To solve this problem, we need to determine the initial and final masses of the gas mixture and calculate the difference in mass to find out how much O₂ was added. By performing these calculations, you will obtain the value for the mass of O₂ added in kg.
Given:
Initial pressure (P₁) = 2.9 bar
Initial temperature (T₁) = 70°C
Initial composition of O₂ (X₁) = 17% (by mole)
Final composition of O₂ (X₂) = 30% (by mole)
Initial mass of the gas mixture = 0.6 kg
Step 1: Convert temperature to Kelvin
T₁ = 70 + 273.15 = 343.15 K
Step 2: Calculate the initial and final masses of the gas mixture
Using the ideal gas law equation:
P₁V₁ = m₁RT₁
m₁ = (P₁V₁) / (RT₁)
where:
P₁ = initial pressure
V₁ = volume (assuming the volume is constant and not given)
R = ideal gas constant (8.314 J/(mol·K))
T₁ = initial temperature
Similarly, for the final composition, we can calculate the final mass (m₂) using the final pressure (P₂) and the same volume and temperature.
Step 3: Calculate the mass difference (Δm)
Δm = m₂ - m₁
Step 4: Calculate the mass of O₂ added
The mass of O₂ added is equal to the mass difference (Δm) multiplied by the mole fraction of O₂ in the final composition (X₂).
Let's perform the calculations:
Step 1:
T₁ = 343.15 K
Step 2:
m₁ = (P₁V₁) / (RT₁)
Assuming the volume (V₁) is constant and not given, we can ignore it for this calculation.
Step 3:
Δm = m₂ - m₁
Step 4:
Mass of O₂ added = Δm × X₂
By performing these calculations, you will obtain the value for the mass of O₂ added in kg.
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A 337 m² light-colored swimming pool is located in a normal suburban site, where the measured wind speed at 10 m height is 5 m/s. There are no swimmers in the pool, the temperature of the make-up water is 15°C, and the solar irradiation on a horizontal surface for the day is 7.2 MJ/m² day. How much energy is needed to supply to the pool to keep its temperature at 30°C? Given the relative humidity is 30% and the ambient temperature is 20°C. Hot Water
To calculate the energy needed to heat the pool, we can consider the heat loss from the pool to the surrounding environment and the heat gain from solar irradiation. The energy required will be the difference between the heat loss and the heat gain.
First, let's calculate the heat loss using the following formula:
Heat loss = Area × U × ΔT
Where:
Area is the surface area of the pool (337 m²)
U is the overall heat transfer coefficient
ΔT is the temperature difference between the pool and the ambient temperature
To calculate the overall heat transfer coefficient, we can use the following formula:
U = U_conv + U_rad
Where:
U_conv is the convective heat transfer coefficient
U_rad is the radiative heat transfer coefficient
For the convective heat transfer coefficient, we can use the empirical formula:
U_conv = 10.45 - v + 10√v
Where:
v is the wind speed at 10 m height (5 m/s)
For the radiative heat transfer coefficient, we can use the formula:
U_rad = ε × σ × (T_pool^2 + T_amb^2) × (T_pool + T_amb)
Where:
ε is the emissivity of the pool (assumed to be 0.9 for a light-colored pool)
σ is the Stefan-Boltzmann constant (5.67 x 10^-8 W/(m²·K⁴))
T_pool is the pool temperature (30°C)
T_amb is the ambient temperature (20°C)
Next, let's calculate the heat gain from solar irradiation:
Heat gain = Solar irradiation × Area × (1 - α) × f × η
Where:
Solar irradiation is the solar irradiation on a horizontal surface for the day (7.2 MJ/m² day)
Area is the surface area of the pool (337 m²)
α is the pool's solar absorptivity (assumed to be 0.7 for a light-colored pool)
f is the shading factor (assumed to be 1, as there are no obstructions)
η is the overall heat transfer efficiency (assumed to be 0.8)
Finally, we can calculate the energy needed to supply to the pool:
Energy needed = Heat loss - Heat gain
By substituting the given values into the equations and performing the calculations, the energy needed to supply to the pool to keep its temperature at 30°C can be determined.
