Correcting for Wettability and Capillary Pressure Effects on Formation Tester Measurements

Similar documents
Capillary Pressure and Rock Wettability Effects on Wireline Formation Tester Measurements

A VALID APPROACH TO CORRECT CAPILLARY PRESSURE CURVES- A CASE STUDY OF BEREA AND TIGHT GAS SANDS

Flow in Porous Media. Module 1.c Fundamental Properties of Porous Media Shahab Gerami

COPYRIGHT. Reservoir Rock Properties Fundamentals. Saturation and Contacts. By the end of this lesson, you will be able to:

Oil Mobility in Transition Zones

SURPRISING TRENDS ON TRAPPED HYDROCARBON SATURATION WITH WETTABILITY

Reservoir Engineering 3 (Flow through Porous Media and Applied Reservoir Engineering)

GeoNeurale. Testing, Testing 1,2,3. GeoNeurale. by Gene Ballay PART 1. Lichtenbergstrasse Munich Garching

Effect of Implementing Three-Phase Flow Characteristics and Capillary Pressure in Simulation of Immiscible WAG

SPE Copyright 2001, Society of Petroleum Engineers Inc.

THREE-PHASE UNSTEADY-STATE RELATIVE PERMEABILITY MEASUREMENTS IN CONSOLIDATED CORES USING THREE IMMISCIBLE LIQUIDS

W I L D W E L L C O N T R O L PRESSURE BASICS AND CONCEPTS

PREDICTION OF FORMATION WATER SATURATION FROM ROUTINE CORE DATA POPULATIONS

FORMATION TESTER MOBILITY. Lachlan Finlayson, Chief Petrophysicist Petrofac Engineering & Production Services Engineering Services Consultancy

PROTOCOLS FOR CALIBRATING NMR LOG-DERIVED PERMEABILITIES

IMPROVED CORE ANALYSIS MEASUREMENTS IN LOW PERMEABILITY TIGHT GAS FORMATIONS

Accurate Measurement of Steam Flow Properties

AN EXPERIMENTAL STUDY OF IRREDUCIBLE WATER SATURATION ESTABILISHMENT

COMPARISON OF FOUR NUMERICAL SIMULATORS FOR SCAL EXPERIMENTS

Vapour pressure of liquids SURFACE TENSION

Pore-scale simulation of water alternate gas injection

Situated 250km from Muscat in

4 RESERVOIR ENGINEERING

Chapter 8: Reservoir Mechanics

CHDT Cased Hole Dynamics Tester. Pressure testing and sampling in cased wells

NEW LABORATORY DATA BASED MODELING OF MISCIBLE DISPLACEMENT IN COMPOSITIONAL SIMULATION

Introduction to Relative Permeability AFES Meeting Aberdeen 28 th March Dave Mogford ResLab UK Limited

A REAPPRAISAL OF THE EVIDENCE FOR DAMAGE CAUSED BY OVEN DRYING OF HYDROCARBON ZONE CORE

New power in production logging

An Improved Understanding of LNAPL Behavior in the Subsurface LNAPL - Part 1

Formation Pressure Testers, Back to Basics. Mike Millar

SCA : TRAPPED VERSUS INITIAL GAS SATURATION TRENDS FROM A SINGLE CORE TEST Dan Maloney and David Zornes, ConocoPhillips

Improvements of the Semidynamic Method for Capillary Pressure Measurements

RMAG, Snowbird, UT, October 6-9, Michael Holmes, Antony M. Holmes, and Dominic I. Holmes, Digital Formation, Inc.

LOW PERMEABILITY MEASUREMENTS USING STEADY-STATE AND TRANSIENT METHODS

STEAM-WATER RELATIVE PERMEABILITY BY THE CAPILLARY PRESSURE METHOD

An approach to account ESP head degradation in gassy well for ESP frequency optimization

Positive imbibition capillary pressure curves using the centrifuge technique.

Assessment of Residual Hydrocarbon Saturation with the Combined Quantitative Interpretation of Resistivity and Nuclear Logs 1

Petroleum Reservoir Rock and Fluid Properties

Technical Note. Determining the surface tension of liquids by measurements on pendant drops

Novel empirical correlations for estimation of bubble point pressure, saturated viscosity and gas solubility of crude oils

Measuring Relative Permeability With NMR

Two interconnected rubber balloons as a demonstration showing the effect of surface tension

IMPROVING THE ASSESSMENT OF RESIDUAL HYDROCARBON SATURATION WITH THE COMBINED QUANTITATIVE INTERPRE- TATION OF RESISTIVITY AND NUCLEAR LOGS

Gas injection in a water saturated porous medium: effect of capillarity, buoyancy, and viscosity ratio

Simposium Nasional dan Kongres X Jakarta, November 2008 Makalah Profesional IATMI

Sarah N. S. All-Said Noor * ; Dr. Mohammed S. Al-Jawad ** ; Dr. Abdul Aali Al- Dabaj ***

SPE Copyright 2012, Society of Petroleum Engineers

REVIEW OF THE INTERCEPT METHOD FOR RELATIVE PERMEABILITY CORRECTION USING A VARIETY OF CASE STUDY DATA

Th CO2 P05 Influencing The CO2-Oil Interaction For Improved Miscibility And Enhanced Recovery In CCUS Projects

Chapter 5 Multiphase Pore Fluid Distribution

Permeability. Darcy's Law

Reservoir Simulator Practical

Interpretation of Water Saturation Above the Transitional Zone in Chalk Reservoirs

3 1 PRESSURE. This is illustrated in Fig. 3 3.

Proceedings of Meetings on Acoustics

SPE The paper gives a brief description and the experience gained with WRIPS applied to water injection wells. The main

WATER OIL RELATIVE PERMEABILITY COMPARATIVE STUDY: STEADY VERSUS UNSTEADY STATE

A07 Surfactant Induced Solubilization and Transfer Resistance in Gas-Water and Gas-Oil Systems

Prof. B V S Viswanadham, Department of Civil Engineering, IIT Bombay

Air Bubble Departure on a Superhydrophobic Surface

Comparison of methods to calculate relative permeability from capillary pressure in consolidated water-wet porous media

HRLA High-Resolution Laterolog Array Tool. Improving the accuracy of Rt

THREE-PHASE CAPILLARY PRESSURE MEASUREMENTS IN CENTRIFUGE AT RESERVOIR CONDITIONS

EVALUATION OF WATER SATURATION FROM RESISTIVITY IN A CARBONATE FIELD. FROM LABORATORY TO LOGS.

