CPGE Department Seminar, Apr 18, 2011 Petroleum and Geosystems Engineering The University of Texas at Austin Austin, TX How the pore scale affects the.

Slides:



Advertisements
Similar presentations
Concept of relative permeability
Advertisements

Impact of capillary trapping on geological CO2 storage
Challenge: How are oil and gas extracted? Teachers notes.
The influence of wettability and carbon dioxide injection on hydrocarbon recovery Saif Al Sayari Martin J. Blunt.
Modelling Rate Effects in Imbibition
Normal text - click to edit NMR T2 Relaxation for Fluid Saturation and Wettability Determination G. ERSLAND IRTG, Oct. 16 th, 2012.
Surfactant/Polymer Flood of Midland Farms Dolomite Core D6
Estimation of characteristic relations for unsaturated flow through rock fractures Jerker Jarsjö Department of Physical Geography and Quaternary Geology,
Pore-Scale Analysis of WAG Flooding V. Sander Suicmez Dr. Mohammad Piri Prof. Martin J. Blunt 5 Jan 2005 Centre for Petroleum Studies Department of Earth.
Preformed Particle Gel (PPG) for Conformance Control
Zaki Al Nahari, Branko Bijeljic, Martin Blunt
Flow Visualization & Pore Network Simulation of Immiscible/ Miscible Displacement with Gravity Domination M. Haghighi M. Haghighi09/09/09.
11 Pore-scale modelling of WAG: impact of wettability Rink van Dijke and Ken Sorbie Institute of Petroleum Engineering Heriot-Watt University WAG Workshop.
Visit from DONG Energy Åsmund Haugen, Bergen, 9 jan
Dual Mesh Method in Upscaling Pascal Audigane and Martin Blunt Imperial College London SPE Reservoir Simulation Symposium, Houston, 3-5 February 2003.
Peyman Mostaghimi, Prof. Martin Blunt, Dr. Branko Bijeljic 16 January 2009, Imperial College Consortium on Pore-Scale Modelling The level set method and.
Boundary Tension and Wettability. Immiscible Phases Earlier discussions have considered only a single fluid in the pores –porosity –permeability Saturation:
Petroleum & Natural Gas Eng. Dept.
Finite-Element-Based Characterisation of Pore- scale Geometry and its Impact on Fluid Flow Lateef Akanji Supervisors Prof. Martin Blunt Prof. Stephan Matthai.
Peyman Mostaghimi, Martin Blunt, Branko Bijeljic 11 th January 2010, Pore-scale project meeting Direct Numerical Simulation of Transport Phenomena on Pore-space.
Dr. Mohammed M. Amro Petroleum Engineering Dept. King Saud University Effect of Scale and Corrosion Inhibitors on Well Productivity in Reservoirs Containing.
E. Putra, Y. Fidra and D.S. Schechter
CIPC Application of X-Ray CT for Investigation of CO 2 and WAG Injection in Fractured Reservoirs D. Chakravarthy, V. Muralidharan, E. Putra and.
Stefan Iglauer, Saleh K Al-Mansoori, Christopher H Pentland, Branko Bijeljic, Martin J Blunt 2 Phase Measurement of Non-Wetting Phase Trapping.
From pore-space images to multiphase transport predictions
Imbibition Assisted Recovery
Saleh K Al-Mansoori, Stefan Iglauer, Christopher H Pentland, Martin J Blunt Three-Phase Measurements of Non-Wetting Phase Trapping Applied to Carbon Dioxide.
Predictive Pore-Scale Modelling
Introduction to Capillary Pressure Some slides in this section are modified from NExT PERF Short Course Notes, However, many of the slides appears.
Introduction to Effective Permeability and Relative Permeability
3D Images of residual oil in an Ottawa sand Congjiao Xie, Saif Ai-Sayari and Martin Blunt Earth Science and Engineering, Imperial College London.
The Effect of Wettability on Relative Permeability, Capillary Pressure, Electrical Resistivity and NMR Saif AL-Sayari Prof. Martin Blunt.
Pore-Scale Analysis of WAG & Development of a New Empirical Model