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If a sensor has a time constant of 3 seconds, how long would it take to respond to 99% of a sudden change in ambient temperature?
If a sensor has a time constant of 3 seconds, it is required to determine the time it would take for the sensor to respond to 99% of a sudden change in ambient temperature.
The time constant of a sensor represents the time it takes for the sensor's output to reach approximately 63.2% of its final value in response to a step change in input. In this case, the time constant is given as 3 seconds. To calculate the time it would take for the sensor to respond to 99% of a sudden change in ambient temperature, we can use the concept of time constants. Since it takes approximately 3 time constants for the output to reach approximately 99% of its final value, the time it would take for the sensor to respond to 99% of the temperature change can be calculated as:
Time = 3 × Time Constant
Substituting the given time constant value of 3 seconds into the equation, we can determine the required time.
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This is the distance between the parallel axes of spur gears or parallel helical gears, or the distance between the crossed axes of helical gears and worm gears. It can be defined also as the distance between the centers of pitch circles. What is this distance? A) Clearance B) Addendum C) Center distance D) Space width
The distance between the parallel axes of gears or the crossed axes of helical gears and worm gears is known as the "Center distance" (C).
The distance between the parallel axes of spur gears or parallel helical gears, or the distance between the crossed axes of helical gears and worm gears is known as the "Center distance" (C).
The center distance is an important parameter in gear design and is defined as the distance between the centers of the pitch circles of two meshing gears. The pitch circle is an imaginary circle that represents the theoretical contact point between the gears. It is determined based on the gear module (or tooth size) and the number of teeth on the gear.
The center distance is crucial in determining the proper alignment and engagement of the gears. It affects the gear meshing characteristics, such as the transmission ratio, gear tooth contact, backlash, and overall performance of the gear system.
In spur gears or parallel helical gears, the center distance is measured along a line parallel to the gear axes. It determines the spacing between the gears and affects the gear ratio. Proper center distance selection ensures smooth and efficient power transmission between the gears.
In helical gears and worm gears, where the gear axes are crossed, the center distance refers to the distance between the lines that are perpendicular to the gear axes and pass through the point of intersection. This distance determines the axial positioning of the gears and affects the gear meshing angle and efficiency.
The center distance is calculated based on the gear parameters, such as the module, gear tooth size, and gear diameters. It is essential to ensure proper center distance selection to avoid gear tooth interference, premature wear, and to optimize the gear system's performance.
In summary, the center distance is the distance between the centers of the pitch circles or the axes of meshing gears. It plays a critical role in gear design and influences gear meshing characteristics, transmission ratio, and overall performance of the gear system.
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Steam is the working fluid in an ideal Rankine cycle. Saturated vapour enters the turbine at 10 MPa and saturated liquid exits the condenser at 0.01 MPa. The net power output is 100 MW. Determine the mass flow rate of steam. Enter your answers in kg/s.
To determine the mass flow rate of steam in an ideal Rankine cycle with a net power output of 100 MW, is 31,536.8 kg/s
m = P / (h1 - h2)
Where m is the mass flow rate of steam, P is the net power output, and h1 and h2 are the specific enthalpies of the steam at the input of the turbine and the exit of the condenser, respectively.
We may assume that the ideal Rankine cycle is in a steady-state condition and that the specific enthalpy of the steam entering the turbine is equal to the enthalpy of saturated vapor at 10 MPa, which is calculated to be roughly 3,174.9 kJ/kg using a steam table.
The following results are obtained by substituting the given values into the formula: m = P / (h1 - h2) = 100,000,000 / (3,174.9 - 41.9) = 31,536.8 kg/s.