Gas viscosity ( ) Carr-Kobayashi-Burrows Correlation Method Lee-Gonzalez-Eakin Method. Carr-Kobayashi-Burrows Correlation Method

COMPUTATIONAL FLOW MODEL OF WESTFALL'S LEADING TAB FLOW CONDITIONER AGM-09-R-08 Rev. B. By Kimbal A. Hall, PE

Influence of Capillary Pressure on Estimation of Relative Permeability for Immiscible WAG Processes

Compaction, Permeability, and Fluid Flow in Brent-type Reservoirs Under Depletion and Pressure Blowdown

LOW PRESSURE EFFUSION OF GASES revised by Igor Bolotin 03/05/12

Wave Motion. interference destructive interferecne constructive interference in phase. out of phase standing wave antinodes resonant frequencies

Effect of Gas-wetness on Gas-water Two-phase Seepage in Visual Microscopic Pore Models

Drilling Efficiency Utilizing Coriolis Flow Technology

Ermenek Dam and HEPP: Spillway Test & 3D Numeric-Hydraulic Analysis of Jet Collision

SPE Effect of Initial Water Saturation on Spontaneous Water Imbibition Kewen Li, SPE, Kevin Chow, and Roland N. Horne, SPE, Stanford University

MATCHING EXPERIMENTAL SATURATION PROFILES BY NUMERICAL SIMULATION OF COMBINED AND COUNTER-CURRENT SPONTANEOUS IMBIBITION

TRANSITION ZONE CHARACTERIZATION WITH APPROPRIATE ROCK- FLUID PROPERTY MEASUREMENTS

Optimization of Separator Train in Oil Industry

A Hare-Lynx Simulation Model

SAMPLE MAT Proceedings of the 10th International Conference on Stability of Ships

COURSE NUMBER: ME 321 Fluid Mechanics I Fluid statics. Course teacher Dr. M. Mahbubur Razzaque Professor Department of Mechanical Engineering BUET

Pore-Air Entrapment during Infiltration

Comparative temperature measurements in an experimental borehole heat exchanger. Vincent Badoux 1, Rita Kobler 2

Ali Al-Harrasi, Zaal Alias, Abhijit Mookerjee, Michiel Van Rijen, Khalid Maamari (Petroleum Development Oman)

Determination of Capillary pressure & relative permeability curves

Coal Bed Methane (CBM) Permeability Testing


Casing Design. Casing Design. By Dr. Khaled El-shreef

CHAPTER 5: VACUUM TEST WITH VERTICAL DRAINS

LOW PRESSURE EFFUSION OF GASES adapted by Luke Hanley and Mike Trenary

Reserve Estimation Using Volumetric Method

PRODUCTION I (PP 414) ANALYSIS OF MAXIMUM STABLE RATE AND CHOKES RESOLVE OF OIL WELLS JOSE RODRIGUEZ CRUZADO JOHAN CHAVEZ BERNAL

A Quick Start Guide for the ER 4123D CW-Resonator

IMPROVEMENTS OF COREFLOOD DESIGN AND INTERPRETATION USING A NEW SOFTWARE.

Process Dynamics, Operations, and Control Lecture Notes - 20

Extended leak off testing

GAS CONDENSATE RESERVOIRS. Dr. Helmy Sayyouh Petroleum Engineering Cairo University

SPE Copyright 2003, Society of Petroleum Engineers Inc.

APPLICATIONS OF THE INTERCEPT METHOD TO CORRECT STEADY-STATE RELATIVE PERMEABILITY FOR CAPILLARY END-EFFECTS

Transcription:

SPE 63075 Correcting for Wettability and Capillary Pressure Effects on Formation Tester Measurements H. Elshahawi, SPE, M. Samir, SPE, and K. Fathy, SPE, Schlumberger Oilfield Services Copyright 2000, Society of Petroleum Engineers Inc. This paper was prepared for presentation at the 2000 SPE Annual Technical Conference and Exhibition held in Dallas, Texas, 1 4 October 2000. This paper was selected for presentation by an SPE Program Committee following review of information contained in an abstract submitted by the author(s). Contents of the paper, as presented, have not been reviewed by the Society of Petroleum Engineers and are subject to correction by the author(s). The material, as presented, does not necessarily reflect any position of the Society of Petroleum Engineers, its officers, or members. Papers presented at SPE meetings are subject to publication review by Editorial Committees of the Society of Petroleum Engineers. Electronic reproduction, distribution, or storage of any part of this paper for commercial purposes without the written consent of the Society of Petroleum Engineers is prohibited. Permission to reproduce in print is restricted to an abstract of not more than 300 words; illustrations may not be copied. The abstract must contain conspicuous acknowledgment of where and by whom the paper was presented. Write Librarian, SPE, P.O. Box 833836, Richardson, TX 75083-3836, U.S.A., fax 01-972-952-9435. Abstract Conventional formation tester interpretation techniques have long assumed that the measured tester pressure is identical to the pressure of the continuos phase in the virgin zone of the formation. As such, a series of pressure measurements at different depths would be expected to consistently yield a pressure gradient corresponding to the density of the formation fluid. Recent work by the authors of this papers as well as by others has shown that the formation testers will actually measure the pressure of the continuos phase present in the invaded region, typically the drilling fluid filtrate. The measured tester pressure is, thus, different from formation pressure by the amount of capillary pressure. This capillary pressure has been shown to be a strong a function of the wetting phase saturation. The effects of the rock wettability and capillary pressure on wireline formation tester measurements are manifested as pressure gradient changes and/or fluid contact level changes on many logs, particularly those recorded with oil-based mud in the borehole. This paper summarizes the effects of wettability and capillary on wireline formation measurements and investigates in detail the possible techniques for recognition and estimation of and correction for those effects. The older techniques rely on the use of core capillary pressure data log-computed flushed zone saturations, but they can often yield inconsistent results. Amongst the more innovative techniques suggested in this paper is the use of NMR measurements to estimate the magnitude of capillary pressure effects and hence correct the measured tester pressure. Also discussed in the use of the pump-out capability of the Modular Dynamics Tester (MDT TM ) to estimate the capillary pressure effect by making measurements before and after the removal of drilling mud filtrate. This allows accurate correction for capillary pressure effects, or better still, the elimination of the need for the correction altogether. Introduction In an oil reservoir, water will normally compete with oil and gas for pore space. This is because water was present in the pores before oil migrated into the reservoir. Thus, at the same depth in a formation, pressures will be different depending on whether oil or water is filling the pores. The amount of pressure difference between the two fluids is largely controlled by pore geometry, rock wettability and the interplay of capillary pressures between rocks and fluids. Capillary pressure (P c ), represents the pressure differential that must be applied to the nonwetting fluid in order to displace a wetting fluid. The value of capillary pressure is dependent on the saturation of each phase, on which phase is the wetting phase, and on the shape and size of the pores and pore throats. Wettability is the property of a liquid to stick to and spread onto a solid surface. It is normally quantified by the value of the contact angle, such that a value less than 90 degrees indicates a water-wet system, and a value greater than 90 degrees indicates an oil-wet system. The following paragraphs take a closer look at the wettability and capillary pressure concepts. Wettability Wettability is an important petrophysical parameter, which determines the fluid distribution in a porous medium and thus affects saturation and recovery. In order to minimize the system s specific surface free energy, the wetting phase coats the surface of the solid grains, occupies the small pores, which have high specific surface area, and occupies the corners of

