This document provides an overview of reservoir fluid properties, including crude oil, water, and gas properties. It discusses key properties such as formation volume factors, viscosity, surface tension, and gas solubility. It summarizes various empirical correlations used to estimate these properties based on temperature, pressure, oil composition and other factors. The document is from a course on reservoir fluid properties and focuses on definitions and methods for calculating important PVT properties.
2. 1. Crude Oil Properties:
A.
B.
C.
D.
Formation volume factor for P=<Pb (Bo)
Isothermal compressibility coefficient (Co)
Formation volume factor for P>Pb (Bo)
Density
3. 1. Crude Oil Properties:
A. Total formation volume factor (Bt)
B. Viscosity (μo)
a. Dead-Oil Viscosity
b. Saturated(bubble-point)-Oil Viscosity
c. Undersaturated-Oil Viscosity
C. Surface Tension (σ)
2. Water Properties
A.
B.
C.
D.
Water Formation Volume Factor (Bw)
water viscosity (μw)
Gas Solubility in Water (Rsw)
Water Isothermal Compressibility (Cw)
4.
5. Total Formation Volume Factor
To describe the P-V relationship of hydrocarbon
systems below their bubble-point pressure,
it is convenient to express this relationship
in terms of the total formation volume factor
as a function of pressure.
the total formation volume factor (Bt)
defines the total volume of a system
regardless of the number of phases present.
is defined as the ratio of the total volume of the
hydrocarbon mixture (i.e., oil and gas, if present),
at the prevailing pressure and temperature
per unit volume of the stock-tank oil.
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6. Two-Phase Formation Volume Factor
expression
Because naturally occurring hydrocarbon systems
usually exist in either one or two phases, the term
“two-phase formation volume factor” has become
synonymous with the total formation volume.
Mathematically, Bt is defined by :
above the Pb; no free gas exists
the expression is reduced to the equation that describes
the oil formation volume factor, Bo, that is:
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7. Bt and Bo vs. Pressure
A typical plot of Bt
as a function of
pressure for an
undersaturated
crude oil.
at pressures below
the Pb, the
difference in the
values of the two
oil properties
represents
the volume of the
evolved solution
gas as measured at
system conditions
per stock-tank
barrel of oil.
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8. Volume of the Free Gas at P and T
Consider a crude oil sample placed in a PVT cell at its
bubble-point pressure, Pb, and reservoir temperature.
Assume that the volume of the oil sample is sufficient
to yield one stock-tank barrel of oil at standard conditions.
Let Rsb represent the gas solubility at Pb.
If the cell pressure is lowered to p,
a portion of the solution gas is evolved and
occupies a certain volume of the PVT cell.
Let Rs and Bo represent the corresponding
gas solubility and oil formation volume factor at p.
the term (Rsb – Rs) represents
the volume of the free gas
as measured in scf per stock-tank barrel of oil.
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9. Bt Calculation
The volume of
There are several
the free gas
correlations that
at the cell conditions is
can be used to estimate
the two phase formation
(Vg)p,T [bbl of gas/STB of volume factor
when the experimental
oil] and Bg [bbl/scf]
data are not available;
The volume of
the remaining oil
three of these methods
at the cell condition is
are:
from the definition
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Standing’s correlations
Glaso’s method
Marhoun’s correlation
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10. Bt: Standing’s and
Whitson-Brule Correlation
for predicting Bt Standing (1947)
used a total of 387 experimental data points
to develop a graphical correlation
with a reported average error of 5%
In developing his graphical correlation, Standing
used a combined correlating parameter by:
Whitson and Brule (2000) expressed Standing’s
graphical correlation by:
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11. Bt: Glaso’s Correlation
Glaso (1980) developed
a generalized correlation for estimating Bt
The experimental data on 45 crude oil samples
from the North Sea.
a standard deviation of 6.54% for Bt correlation
Glaso modified Standing’s correlating parameter A* and
used a regression analysis model
with the exponent C given by:
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12. Bt: Marhoun’s Correlation
Marhoun (1988)
Based on 1,556 experimentally determined Bt
used a nonlinear multiple-regression model
to develop a mathematical expression for Bt.
an average absolute error of 4.11%
with a standard deviation of 4.94% for the correlation
The empirical equation is:
with the correlating parameter F given by:
a = 0.644516, b = −1.079340,
c = 0.724874, d = 2.006210,
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e = − 0.761910
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13.