Imperial College, PETROLEUM ENGINEERING AND ROCK MECHANICS GROUP 10 th January 2003 PETROLEUM ENGINEERING AND ROCK MECHANICS GROUP Pore Scale Modeling.
CO 2 sequestration in geological formations – application of Computer Tomography (CT)
1 Saleh AlMansoori Dr. Stefan Iglauer Christopher Pentland Professor Martin J. Blunt Measurements of Residual Saturation Implications for CO 2 Trapping.
Micro-Emulsion Xiaowen Feng Peking University, Department of Chemistry.
Rheology of Viscoelastic surfactants and foam in homogeneous porous media Aarthi Muthuswamy, Clarence Miller, Rafael Verduzco and George Hirasaki Chemical.
Alkali-Surfactant-Polymer Process
In the name of God Three-Phase Flow in Mixed-Wet Porous Media Mohammad Piri Prof. Martin Blunt Petroleum Eng. and Rock Mechanics (PERM) Research Group.
A level set method for fluid displacement in realistic porous media
Prediction of wettability variation and its impact on flow using pore- to reservoir-scale simulations Matthew Jackson, Per Valvatne and Martin Blunt Centre.
Introduction to NAPLs Review of general concepts
Estimation of parameters for simulation of steady state foam flow in porous media Kun Ma, Sibani Lisa Biswal and George J. Hirasaki Department of Chemical.
Water underground MS. COULTER. How water moves underground  Water underground trickles down between particles of soil and through cracks and spaces in.
In the name of God Pore-Scale Modeling of Three-Phase Flow in Mixed-Wet Systems Mohammad Piri Martin Blunt Centre for Petroleum Studies Department of Earth.
CPGE Surfactant-Based Enhanced Oil recovery Processes and Foam Mobility Control Task 4: Simulation of Field-Scale Processes Center for Petroleum and Geosystems.
Pore-Scale Model for Rate Dependence of Two-Phase Flow in Porous Media Mohammed Al-Gharbi Supervisor: Prof. Martin Blunt.
Walt King, Petroleum Engineer1 PTTC Simulation Users Group An Overview of the Exodus Simulation Computer Program October 23, 2003 Presented by Walt King,
Fluid Saturation Introduction
Purpose: To provide a multi-scale theoretical and computational model of variably saturated granular/porous media that will improve our ability to perform.
© IFP Controlled CO 2 | Diversified fuels | Fuel-efficient vehicles | Clean refining | Extended reserves WAG-CO2 process : pore- and core-scale experiments.
1 Pore-Scale Simulation of NMR Response in Porous Media Olumide Talabi Supervisor: Prof Martin Blunt Contributors: Saif AlSayari, Stefan Iglauer, Saleh.
Ground Water Notes. I like science. Water Table The spaces between the grains are filled with air. The spaces between the grains are filled with water.
Ran Qi, Valcir T Beraldo, Tara C LaForce, Martin J Blunt Design of CO 2 storage in aquifers 17 th Jan Imperial College Consortium on Pore-Scale Modelling.
Christopher H Pentland, Stefan Iglauer, Yukie Tanino, Rehab El-Magrahby, Saleh K Al Mansoori, Puneet Sharma, Endurance Itsekiri, Paul Gittins, Branko Bijeljic,
Groundwater. 1. Zone of Aeration 2. Water table.
Research Institute of Petroleum Industry
Imperial College, London Pore Scale Modelling: Pore - to - Reservoir Upscaling Project Plans by IDOWU N. A.
1 David DiCarlo 2, Roy Wung 2, Sid Senthilnathan 2, Chang Da 2, Prasanna Krishnamurthy 2, Keith Johnston 2, Chun Huh 2, Tip Meckel 2, and Hongkyu Yoon.
Drilling and Production
Hasan Nourdeen Martin Blunt 10 Jan 2017
PETROLEUM ENGINEERING AND ROCK MECHANICS GROUP
Date of download: 10/22/2017 Copyright © ASME. All rights reserved.
Ground Water Revised 12/16/09.
Introduction to Effective Permeability and Relative Permeability
Ground Water Revised 12/16/09.
Relative permeability
Kendra I. Brown, Dorthe Wildenschild, and Mark L. Porter H41F-0935
Presentation transcript:

