Concept explainers
(a)
Interpretation:
A flowchart for the given process is to be drawn and labelled. The validation of the given statement that subsystem containing the point where the bypass stream splits off from the evaporator feed has one degree of freedom is to be stated. The degree of freedom analysis for the overall system, the evaporator, bypass-evaporator product and the mixing point is to be predicted. The equations to determine all unknown stream variable are to be shown. The variable in each equation is to be circled.
Concept introduction:
The evaporation is a process that aids in the conversion of a liquid into gas due to rise in temperature. The process of evaporation becomes faster with the increase in surface area because it permits the liquid molecules to acquire more heat. It results in the increase in kinetic energy of molecules, which aids to overcome of attractive forces between molecules of liquid.
In reverse osmosis, the solvent passes in the opposite direction to that of osmosis.
(b)
Interpretation:
The amount of product produced per
Concept introduction:
The evaporation is a process that aids in the conversion of a liquid into gas due to rise in temperature. The process of evaporation becomes faster with the increase in surface area because it permits the liquid molecules to acquire more heat. It results in the increase in kinetic energy of molecules, which aids to overcome of attractive forces between molecules of liquid.
In reverse osmosis, the solvent passes in the opposite direction to that of osmosis.
(c)
Interpretation:
The possible drawbacks for the given proposal are to be stated.
Concept introduction:
The evaporation is a process that aids in the conversion of a liquid into gas due to rise in temperature. The process of evaporation becomes faster with the increase in surface area because it permits the liquid molecules to acquire more heat. It results in the increase in kinetic energy of molecules, which aids to overcome of attractive forces between molecules of liquid.
In reverse osmosis, the solvent passes in the opposite direction to that of osmosis.
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Chapter 4 Solutions
Elementary Principles of Chemical Processes
- 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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