MATERIAL BALANCE EQUATION

Slides:



Advertisements
Similar presentations
QUICK QUIZ 22.1 (end of section 22.1)
Advertisements

DESIGNING A WATERFLOOD Designing a water flood involves both technical and economic consideration. Economic analysis are based on estimates of water.
Title Petrophysical Analysis of Fluid Substitution in Gas Bearing Reservoirs to Define Velocity Profiles – Application of Gassmann and Krief Models Digital.
Gas Material Balance.
Technical Aspects of Waterflooding October 23 rd Long Beach, California Baldev Singh Gill Oil Operations Bureau Department of Gas and Oil.
Well Control Gas Solubility.
Introduction to Petroleum Production Engineering
Forensic Analysis Why Did This Field Die? Presented at Western Australia Section of SPE June 19, 2012 Perth, Australia Dr. Bill Cobb William M. Cobb &
PETE 310 Lectures # 32 to 34 Cubic Equations of State …Last Lectures.
17 Chemical Equilibrium.
Reservoir performance prediction methods
Chapter 2 Simple Thermodynamics Systems
Chapter 2 Pressure-Volume-Temperature for Oil
CE 230-Engineering Fluid Mechanics Lecture # 18 CONTINUITY EQUATION Section 5.3 (p.154) in text.
Oil Field Manager ~ Presentation
The Straight-Line Solution Method to the MBE
STRAIGHT LINE REPRESENTATION of the MATERIAL BALANCE EQUATION
OIL RECOVERY MECHANISMS AND THE MATERIAL BALANCE EQUATION
Lecture # 15 Properties of Black Oils Definitions (pages )
Chapter 10 – Properties of Black Oils - Reservoir Fluid Studies
Material Balance for Oil Reservoirs
Reservoir Performance Curves
OilTank OilTank uses reservoir pressure and produced volumes of oil, water and gas from individual wells and determines the IOIP using volumetric and.
COMPRESSIBILITY OF RESERVOIR ROCKS.
4. Phase Relations (Das, Chapter 3) Sections: All except 3.6
REVIEW OF BASIC STEPS IN DERIVATION OF FLOW EQUATIONS NTNU Author: professor Jon Kleppe Assistant producers: Farrokh Shoaei Khayyam Farzullayev.
OIL RECOVERY MECHANISMS AND THE MATERIAL BALANCE EQUATION
17.4 State Variables State variables describe the state of a system
Reserve Evaluation for Enhance Oil Recovery Purposes Using Dynamic Reserve Evaluation Model Woodside Research Facility GPO Box U 1987 Perth West Australia.
UNDERSATURATED OIL-GAS SIMULATION IMPES SOLUTION
Reservoir Simulation Study
Chapter 3 Material Balance Applied to Oil Reservoirs
Material Balance Equations Author: Jon Kleppe, NTNU Assistant producer: Vidar W. Moxness The Statfjord area in the North Sea. Source: Statoil.
Fluid Saturation Introduction
Dr.Mostafa Mahmoud Kinawy
Base Case Simulation Model
1 SPE Distinguished Lecturer Program Primary funding is provided by The SPE Foundation through member donations and a contribution from Offshore Europe.
1 Chapter 7. Applications of the Second Law. 2 Consider entropy changes in various reversible (!!!) processes We have: (a) Adiabatic process Hence a reversible.
Applications of Intermolecular Potentials. Example 1. A gas chromatograph is to be used to analyze CH 4 -CO 2 mixtures. To calibrate the response of the.
Pressure – Volume – Temperature Relationship of Pure Fluids.
A more appropriate definition of K (for the same chemical reaction discussed previously) is With this definition, each concentration term is divided by.
1 Second Law of Thermodynamics - Entropy. 2 Introduction The second low often leads to expressions that involve inequalities.
Volume and Moles. Avogadro’s Law  When the number of moles of gas is doubled (at constant temperature and pressure, the volume doubles.  The volume.
Lecture 11 Oilfield Development
Prediction of Solution Gas drive reservoir performance.
Day 1 Session 1 Day 1Introductions Economics and accounting Building a basic project cash flow Economic and risk indicators The.
10/18/20161 Reserves Estimation and Classification.
Fluid Sampling and Hydrates. Group Members:  Mohammad Afaq Akbar(23)  Nisar Ali(39)  Saif Ur Rehman(43)  Shahnawaz(46)  Uzair Ahmed Khan(49)
RESERVOIR ENGINEERING
Gas Condensate PVT – What’s Really Important and Why?
Water Drive Reservoir Performance Prediction
461 PE Reservoir Engineering
Gas Properties & PVT Tests
5. WEIGHT VOLUME RELATIONSHIPS
Gas Condensate PVT A worked example to estimate
PETE 323-Reservoir Models
Gas Condensate PVT A worked example to estimate
e-notes (c) Curtis H. Whitson, Robert E. Mott
The material balance for simple depletion defines the relation between average reservoir pressure and (a) cumulative wellstream produced, (b) cumulative.
CCE and CVD results The usual PVT measurements on gas condensates are
Fluid Saturations Introduction
Properties of crude oil
Introduction to Effective Permeability and Relative Permeability
CCE and CVD results The usual PVT measurements on gas condensates are
Natural Gas Production
A. Dollari*, Ch. Chatzichristos and A. G. Yiotis
Thermodynamics AP Physics B.
e-notes (c) Curtis H. Whitson, Robert E. Mott
Gas Condensate PVT A worked example to estimate
The material balance for simple depletion defines the relation between average reservoir pressure and (a) cumulative wellstream produced, (b) cumulative.
Presentation transcript:

MATERIAL BALANCE EQUATION

THE MATERIAL BALANCE EQUATION The material balance equation (MBE) is one of the basic tools of reservoir engineers for interpreting and predicting reservoir performance. The MBE can be used to: • Estimate initial hydrocarbon volumes in place • Predict future reservoir performance • Predict ultimate hydrocarbon recovery under various types of primary driving mechanisms

THE MATERIAL BALANCE EQUATION The equation can be written on volumetric basis as: Initial volume = volume remaining + volume removed Before deriving the material balance, it is convenient to denote certain terms by symbols for brevity. The symbols used conform where possible to the standard nomenclature adopted by the Society of Petroleum Engineers.

THE MATERIAL BALANCE EQUATION Terms Symbols Initial reservoir pressure, psi Pi Change in reservoir pressure = pi − p, psi Δp Bubble point pressure, psi pb Initial (original) oil in place, STB N Cumulative oil produced, STB Np Cumulative water produced, bbl Wp Cumulative gas produced, scf Gp Cumulative gas-oil ratio, scf/STB Rp Instantaneous gas-oil ratio, scf/STB GOR Initial gas solubility, scf/STB Rsi Gas solubility, scf/STB Rs

THE MATERIAL BALANCE EQUATION Terms Symbols Initial oil formation volume factor, bbl/STB Boi Oil formation volume factor, bbl/STB Bo Initial gas formation volume factor, bbl/scf Bgi Gas formation volume factor, bbl/scf Bg Cumulative water injected, STB Winj Cumulative gas injected, scf Ginj Cumulative water influx, bbl We Ratio of initial gas-cap-gas reservoir volume to initial reservoir oil volume , bbl/bbl m Initial gas-cap gas, scf G Pore volume, bbl P.V

THE MATERIAL BALANCE EQUATION Terms Symbols Water compressibility, psi−1 cw Formation (rock) compressibility, psi−1 cf Gas formation volume factor of the gas cap gas ,bbl/scf Bg c Gas formation volume factor of the solution gas ,bbl/scf Bg s cumulative gas production from gas cap Gpc cumulative gas production from solution gas. Gps

Derivation of the oil MBE Let us define the following quantities: N= the initial oil in place(STB) = VBO (*1-Swi) /Boi Gas cap expansion = New gas cap volume - original gas cap volume New gas cap volume = (G-Gpc) B gc Original gas cap volume = G x Bgci (1)Gas cap expansion = (G-Gpc) B gc - G x Bgci

THE MATERIAL BALANCE EQUATION (2) Remaining release gas = original soluble gas – remaining soluble gas – cumulative produced gas = [N Rsi -(N-Np)Rs -Gps] Bgs (3) Remaining oil volume = (N-Np) Bo (4) Net water influx = (We -Wp Bw) (5) Rock and water expansion is neglected in the presence of gas.

