8.1. The specific internal energy of formaldehyde (HCHO) vapor at 1 atm and moderate temperatures is given by the formula
where T is in °C.
Calculate the specific internal energies of formaldehyde vapor at 0°C and 200°C. What reference temperature was used to generate the given expression for
- ?
- The value of U calculated for 200°C is not the true value of the specific internal energy of formaldehyde vapor at this condition. Why not? (Him: Refer back to Section 7.5a.) Briefly state the physical significance of the calculated quantity.
- Use the closed system energy balance to calculate the heat (J) required to raise the temperature of 3.0 mol HCHO at constant volume from 0°C to 200°C. List all of your assumptions. From the definition of heat capacity at constant volume, derive a formula for
Then use this formula and Equation 8.3-6 to calculate the heat (J) required to raise the temperature of 3.0 mol of HCHO(v) at constant volume from 0°C to 200°C. [You should get the same result you got in Part (c).]
(a)
Interpretation:
The specific internal energies of formaldehyde vapor and the temperature should be calculated.
Concept introduction:
In the thermodynamic closed system, the exchange of matter does not take place but heat can be exchanged and thus, the work done by the system is considered to be zero.
The specific internal energy of formaldehyde Vapor is given by:
Where T= temperature of formaldehyde
Answer to Problem 8.1P
Explanation of Solution
Calculate the internal energy of formaldehyde at 0 and 200° C as,
Since the reference temperature is that temperature at which internal energy becomes zero.
The reference temperature is
(b)
Interpretation:
The importance of calculated quantity should be explained.
Concept introduction:
Thermodynamic closed system in which no exchange of matter takes place but the exchange of heat occurs then the work done by the system is considered to be zero.
The specific internal energy of formaldehyde Vapor is given by:
Where T= temperature of formaldehyde
Explanation of Solution
The calculation of the absolute value of internal energy for a process material is not possible. However, it is possible to estimate the change in internal energy for a defined change of state like solid, liquid or gas.
In part (a) calculation, the change in internal energy is calculated with references to 0 °C.
(c)
Interpretation:
The heat required to raise the temperature for the given range by stating the assumptions should be calculated.
Concept introduction:
Thermodynamic closed system in which no exchange of matter takes place, but the exchange of heat occurs then the work done by the system is zero.
The specific internal energy of formaldehyde Vapor is given by:
Where T= temperature of formaldehyde
Answer to Problem 8.1P
- Work done by the system is zero.
- Potential energy drop is zero.
- Kinetic energy drop is also 0.
- No moving parts in the system.
- There is no energy transfer to and from the system
Explanation of Solution
From total energy balance,
Since the kinetic energy, potential energy and the work done are zero.
Using part (a),
Therefore, total energy for the system is,
Assumptions.
- Work done by the system is zero.
- Potential energy drop is zero.
- Kinetic energy drop is also 0.
- No moving parts in the system.
- There is no energy transfer to and from the system
(d)
Interpretation:
A formula for Cv should be derived and it should be used to calculate the heat required for the given case.
Concept introduction:
Thermodynamic closed system in which no exchange of matter takes place, but the exchange of heat occurs then the work done by the system is zero.
The specific internal energy of formaldehyde Vapor is given by:
Where T= temperature of formaldehyde
Answer to Problem 8.1P
Explanation of Solution
Use the given equation,
Differentiate both sides,
Rearranging the above equation,
At constant volume,
Apply the given values as,
Differentiate the equation as,
Finally, calculate the change of moles for the given case as,
Want to see more full solutions like this?
Chapter 8 Solutions
ELEM PRIN OF CHEMICAL PROC(LL)+NEXTGEN
Additional Engineering Textbook Solutions
Starting Out with Programming Logic and Design (5th Edition) (What's New in Computer Science)
Modern Database Management
Java: An Introduction to Problem Solving and Programming (8th Edition)
Starting Out With Visual Basic (8th Edition)
Electric Circuits. (11th Edition)
Management Information Systems: Managing The Digital Firm (16th Edition)
- 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
- Introduction to Chemical Engineering Thermodynami...Chemical EngineeringISBN:9781259696527Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark SwihartPublisher:McGraw-Hill EducationElementary Principles of Chemical Processes, Bind...Chemical EngineeringISBN:9781118431221Author:Richard M. Felder, Ronald W. Rousseau, Lisa G. BullardPublisher:WILEYElements of Chemical Reaction Engineering (5th Ed...Chemical EngineeringISBN:9780133887518Author:H. Scott FoglerPublisher:Prentice Hall
- Industrial Plastics: Theory and ApplicationsChemical EngineeringISBN:9781285061238Author:Lokensgard, ErikPublisher:Delmar Cengage LearningUnit Operations of Chemical EngineeringChemical EngineeringISBN:9780072848236Author:Warren McCabe, Julian C. Smith, Peter HarriottPublisher:McGraw-Hill Companies, The