2 H. ELSHAHAWI, M. SAMIR, K. FATHY SPE 63075 grain contacts. The non-wetting phase, on the other hand, stays in the center of the pores and is concentrated in the larger pores. Fig.1 shows the situation that would occur if the rock had a preference for being water-wet, wherein an isolated droplet of oil is being squeezed from all directions by water. As a result, the pressure of the oil becomes higher than that of the surrounding water by an excess amount termed capillary pressure. On the other hand, if a rock is preferentially oil-wet, the reverse occurs, with the oil being the continuous phase and the pressure being higher in the water. Fig.2 shows how the surrounding oil in an oil-wet rock squeezes the water droplets from all directions. In their natural state, rocks may be either water-wet or oil-wet according to the atoms exposed in the grain or pore surface. In the case of water-wet rocks, they become thus when the oxygen atoms exposed at their surfaces attract hydrophilic hydrogen from the water molecules. If polar impurities such as resins or asphaltenes can reach the surface, they will substitute lipophilic radicals for the H or OH, rendering the surfaces oilwet (Chiligarian and Chen, 1983). Note that while only basic impurities will attach to quartz, both basic and acidic impurities can attach to calcite. This might explain the large percentage of carbonate reservoirs found by several researchers to be oil-wet. Few formations are neutrally wet, but some researchers have reported fractional wettability conditions, in which some portions of the rock are strongly oil-wet and others strongly water-wet (Chiligarian and Chen, 1983). Salathiel (1972) identified mixed wettability reservoirs in which the polar impurities reach the larger but not the smaller pores, resulting in a case wherein the larger pores (higher porosity) become oil-wet, the smaller pores (lower porosity) remain water-wet, and both remain continuously connected. He hypothesized that configurations of oil in pores involve either direct contact between oil and rock in the larger grains and pores (Fig.3); or separation of the oil phase from the solid by aqueous films in the smaller grains and pores (Fig.4). In the larger grains and pores, the oil saturation is highest. When a critical capillary pressure is exceeded, water films destabilize and rupture to an adsorbed molecular film of up to several water mono-layers. Crude oil now contacts rock directly, allowing the polar oil species to adsorb and/or deposit onto the rock. It is this process that locally reverses the wettability of certain sections of the rock from water-wet to oil-wet (Hirasaki et al., 1996). (Elshahawi et al., 1999) detail the case of a mixed wettability reservoir which displays either water-wet or oil-wet features depending on the petrophysical properties of the rock. Capillary Pressure Capillary pressure is defined by the following equation: P c = P nonwetting phase - P wetting phase (1) where P c is the capillary pressure and P nonwetting phase, P wetting phase are the pressure of the nonwetting phase and wetting phase, respectively. The combined effects of wettability and interfacial tension cause a wetting fluid to be simultaneously imbibed into a capillary tube, an often used, yet admittedly simplistic, representation of a pore throat. For the capillary tube, capillary pressure can be expressed as: P c = P nw P w = 2σ cosθ/r = (ρ w -ρ nw ) gh (2) Where σ is the interfacial tension between the two fluids, θ represents the wettability of the capillary tube, r is the radius of the capillary tube, P w, Pn w are the pressures of the wetting and non-wetting phases, respectively, and ρ w and ρ nw are the wetting and non-wetting phase densities, respectively. For a pendular ring at the contacts of two spherical sand grains in an idealized porous medium consisting of a cubic pack of uniform spheres (Fig. 5), the capillary pressure can be expressed by the following Laplace equation (Eq.3). P c = σ (1/r 1 + 1/r 2 ) (3) Where r 1 and r 2 are the two principal radii of curvatures of the interface in two perpendicular planes as shown on Fig 5. As the wetting fluid saturation in the pendular ring is increased, the radii of curvature will be increased, and capillary pressure will decrease. Vice versa, as the wetting fluid saturation in the pendular ring is reduced, the radii of curvature will be reduced and capillary pressure will increase. This can be expressed in the general form below: P c = fn(sw) σ/r m (4) Where r m represents mean radius of curvature. Of course, for an actual porous medium, the complexity of the pore structure and the fluid interface arrangements therein precludes the use of the above equation directly to calculate the capillary pressure. Instead, the capillary pressure is measured experimentally as a function of the wetting fluid saturation. The Capillary Pressure Curve The capillary pressure curve for a porous medium is a function of pore size, pore size distribution, pore geometry, fluid saturation, fluid saturation history or hysterisis, wettability, and interfacial tension. Fig.6 shows drainage and imbibition capillary pressure curves. The drainage capillary pressure curve describes the displacement of the wetting phase from the porous medium by a non-wetting phase, as is relevant for the initial fluid distribution in a water-wet reservoir as well as for the water front advance in an oil-wet reservoir. The imbibition capillary pressure curve, on the other hand, describes the displacement of a non-wetting phase by the wetting phase, as is relevant for water front advance in a water-wet reservoir. In both cases, the capillary pressure is equal to the non-wetting phase pressure minus the wetting phase pressure as given by Eq.2. The capillary pressure curve has several characteristic features. Focusing on the drainage curve and describing it in more detail, one finds that the minimum threshold pressure is the displacement pressure that must be applied to the wetting phase in order to displace the non-wetting phase from the largest pore connected to the surface of the medium such that: P c(displace) =(P nw P w ) displace =2σcosθ/r Largest pore..... (5)