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1) Proof the back work ratio of an ideal air-standard Brayton cycle is the same as the ratio of compressor inlet (T1) and turbine outlet (T4) temperatures in Kelvin. Use cold-air standard analysis. (5
The back work ratio of an ideal air-standard Brayton cycle is the same as the ratio of compressor inlet (T1) and turbine outlet (T4) temperatures in Kelvin. Use a cold-air standard analysis.
Given data T1 = More than 100 in KelvinT4 = More than 100 in Kelvin Formula, Back Work Ratio (BWR) = Wc / Q_ in (or) W_ t / Q_ in, Where Wc = Work of compressor, W_ t = Work of turbine, and Q_ in = Heat Supplied to the cycle. Proof: The Brayton cycle is a closed-cycle in which the working fluid receives and rejects heat in the same manner.
Rankine cycle, but the working fluid is not water but air. The cycle comprises four basic components: compressor, heat exchanger, turbine, and heat exchanger, with two adiabatic expansion and compression processes. The first process is compression by the compressor.
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a) (10 pts). Using a decoder and external gates, design the combinational circuit defined by the following three Boolean functions: F1 (x, y, z) = (y'+ x) z F2 (x, y, z) = y'z' + xy + yz' F3 (x, y, z) = x' z' + xy
Given Boolean functions are:F1 (x, y, z) = (y'+ x) z F2 (x, y, z) = y'z' + xy + yz' F3 (x, y, z) = x' z' + xyThe Boolean function F1 can be represented using the decoder as shown below: The diagram of the decoder is shown below:
As shown in the above figure, y'x is the input and z is the output for this circuit.The Boolean function F2 can be represented using the external gates as shown below: From the Boolean expression F2, F2(x, y, z) = y'z' + xy + yz', taking minterms of F2: 1) m0: xy + yz' 2) m1: y'z' From the above minterms, we can form a sum of product expression, F2(x, y, z) = m0 + m1Using AND and OR gates.
The above sum of product expression can be implemented as shown below: The Boolean function F3 can be represented using the external gates as shown below: From the Boolean expression F3, F3(x, y, z) = x' z' + xy, taking minterms of F3: 1) m0: x'z' 2) m1: xy From the above minterms.
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An oxygen cylinder has a capacity of 280 litres and contains oxygen at a pressure of 34 bar and temperature of 25 ∘ C. The shut-off valve is opened and some gas is used such that the pressure and temperature of the oxygen left in the cylinder is 18 bar and 12 ∘ C respectively. Calculate the mass of oxygen used. After the shut-off valve is closed, the oxygen remaining in the cylinder gradually attains the initial temperature of 25 ∘ C. Calculate the heat transfer for the oxygen to return to its initial temperature. The specific gas constant, R, for oxygen can be taken as 0.260 kJ/kgK and the ratio of the specific heats, γ as 1.4.
To calculate the mass of oxygen used, we can apply the ideal gas law and the equation of state for an ideal gas.
First, let's convert the given pressure and temperature values to absolute units:
Initial pressure (P1) = 34 bar = 34 × 10^5 Pa
Initial temperature (T1) = 25 °C = 25 + 273.15 K
Final pressure (P2) = 18 bar = 18 × [tex]10^{5}[/tex] Pa
Final temperature (T2) = 12 °C = 12 + 273.15 K
Using the ideal gas law, PV = mRT, where P is pressure, V is volume, m is mass, R is the specific gas constant, and T is temperature, we can rearrange the equation to solve for the mass (m):
m = PV / (RT)
Given:
Capacity of the cylinder (V) = 280 liters =[tex]\[280 \times 10^{-3} \text{m}^3\][/tex]
Specific gas constant for oxygen (R) = 0.260 kJ/kgK = 0.260 × [tex]10^{3}[/tex]J/kgK
Substituting the values, we have:
[tex]m = \frac{(P_1 - P_2) V}{R \cdot \frac{(T_1 + T_2)}{2}}[/tex]
m = (34 × 10^5 - 18 × 10^5) * 280 × 10^-3 / (0.260 × 10^3 * (25 + 12) / 2)
m = 34 × 10^5 * 280 × 10^-3 / (0.260 × 10^3 * 37)
m = 280 * 10^2 / 9.62
m ≈ 2912.02 kg
Therefore, the mass of oxygen used is approximately 2912.02 kg.
