(a)
Interpretation:
To determine the amount of work done on the water.
Concept Introduction:
This is a case of steady flow process as we assume that the fluid flowing is incompressible and has a constant density throughout the flow. Thus, use the concept of calorimetry to find out the final temperature of water.
(a)
Answer to Problem 2.1P
The amount of work done on water is
Explanation of Solution
Given information:
Total mass,
Acceleration due to gravity,
Height,
Specific heat of water,
Mass of water,
Initial temperature,
The amount of work done on water is given by,
Therefore, the amount of work done on water is
(b)
Interpretation:
To determine the internal energy change of the water.
Concept Introduction:
Internal Energy - The energy which is present within the system itself. It eliminates kinetic energy causes due to motion of the system and the potential energy of the system.
(b)
Answer to Problem 2.1P
The internal energy change of water is
Explanation of Solution
Given Data:
Total mass,
Acceleration due to gravity,
Height,
Specific heat of water,
Mass of water,
Initial temperature,
This is a case of steady flow process as we assume that the fluid flowing is incompressible and has a constant density throughout the flow. You also use the concept of calorimetry to find out the final temperature of water.
Calculation:
The internal energy change of water is given by,
Therefore, the internal energy change of water is
(c)
Interpretation:
To determine the final temperature of water, for which
Concept Introduction:
This is a case of steady flow process as we assume that the fluid flowing is incompressible and has a constant density throughout the flow. You also use the concept of calorimetry to find out the final temperature of water.
(c)
Answer to Problem 2.1P
The final temperature of water is
Explanation of Solution
Given Data:
Total mass,
Acceleration due to gravity,
Height,
Specific heat of water,
Mass of water,
Initial temperature,
This is a case of steady flow process as we assume that the fluid flowing is incompressible and has a constant density throughout the flow.
Calculation:
To determine the final temperature of water, use the first law of thermodynamics as well as with calorimetry given by the equation,
Since P is constant the equation can also be written as,
Take
Therefore, the final temperature of water is
(d)
Interpretation:
To determine the amount of heat that must be removed from the water to return it to its initial temperature.
Concept Introduction:
The specific heat is the quantity of energy that is needed to increase the temperature by
(d)
Answer to Problem 2.1P
The amount of heat removed from the water to return to its initial temperature is
Explanation of Solution
Given Data:
Total mass,
Acceleration due to gravity,
Height,
Specific heat of water,
Mass of water,
Initial temperature,
This is a case of steady flow process as we assume that the fluid flowing is incompressible and has a constant density throughout the flow. You also use the concept of calorimetry to find out the final temperature of water.
Calculation:
For the process of restoration, i.e. water returns to its initial temperature, the change in internal energy is equal but opposite to that of the initial process.
Therefore, the amount of heat removed from the water to return to its initial temperature is
(e)
Interpretation:
To determine the total energy change of the universe because of (1) the process of lowering the weight, (2) the process of cooling the water back to its initial temperature, and (3) both processes together.
Concept Introduction:
The total energy of the system is equal to the sum of all the energies.
(e)
Answer to Problem 2.1P
The total energy change in universe due to process
Explanation of Solution
Given Data:
Total mass,
Acceleration due to gravity,
Height,
Specific heat of water,
Mass of water,
Initial temperature,
This is a case of steady flow process as we assume that the fluid flowing is incompressible and has a constant density throughout the flow. You also use the concept of calorimetry to find out the final temperature of water.
Calculation:
The change in internal energy in all the processes i.e. Process
Therefore, the total energy change in universe due to process
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Chapter 2 Solutions
EBK INTRODUCTION TO CHEMICAL ENGINEERIN
- (30) 6. In a process design, the following process streams must be cooled or heated: Stream No mCp Temperature In Temperature Out °C °C kW/°C 1 5 350 270 2 9 270 120 3 3 100 320 4 5 120 288 Use the MUMNE algorithm for heat exchanger networks with a minimum approach temperature of 20°C. (5) a. Determine the temperature interval diagram. (3) (2) (10) (10) b. Determine the cascade diagram, the pinch temperatures, and the minimum hot and cold utilities. c. Determine the minimum number of heat exchangers above and below the pinch. d. Determine a valid heat exchange network above the pinch. e. Determine a valid heat exchange network below the pinch.arrow_forwardUse this equation to solve it.arrow_forwardQ1: Consider the following transfer function G(s) 5e-s 15s +1 1. What is the study state gain 2. What is the time constant 3. What is the value of the output at the end if the input is a unit step 4. What is the output value if the input is an impulse function with amplitude equals to 3, at t=7 5. When the output will be 3.5 if the input is a unit steparrow_forward
- give me solution math not explinarrow_forwardExample (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 O Transcribed Image Text: Example (7): Determine thearrow_forward14.9. 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/kgarrow_forward
- 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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