PNGE 332 Homework 2 Properties of Petroleum Fluids Assignment Paper

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in the files i included the homework assignment paper. please answer the question in a word document.

the textbook used is William D. McCain, Jr., The Properties of Petroleum Fluids, 2nd edition

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Spring 2019 Due Jan 29th PNGE 332 HOMEWORK #2 (Submit the typed HW in single pdf file through ecampus) 1. Pure Heptane is contained in a laboratory cell in which the volume can be varied. The cell is maintained at a temperature of 400°F. The volume is changed until a few drops of liquid Heptane are present. What is the pressure in the cell? The volume is reduced until the cell is essentially full of liquid Heptane with only a few bubbles of Heptane gas remaining. What is the pressure? Explain. 2. The densities of methane liquid and gas in equilibrium along the vapor-pressure line are given below. Estimate the density of methane at its critical point of -116.7°F Temperature °F -253 -235 -217 -199 -181 -163 Density of saturated methane Liquid Gas lb/ft3 lb/ft3 26.17 0.1443 25.25 0.2747 24.28 0.4766 23.18 0.7744 21.89 1.202 20.48 1.810 3. Estimate the critical pressure of a mixture of methane and n-butane if the critical temperature of the mixture is known to be 200°F. Compare your answer with the critical pressures of pure methane and pure n-butane (Use Appendix A). 4. Determine the compositions and quantities of gas and liquid when 2 lb mole of a mixture of 35 mole percent methane and 65 mole percent ethane is brought to equilibrium at 400 psia and -40°F. 5. Determine the compositions and quantities of gas and liquid when 2 lb mole of a mixture of 65 mole percent methane and 35 mole percent ethane is brought to equilibrium at 400 psia and -40°F. Compare your answer with the answer to problem 4. What was the effect of changing the composition of the mixture? 6. Determine the compositions and quantities of gas and liquid when 10 lb moles of a mixture of 55 mole percent methane, 30 mole percent propane and 15 mole percent npentane is brought to equilibrium at 160°F and 1500 psia. 7. A liquid of 80 mole percent propane and 20 mole percent n-pentane is to be diluted with methane. Wi11 all mixtures of the liquid and methane be single phase at 160°F and 1500 psia? Explain the reason for your answer. 8. A liquid of 20 mole percent propane and 80 mole percent n-pentane is to be diluted with methane. Wi11 all mixtures of the liquid and methane be single phase at 160°F and 1500 psia? Explain the reason for your answer.
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Hi, here is your assignment :). I will send you both word file and pdf file :). They were both the same :)

Spring 2019 Due Jan 29th

PNGE 332

HOMEWORK #2
(Submit the typed HW in single pdf file through ecampus)
1. Pure Heptane is contained in a laboratory cell in which the volume can be varied. The
cell is maintained at a temperature of 400°F. The volume is changed until a few drops of
liquid Heptane are present. What is the pressure in the cell? The volume is reduced until
the cell is essentially full of liquid Heptane with only a few bubbles of Heptane gas
remaining. What is the pressure? Explain.
Answer:
Hence, we have to do a chart of vapor pressure of normal paraffin's and with the help of
that chart, we can easily find out the vapor pressure i. e 400 psi. Temperature of 4000f
for pure n-butane. Here we have isothermal system and are substance is pure. So we can
expect that during liquid/gas phase (which is substance is in), the pressure will relatively
constant.
pressure at 4000f
400
300

vapor pressure of n-butane

200
100

100

200

300

400

2. The densities of methane liquid and gas in equilibrium along the vapor-pressure line are
given below. Estimate the density of methane at its critical point of -116.7°F

Temperature °F
-253
-235
-217
-199
-181
-163

Density of saturated methane
Liquid
Gas
lb/ft3
lb/ft3
26.17
0.1443
25.25
0.2747
24.28
0.4766
23.18
0.7744
21.89
1.202
20.48
1.810

Answer:
Here we made the tabulate values shown on the table below as we convert the given temperature in
Fahrenheit to Kelvin:
T(F)
-253
-253
-217
-199
-181
-163

T(K)
114.817
124.8 17
134.817
144.817
154.817
164.817

Liquid
26.17
25.25
24.28
23.18
21.89
20.48

Vapor
0.1443
0.2747
0.4766
0.7744
1.202
1.81

Plot:

At the critical point, the two phase's liquid and vapor becomes indistinguishable and the density of
saturated liquid and vapor are the same. From the above plot, at a critical point of (190.53 𝐾/
116.7℉), the density at that critical point is 10.12 lb/ft3.

3. Estimate the critical pressure of a mixture of methane and n-butane if the critical
temperature of the mixture is known to be 200°F. Compare your answer with the critical
pressures of pure methane and pure n-butane (Use Appendix A).
Answer:
The Critical pressure of methane (1):
45.99 𝑏𝑎𝑟
= 46 ∗ 10^5 𝑝𝑎𝑠𝑐𝑎𝑙
The critical pressure of pure hexane (2) :
30.20 𝑏𝑎𝑟
= 30.2 ∗ 10^5 𝑝𝑎𝑠𝑐𝑎𝑙
We have from van der waals law that:
𝑃𝑐𝑉𝑐
𝑅𝑇𝑐
8
=
3
= 0.375
Vc1=
𝑅𝑡𝑐1
0.375 ∗
𝑝𝑐1
366.33
= 8.314 ∗
∗ 105
46
= 2.483 ∗ 10^ − 4 𝑚^3
Vc2=
𝑅𝑡𝑐2
0.375 ∗
𝑝𝑐2
366.33
= 8.314 ∗
∗ 105
30.2
= 3.782 ∗ 10^ − 4 𝑚3
We have from vanderwaals law that,
𝑃𝑐𝑉𝑐
𝑅�...


Anonymous
I was struggling with this subject, and this helped me a ton!

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