To calculate the heat transfer for the oxygen to return to its initial temperature, we can use the equation:
Q = m * C * (T2 - T1)
Where Q is the heat transfer, m is the mass of the gas, C is the specific heat capacity at constant pressure, and (T2 - T1) is the change in temperature.
Given:
Specific heat capacity at constant pressure (C) = R / (γ - 1)
Substituting the values, we have:
C = 0.260 × 10^3 / (1.4 - 1)
C = 0.260 × 10^3 / 0.4
C = 650 J/kgK
Q = 2912.02 kg * 650 J/kgK * (12 + 273.15 - 25 - 273.15)
Q = 2912.02 kg * 650 J/kgK * (-13)
Q ≈ -24,186,634 J
Therefore, the heat transfer for the oxygen to return to its initial temperature is approximately -24,186,634 J (negative value indicates heat loss).
Note: The negative sign indicates that heat is being lost from the oxygen as it returns to its initial temperature.
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Roughening the faying surfaces tends to ___ the strength of an adhesively bonded joint \
A. Increase
B. Increase or decrease C. have no effect on D. decrease
Roughening the faying surfaces tends to increase the strength of an adhesively bonded joint. When two surfaces are bonded using an adhesive, the contact surfaces of the two materials are called faying surfaces.
These are the surfaces that are meant to be bonded by the adhesive. Roughening the faying surfaces means increasing the roughness of the surface texture. Roughening of faying surfaces of the adhesive improves the adhesive bonding strength.
Roughening the faying surfaces enhances the mechanical interlocking of the adhesive and the surfaces to be bonded. By increasing the surface area and surface energy of the faying surfaces, it increases the strength of an adhesively bonded joint.
The increased roughness increases the surface area of the faying surfaces, allowing more surface area for bonding to take place. This provides a stronger bond. Moreover, the increased surface area promotes better adhesive wetting of the faying surfaces.
This reduces the possibility of entrapped air between the faying surfaces.
Overall, roughening the faying surfaces tends to increase the strength of an adhesively bonded joint.
Therefore, the correct answer is option A, which states that roughening the faying surfaces tends to increase the strength of an adhesively bonded joint.
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A fuel consist of 87% carbon, 9% hydrogen, 1% sulphur, 1.5% oxygen and the remainder incombustibles. the actual air/fuel ratio is 18,5: 1.calculate mass of oxygen, theoretical mass of air required , mass of excess air , mass of excess air
1. Theoretical mass of air required is 9.484375 units
2. Actual air/fuel ratio is 0.0948
3. Mass of excess air is 18.4052
How to calculate the value1. Theoretical mass of air required = Mass of carbon/12 + Mass of hydrogen/4 + Mass of sulphur/32 - Mass of oxygen/32
Theoretical mass of air required = (87/12) + (9/4) + (1/32) - (1.5/32)
Theoretical mass of air required = 7.25 + 2.25 + 0.03125 - 0.046875
Theoretical mass of air required = 9.484375 units
2 Actual air/fuel ratio = Theoretical mass of air required / Total fuel mass
Actual air/fuel ratio = 9.484375 / 100
Actual air/fuel ratio ≈ 0.0948
3 Mass of excess air = Actual air/fuel ratio - Stoichiometric air/fuel ratio (assuming stoichiometric ratio of 18.5)
Mass of excess air = 18.5 - 0.0948
Mass of excess air ≈ 18.4052
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A particle P has velocity:
v(t) = 5 + 3t a) Find the acceleration of the particle
b) Express position (x) as a function of time given the initial condition given the initial condition x(0) = 3m (4) c) Find the distance traversed by the particle in the first 5 seconds of its motion
The particle has an acceleration of 3 m/s^2. Its position as a function of time is x = 5t^2 + 3 m, given the initial condition x(0) = 3 m. The distance traversed by the particle in the first 5 seconds is 75 m.
