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Petroleum Engineering Fluid Properties HW

This document contains 9 practice problems related to fluid properties for 2nd year petroleum engineering students at Suez University. The problems cover topics like gas density calculations, gas compressibility, gas formation volume factors, gas molecular weight, gas deviation factors, and gas viscosity. Students are asked to calculate properties for various gas mixtures given their compositions and conditions of pressure, temperature, density, and volume.
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0% found this document useful (0 votes)
627 views2 pages

Petroleum Engineering Fluid Properties HW

This document contains 9 practice problems related to fluid properties for 2nd year petroleum engineering students at Suez University. The problems cover topics like gas density calculations, gas compressibility, gas formation volume factors, gas molecular weight, gas deviation factors, and gas viscosity. Students are asked to calculate properties for various gas mixtures given their compositions and conditions of pressure, temperature, density, and volume.
Copyright
© © All Rights Reserved
We take content rights seriously. If you suspect this is your content, claim it here.
Available Formats
Download as PDF, TXT or read online on Scribd
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New

Viscosity by correlation and graph


Suez University Cg by zp slope and Trube Graph
Faculty of Petroleum & Mining Engineering
Petroleum Engineering Department
Fluid Properties
2nd Year Students
H.W # 1

1- Assuming an ideal gas behavior, calculate the density of n-butane at 220°F


and 50 psia.

2- Show that :
yi = ∑

3-A gas has the following composition:


component yi
Co2 0.06
N2 0.03
C1 0.75
C2 0.07
C3 0.04
n-C4 0.03
n-C5 0.02
If the reservoir pressure and temperature are 2,500 psia and 175°F respectively,
calculate :
a. The gas density.
b. Isothermal gas compressibility coefficient.
c. The gas formation volume factor

4- A gas mixture has a density of 1.92 lb/ft3 at 500 psia and 100°F Calculate the
apparent molecular weight of the gas mixture.

5- A high-pressure cell has a volume of 0.33 ft3 and contains gas at 2,500 psia
and 130°F, at which conditions its z-factor is 0.75. When 43.6 scf of the gas are

Eng.Mohamed Elnoby Page 1


bled from the cell, the pressure dropped to 1,000 psia, the temperature remaining
at 130°F. What is the gas deviation factor at 1,000 psia and 130°F.

6- A hydrocarbon gas mixture with a specific gravity of 0.7 has a density of 9


lb/ft3 at the prevailing reservoir pressure and temperature. Calculate the gas
formation volume factor in bbl/scf.

7- A gas reservoir exists at a 150°F. The gas has the following composition
component yi
C1 0.89
C2 0.07
C3 0.04
The gas expansion factor Eg was calculated as 204.648 scf/ft3 at the existing
reservoir pressure and temperature. Calculate the viscosity of the gas.

8- A 20 ft3 tank at a pressure of 2,500 psia and 212°F contains ethane gas. How
many pounds of ethane are in the tank.

9-A hydrocarbon gas system has the following composition


component yi
C1 0.83
C2 0.06
C3 0.03
n-C4 0.02
n-C5 0.02
C6 0.01
C7+ 0.03

The heptanes-plus fraction is characterized by a molecular weight and specific


gravity of 161 and 0.81, respectively. Using Sutton’s methodology, calculate the
density of the gas 2000 psi and 150°F

Eng.Mohamed Elnoby Page 2

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