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47 Cards in this Set

  • Front
  • Back
Challenges of res engr
1. Know the res. and model it properly
2. Understanding fftpm eqs
3. " " fluid properties
4. " " material balance
5. " " natural drive mechs and augmented
6. make forecasts
7. suggest ways for EOR
Steady State laplace equation
d^2P/dx^2 + d^2P/dy^2=0
Unsteady state eq
d^2P/dx^2 + d^2P/dy^2=(1/alpha)(dP/dt)
Darcy's Law

What is C?
q= k A dP/ mew L

c=coefficient of conversion
API
Measurement of gravity (density)

API= 141.5/SG - 131.5
Crude Oils
Alkanes
Cyclic--- cyclohexane....
aromatic--- benzene
Largest Oil Field
Ghawar Field

active water flooding program to maintain pressure
Gas Laws
1. Boyle's Law
2. Charles Law--- PT=const
3. Ideal gas law--- PV/T= const
gas constant R for field units
R=10.730 psia ft^3 / (lb-mole) R
Mixing Rules
Kays Mixing Rule
--use correlations if gas grav>.75
impurity corrections
Carr-Kobayashi-Burrows (for all)

Wichert-Aziz (absence of N2)
Cubic EOS
Van Der Waals
Soave-Redlich-Kwong
Peng-Robinson
Peneloux correction for SRK and PR
(omega)

BIC
omega= composition eccentricity factor

BIC= Binary Interaction Coefficient
More EOS
Virial
Benedict-Webb-Rubin
Lawal-Lake-Silberberg
LGE
Lee Gonzalez Eakins

bad for high co2 good for H2S

up to 2500 psi
What natural gas property can be obtained by using Trube's charts?
compressibility
isothermal compressibility of a real gas in terms of pressure and z factor in differential form
Cg=1/P-1/z(dz/dp) (sub) T
what is C7+
Heavy hydrocarbon fraction

includes C7
Three coordinate systems for fftpm
radial cylindrical
radial spherical
linear
Domain for smaller samples than those in domain of continuity
microscopic domain
constitutive equation for deriving the fftpm
Darcy's Law
The finite difference method can be used to do numerical differentiation of a function
true
the gas formation volume vactor in reservoir ft^3/scf is given by the expression Bg=0.02827 ZT/p
true
In an inverse problem the input and output are known but the system is unknown
true
The term (phi*mew*c/k) is what
1/alpha

alpha=hydraulic diffusiity
Types of Oil
Ordinary black oil
low shrinkage oil
high shrinkage oil
Near critical oil
Types of Gas
Retrograde Gas
Near Critical Gas
Wet Gas
dry Gas
Gas density in terms of pressure, molecular weight, R and T
rho(g)=PM/RT
parameters for radial-cylindrical system
r, theta, z
parameters for radial-spherical system
r, theta, alpha
REV
representative elemental volume
isotropic and homogeneous reservoir
kx1=kx2=kx3=ky1=ky2=ky3
isotropic but hetero reservoir
kx1=ky1 but

kx1=/= ky2
anisotropic and homo reservoir
kx1=kx2
but
kx1 =/= ky1
anisotropic but hetero
kx1 =/= kx2 and
kx1 =/= ky1
Darcy's law for radial cylindrical
Qr=-(k/mew)(dp/dr)
expression for psuedo pressure (psi)
=2*int(0-p)(p/mew/z)dp=2A
The value of the pseudo pressure function is usually calculated using a numerical integration technique
true
Simple analytical solution of the equation of fluid flow through a res is possible if one makes the assumption of isotropic and homogeneous reservoir
true
it is better to use the pseudo pressure approach for solving gas flow eqs in all three regions because most reservoirs dont fall within regions I and III
True
in the gas flow expression using the p-approach the gas viscosity and the gas compressibility are evaluated at the initial pressure
false
the dimensionless radius at any point in the reservoir is calculated by dividing rw (well radius) by its distance from the center of the well
false
for slightly compressible liquids the following expression is used for compressibility c=1/p(drho/dp)
true
Riazi and Daubert correlation is used to get critical properties of mixtures for which only molecular weight and density are known
True
the pseudo critical temperature of a mixture of HC gas will be greater than any individual Tc value of a gas present in the mixture
false
the pseduo critical pressure of a mixture of HC gas will be less than any individual Pc value of a gas present in the mixture
false
the Sarem correlation uses an iterative technique to calculate the z factor
true