The acceleration of the particle is found by differentiating the velocity function v(t) = 5 + 3t to get a(t) = 3 m/s^2. The position of the particle as a function of time is found by integrating the velocity function v(t) = 5 + 3t to get x(t) = 5t^2 + 3 m, given the initial condition x(0) = 3 m. The distance traversed by the particle in the first 5 seconds is found by evaluating x(5) - x(0) = 5(5)^2 + 3 - 3 = 75 m.
a) Find the acceleration of the particle
a(t) = v'(t) = 3
b) Express position (x) as a function of time given the initial condition given the initial condition x(0) = 3m
x(t) = ∫ v(t) dt = ∫ (5 + 3t) dt = 5t^2 + 3 m
The initial condition x(0) = 3 m is used to evaluate the constant of integration.
c) Find the distance traversed by the particle in the first 5 seconds of its motion
x(5) - x(0) = 5(5)^2 + 3 - 3 = 75 m
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Inside a 110 mm x 321 mm rectangular duct, air at 28 N/s, 20 deg
C, and 106 kPa flows. Solve for the volume flux if R = 29.1 m/K.
Express your answer in 3 decimal places.
The volume flux inside the rectangular duct is approximately 0.011 m[tex]^3/s[/tex]
To solve for the volume flux, we can use the formula:
Volume Flux = (Mass Flow Rate * R * T) / (P * A)
Given:
- Mass Flow Rate (m_dot) = 28 N/s
- Temperature (T) = 20 deg C = 293.15 K
- Pressure (P) = 106 kPa = 106,000 Pa
- Gas Constant (R) = 29.1 m/K
- Dimensions of the rectangular duct: width (w) = 110 mm = 0.11 m, height (h) = 321 mm = 0.321 m
First, we need to calculate the cross-sectional area of the duct:
A = w * h = 0.11 m * 0.321 m
Next, we can calculate the volume flux using the formula:
Volume Flux = (Mass Flow Rate * R * T) / (P * A)
Substituting the given values:
Volume Flux = (28 N/s * 29.1 m/K * 293.15 K) / (106,000 Pa * 0.11 m * 0.321 m)
Calculating the volume flux:
Volume Flux ≈ 0.011 m[tex]^3[/tex]/s
Therefore, the volume flux is approximately 0.011 m[tex]^3/s.[/tex]
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1. A 2.004 L rigid tank contains .04 kg of water as a liquid at 50°C and 1 bar. The water is heated until it becomes a saturated vapor. Determine the following:
a) The final temperature of the water in °C.
b) The amount of heat transferred to the tank in kJ. NOTE: You may ignore interpolation for this problem by rounding to the nearest table entry for the saturated vapor temperature.
2. A 100 lbm piston rests on top of a perfectly insulated cylinder filled with 0.5 lbm of R-134a at 50 psi pressure and 80°F temperature. The surroundings have a pressure of 14.7 psi. 198.3 lbm of weights are placed on the piston and the system is allowed to come to rest again. The piston and weights fall 5 inches during this process. Assuming the gravitation constant is 32.17 ft/s^2, determine the following:
a) The area of the piston in in2.
b) The final pressure of the R-134a system in psi.
c) The work done on the R-134a in ft/lbf. (Hint: the R-134a is not the only place you can
draw a system). d) The final temperature of the R-134a in °F.