CPGE Department Seminar, Apr 18, 2011 Petroleum and Geosystems Engineering The University of Texas at Austin Austin, TX How the pore scale affects the field scale: Real world examples David A. DiCarlo

CPGE Department Seminar, Apr 18, 2011 Acknowledgments Stanford University Akshay Sahni Martin Blunt University of Texas Hassan Dehghanpour Behdad Aminzadeh Mohammad Mirzaei

CPGE Department Seminar, Apr 18, 2011 Variety of flow scales Continuum ScalePore ScaleField Scale Gas Oil

CPGE Department Seminar, Apr 18, 2011 Interests and motivation The configuration of fluids at the pore-scale controls flow and transport at field scales Three-phase (gas, oil, water) flow Preferential flow Unsaturated flow in fractures In-situ measurements of pore filling Fluid-fluid interfacial area in porous media Continuum and discrete formulations of flow

CPGE Department Seminar, Apr 18, 2011 NAPL Water Three-phase (gas, oil, water) flow Essential component of oil recovery or aquifer remediation Gas Oil Oil recovery by gas injection Leaking gasoline Key parameters: Residual oil (S or ) and flow speed (k ro )

CPGE Department Seminar, Apr 18, 2011 Prudhoe Bay’s extra oil At best, only 50% of the original oil in a reservoir is recovered by a waterflood Prudhoe Bay’s eventual recovery will be over 70%! (>$100 B difference) Why? Prudhoe Bay is the world’s largest gas injection operation

CPGE Department Seminar, Apr 18, 2011 Objectives Understand at a basic physical level why high recoveries are possible for three-phase flow Develop a quick method to measure three- phase relative permeability (normalized recovery rate) Systematically measure three-phase relative permeability as a function of wettability and saturation history

CPGE Department Seminar, Apr 18, 2011 Experimental set-up Create 1m long sandpacks with varying degrees of wettability Fill sandpacks with oil and water, then open the bottom and let drain out Use dual-energy computed tomography (CT) to measure the saturation of each phase versus position and time

CPGE Department Seminar, Apr 18, Experimental Set-up Oil phase  N-octane, Aqueous phase  10 wt % NaBr, Gas phase  Air Vertical Positioning System Effluent Gas Invades the System

CPGE Department Seminar, Apr 18, 2011 Long time saturation vs position and time – initial experiments

CPGE Department Seminar, Apr 18, 2011 Calculating Relative Permeabilities u i = -(K/  ) k r (S i )  P i /  x To directly measure the relative permeability of a phase you need The fluid saturation - S i The flux - u i The pressure gradient -  P i /  x

CPGE Department Seminar, Apr 18, 2011 Saturation vs Position and Time oil moved saturation

CPGE Department Seminar, Apr 18, 2011 Measured Relative Permeability Can measure relative permeability over 6 orders of magnitude Measure with different wettabilities Measure with different initial states

CPGE Department Seminar, Apr 18, 2011 Oil Permeability Remains Finite to Low Saturations Oil relative permeability depends on wettability

CPGE Department Seminar, Apr 18, 2011 Oil trapping after waterflood solid grain water trapped oil

CPGE Department Seminar, Apr 18, 2011 No oil trapping after gasflood oil layers gas

CPGE Department Seminar, Apr 18, 2011 Oil remains mobile to very low saturations Water becomes immobile at around S w = 0.1 Oil and water are not interchangeable

CPGE Department Seminar, Apr 18, 2011 Fluids on water-wet and oil-wet surfaces gw   ow go  go  gas water-wet surface oil water  g w  o w go  w a t e r o il gas gw  o il-w e t su rf ace Oil spreads on water Water beads on oil

CPGE Department Seminar, Apr 18, 2011 Fluids in pore corners Oil layers at low S o Oil cannot be trapped  go   ow o il gas w a t e r   ow gas  gw w a t e r o il water-wet corner oil-wet corner No water layers! Water can be trapped

CPGE Department Seminar, Apr 18, 2011 Layers Show up at Low Sat All oil in layers q ~ r 4 S o ~ A~ r 2 k ro ~ S o 2  go   ow o il gas w a t e r

CPGE Department Seminar, Apr 18, 2011 Current work – Three Phase Comparing results to Stone and saturated average three-phase permeability models Can possibly fit by changing the residuals Extending reconnection work to different wettabilities Measure pressures, and do with real rock cores and CO2 ?????

CPGE Department Seminar, Apr 18, 2011 Interests and motivation The configuration of fluids at the pore-scale controls flow and transport at field scales Three-phase (gas, oil, water) flow Preferential flow – flow at frontal interfaces Unsaturated flow in fractures In-situ measurements of nano-particles Surfactant imbibition into oil-wet media Continuum and discrete formulations of flow

CPGE Department Seminar, Apr 18, 2011 Thanks for your attention!