Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN: 9781259696527
Author: J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher: McGraw-Hill Education
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Textbook Question
Chapter 12, Problem 12.31P
Problems 12.29 through 12.33 refer to the xy diagram provided in Fig. 12.23. This diagram shows xy curves both for ethanol(1)/ethyl acetate(2) and for chloroform(1)/tetrahydrofuran(2), both at a constant pressure of 1 bar. The curves are intentionally unlabeled. Readers should refer to Figs. 12.19 through 12.22 to deduce which curve is for which pair of substances.
12.31. What is the composition of the vapor phase in equilibrium with a liquid-phase chloroform(1)/tetrahydrofuran( 2) mixture of the following compositions at P = 1 bar?
(a) x1= 0.1
(b) x1= 0.2
(c) x1= 0.3
(d) x1= 0.45
(e) x1= 0.6
(f) x1= 0.8
(g) x1= 0.9
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Example (6):
An evaporator is concentrating F kg/h at
311K of a 20wt% solution of NaOH to 50wt
%. The saturated steam used for heating is
at 399.3K. The pressure in the vapor space
of the evaporator is 13.3 KPa abs. The
5:48
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Transcribed Image Text: Example (7): Determine the
14.9. A forward feed double-effect vertical
evaporator, with equal heating areas in
each effect, is fed with 5 kg/s of a liquor
of specific heat capacity of 4.18 kJ/kg K.
and with no boiling point rise, so that 50
per cent of the feed liquor is evaporated.
The overall heat transfer coefficient in the
second effect is 75 per cent of that in the
first effect. Steam is fed at 395 K and the
boiling point in the second effect is 373 K.
The feed is heated by an external heater to
the boiling point in the first effect.
It is decided to bleed off 0.25 kg/s of
vapour from the vapour line to the second
effect for use in another process. If the
feed is still heated to the boiling point of
the first effect by external means, what
will be the change in steam consumption
of the evaporator unit? For the purpose of
calculation, the latent heat of the vapours
and of the steam may both be taken as
2230 kJ/kg
Chapter 12 Solutions
Introduction to Chemical Engineering Thermodynamics
Ch. 12 - Prob. 12.1PCh. 12 - Prob. 12.2PCh. 12 - Prob. 12.3PCh. 12 - Problems 12.3 through 12.8 refer to the Pxy...Ch. 12 - Problems 12.3 through 12.8 refer to the Pxy...Ch. 12 - Problems 12.3 through 12.8 refer to the Pxy...Ch. 12 - Problems 12.3 through 12.8 refer to the Pxy...Ch. 12 - Problems 12.3 through 12.8 refer to the Pxy...Ch. 12 - Problems 12.9 through 12.14 refer to the Txy...Ch. 12 - Problems 12.9 through 12.14 refer to the Txy...
Ch. 12 - Problems 12.9 through 12.14 refer to the Txy...Ch. 12 - Problems 12.9 through 12.14 refer to the Txy...Ch. 12 - Problems 12.9 through 12.14 refer to the Txy...Ch. 12 - Problems 12.9 through 12.14 refer to the Txy...Ch. 12 - Prob. 12.15PCh. 12 - Problems 12.16 through 12.21 refer to the Pxy...Ch. 12 - Problems 12.16 through 12.21 refer to the Pxy...Ch. 12 - Problems 12.16 through 12.21 refer to the Pxy...Ch. 12 - Problems 12.16 through 12.21 refer to the Pxy...Ch. 12 - Problems 12.16 through 12.21 refer to the Pxy...Ch. 12 - Prob. 12.21PCh. 12 - Problems 12.22 through 12.28 refer to the Txy...Ch. 12 - Problems 12.22 through 12.28 refer to the Txy...Ch. 12 - Problems 12.22 through 12.28 refer to the Txy...Ch. 12 - Problems 12.22 through 12.28 refer to the Txy...Ch. 12 - Problems 12.22 through 12.28 refer to the Txy...Ch. 12 - Problems 12.22 through 12.28 refer to the Txy...Ch. 12 - Prob. 12.28PCh. 12 - Problems 12.29 through 12.33 refer to the xy...Ch. 12 - Problems 12.29 through 12.33 refer to the xy...Ch. 12 - Problems 12.29 through 12.33 refer to the xy...Ch. 12 - Problems 12.29 through 12.33 refer to the xy...Ch. 12 - Problems 12.29 through 12.33 refer to the xy...Ch. 12 - Consider a binary liquid mixture for which the...Ch. 12 - Prob. 12.35PCh. 12 - Prob. 12.36P
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- Example(3): It is desired to design a double effect evaporator for concentrating a certain caustic soda solution from 12.5wt% to 40wt%. The feed at 50°C enters the first evaporator at a rate of 2500kg/h. Steam at atmospheric pressure is being used for the said purpose. The second effect is operated under 600mmHg vacuum. If the overall heat transfer coefficients of the two stages are 1952 and 1220kcal/ m2.h.°C. respectively, determine the heat transfer area of each effect. The BPR will be considered and present for the both effect 5:49arrow_forwardالعنوان ose only Q Example (7): Determine the heating surface area 개 required for the production of 2.5kg/s of 50wt% NaOH solution from 15 wt% NaOH feed solution which entering at 100 oC to a single effect evaporator. The steam is available as saturated at 451.5K and the boiling point rise (boiling point evaluation) of 50wt% solution is 35K. the overall heat transfer coefficient is 2000 w/m²K. The pressure in the vapor space of the evaporator at atmospheric pressure. The solution has a specific heat of 4.18kJ/ kg.K. The enthalpy of vaporization under these condition is 2257kJ/kg Example (6): 5:48 An evaporator is concentrating F kg/h at 311K of a 20wt% solution of NaOH to 50wt %. The saturated steam used for heating is at 399.3K. The pressure in the vapor space of the evaporator is 13.3 KPa abs. The 5:48 1 J ۲/۱ ostrarrow_forwardExample 8: 900 Kg dry solid per hour is dried in a counter current continues dryer from 0.4 to 0.04 Kg H20/Kg wet solid moisture content. The wet solid enters the dryer at 25 °C and leaves at 55 °C. Fresh air at 25 °C and 0.01Kg vapor/Kg dry air is mixed with a part of the moist air leaving the dryer and heated to a temperature of 130 °C in a finned air heater and enters the dryer with 0.025 Kg/Kg alry air. Air leaving the dryer at 85 °C and have a humidity 0.055 Kg vaper/Kg dry air. At equilibrium the wet solid weight is 908 Kg solid per hour. *=0.0088 Calculate:- Heat loss from the dryer and the rate of fresh air. Take the specific heat of the solid and moisture are 980 and 4.18J/Kg.K respectively, A. =2500 KJ/Kg. Humid heat at 0.01 Kg vap/Kg dry=1.0238 KJ/Kg. "C. Humid heat at 0.055 Kg/Kg 1.1084 KJ/Kg. "C 5:42 Oarrow_forward
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