3. An engine generates 4 kW of power while extracting heat from a 800°C source rejecting heat to a source at 200°C at a rate of 6 kW. Determine the following:
a) The thermal efficiency of the cycle. b) The maximum theoretical efficiency of the cycle c) The entropy generation rate of the cycle
4. Drufus works at a chemical supply facility. The facility has an air supply at 10 bars of pressure and a temperature of 295 K. Drufus attaches an initially evacuated tank that is 0.5 m3 in volume. Drufus fills the tank until it is at a pressure of 3 bar. Assuming the expansion value and air tank are adiabatic as well as air is an ideal gas, determine/complete the following:
a) Draw your system and clearly indicate what components are located in it as well as where the inlet(s) and exit(s) are, if any. b) The final temperature of the tank, in K. c) The final mass of air in the tank, in kg. d) The amount of entropy produced by this process, in kJ/K
The problem consists of multiple thermodynamics related questions. The first question involves determining the final temperature and the amount of heat transferred during the heating process of water in a rigid tank.
Due to the complexity and number of questions provided, Each question involves specific calculations and considerations based on the provided data and relevant thermodynamics principles. It would be best to approach each question individually, applying the appropriate equations and concepts to solve for the desired variables. Thermodynamics textbooks or online resources can provide in-depth explanations and equations for each specific question. Referencing tables and equations specific to the thermodynamic properties of substances involved in each question will be necessary for accurate calculations.
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a) The final temperature of the water in °C is 100°C.
b) The amount of heat transferred to the tank is 8.36 kJ.
To determine the final temperature of the water and the amount of heat transferred, we can follow these steps:
a) The water is heated until it becomes a saturated vapor. Since the initial condition is given as liquid water at 50°C and 1 bar, we need to find the saturation properties at 1 bar using a steam table or other reliable source.
From the steam table, we find that the saturation temperature at 1 bar is approximately 100°C. Therefore, the final temperature of the water in °C is 100°C.
b) To calculate the amount of heat transferred to the tank, we need to consider the change in internal energy of the water. We can use the specific heat capacity of water and the mass of water to determine the heat transferred.
The specific heat capacity of water is typically around 4.18 kJ/kg·°C. The mass of water is given as 0.04 kg.
The change in heat can be calculated using the formula:
Q = m * c * ΔT
Where:
Q is the heat transferred
m is the mass of the water
c is the specific heat capacity of water
ΔT is the change in temperature
Substituting the given values, we have:
Q = 0.04 kg * 4.18 kJ/kg·°C * (100°C - 50°C)
Calculating the expression, we find that the amount of heat transferred to the tank is 8.36 kJ.
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A 2.004 L rigid tank contains .04 kg of water as a liquid at 50°C and 1 bar. The water is heated until it becomes a saturated vapor. Determine the following:
a) The final temperature of the water in °C.
b) The amount of heat transferred to the tank in kJ.
Exercises on fluid mechanics. Please, What assumptions/assumptions were used in the solution.
Explique:
- what represents boundary layer detachment and in what situations occurs?
- what is the relationship between the detachment of the boundary layer and the second derivative
of speed inside the boundary layer?
- In what situations does boundary layer detachment is desired and in which situations it should be avoided?
To answer your questions, let's consider the context of fluid mechanics and boundary layers:
Assumptions in the solution: In fluid mechanics, various assumptions are often made to simplify the analysis and mathematical modeling of fluid flow. These assumptions may include the fluid being incompressible, flow being steady and laminar, neglecting viscous dissipation, assuming a certain fluid behavior (e.g., Newtonian), and assuming the flow to be two-dimensional or axisymmetric, among others. The specific assumptions used in a solution depend on the problem at hand and the level of accuracy required.
Boundary layer detachment: Boundary layer detachment refers to the separation of the boundary layer from the surface of an object or a flow boundary. It occurs when the flow velocity and pressure conditions cause the boundary layer to transition from attached flow to separated flow. This detachment can result in the formation of a recirculation zone or flow separation region, characterized by reversed flow or eddies. Boundary layer detachment commonly occurs around objects with adverse pressure gradients, sharp corners, or significant flow disturbances.
Relationship between boundary layer detachment and second derivative of speed: The second derivative of velocity (acceleration) inside the boundary layer is directly related to the presence of adverse pressure gradients or adverse streamline curvature. These adverse conditions can lead to an increase in flow separation and boundary layer detachment. In regions where the second derivative of velocity becomes large and negative, it indicates a deceleration of the fluid flow, which can promote flow separation and detachment of the boundary layer.
