1997, “Phase Inversion Prediction Study,” Rev. Inst. Fr. Pet., 52, pp. 415–424) and Braunerand Ullmann (2002, “Modeling of Phase Inversion Phenomenon in Two-Phase Pipe Flows,” Int. J. Multiph. Flow, 28, pp. 1177–1204), based on minimization of system total energy, seem to be invalidated for high viscosity oil.

Author(s):  
Hai-Yuan Yao ◽  
Jing Gong

In this paper, an experimental research on the oil-water liquid-liquid two-phase flow patterns and their transitions in horizontal pipes are carried out. According to online oil-water flow structures and the analysis of pressure drop signals., different flow patterns are defined and distinguished. A new classification for oil-water flow patterns is proposed. The flow pattern maps are obtained from the experimental data, and the factors affecting the transition mechanism of different flow regimes are discussed. In addition, some semi-theoretical criteria for the transition between different flow patterns are proposed. Especially, an accurate model is developed to predict the critical conditions for phase inversion. Comparisons of the proposed criteria with other experimental data show reasonable agreements.


1989 ◽  
Author(s):  
S. Arirachakaran ◽  
K.D. Oglesby ◽  
M.S. Malinowsky ◽  
O. Shoham ◽  
J.P. Brill

SPE Journal ◽  
2012 ◽  
Vol 17 (01) ◽  
pp. 243-250 ◽  
Author(s):  
H.Q.. Q. Zhang ◽  
D.H.. H. Vuong ◽  
C.. Sarica

Summary Water is produced along with heavy oil either during the primary production or during enhanced oil recovery. Therefore, cocurrent oil/water flow is a common occurrence in heavy-oil production and transportation. Production-system design is strongly dependent on accurate predictions of the oil-/water-flow behavior. The predictions of previous mechanistic models for pressure gradient and water holdup are tested with the data acquired, and significant discrepancies are identified, especially for horizontal flow (Vuong 2009). The model performance is largely dependent on the predictions of phase inversion, distribution, and interaction. On the basis of the new understandings from experimental observations, the Zhang and Sarica (2006) unified model is modified by adding a new closure relationship for water-wetted-wall fraction in stratified flow and a new interfacial shear model based on mixing-length theory. The new model is compared with both high-viscosity and low-viscosity oil-/water-flow experimental results, and significant improvements are observed.


2016 ◽  
Vol 819 ◽  
pp. 300-304 ◽  
Author(s):  
Zahid Ibrahim Al-Hashimy ◽  
Hussain H. Al-Kayiem ◽  
Mohammad Shakir Nasif ◽  
Abdalellah. O. Mohmmed

Slug flow regime in two and multi-phase flow in pipes is a complicated flow phenomena representing challenge in the design of the piping system. In the present work, water/air two phase flow was modeled and simulated as 3 dimensional, transient, and incompressible flow using Volume of Fluid technique in STAR-CCM+ software. The simulation was conducted to predict and evaluate the air-water slug flow in a horizontal pipe with 0.16 m diameter and 7 m long. The superficial velocities for both phases were extracted from Baker chart slug zone. The results were validated against experimental bench marking referenced in Baker chart and the proposed VOF technique shows a good capability in simulating the development of the slug flow regime. This model could be utilized for simulation of various two phase flow regimes.


2014 ◽  
Vol 501 ◽  
pp. 012015 ◽  
Author(s):  
L P M Colombo ◽  
M Guilizzoni ◽  
G M Sotgia ◽  
S Bortolotti ◽  
L Pavan

2019 ◽  
Vol 58 (31) ◽  
pp. 14436-14445 ◽  
Author(s):  
Laura Prieto ◽  
Andrés Pinilla ◽  
Deisy Becerra ◽  
Paula Pico ◽  
Juan P. Valdés ◽  
...  

2006 ◽  
Vol 32 (9) ◽  
pp. 1087-1099 ◽  
Author(s):  
K. Piela ◽  
R. Delfos ◽  
G. Ooms ◽  
J. Westerweel ◽  
R.V.A. Oliemans ◽  
...  

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