SPE 63075 CORRECTING FOR WETTABILITY AND CAPILLARY PRESSURE EFFECTS ON FORMATION TESTER MEASUREMENTS 3 A lower displacement pressure indicates larger pores connected to the surface, which generally implies higher permeability. As the pressure of the non-wetting phase is increased, increasingly smaller pores are invaded corresponding to the flat section of the curve. A lower capillary flat section indicates larger pores, and consequently higher permeability. A capillary pressure curve that remains essentially flat over its middle section indicates that many pores are being invaded by the non-wetting fluid at the same time, implying that the grains are well sorted and the rock is fairly homogeneous. Inversely, the higher the slope of the middle section of the capillary pressure curve, the worse the sorting and the wider the grain and pore size distributions. Such a rock has lower porosity and generally lower permeability as well. A very steep capillary pressure curve that is nearly vertical over its middle section implies poor reservoir rock with extremely fine grains, very poor sorting, low porosity, and low permeability. Eventually, when the irreducible wetting fluid saturation is reached, the capillary pressure curve becomes nearly vertical. At this stage, the wetting phase becomes discontinuous and can no longer be displaced from the porous medium simply by increasing the non-wetting phase pressure. A lower wetting phase irreducible saturation is generally indicative of relatively larger grains and pores. Generally speaking, therefore, a higher capillary pressure curve describes poorer reservoir quality compared to a lower curve. The Static Pressure Gradient of a Reservoir All petroleum reservoirs were initially saturated with water before oil migrated into the reservoir, displacing the water. The resulting fluid distribution is governed by the equilibrium between gravitational and capillary forces. In the case of a water-wet reservoir, this distribution is simulated by a drainage capillary pressure curve. The Free water level (FWL) in a reservoir is the level at which the oil-water capillary pressure vanishes. It is the oil-water interface that would exist at equilibrium in an observation borehole, free of capillary effects, if it were to be drilled in the porous medium and filled with oil and water. The Oil-water contact (OWC), on the other hand, is the level at which oil saturation starts to increase from some minimum saturation. In a water-wet rock, that minimum saturation is essentially zero. Using the FWL as the reference datum, The water and oil phase pressure at a distance z above the FWL datum are given by the following two expressions: P w (z) = P FWL - ρ w gz (6) P o (z) = P FWL - ρ o gz (7) Subtracting the two equation yields an expression for the capillary pressure, P c : P c (z) = (ρ w gz - ρ o gz)/144 = ρgz/144 (8) where P c is in psi, ρ is in lbm/cu.ft, and z is in ft. The FWL is generally not coincident with the OWC but, instead, differs by an amount related to the displacement pressure. In a water-wet reservoir, the FWL occurs at a depth d o below the oil-water contact given by: d o = (P D / ρg) x 144 (9) where P D is the displacement pressure (oil displacing water) in psi, ρ is in lbm/cu.ft, and z is in ft. It is determined by largest pore of the pore size distribution. The capillary transition zone (Fig. 10) is the region above the OWC where the water saturation decreases from its maximum to the irreducible water saturation. The height of the transition zone is a function of wettability, the fluid density contrast, and the oil-water interfacial tension. The shape of this transition zone is also dependent on the same factors that affect the capillary pressure curve. The elevation (h) above the OWC of any particular saturation within the transition zone is given by: h( ) = (P c ( ) - P D ) / ρg x 144 (10) In an oil-wet reservoir (Fig.11), the situation described above is slightly different. In this case, it is the water that is the nonwetting phase, and hence, its pressure is higher than it would be in a water-wet medium. Even though the reservoir was initially saturated with water before oil migrated into the reservoir and displaced the oil, an imbibition capillary pressure curve, rather than a drainage curve better describes the situation once the reservoir has become preferentially oilwet reservoir. As an imbibition curve would predict, the minimum oil saturation encountered below the zero capillary pressure line is not zero, but rather a residual value, r. Since it is easier to displace water than oil in this case, the portion of the capillary pressure curve below the zero line (corresponding to the FWL) is larger than the part above. Consequently, he OWC in this case is the lowest level that the oil will reach (at which the oil saturation will start to increase from its minimum value). The FWL is located above the OWC by a distance d o given by: d o = (P D / ρg) x 144 (11) Which is generally larger than the equivalent distance in a water-wet rock. Also unlike for a water-wet reservoir, this distance is determined by the smallest-rather than the largestpore of the pore size distribution. Recognizing Wettability and Capillary Pressure Effects on Tester Gradient Measurements Conventional formation tester interpretation methods assume that the tool measures the true formation pressure of the continuous mobile formation fluid in the virgin zone. The fallacy of this assumption is made clear by examining Fig.7 (a to h), which details the saturation profile for various wetting fluid-drilling mud-formation fluid combinations. Fig.8 (a to h), on the other hand, details the capillary pressure distribution corresponding to each combination while Fig.9 (a and b) details the effect of these combinations on the wireline pressure tester gradient measurements. For a well drilled with water-based mud in a water-wet formation, the oil in the flushed zone of an oil-bearing interval (Fig.7-c) is close to residual saturation so that the capillary pressure in the invaded

4 H. ELSHAHAWI, M. SAMIR, K. FATHY SPE 63075 zone becomes small (Fig.8-c). The result is that the waterphase pressure actually measured is only marginally lower than the oil phase pressure that we desire to measure, shifting the oil gradient slightly to the left (top of left plot of (Fig.9-a)). In the water-bearing interval (Fig.8-a), there will be no capillary pressure difference between the mud filtrate and the formation water, and the tool measures the true formation pressure (Fig. 8-a) and (bottom of left plot of (Fig.9-a)). For a well drilled with oil-based mud in a water-wet formation, there is no capillary pressure difference between the mud filtrate and the formation oil in an oil-bearing interval. Thus, the tool measures the actual formation gradient (Fig.7-d), (Fig.8-d) and by The formation tester over-estimates the value of the true formation gradient by In the waterbearing zone (Fig.7-b), the water saturation in the invaded zone is close to connate or irreducible, and the capillary pressure is large (Fig.8-b). The value of the oil pressure actually measured is thus higher than the water pressure that is desired by P c (Swc). The measured water gradient is thus shifted to the right (bottom of right plot of (Fig.9-a)). In a gas reservoir drilled with oil-based mud, the pressure measured in the water zone is similarly boosted by an amount equal to the capillary pressure. The situation is further complicated by the existence of three phases but can be simplified by treating the water and oil as a single wetting phase and the gas as the nonwetting phase which controls the capillary pressure. In the invaded zone, however, gas saturations are normally close to residual levels, and the capillary pressure is nearly nil, so the capillary effect on the pressure measurement can be safely neglected. For a well drilled with water-based mud in an oil-wet formation, the oil in the flushed zone of an oil-bearing interval is close to residual saturation (Fig.7-g), and the capillary pressure is maximum (Fig.8-g). The measured water phase pressure is higher than the oil phase pressure by the amount of P c (Sor). The formation tester thus over-estimates the value of the true formation pressure, shifting the oil gradient line to the right (top of left plot of (Fig.9-b)). In the water-bearing interval, there will be no capillary pressure difference between the mud filtrate and the water, and the tool measures the true formation gradient (Fig.7-e, Fig.8-e and bottom of left plot of (Fig.9-b)). For a well drilled with oil-based mud in an oil-wet formation, there is no capillary pressure difference between the mud filtrate and the formation oil in an oil-bearing interval, so the tool measures the actual formation gradient (Fig.7-h, Fig. 8-h and top of right plot of (Fig.9-b)). In the water-bearing zone, the water saturation in the invaded zone is close to irreducible, and the capillary pressure is a small value (Fig.7-f and Fig.8- f). The result is that the measured oil pressure is slightly lower than the desired water pressure. Thus, the measured water gradient is slightly shifted to the left (bottom of left plot of (Fig.9-b)). When one of the two phases becomes discontinuous at low saturation, its pressure follows the gradient of the other (continuous) phase. The pressure of a discontinuous phase is unobservable except under lab conditions and is of no practical importance. In silty sandstone reservoirs, the irreducible water saturation corresponding to the top of the capillary transition zone may be quite high yet the oil phase is continuous and the well produces oil. A magnetic resonance log would be able to differentiate moveable from bound fluid, but if only conventional logs are available, potential recoverable oil will probably be missed. In such a case, formation tester gradients can be used to distinguish between moveable oil, which appears as a continuous oil gradient on the pressure measurements despite the high water saturation, and residual oil, which appears as a continuous water gradient. The importance of this for reserve estimation is obvious. Recognizing Wettability and Capillary Pressure Effects on Tester Fluid Level Measurements The effects of wettability and capillary pressure on the wireline formation tester s fluid level measurement are closely linked to their effects on gradient measurements. Ordinarily, the intersection of the continuous phase pressure lines on a depth-pressure diagram occurs at the FWL as shown in Fig.10 and Fig.11 for water-wet and oil-wet reservoirs, respectively. The intersection of the water and hydrocarbon continuous phase pressure lines as measured by the wireline formation tester is an indication of the FWL. In general, however, this intersection will differ from the FWL in a direction that reflects the rock wettability and by an amount that is dependent on the degree of wettability, the magnitude of capillary pressure, and the type of drilling mud used (Fig.9a and b). In a water-wet medium, the capillary pressures in the oil-filled pores are higher than in the water-filled ones, and the FWL is located below the OWC by a distance determined by the capillary threshold or displacement pressure (Fig.10). As shown in Fig.9-a, the actual intersection of the oil and water gradients from the wireline formation will be generally higher than the true FWL. This is true for wells drilled with either water and oil-based muds. As explained in the previous section, with water-based mud () in the oil zone, the measured pressure will be the water phase pressure, which will be lower than the oil phase pressure we are aiming to measure. Therefore, the measured oil line will be shifted to the left of the true formation oil pressure line, making the intersection higher than the actual FWL (left plot of Fig.9a). On the other hand, with an oil-based mud () in the water zone, the measured pressure is the oil filtrate pressure, which will be greater than the water phase pressure. Thus, the measured water line will be shifted to the right of the true formation water pressure line, making the intersection again higher than the actual FWL (right plot of Fig.9a).