14. Crude Oil Viscosity
Crude oil viscosity is an important physical property
that controls and influences
the flow of oil through porous media and pipes.
The oil viscosity
in general, is defined as
the internal resistance of the fluid to flow.
is a strong function of the T, P, oil gravity, γg, and Rs.
Whenever possible, should be determined
by laboratory measurements at reservoir T and P.
The viscosity is usually reported in standard PVT analyses.
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15. Crude Oil Viscosity Calculation
In absence of laboratory data, correlations, which
usually vary in complexity and accuracy depending
upon the available data on the crude oil, may used.
According to the pressure, the viscosity of crude
oils can be classified into three categories:
Dead-Oil Viscosity:
the viscosity of crude oil at atmospheric pressure
(no gas in solution) and system temperature.
Saturated(bubble-point)-Oil Viscosity:
the viscosity of the crude oil at the Pb and reservoir T
Undersaturated-Oil Viscosity:
the viscosity of the crude oil at a P above the Pb and reservoir T
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16. Estimation of the Oil Viscosity
Estimation of the oil viscosity at
P equal to or below the Pb is a two-step procedure:
Step 1. Calculate the viscosity of the oil without
dissolved gas (dead oil), μob, at the reservoir T
Step 2. Adjust the dead-oil viscosity to account for the
effect of the gas solubility at the pressure of interest.
At pressures greater than the Pb of the crude oil,
another adjustment step, i.e. Step 3, should be made
to the bubble-point oil viscosity, μob, to account for
the compression and
the degree of under-saturation in the reservoir.
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17. Methods of Calculating Viscosity of
the Dead Oil
Several empirical methods are proposed
to estimate the viscosity of the dead oil, including:
Beal’s correlation
The Beggs-Robinson correlation
Glaso’s correlation
Sutton and Farshad (1986) concluded that
Glaso’s correlation showed the best accuracy
of the three correlations.
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18. μod: Beal’s Correlation
Beal (1946) graphical correlation
for determining the viscosity of the dead oil
From a total of 753 values
for dead-oil viscosity at and above 100°F,
as a function of T and the API gravity of the crude
Standing (1981) expressed the proposed graphical
correlation in a mathematical relationship as follows:
μod = viscosity of the dead oil as measured
at 14.7 psia and reservoir temperature, cp
T = temperature, °R
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19. μod: The Beggs-Robinson Correlation
Beggs and Robinson (1975)
originated from analyzing 460 dead-oil viscosity
measurements.
An average error of −0.64% with a standard deviation of
13.53% was reported for the correlation when tested
against the data used for its development.
Sutton and Farshad (1980) reported an error of 114.3%
when the correlation was tested against 93 cases from
the literature.
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20. μod: Glaso’s Correlation
Glaso (1980) proposed a generalized mathematical
relationship for computing the dead-oil viscosity.
from experimental measurements on 26 crude oil
samples
The above expression can be used
within the range of 50–300°F for the system
temperature and 20–48° for the API gravity of the crude.
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21.
22.
23. Methods of Calculating
the Saturated Oil Viscosity
Several empirical methods are proposed to
estimate the viscosity of the saturated oil,
including:
The Chew-Connally correlation
The Beggs-Robinson correlation
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24. μob: The Chew-Connally correlation
Chew and Connally (1959) presented a graphical correlation
to adjust the dead-oil viscosity according to Rs at saturation
pressure. (from 457 crude oil samples)
Standing (1977) expressed the correlation:
μob = viscosity of the oil at Pb, cp
μod = viscosity of the dead oil at 14.7 psia and reservoir T, cp
The experimental data used by Chew and Connally to
develop their correlation encompassed the following ranges
of values for the independent variables:
Pressure, psia: 132–5,645, Temperature, °F: 72–292
Rs , scf/STB: 51–3,544, Dead oil viscosity, cp: 0.377–50
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25. μob: The Beggs-Robinson correlation
Beggs and Robinson (1975) empirical correlation
From 2,073 saturated oil viscosity measurements
accuracy of −1.83% with a standard deviation of 27.25%.
