(a)
Interpretation:
For the given binary mixture, whether one or two liquid phases are present is to be determined. Also, their composition is to be calculated if two phases are present.
Concept Introduction:
The general equation for
Here,
The relationship for
For liquid-liquid equilibrium where two phases,
Also, the relationship between
(a)
Answer to Problem 12.36P
Two phases are present in the given system of binary mixture with phase composition as:
Explanation of Solution
Given information:
Excess Gibbs energy for a binary liquid mixture is given by,
Overall composition of the system is given as
Rewrite the given equation of
Compare this equation by equation (1) so that the value of
Let, the binary mixture contains two phases of liquid and the system is in liquid-liquid equilibrium. Now, use equations set (2) along with equations (3) and (4) to eliminate
The value of
At this point, there exist equilibrium between two phases for the given system.
Therefore, the assumption that the system is a two-phase system is correct and two phases are present.
(b)
Interpretation:
For the given binary mixture, whether one or two liquid phases are present is to be determined. Also, their composition is to be calculated if two phases are present.
Concept Introduction:
The general equation for
Here,
The relationship for
For liquid-liquid equilibrium where two phases,
Also, the relationship between
(b)
Answer to Problem 12.36P
Two phases are present in the given system of binary mixture with phase composition as:
Explanation of Solution
Given information:
Excess Gibbs energy for a binary liquid mixture is given by,
Overall composition of the system is given as
Rewrite the given equation of
Compare this equation by equation (1) so that the value of
Let, the binary mixture contains two phases of liquid and the system is in liquid-liquid equilibrium. Now, use equations set (2) along with equations (3) and (4) to eliminate
The value of
At this point, there exist equilibrium between two phases for the given system.
Therefore, the assumption that the system is a two-phase system is correct and two phases are present.
(c)
Interpretation:
For the given binary mixture, whether one or two liquid phases are present is to be determined. Also, their composition is to be calculated if two phases are present.
Concept Introduction:
The general equation for
Here,
The relationship for
For liquid-liquid equilibrium where two phases,
Also, the relationship between
(c)
Answer to Problem 12.36P
Two phases are present in the given system of binary mixture with phase composition as:
Explanation of Solution
Given information:
Excess Gibbs energy for a binary liquid mixture is given by,
Overall composition of the system is given as
Rewrite the given equation of
Compare this equation by equation (1) so that the value of
Let, the binary mixture contains two phases of liquid and the system is in liquid-liquid equilibrium. Now, use equations set (2) along with equations (3) and (4) to eliminate
The value of
At this point, there exist equilibrium between two phases for the given system.
Therefore, the assumption that the system is a two-phase system is correct and two phases are present.
(d)
Interpretation:
For the given binary mixture, whether one or two liquid phases are present is to be determined. Also, their composition is to be calculated if two phases are present.
Concept Introduction:
The general equation for
Here,
The relationship for
For liquid-liquid equilibrium where two phases,
Also, the relationship between
(d)
Answer to Problem 12.36P
Two phases are present in the given system of binary mixture with phase composition as:
Explanation of Solution
Given information:
Excess Gibbs energy for a binary liquid mixture is given by
Overall composition of the system is given as
Rewrite the given equation of
Compare this equation by equation (1) so that the value of
Let, the binary mixture contains two phases of liquid and the system is in liquid-liquid equilibrium. Now, use equations set (2) along with equations (3) and (4) to eliminate
The value of
At this point, there exist equilibrium between two phases for the given system.
Therefore, the assumption that the system is a two-phase system is correct and two phases are present.
(e)
Interpretation:
For the given binary mixture, whether one or two liquid phases are present is to be determined. Also, their composition is to be calculated if two phases are present.