THE MATERIAL BALANCE EQUATION Condition I Condition II Pressure = Pi P<Pi NP = Zero NP = +ive GP = Zero GP = +ive WP = Zero WP = +ive p Condition I Condition II Pressure = Pi P<Pi NP = Zero NP = +ive GP = Zero GP = +ive WP = Zero WP = +ive

THE MATERIAL BALANCE EQUATION Now, by equating the initial conditions , to the final conditions resulting from a finite pressure drop: N Boi = (N-NP) Bo + [(G-GPC) Bgc -G Bgci] +[NRsi – -(N-NP)Rs–GPS ]Bgs+(We -WPBw) N Boi = NBo – NPBo + G Bgc- GPC Bgc - G Bgci + N RSi Bgs - N RS Bgs+ NP Rs Bgs - GPS Bgs + + (We-WP Bw)

THE MATERIAL BALANCE EQUATION NBoi-NBo-NRsi Bgs +NRsBgs=-NPBo+NPRsBgs - GPSBgs+ +GBgc-GPcBgc-GBgci+(We-WPBw) N[Boi-Bo-RsiBgs+RsBgs] =Np[-Bo+RsBgs]-Gps Bgs+GBgc- Gpc Bgc-GBgci+(We-WpBw) But : Bgc = Bgs = Bg and Bgci = Bgsi Bgi N[Boi-Bo+(-Rsi+Rs)Bg] = Np[-Bo+RsBg]-Gps Bg+GBg –GpcBg-GBgi+(We-WpBw)

THE MATERIAL BALANCE EQUATION Np[Bo-RsBg]+(Gps+Gpc)Bg =N[Bo-Boi+(Rsi-Rs)Bg]+ +G(Bg-Bgi)+(We-WpBw) But : (Gpc+Gps)Bg = GpBg and Rp = Gp/Np and Bt = Bo+(Rsi-Rs)Bg Therefore , Np [ Bo - RsBg]+Gp Bg =N[(Bo-Boi)+(Rsi-Rs)Bg] + G(Bg-Bgi)+(We-WpBw)

THE MATERIAL BALANCE EQUATION By adding and subtracting RsiBg –RsiBg: Np [Bo -(Rsi-Rs)Bg]- RsiBg]+Gp Bg =N[(Bo Boi)+ + (Rsi-Rs)Bg]+ G(Bg-Bgi)+(We-WpBw) Np[Bt-RsiBg]+Np Rp Bg =N[(Bo-Boi)+(Rsi-Rs)Bg] + G(Bg-Bgi)+(We-WpBw) Np[Bt – Rsi Bg + Rp Bg]= N[(Bo - Boi)+(Rsi-Rs) Bg] + G(Bg-Bgi) +(We-WpBw)

THE MATERIAL BALANCE EQUATION And finally : Np [Bt + (Rp - Rsi) Bg] = N (Bt – Bti ) + mNBoi(Bg - Bgi) + (We-WpBw) …..(1) Bgi

THE MATERIAL BALANCE EQUATION Np [Bt +(Rp - Rsi) Bg]=N (Bt – Bti )+mNBoi(Bg - Bgi) + (We-WpBw) Bgi Cumulative oil Depletion Drive Gas cap drive Water drive withdrawal mechanism mechanism mechanism And this is the generalized material balance equation for combination drive reservoir neglecting the rock and connate water expansion.

THE MATERIAL BALANCE EQUATION N ( B t – B t I ) = D.D.I Np[Bt+(Rp-Rsi)Bg] (m N Boi/ Bgi) (Bg - Bgi) = GCDI Np [Bt + (Rp - Rsi) Bg] ( We- Wp Bw) = WDI

THE MATERIAL BALANCE EQUATION Driving indices : The driving index of any mechanism represents the fractional contribution of the total oil withdrawal produced by that mechanism.

THE MATERIAL BALANCE EQUATION Driving indices Driving indexes in a combination-drive reservoir

Driving indices

THE MATERIAL BALANCE EQUATION Several of the material balance calculations require the total pore volume (P.V) as expressed in terms of the initial oil volume N and the volume of the gas cap. The expression for the total pore volume can be derived by conveniently introducing the parameter m into the relationship as follows:

THE MATERIAL BALANCE EQUATION Change in Pore Volume Due to Initial Water :and Rock Expansion

THE MATERIAL BALANCE EQUATION where ΔV represents the net changes or expansion of the material as a result of changes in the pressure. Therefore, the reduction in the pore volume due to the expansion of the connate water in the oil zone and the gas cap is given by:

THE MATERIAL BALANCE EQUATION Connate water expansion = [(pore volume) Swi] x cw Δp Substituting for the pore volume (P.V) with Equation 11-1 gives:

THE MATERIAL BALANCE EQUATION The total volume of the hydrocarbon system is then given by: Initial oil volume + initial gas cap volume = (P.V)(1− Swi) N Boi + m N Boi = (P.V) (1 − Swi) or