The ranges of the data used
to develop Beggs and Robinson’s equation are:
Pressure, psia: 132–5,265,
Temperature, °F: 70–295
API gravity: 16–58,
Gas solubility, scf/STB: 20–2,070
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26. Method of Calculating
the Viscosity of the Undersaturated Oil
Oil viscosity at pressures above the bubble point is
estimated by first calculating the oil viscosity at its
Pb and adjusting the bubble-point viscosity to
higher pressures.
The Vasquez-Beggs (1980) Correlation
From a total of 3,593 data points,
The average error of the viscosity correlation is −7.54%
The data used have the following ranges:
• P, psia: 141–9,151, Rs, scf/STB: 9.3–2,199,
• Viscosity, cp: 0.117–148, γg: 0.511–1.351, API : 15.3–59.5
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27.
28. Surface/Interfacial Tension
The surface tension is defined as
the force exerted on the boundary layer between a
liquid phase and a vapor phase per unit length.
This force is caused by differences between the molecular
forces in the vapor phase and those in the liquid phase, and
also by the imbalance of these forces at the interface.
The surface tension can be measured in the
laboratory and is unusually expressed in dynes per
centimeter.
The surface tension is an important property in
reservoir engineering calculations and
designing enhanced oil recovery projects.
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29. Surface Tension Correlation for
Pure Liquid
Sugden (1924) suggested a relationship that
correlates
the surface tension of a pure liquid
in equilibrium with its own vapor.
The correlating parameters are
molecular weight M of the pure component,
the densities of both phases, and
a newly introduced temperature independent parameter
Pch (parachor).
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30. Parachor Parameter
The parachor
is a dimensionless constant
characteristic of a pure
compound and
is calculated by imposing
experimentally measured
surface tension and density Fanchi’s linear equation
data on the Equation and
is only valid for components
solving for Pch.
heavier than methane.
The Parachor values for a
(Pch) i = 69.9 + 2.3 Mi
selected number of pure
compounds are given in
the Table as reported by
Weinaug and Katz (1943).
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Mi = molecular weight of
component i
(Pch)i =
parachor of component i
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31. Surface Tension Correlation for
Complex Hc Mixtures
For a complex hydrocarbon mixture, Katz et al.
(1943)
employed the Sugden correlation for mixtures by
introducing the compositions of the two phases into the
Equation.
Mo & Mg = apparent molecular weight of the oil & gas phases,
xi and yi = mole fraction of component i in the oil & gas phases,
n = total number of components in the system,
ρo & ρg = density of the oil and gas phase, lb/ft3
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32.
33. Water Formation Volume Factor
The water formation volume factor can be
calculated by the following mathematical
expression:
Where the coefficients A1 − A3 are: (T in °R)
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34. μw: Meehan
Meehan (1980) proposed a water viscosity correlation
that accounts for both the effects of P and salinity:
μwT = brine viscosity at 14.7 psi & reservoir temperature T, cp
ws = weight percent of salt in brine, T = temperature in °R
The effect of pressure “p” on the brine viscosity
can be estimated from:
μw = viscosity of the brine at pressure and temperature
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35. μw: Brill and Beggs
Brill and Beggs (1978)
presented a simpler equation,
which considers only temperature effects:
T is in °F and
μw is in cP
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36. Gas Solubility in Water
The following correlation can be used to determine
the gas solubility in water:
The temperature T is expressed in °F
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37. Water Isothermal Compressibility
Brill and Beggs (1978) proposed
the following equation for estimating
water isothermal compressibility,
ignoring the corrections for
dissolved gas and solids:
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38. 1. Ahmed, T. (2010). Reservoir engineering
handbook (Gulf Professional Publishing).
Chapter 2