SPE 63075 CORRECTING FOR WETTABILITY AND CAPILLARY PRESSURE EFFECTS ON FORMATION TESTER MEASUREMENTS 5 In an oil-wet medium, the capillary pressures in the waterfilled pores are higher than in the oil-filled pores, and the FWL is located above the OWC by a distance again determined by the capillary threshold or displacement pressure (Fig.11). The actual intersection of the oil and water gradients from the wireline formation tester will be generally lower than the true FWL as shown by Fig.9b. This is true for wells drilled with either water and oil-based muds. As discussed in the previous section, with a in the oil zone, the measured pressure will be the water phase pressure, which will be higher than the oil phase pressure we are aiming to measure. Therefore, the measured oil line will be shifted to the right of the true formation oil pressure line, making the intersection lower than the actual FWL (left plot of Fig. 9b). On the other hand, with in the water zone, the measured pressure is the oil filtrate pressure, which will be lower than the water phase pressure. Thus, the measured water line will be shifted to the left of the true formation water pressure line, making the intersection again lower than the actual FWL (right plot of Fig. 9a). Fig. 12 and Fig.13 show how rock wettability was detected insitu in a mixed-wettability sandstone by its effect on the wireline formation pressure measurements (Hiekal at al., 1998). Fig.12 shows the OWC at a depth of 4835 ft-tvdss, 20 ft-tvd below the FWL at 4815 ft-tvdss in a high porosity system of the reservoir with strong preference to be oil wet. On the other hand, Fig.13 shows the OWC at a depth of 4835 ft-tvdss, 35 ft-tvd above the FWL at 4870 ft- TVDss in a low porosity system reservoir which has a strong affinity to be water-wet. Recognizing and Correcting for Supercharging Effects on Formation Tester Measurements As a consequence of mud filtrate invasion in the immediate vicinity of the wellbore, the formation may exhibit pressures higher than the actual formation pressure. This over-pressure tends to dissipate when a mud cake is established and further invasion becomes negligible. Even if a mud cake is built, however, this overpressure may still exist at the time of the pressure measurement. This effect is called supercharging and should not be confused with capillary or intrinsic formation over-pressures. Such confusion is common since supercharging is similar to capillary over-pressure effects in the sense that both are inversely related to effective permeability. As a consequence of supercharging, all permeable zones are locally, and often temporarily, overpressured by the invading filtrate. Levels affected by supercharging in either the oil or the water zones will appear to the right of the expected formation pressure line, with gradients tending to be more scattered as the mobility of the measured phase decreases. In capillary transition zones, where often both oil and water phases are mobile, the total mobility is reduced, leading to an increase in the possibility of supercharging. As the pressure difference between the mud column and the formation increases with depth, and with everything else being equal, supercharging could possibly lead to an apparent increase in gradient. The primary factors affecting supercharging are the degree of pressure differential across the sand-face, the extent of mud cake build-up and its effectiveness in preventing filtrate-fluid loss into the formation, and the total mobility of the formation. Fergusson and Koltz (1954) defined three stages of mud filtrate invasion. These are the initial spurt loss leading to a rapid buildup of mud cake; the dynamic filtration, which occurs when the mud cake attains an equilibrium thickness and while mud is still circulated; and the static filtration which takes place after circulation of the mud has ceased. Halford (1983) reviewed the processes of mud filtrate invasion and made some conclusions, which can be summarized as follows. Firstly, if filtration is governed by the mud cake, which is the case except in very low permeability formations, then after several hours, the dynamic rate converges to a constant rate equilibrium rate. Secondly, after about fifteen hours of static filtration, which is typical of the condition wherein formation tester surveys are run, that static loss rate may be considered constant. Thirdly, oil-based muds show lower dynamic and static loss rates compared to water-based muds. Despite this latter conclusion, oil-based muds do not always form mud cakes, and dynamic filtrate invasion continues even during the wireline formation tester survey. In extreme cases, even moderately high permeability zones may appear supercharged at the time of the survey. To reduce the effects of supercharging, the formation tester survey should be run as late as possible after a circulation of the well in order to maximize the time-dependent decay of the relatively large dynamic filtrate loss-rate. In fact, the usefulness of the widely used practice of routinely running wiper trips prior to wireline formation tester surveys is rather dubious, since these trips often only serve to stir up the mud column and scrape off the mud cake, leading to increased filtration rates, increased supercharging effects, and greater chances of getting differentially stuck. The true formation pressure can be obtained by applying a correction technique to correct the effects of supercharging in low permeability formation. This method can be applied by measuring Pbh wireline borehole pressure and Pwf wireline formation pressure more than two times at the same point. By plotting Pwf versus Pbh, the true formation pressure is obtained at the point where a line drawn through the data crosses a 45 o line with Pbh =Pwf as shown in Fig.14. This technique was applied to correct the effect of supercharging in a low-permeability formation. Fig.15 shows the pressure profile obtained with the formation tester tool. Two pretest points were identified as supercharged. The pretests were repeated after applying 300 at the mud column. The measured pressures changed at both depths, and the correction was computed according to the technique described above.

