Computer Methods in Chemical
Engineering – 1st Edition
ST
SOLUTIONS
UV
MANUAL
IA
_A
Nayef Ghasem
PP
RO
Comprehensive Solutions Manual for
Instructors and Students
VE
© Nayef Ghasem. All rights reserved. Reproduction or distribution without permission is
D?
prohibited.
©MedConnoisseur
, Solutions Manual for Computer Methods in
Chemical Engineering, 1e by Nayef Ghasem
(All Chapters)
Chapter 1
1.1 Dew point calculation
ST
Calculate the temperature and composition of a liquid in equilibrium with a gas mixture
containing 10.0 mol% benzene, 10.0 mol% toluene, and balance nitrogen (considered
noncondensable) at 1 atm
UV
UniSim solution (Fig. 1.1)
The liquid at equilibrium with its gas mixture is at the dew point, setting the vapor/phase ratio
to 1. The pressure is 1 atm, and as the basis, set the molar flow rate to 1 kgmol/s
The temperature is 51.1oC. The compositions of the vapor and liquid are shown in the figure
below
IA
_A
PP
RO
Fig. 1.1 Stream vapor and liquid compositions
PRO/II solution (Fig. 1.2)
VE
D?
Fig. 1.2 PRO/II simulated results for the case described in problem 1.1.
1
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, 1.2 Compressibility Factors
Fifty cubic meters per hour of methane flow through a pipeline at 40.0 bar absolute and 300.0
K. Estimate the mass flow rate.
UniSim solution (Fig. 1.3)
In the molar flow rate cell, set the volumetric flow rate to 50 m3/h.
Equation of state: Peng Robinson.
ST
UV
IA
_A
PP
Fig. 1.3 stream conditions
RO
The compressibility factor (Z) = 0.9199
VE
D?
Fig. 1.4 Compressibility factor
2
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, PRO/II simulation (Fig. 1.5)
ST
UV
Fig. 1.5 PRO/II generated the molar flow rate of 50m3/h of methane.
IA
_A
PP
RO
VE
Fig. 1.6 Compressibility factor (Z)
D?
1.3 Use of Raoult’s law
A liquid mixture contains 40 % (mole percent) benzene, and balance is toluene equilibrium
with its vapor at 30.0°C. What are the system pressure and the composition of the vapor? Use
Unisim, PRO/II, and Aspen Plus.
3
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Distribution of this document is illegal extra per year?
Engineering – 1st Edition
ST
SOLUTIONS
UV
MANUAL
IA
_A
Nayef Ghasem
PP
RO
Comprehensive Solutions Manual for
Instructors and Students
VE
© Nayef Ghasem. All rights reserved. Reproduction or distribution without permission is
D?
prohibited.
©MedConnoisseur
, Solutions Manual for Computer Methods in
Chemical Engineering, 1e by Nayef Ghasem
(All Chapters)
Chapter 1
1.1 Dew point calculation
ST
Calculate the temperature and composition of a liquid in equilibrium with a gas mixture
containing 10.0 mol% benzene, 10.0 mol% toluene, and balance nitrogen (considered
noncondensable) at 1 atm
UV
UniSim solution (Fig. 1.1)
The liquid at equilibrium with its gas mixture is at the dew point, setting the vapor/phase ratio
to 1. The pressure is 1 atm, and as the basis, set the molar flow rate to 1 kgmol/s
The temperature is 51.1oC. The compositions of the vapor and liquid are shown in the figure
below
IA
_A
PP
RO
Fig. 1.1 Stream vapor and liquid compositions
PRO/II solution (Fig. 1.2)
VE
D?
Fig. 1.2 PRO/II simulated results for the case described in problem 1.1.
1
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Distribution of this document is illegal extra per year?
, 1.2 Compressibility Factors
Fifty cubic meters per hour of methane flow through a pipeline at 40.0 bar absolute and 300.0
K. Estimate the mass flow rate.
UniSim solution (Fig. 1.3)
In the molar flow rate cell, set the volumetric flow rate to 50 m3/h.
Equation of state: Peng Robinson.
ST
UV
IA
_A
PP
Fig. 1.3 stream conditions
RO
The compressibility factor (Z) = 0.9199
VE
D?
Fig. 1.4 Compressibility factor
2
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Distribution of this document is illegal extra per year?
, PRO/II simulation (Fig. 1.5)
ST
UV
Fig. 1.5 PRO/II generated the molar flow rate of 50m3/h of methane.
IA
_A
PP
RO
VE
Fig. 1.6 Compressibility factor (Z)
D?
1.3 Use of Raoult’s law
A liquid mixture contains 40 % (mole percent) benzene, and balance is toluene equilibrium
with its vapor at 30.0°C. What are the system pressure and the composition of the vapor? Use
Unisim, PRO/II, and Aspen Plus.
3
Downloaded by: tutorsection | Want to earn $1.236
Distribution of this document is illegal extra per year?
