2. Consider this item as REAL gases: Two hundred and fifty pounds of a mixture of 6.63.% propane 17.47% n-butane, and 75.9%-pentane is completely vaporized in a pipe still in one hour. At the outlet, the temperature anc pressure are 433 F and 600 psia. What is the volumetric flow rate in CFS at the outlet conditions? Above data are Xi values. Answer: cubic feet per second

Chemistry
10th Edition
ISBN:9781305957404
Author:Steven S. Zumdahl, Susan A. Zumdahl, Donald J. DeCoste
Publisher:Steven S. Zumdahl, Susan A. Zumdahl, Donald J. DeCoste
Chapter1: Chemical Foundations
Section: Chapter Questions
Problem 1RQ: Define and explain the differences between the following terms. a. law and theory b. theory and...
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UPVOTE WILL BE GIVEN. PLEASE WRITE THE COMPLETE SOLUTIONS LEGIBLY. SHOW THE STEP-BY-STEP PROCESS WITH SHORT COMMENT/EXPLANATION. ANSWER IN 3 DECIMAL PLACES.

ANSWER #2 ONLY not all. Thank you.

Z=RT
Note: Use values of MW, Cp, Cv, etc., from the Tables provided below. Indicate your answers in this page.
Show your solutions in separate pages.
2. Consider this item as REAL gases:
Two hundred and fifty pounds of a mixture of 6.63.% propane
17.47% n-butane, and 75.9%-
h-pentane is completely vaporized in a
pipe still in one hour. At the outlet, the temperature anc
pressure are 433 F and 600 psia. What is the volumetric flow
rate in CFS at the outlet conditions? Above data are Xi values.
Answer:
cubic feet per second
1.1
1.0
Answers: (a).
(c).
(e)
0.9
0.8
0.7
0.6
0.5
0.4
0.3
1. Consider this item as ideal gas: A rigid tank
containing 3 lb of gaseous mixture of nitrogen, helium
and carbon dioxide, each 33.33% by volume at 40 psia,
0.2
and 150°F receives 1 lb more of nitrogen with the temperature
remaining at 150°F. For the resulting 4lb, determine (a) the
gravimetric and volume analyses, (b) the pressure and (c) the
molecular weight.
For the initial mixture, determine (d) Cp, (e) Cv,
and, (f) R
0.1
0
0.5
Gas
1.0
TR=1.00
1.5
Nitrogen N₂
Helium
He
Carbon CO₂
Dioxide
TR= 1.10
2.0
Formula
L
TR=1.20
aque
y
X
2.5
oot
28
4
44
C
X
Do
3.0
(f).
X
_(b)_
_(d)_
TR= 1.50
●
TR= 2.00
MW
TR=1.30
3.5 4.0
Reduced pressure PR
DAX
4.5
Density
(kg/m3)
1.1648
0.1663
1.8417
Legend:
x Methane
o Ethylene
▲ Ethane
O Propane
On-Butane
5.0
• Water
Average curve based on data on
hydrocarbons
5.5
■ Iso-pentane
• n-Heptane
A Nitrogen
0.297
2.078
0.189
Carbon dioxide.
R
(Gas
constant)
kJ/(kg.K)
6.0
The physical properties of the gas are:
I
6.5
Cp
kJ/(kg.K)
1.034
5.234
7.0
0.858
Tc
Pc
MW
Propane
369.9 K
665.8 R
42.0 atm
No. 3. Consider this item as ideal gas:
0.733
3.153
0.66
44
Cv
A drum 6 inches in diameter and 40 inches long
contained acetylene at 250 psia and 80°F. After some of the
acetylene was used the pressure was 200 psia and the
temperature was 70°F (a) what portion of the acetylene was
used, and (b) what volume would the used acetylene occupy
at 14.7 psia and 60°F.
R(acetylene) = 59.35 ft-lbf/lbm-R
Answer: a.
kJ/(kg.K)
b. V =
Cp/Cv=Y
1.41
Butane
425.17 K
765.31 R
37.47 atm
58
1.66
1.3
Pentane
469.8 K
845.64 R
33.3 atm
% mass
72
Transcribed Image Text:Z=RT Note: Use values of MW, Cp, Cv, etc., from the Tables provided below. Indicate your answers in this page. Show your solutions in separate pages. 2. Consider this item as REAL gases: Two hundred and fifty pounds of a mixture of 6.63.% propane 17.47% n-butane, and 75.9%- h-pentane is completely vaporized in a pipe still in one hour. At the outlet, the temperature anc pressure are 433 F and 600 psia. What is the volumetric flow rate in CFS at the outlet conditions? Above data are Xi values. Answer: cubic feet per second 1.1 1.0 Answers: (a). (c). (e) 0.9 0.8 0.7 0.6 0.5 0.4 0.3 1. Consider this item as ideal gas: A rigid tank containing 3 lb of gaseous mixture of nitrogen, helium and carbon dioxide, each 33.33% by volume at 40 psia, 0.2 and 150°F receives 1 lb more of nitrogen with the temperature remaining at 150°F. For the resulting 4lb, determine (a) the gravimetric and volume analyses, (b) the pressure and (c) the molecular weight. For the initial mixture, determine (d) Cp, (e) Cv, and, (f) R 0.1 0 0.5 Gas 1.0 TR=1.00 1.5 Nitrogen N₂ Helium He Carbon CO₂ Dioxide TR= 1.10 2.0 Formula L TR=1.20 aque y X 2.5 oot 28 4 44 C X Do 3.0 (f). X _(b)_ _(d)_ TR= 1.50 ● TR= 2.00 MW TR=1.30 3.5 4.0 Reduced pressure PR DAX 4.5 Density (kg/m3) 1.1648 0.1663 1.8417 Legend: x Methane o Ethylene ▲ Ethane O Propane On-Butane 5.0 • Water Average curve based on data on hydrocarbons 5.5 ■ Iso-pentane • n-Heptane A Nitrogen 0.297 2.078 0.189 Carbon dioxide. R (Gas constant) kJ/(kg.K) 6.0 The physical properties of the gas are: I 6.5 Cp kJ/(kg.K) 1.034 5.234 7.0 0.858 Tc Pc MW Propane 369.9 K 665.8 R 42.0 atm No. 3. Consider this item as ideal gas: 0.733 3.153 0.66 44 Cv A drum 6 inches in diameter and 40 inches long contained acetylene at 250 psia and 80°F. After some of the acetylene was used the pressure was 200 psia and the temperature was 70°F (a) what portion of the acetylene was used, and (b) what volume would the used acetylene occupy at 14.7 psia and 60°F. R(acetylene) = 59.35 ft-lbf/lbm-R Answer: a. kJ/(kg.K) b. V = Cp/Cv=Y 1.41 Butane 425.17 K 765.31 R 37.47 atm 58 1.66 1.3 Pentane 469.8 K 845.64 R 33.3 atm % mass 72
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