6 H. ELSHAHAWI, M. SAMIR, K. FATHY SPE 63075 Using NMR to Correct for Wettability and Capillary Pressure Effects One possible method of correcting for wettability and capillary pressure effects on wireline formation tester pressures is to construct the Leverett J-function (Leverett, 1941) for the reservoir from core samples and transform it to reservoir fluid conditions. The Leverett J-function is, defined as: J(Sw) = (6.848 Pc (k/φ) lab )/(σ cosθ) lab = (6.848 Pc (k/φ) res )/(σ cosθ) res (12) Lab (core) capillary pressure data can thus be translated to reservoir conditions as follows: Pc) res = Pc) lab ((φ res k lab )/(φ lab k resevoir )) x((σcosθ) res /(σ cosθ) lab ) (13) It is possible to correct the measured formation pressure at each point by adding (or subtracting) the capillary pressure corresponding to the value of invaded zone saturation (S xo ) measured at that point (Awad, 1982) such that P corrected = P measured + P c (S xo ) (14) If a nuclear magnetic resonance (NMR) log is available, then the downhole capillary pressure correction can be computed directly. The NMR signal originates from the hydrogen nuclei present in the pore fluids. The initial signal amplitude provides total porosity while the signal relaxation or decay rate provides indication of pore size. Under some plausible assumptions, the transverse relaxation time of the NMR signals from fluids in an individual pore is proportional to its surface-to-volume ratio. This transverse relaxation time is termed T2-deacy. The total NMR signal, being the superposition of signals from a distribution of individual pores, is simply a summation of the individual exponential decays. A T2-distribution is displayed by plotting the amplitudes versus their associated relaxation times on a logarithmic scale. The computed T2-distribution is used to compute logs of NMR porosities, free fluid porosities, capillary bound fluid porosities and logarithmic mean relaxation times. In a rock where the saturating phase is the same as the wetting phase, T2-relaxation will relate directly to pore size. Providing T2-relaxation takes place within the fastdiffusion limit, and the transverse surface relaxivity (ρ 2 ) is known, T2 can be converted to pore size and capillary pressure using the following process (Marschall et al, 1995): 1) Convert T2 to pore size (Fig. 16) using data obtained from core analysis (e.g. laboratory NMR vs Mercury Injection Capillary Pressure, MICP) or from published scaling factors such as those found in the NMR Sandstone and Carbonate Rock Catalogs, if core data is not available (Kleinberg, 1996). 2) Convert pore size to a cumulative plot by summing NMR non-shale porosity (φ Effective ) such that φ at max pore diameter=0, and φ at min pore diameter=(φ Effective ). Whenever small pores (short T2's) can be shown to relate to clay-bound water, they should be removed from the total NMR porosity before summing up, otherwise clay-bound water will be treated as capillary bound water in the conversion to Pc. 3) Convert pore size to capillary pressure using equation 15 (Fig. 17) Capillary pressure can be computed for dual combinations of gas/air/water/oil/mercury using appropriate interfacial tension and contact angle constants. The number of pressure steps in the T2-derived Pc curve depends on the number of points or bins used in the inversion of the time-domain data (echo train), which in turn is limited by the signal to noise ratio. Core NMR experiments typically achieve S/N levels > 100/1, which allows 50 to 100 points to be used in the inversion. Log NMR experiments typically achieve S/N levels <10/1, which allows between 10-30 points to be used in the inversion. Stacking the log data will increase S/N and hence the number of points used in the inversion, but stacking will also reduce the vertical resolution of the measurement. In wells drilled with oil-based mud (), or where there is a native oil remaining in the flushed zone, the T2 distribution will contain a combination of pore size and bulk fluid information. In water-wet rocks, the lower mode at short T2s normally represents bound water (unless gas or heavy oil is present) and contains pore size information because water is in contact with the pore walls. On the other hand, the mode at long T2s represents oil from the filtrate, formation oil, or a combination of these and contains bulk fluid information because the oil is not in contact with the pore walls. Under these conditions, only the early part of the T2 distribution can be converted to pore size, and hence Pc. Generating the complete Pc curve (i.e. Sw=0-1) requires extrapolation of the T2 distribution out to long T2s. Volikitin et al. (1999) presented a method for completing the T2 distribution in rocks with partial water saturation. Their method uses a predicted mean T2 value obtained from an empirical relationship between geometric mean T2 and Swirr. A moveable water spectrum is then added to the T2 distribution such that the sum of amplitudes equals porosity, and the resultant mean T2 value matches the predicted mean T2 value. Thomeer (1960) and Swanson (1981) showed the maximum turning point on a hyperbola fitted through an air/mercury capillary pressure curve (log Pc vs log Sw expressed as % bulk volume) could be used to predict permeability. Based on this work, Lowden (2000) developed a method predicting the T2 values at long times by fitting a hyperbola through the early times. The method involves converting T2 and cumulative NMR porosity to log scales with 1/T2 ( Pc) on the Y-axis and NMR porosity ( Sw) on the X-axis Fig. 18a. The data is normalized such that they both sum up to unity so that it is in a form suitable for fitting a rectangular hyperbola.

