Coplanar electrical/ultrasonic dual-modality tomography for water continuous gas/oil/water three-phase distribution imaging

Author(s):  
Guanghui Liang ◽  
Shangjie Ren ◽  
Feng Dong
IEEE Access ◽  
2020 ◽  
Vol 8 ◽  
pp. 125163-125178 ◽  
Author(s):  
Felipe D. A. Dias ◽  
Eduardo N. dos Santos ◽  
Marco J. da Silva ◽  
Eckhard Schleicher ◽  
Rigoberto E. M. Morales ◽  
...  

2018 ◽  
Vol 62 ◽  
pp. 152-166 ◽  
Author(s):  
Qiang Wang ◽  
Jiri Polansky ◽  
Mi Wang ◽  
Kent Wei ◽  
Changhua Qiu ◽  
...  

Author(s):  
Jose Zaghloul ◽  
Michael Adewumi ◽  
M. Thaddeus Ityokumbul

The transport of unprocessed gas streams in production and gathering pipelines is becoming more attractive for new developments, particularly those is less friendly enviroments such as deep offshore locations. Transporting gas, oil, and water together from wells in satellite fields to existing processing facilities reduces the investments required for expanding production. However, engineers often face several problems when designing these systems. These problems include reduced flow capacity, corrosion, emulsion, asphaltene or wax deposition, and hydrate formation. Engineers need a tool to understand how the fluids travel together, quantify the flow reduction in the pipe, and determine where, how much, and the type of liquid that would from in a pipe. The present work provides a fundamental understanding of the thermodynamics and hydrodynamic mechanisms of this type of flow. We present a model that couples complex hydrodynamic and thermodynamic models for describing the behavior of fluids traveling in near-horizontal pipes. The model incorporates: • A hydrodynamic formulation for three-phase flow in pipes. • A thermodynamic model capable of performing two-phase and three-phase flow calculations in an accurate, fast and reliable manner. • A new theoretical approach for determining flow pattern transitions in three-phase (gas-oil-water) flow, and closure models that effectively handle different three-phase flow patterns and their transitions. The unified two-fluid model developed herein is demonstrated to be capable of handling systems exhibiting two-phase (gas-water and gas-oil) and three-phase (gas-oil-water) flow. Model predictions were compared against field and experimental data with excellent matches. The hydrodynamic model allows: 1) the determination of flow reduction due to the condensation of liquid(s) in the pipe, 2) assessment of the potential for forming substances that might affect the integrity of the pipe, and 3) evaluation of the possible measures for improving the deliverability of the pipeline.


2012 ◽  
Vol 15 (06) ◽  
pp. 706-711 ◽  
Author(s):  
M.. Feali ◽  
W.V.. V. Pinczewski ◽  
Y.. Cinar ◽  
C.H.. H. Arns ◽  
J.-Y.. -Y. Arns ◽  
...  

Summary It is now widely acknowledged that continuous oil-spreading films observed in 2D glass-micromodel studies for strongly water-wet three-phase oil, water, and gas systems are also present in real porous media, and they result in lower tertiary-gasflood residual oil saturations than for corresponding negative spreading systems that do not display oil-spreading behavior. However, it has not yet been possible to directly confirm the presence of continuous spreading films in real porous media in three dimensions, and little is understood of the distribution of the phases within the complex geometry and topology of actual porous media for different spreading conditions. This paper describes a study with high-resolution X-ray microtomography to image the distribution of oil, water, and gas after tertiary gasflooding to recover waterflood residual oil for two sets of fluids, one positive spreading and the other negative spreading, in strongly water-wet Bentheimer sandstone. We show that, for the positive spreading system, oil-spreading films maintain the connectivity of the oil phase down to low oil saturation. At similar oil saturation, no oil films are observed for the negative spreading system, and the oil phase is disconnected. The spatial continuity of the oil-spreading films over the imaged volume is confirmed by the computed Euler characteristic for the oil phase.


2017 ◽  
Vol 156 ◽  
pp. 468-483 ◽  
Author(s):  
G. Ersoy ◽  
C. Sarica ◽  
E. Al-Safran ◽  
H.-Q. Zhang
Keyword(s):  
Gas Oil ◽  

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