THE MATERIAL BALANCE EQUATION Similarly, the reduction in the pore volume due to the expansion of the reservoir rock is given by:

THE MATERIAL BALANCE EQUATION The total pore volume occupied by the two injected fluids is given by: Total volume = Ginj Bginj +Winj Bw

THE MATERIAL BALANCE EQUATION The most general form of Material Balance Equation is Np [Bt + (Rp - Rsi) Bg] = N (Bt – Bti ) + mNBoi(Bg - Bgi) + (We-WpBw) + Bgi + (Cf +CwSw) (NBoi ) (Pi-P) ……(2) (1-Swi )

THE MATERIAL BALANCE EQUATION Case (1): Water drive reservoir: A-Below the bubble point pressure: The driving mechanisms involved are : 1.Water drive mechanism 2.Depletion drive mechanism The material balance equation is : Np [Bt + (Rp - Rsi) Bg]=N(Bt – Bti ) +(We-WpBw) ………………..(3)

THE MATERIAL BALANCE EQUATION B) Above the bubble point pressure: The driving mechanisms involved are : 1.Water drive mechanism 2.Depletion drive mechanism and 3.Rock and water expansion mechanism. The material balance equation is : Np Bo = N (Bo – Boi ) + ( We –Wp Bw ) + (Cf +CwSw) (NBoi ) (Pi-P )..................(4) (1-Swi)

THE MATERIAL BALANCE EQUATION (Since Rp = Rsi = Rs = Constant) . Effective oil compressibility : Co = -  Vo 1 = Bo-Boi 1 Vo P Boi (Pi-P) Bo - Boi = Co Boi (Pi-P) Substitute this value in equation (4): Np Bo = N Co Boi (Pi-P) + ( We –Wp Bw ) + (Cf +CwSw) (NBoi ) (Pi-P ) ……………………….(5) (1-Swi)

THE MATERIAL BALANCE EQUATION Np Bo + Wp Bw = N Boi (Pi-P) Cf +CwSw + Co + We ( 1-Swi ) ……………………….………………………..………………………..(6) Np Bo + Wp Bw = N Boi (Pi-P) Cf +CwSw +Co So (1-Swi ) + We …....……………………………………………………...(7) Np Bo + Wp Bw = N Boi Ce (Pi-P) + We ……….(8)

THE MATERIAL BALANCE EQUATION Where : Ce = Cf + Cw Sw +So So 1-Swi Ce = effective oil compressibility.

THE MATERIAL BALANCE EQUATION Case (2): Gas cap drive reservoir: The driving mechanisms involved are : 1.Gas cap drive mechanism and 2.Depletion (solution gas) drive mechanism Np [Bt + (Rp - Rsi) Bg] = N (Bt – Bti ) + + mNBoi (Bg - Bgi) Bgi

THE MATERIAL BALANCE EQUATION Case (3): Depletion drive reservoir: A) Below the bubble point pressure: The driving mechanism involved is : Depletion (solution gas) drive mechanism only. The material balance equation is: Np [Bt + (Rp - Rsi) Bg] = N (Bt – Bti )

THE MATERIAL BALANCE EQUATION B-Above the bubble point pressure The driving mechanism involved is : Rock and fluid expansion only. The material balance equation is: Np Bo = N(Bo-Boi) + Cf +CwSw +Co So (1-Swi ) +N Boi ( Pi - P ) + We

THE MATERIAL BALANCE EQUATION Bo-Boi = Co Boi (Pi –P ) , finally: Np Bo = N Boi Ce P If there is water production :, the equation form becomes : Np Bo + Wp Bw = N Boi Ce P This is the material balance equation for depletion drive reservoir (DDR) producing above the bubble point pressure (under- saturated reservoir).

THE MATERIAL BALANCE EQUATION When the rock and water expansion mechanism cancelled. Therefore , the equation will be as follows: Np Bo = N (Bo - Boi ) Np Bo = N Bo - N Boi and therefore : (N – Np ) Bo = N Boi

THE MATERIAL BALANCE EQUATION this is the simplest form of the material balance equation which represents a depletion drive reservoir (DDR) producing above the bubble point pressure (under- saturated reservoir) neglecting the rock and water expansion mechanism. The last equation can be driven simply by considering the initial and remaining oil in-place only ( of course , in addition to the connate water).

THE MATERIAL BALANCE EQUATION