SPE 63075 CORRECTING FOR WETTABILITY AND CAPILLARY PRESSURE EFFECTS ON FORMATION TESTER MEASUREMENTS 7 A curve is then fitted through the data ensuring the best match occurs at short T2s equation 16. The shape of the curve is adjusted by changing the point where the asymptotes to the curve intercept the X and Y axes, and by adjusting the exponent a for values of Y ranging from 0 to 1. The values of X and Y for the predicted curve are then converted to conventional units, Sw (%), and Pc (psi), to generate the complete Pc curve (Fig. 18b). A drawback of this curve fitting method compared to the method of Volikitin is that it does not take into account fluid lining the walls of large pores. Porelining fluid increases amplitude (porosity) at short T2s, and in order to generate a correct Pc curve, this additional porosity should be redistributed to long T2s (=large pores). If porelining fluid is expected, the fitted curve should be shifted just below the actual curve, thus redistributing the pore lining fluid to longer T2s since the sum of porosities is always maintained at the same value. Using the MDT to Overcome Wettability and Capillary Pressure Effects The state of the art Modular Dynamics Tester MDT offers convenient solutions to overcome the wettability and capillary pressure effects described earlier. The MDT can be equipped with a probe module (similar to RFT probe) and with an inflatable dual packer module simultaneously (Fig. 19). More information about MDT can be found in Zimmerman et al. (1998). The measurement of the formation pressure with MDT single probe follows the same principle as the RFT, however, it has more advanced features. The MDT probe reading will be affected by capillary pressure in a similar way as the RFT when carrying out a standard pretest. The ability to pump out mud filtrate enables the measurement of formation pressure before and after capillary pressure effect removal, and hence allows the estimation of the amount of capillary pressure. The same facility also minimizes supercharging and reduces its disturbing effect on the measured gradients. On the other hand, the flow identification abilities of the MDT such as the flow line resistivity and the optical fluid density can indicate the type and quantity of mud filtrate as well as the moveable reservoir fluid, which would help establish and confirm and correct the measured pressure gradient. The dual packer module is made of two inflatable rubber elements. Each element is about one meter and the distance between them is about one meter. The two elements are inflated in with a downhole pump out module isolating onemeter or longer of the formation between the two elements. The same downhole pump is activated to remove the mud filtrate and to pump it to the borehole, until formation fluid is sensed via an optical fluid analyzer. Once the pump outs is stopped, a build-up is initiated to measure the "true" formation fluid phase directly. This pressure will be little affected by capillary pressure effects since mud filtrate is removed before prior to making the measurement. The dual packer arrangement provides the ability to test formations too tight or too unconsolidated to respond to the standard probe. An example is shown in Fig. 20. Without pumping out, the single probe measures the mud filtrate pressure. Assuming a waterwet system, the water base mud filtrate pressure (wetting phase) can be expected to be lower than the gas pressure (nonwetting phase) by the amount of capillary pressure. As expected, the single probe data reads less than the true formation pressure in the gas zone due to capillary pressure effects. The dual packer, on the other hand, yields what can be considered as true pressure because its measurements were made after the mud filtrate had been pumped out for nearly 20 mins at each depth. Note also that the FWL measured by the single probe is displaced upward when compared to the dualpacker-indicated contact. This situation is very similar to the hypothetical one depicted in Fig. 9(a). Correcting for Wettability and Capillary Pressure Effects in the Absence of NMR and MDT Masurements There are many cases in which neither core data nor NMR data is available, and in which MDT could not be run for whatever reason. In these cases, it is possible to derive a pseudo-drainage capillary curve similar to fig. 10 and 11 by plotting the height above the OWC in the transition zone vs. the water saturation as computed from the openhole logs. This type of correction generally results in adjustment of the gradient towards the correct direction but may result in large scatter. This is due to the simplicity of this type of correction that fails to take into account the vertical flow occurring within the invaded zone as detailed earlier. It is important to realize that without correction, the intersection of the hydrostatic gradients in a well drilled with in a waterwet reservoir will indicate the top of the transition zone rather than the actual FWL. This is a potentially very useful measurement in its own right as it indicates the highest producible water level. Conclusions 1. Wireline formation testers measure the pressure of the continuous phase present in the invaded region. 2. Conventional interpretation techniques assume that this pressure is identical to the pressure of the formation fluid, implying that the wireline tester measurement is unaffected by the invasion process. This in not true as proven by many field examples, particularly in. 3. The concepts of free fluid level, fluid contacts, rock wettability, and pore fluid pressures are intimately related. 4. The effect of wettability and capillary pressure will make the measured formation pressure either too high or too low depending on the specific wetting fluid-drilling mudformation fluid combination. This will result in shifted gradient lines, altered gradient slopes, or greater scatter. 5. In a water-wet medium, the FWL is expected to occur below the OWC, while in an-oil wet medium, the FWL is expected to occur above the FWL.

8 H. ELSHAHAWI, M. SAMIR, K. FATHY SPE 63075 6. In a water-wet medium, the measured contact will generally appear too high compared to the FWL, while in an oil-wet medium, it will generally appear too low compared to the FWL. In the latter case, the measured contact will indicate the highest producible water level. 7. Capillary pressure effects can be corrected for, provided core and intermediate zone saturation data are available. NMR data may supplement or replace these sources. 8. The MDT offers several features that reduce uncertainties arising from capillary and supercharging effects. These include the ability to pump out mud filtrate and formation fluid. Overcoming capillary pressure affects is possible by removing mud filtrate before taking the measurement. References Awad, M.: Phase Pressure Measurement by the RFT in the Hydrocarbon Zone, prepared for the 2 nd Wireline Interpretation Symposium, Ridgefield, 12-15 July, 1982. Chilingarian, G.V. and Chen, T.F.: Some Notes on Wettability and Relative Permeabilities of Carbonate Rocks, Energy Sources, Vol.7, No.1 (1983), pp. 67-75. Elshahawi, H., Samir, M. and Fathy, K.: Wettability and Capillary Pressure Effects on Wireline Formation Tester Measurements, SPE Annual Technical Conference and Exhibition held in Houston, Texas, Paper No. 56712, 3 6 October 1999. Hiekal, S., Kamal, M., Hussein, A and Elshahawi, H.: Time Dependence of Swept Zone Remaining Oil Saturation In a Mixed-Wet Reservoir, Paper presented at SPWLA Japan, 24-25 September, 1998. Hirasaki, G.J.: Dependence of Waterflood Remaining Oil Saturation on Relative Permeability, Capillary Pressure, and Reservoir Parameters in Mixed-Wet Turbidite Sands, SPE Reservoir Engineering, May 1996. Kaminsky, R. and Radk, C.J.: water Films, Asphaltenes, and Wettability Alteration, SPE/DOE IOR Symposium, Tulsa, Oklahoma, Paper No. 39087, 19-22 April 1998. Kleinberg, R.L., 1996. Utility of NMR T2 Distributions, Connection with Capillary Pressure, Clay Effect, and Determination of the Surface Relaxivity Parameter rho2. Magnetic Resonance Imaging 14, 761-767. Leverett, M.C.: Capillary Behaviour in Porous Solids, Trans AIME (1941), Vol. 142. Lowden, B.: Some Simple Methods for Refining Permeability Estimates from NMR and Generating Capillary Pressure Curves, Published in DiaLog (The On-line Newsletter of the London Petrophysical Society), Vol. 8, Issue I, March 2000. Marschall, D., Gardner, J.S., Mardon. D., and Coates, G.R., 1995. Method for correlating NMR relaxometrry and Mercury Injection Data. Trans. International Symposium of the SCA, San Fransisco, California. Sept. 12-15, 1995. Purcell, W.R., 1949. Capillary Pressures - Their Measurement Using Mercury and the Calculation of Permeability Therefrom. Pet. Trans. AIME. 186, 39-48. Phelps, G.D., Stewart, G., and Peden, J.M.: The Analysis of the Invaded Zone Characteristics and Their Influence on Wireline Log and Well Test Interpretation, SPE 13287 (1984). Salathiel, R.A.: Oil Recovery by Surface Film Drainage In Mixed-Wettability Rocks, Journal Schlumberger: Middle East Well Evaluation Review, November 7, 1989, pp. 36-39. Swanson, B.F., 1981. A Simple Correlation Between Permeabilities and Mercury Capillary Pressures. Jour. Pet. Tech. Pp 2498-2504. The NMR Sandstone Rock Catalogue. 1997. Applied Reservoir Technology Ltd. The NMR Carbonate Rock Catalogue. 1999. Applied Reservoir Technology Ltd. Volokitin, Y., Looyestijn, W., Slijkerman, W., and Hofman, J., 1999. Constructing Capillary Pressure Curves From NMR Log Data in the Presence of Hydrocarbons. Trans 40th Annual Logging Symposium, SPWLA, Oslo, Norway, paper KKK. Zimmerman,T., Maclnnis, J, Hoppe, J. and Pop, J., 1998: Application of Emerging Wireline Formation Testing Technologies Trademark of Schlumberger

