1 96% l Verizon LTE 10:23 AM Done 1. (Significant figures having a volume of 4.7 gallons exhibits a pressure of 145 psig at 70.0 °F. Using the compressibility factor chart below determine whether the contents are liquid, gas or a mixture of liquid in equilibrium with its vapor. If the contents are vapor liquid in equilibrium with its vapor, calculate the specific volume of the vapor phase in units of m'/Kg. The critical pressure of propane is 42 atm, its critical temperature is 369.9 K and its molecular weight is 44.09 g/mol important). A 20.0 lbs propane tank a or a 1.5 14 0.00 1.3 Generalized compressibility factors (z=0.27) 1.2 1.1 T. 15.00 10.00-5.00 3.00 1.0 2.00 80 09 0.9 0O 1.70 1.60 Saurated gas 150 0.8 140 1.35 0.7 1.30 1.25. 0.6 0.75 1.20 0.80 0.5 1.15 0.85 1.10 0.90 0.4 1.08 06 0.95 1.04 1.02 0.3 100 0.2 0.50. 0.1 Saturated liquid 0 0.1 1.0 3.0 4.0 5.0 10 30 0.2 0.3 04 05 2.0 20 Reduced pressure, P. X Compressibility factor, z

Question

Hi this is what it can help please provide the explanation for solutions don’t worry about the  exactly values please read from the graph what you can thank

1 96%
l Verizon LTE
10:23 AM
Done
1. (Significant figures
having a volume of 4.7 gallons exhibits a pressure of 145 psig
at 70.0 °F. Using the compressibility factor chart below
determine whether the contents are liquid, gas or a mixture of
liquid in equilibrium with its vapor. If the contents are vapor
liquid in equilibrium with its vapor, calculate the specific
volume of the vapor phase in units of m'/Kg. The critical
pressure of propane is 42 atm, its critical temperature is 369.9
K and its molecular weight is 44.09 g/mol
important). A 20.0 lbs propane tank
a
or a
1.5
14
0.00
1.3
Generalized compressibility factors
(z=0.27)
1.2
1.1
T.
15.00
10.00-5.00
3.00
1.0
2.00
80
09
0.9 0O
1.70
1.60
Saurated gas
150
0.8
140
1.35
0.7
1.30
1.25.
0.6 0.75
1.20
0.80
0.5
1.15
0.85
1.10
0.90
0.4
1.08
06
0.95
1.04
1.02
0.3
100
0.2
0.50.
0.1
Saturated liquid
0
0.1
1.0
3.0 4.0 5.0
10
30
0.2
0.3 04 05
2.0
20
Reduced pressure, P.
X
Compressibility factor, z

Image Transcription

1 96% l Verizon LTE 10:23 AM Done 1. (Significant figures having a volume of 4.7 gallons exhibits a pressure of 145 psig at 70.0 °F. Using the compressibility factor chart below determine whether the contents are liquid, gas or a mixture of liquid in equilibrium with its vapor. If the contents are vapor liquid in equilibrium with its vapor, calculate the specific volume of the vapor phase in units of m'/Kg. The critical pressure of propane is 42 atm, its critical temperature is 369.9 K and its molecular weight is 44.09 g/mol important). A 20.0 lbs propane tank a or a 1.5 14 0.00 1.3 Generalized compressibility factors (z=0.27) 1.2 1.1 T. 15.00 10.00-5.00 3.00 1.0 2.00 80 09 0.9 0O 1.70 1.60 Saurated gas 150 0.8 140 1.35 0.7 1.30 1.25. 0.6 0.75 1.20 0.80 0.5 1.15 0.85 1.10 0.90 0.4 1.08 06 0.95 1.04 1.02 0.3 100 0.2 0.50. 0.1 Saturated liquid 0 0.1 1.0 3.0 4.0 5.0 10 30 0.2 0.3 04 05 2.0 20 Reduced pressure, P. X Compressibility factor, z

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