Concept Introduction:
The general equation for
Here,
The relationship for
For liquid-liquid equilibrium where two phases,
Also, the relationship between
(e)
Answer to Problem 12.36P
Two phases are present in the given system of binary mixture with phase composition as:
Explanation of Solution
Given information:
Excess Gibbs energy for a binary liquid mixture is given by
Overall composition of the system is given as
Rewrite the given equation of
Compare this equation by equation (1) so that the value of
Let, the binary mixture contains two phases of liquid and the system is in liquid-liquid equilibrium. Now, use equations set (2) along with equations (3) and (4) to eliminate
The value of
At this point, there exist equilibrium between two phases for the given system.
Therefore, the assumption that the system is a two-phase system is correct and two phases are present.
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Chapter 12 Solutions
EBK INTRODUCTION TO CHEMICAL ENGINEERIN
- The power out of an adiabatic steam turbine is 5 MW and the steam enters turbine at 2 MPa and velocity of 50 m/s, specific enthalpy (h) of 3248 kJ/kg. The elevation of the inlet is 10 m higher than at the datum. The vapor mixture exits at 15 kPa and a velocity of 180 m/s, specific enthalpy (h) of 2361.01 kJ/kg. The elevation of the exit is 6 m higher than at the datum. Let g = 9.81 m/s². Assuming the ideal gas model and R = 0.462 KJ/(kg.K). The steam specific heat ratio is 1.283. Calculate:arrow_forwardstep by step pleasearrow_forwardstep by step pleasearrow_forward
- step by steparrow_forwardThe power out of an adiabatic steam turbine is 5 MW and the steam enters turbine at 2 MPa and velocity of 50 m/s, specific enthalpy (h) of 3248 kJ/kg. The elevation of the inlet is 10 m higher than at the datum. The vapor mixture exits at 15 kPa and a velocity of 180 m/s, specific enthalpy (h) of 2361.01 kJ/kg. The elevation of the exit is 6 m higher than at the datum. Let g = 9.81 m/s². Assuming the ideal gas model and R = 0.462 KJ/(kg.K). The steam specific heat ratio is 1.283. Calculate:arrow_forwardThe power out of an adiabatic steam turbine is 5 MW and the steam enters turbine at 2 MPa and velocity of 50 m/s, specific enthalpy (h) of 3248 kJ/kg. The elevation of the inlet is 10 m higher than at the datum. The vapor mixture exits at 15 kPa and a velocity of 180 m/s, specific enthalpy (h) of 2361.01 kJ/kg. The elevation of the exit is 6 m higher than at the datum. Let g = 9.81 m/s². Assuming the ideal gas model and R = 0.462 KJ/(kg.K). The steam specific heat ratio is 1.283. Calculate:arrow_forward
- O Consider a 0.8 m high and 0.5 m wide window with thickness of 8 mm and thermal conductivity of k = 0.78 W/m °C. For dry day, the temperature of outdoor is -10 °C and the inner room temperature is 20°C. Take the heat transfer coefficient on the inner and outer surface of the window to be h₁ = 10 W/m² °C and h₂ = 40 W/m² °C which includes the effects of insulation. Determine:arrow_forwardCalculate the mass flow rate of the steam. Determine Cp and C₁ of steam.arrow_forwardstep by step pleasearrow_forward
- step by steparrow_forward4. Show that the fraction, F, of the energy released from a supercritical chain reaction that originates in the final m generations of the chain is given approximately by F= 1 km provided the total number of generations is large.arrow_forwardPLEASE SOLVE STEP BY STEP WITHOUT ARTIFICIAL INTELLIGENCE OR CHATGPT I don't understand why you use chatgpt, if I wanted to I would do it myself, I need to learn from you, not from being a d amn robot. SOLVE BY HAND STEP BY STEP A solution containing 7.5% sulfuric acid by weight at 70 °F is concentrated to 45% by weight by evaporating water. The concentrated solution and the water vapor exit the evaporator at 170 °F and 1 atm. Calculate the rate at which heat must be transferred to the evaporator to process 1500 lbm/hr of the feed solution to the evaporator. It is recommended to use the enthalpy-concentration diagram for sulfuric acid from Chapter 8 of Felder's book or an enthalpy-concentration diagram for sulfuric acid found in another unit operations book or chemical engineering manual such as Perry's.arrow_forward
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