SPE 63075 CORRECTING FOR WETTABILITY AND CAPILLARY PRESSURE EFFECTS ON FORMATION TESTER MEASUREMENTS 9 Oil Water Fig.4:-In smaller grains/pores, the water film covers the grain surfaces completely, thus maintaining those grains water-wet. Fig.1-Schematic of Pore Cross-section in a water-wet porous media, (grains rock are surrounded by thin film of brine and are not contacted by oil). Solid r 1 r 2 Solid Oil Water Fig.5-Radii of curvatures for pendular rings around a spherical sand grain junction. Fig.2-Schematic of Pore Cross-section in an oil-wet porous media, (grains are surrounded by thin film of oil and are not contacted by water). Fig.3-In larger grains/pores, the water film ruptures, and oil and rock in direct contact, locally altering wettability to preferentially oil-wet. Fig.6-Drainage and imbibition capillary pressure curves for a water-wet system.

10 H. ELSHAHAWI, M. SAMIR, K. FATHY SPE 63075 1-r 1-c r c Figure 7-a: Saturation Profile, Water Zone & Water Wet Figure 7-b: Saturation Profile, Water Zone & Water Wet 1-r 1-c r c Figure 7-c: Saturation Profile, Oil Zone & Water Wet Figure 7-d: Saturation Profile, Oil Zone & Water Wet 1-r 1-c r c Figure 7-e: Saturation Profile, Water Zone & Oil Wet. Figure 7-f: Saturation Profile, Water Zone & Oil Wet. 1-r 1-c r c Figure 7-g: Saturation Profile, Oil Zone & Oil Wet. Figure 7-h: Saturation Profile, Oil Zone & Oil Wet

SPE 63075 CORRECTING FOR WETTABILITY AND CAPILLARY PRESSURE EFFECTS ON FORMATION TESTER MEASUREMENTS 11 no oil phase P o P w P w Figure 8-a: Capllary Pressure Profile, Water Zone & Water Wet Figure 8-b: Capllary Pressure Profile, Water Zone & Water Wet P o P w P w Figure 8-c: Capllary Pressure Profile, Oil Zone & Water Wet Figure 8-d: Capllary Pressure Profile, Oil Zone & Water Wet P w P w P o P o Figure 8-e: Capllary Pressure Profile, Water Zone & Oil Wet Figure 8-f: Capllary Pressure Profile, Water Zone & Oil Wet P w no water phase P o P o Figure 8-g: Capllary Pressure Profile, Oil Zone & Oil Wet Figure 8-h: Capllary Pressure Profile, Oil Zone & Oil Wet

Depth Depth Depth Depth 12 H. ELSHAHAWI, M. SAMIR, K. FATHY SPE 63075 Water Base Mud Oil Base Mud Water Base Mud Oil Base Mud Depth Depth True Pressure Measure Pressure True Pressure Measure Pressure Wireline tester interpretation Free water level Free water level Wireline tester interpretation Pressure Pressure Pressure Pressure Fig.9-a: Capillary pressure effects on pressure measurement in a water wet system Fig.9-b: Capillary pressure effects on pressure measurement in an oil wet system P c irreducible water saturation, water may become disconnected Oil Transition zone FWL OWC Capillary threshold Water 0 0 (%) 100 Reservoir Capillary curve Fig.10-Fluid pressure, capillary pressure, and saturation distribution a water-wet reservoir Oil irreducible water saturation, water may become disconnected P c FWL 0 (%) 100 Water OWC Transition zone Reservoir Capillary curve Fig.11-Fluid pressure, capillary pressure, and saturation distribution an oil-wet reservoir

SPE 63075 CORRECTING FOR WETTABILITY AND CAPILLARY PRESSURE EFFECTS ON FORMATION TESTER MEASUREMENTS 13 Saturations and Porosity, (Fraction) 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90 1.00 Saturations and Porosity, (Fraction) 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90 1.00-4750 -4800 FWL OOWC -4800 Swoh OOWC Depth, TVDss, ft -4850-4900 φ oh Depth, TVDss, ft -4850-4900 φ oh FWL -4950-4950 -5000-5000 2200 2250 2300 2350 2400 2450 2500 2200 2250 2300 2350 2400 2450 Pressure (PSIA) Pressure (PSIA) Oil Water Sw-A1 foh Linear (Water) Linear (Oil) Oil Water Sw-A1 foh Linear (Water) Linear (Oil) Fig.12-Example of pressure behavior in oil-wet Nubian Sandstone rocks from well L7. Fig.13-Example of pressure behavior in water-wet Nubian Sandstone rocks from well A1. X200 X220 Wireline formation pressure P fw P fw = P bh Data Depth, ft X240 X260 X280 X300 corrected points Supercharged P bh Wireline borehole pressure X320 X670 X680 X690 X700 X710 X720 Pressure, psi Fig.15: Pressure profile showing how two supercharged points fall into the formation gradient line after correction. Fig.14: Wireline formation pressure plotted against wellbore pressure.

14 H. ELSHAHAWI, M. SAMIR, K. FATHY SPE 63075 Fig. 16 : T2 distribution for brine-saturated core plug converted to pore size using a scaling factor (~rho2) obtained from MICP analysis conducted on an end trim from the same plug Fig. 17: A T2 derive air/mercury capillary pressure curve obtained for a brine-saturated core plug. The predicted Pc curve is plotted against MICP data for the same sample. The red circle shows the threshold pore size controlling flow. Fig. 18 a-b: Illustration of the method used to generate a capillary pressure curve from NMR data when part of the signal is dominated by bulk fluid response. Panel A shows an hyperbolic curve fitted through the short T2s. Panel B shows the complete Pc curve obtained from the equation for the fitted curve.