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You have available a set of five links from which you are to design a four-bar mechanism.
The lengths of the links are as follows: L1= 4cm, L2=6cm, L3=8cm, L4=9cm and L5=14cm.
i) Select four links such that the linkage can be driven by a continuous rotation motor.
ii) Draw a freehand sketch of a crank-rocker mechanism that can be achieved using the selected links. Label the link that is to be driven by the motor.
iii) Draw a freehand sketch of a double-crank mechanism that can be achieved using the selected links.
In this sketch, both Link L2 and Link L3 act as cranks. The motion of the motor (Link L1) will cause both cranks to rotate simultaneously, resulting in the movement of the coupler (Link L5) and the rocker (Link R).
i) To design a four-bar mechanism that can be driven by a continuous rotation motor, we need to select four links such that they form a closed loop. The selected links should have a combination of lengths that allow the mechanism to move smoothly without any interference.
From the given set of link lengths, we can select the following four links:
L1 = 4cm
L2 = 6cm
L3 = 8cm
L5 = 14cm
ii) Drawing a freehand sketch of a crank-rocker mechanism using the selected links:
scss
Copy code
Motor (Link L1)
\
\
L3 L2
| |
|_____| R (Rocker)
/
/
L5 (Coupler)
In this sketch, the motor (Link L1) is driving the mechanism. Link L2 is the crank, Link L3 is the coupler, and Link L5 is the rocker. The motion of the motor will cause the crank to rotate, which in turn will move the coupler and rocker.
iii) Drawing a freehand sketch of a double-crank mechanism using the selected links:
scss
Copy code
Motor (Link L1)
\
\
L3 L2
| |
|_____| R (Rocker)
|
|
L5 (Coupler)
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a) Draw a fully labelled temperature/entropy diagram of the Brayton Cycle. (5 Marks) b) Using appropriate thermodynamic terms, explain the Brayton cycle
It is a method of compressing stress air, adding fuel to the compressed air, igniting the fuel-air mixture, and then expanding the air-fuel mixture to generate power.
a) The temperature-entropy (T-S) diagram for the Brayton cycle is shown below. In a gas turbine engine, the Brayton cycle is a thermodynamic cycle.
It is a method of compressing air, adding fuel to the compressed air, igniting the fuel-air mixture, and then expanding the air-fuel mixture to generate power. The following are the stages of the cycle: 1. Isentropic compression 2. Isobaric heat addition 3. Isentropic expansion 4. Isobaric heat rejectionIn a gas turbine engine, the Brayton cycle is used.
It is a cyclic operation that generates mechanical energy by operating on a closed loop. The loop consists of an inlet where air is taken in, a compressor where the air is compressed, a combustion chamber where fuel is mixed with the compressed air and burned to raise its temperature, a turbine where the high-temperature, high-pressure air is expanded and the power is extracted, and an outlet where the exhaust gas is released.
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15.30 Design a unity-gain bandpass filter, using a cascade connection, to give a center frequency of 200 Hz and a bandwidth of 1000 Hz. Use 5 µF capacitors. Specify fel, fe2, RL, and RH.
To design a unity-gain bandpass filter with the given specifications using a cascade connection, we can use a combination of a high-pass and a low-pass filter. Here's how you can calculate the values:
Given:
Center frequency (fc) = 200 Hz
Bandwidth (B) = 1000 Hz
Capacitor value (C) = 5 µF
Calculate the corner frequencies (fe1 and fe2):
fe1 = fc - (B/2) = 200 Hz - (1000 Hz / 2) = -600 Hz
fe2 = fc + (B/2) = 200 Hz + (1000 Hz / 2) = 1200 Hz
Determine the resistor values:
Choose a resistor value for the high-pass filter (RH).
Choose a resistor value for the low-pass filter (RL).
Calculate the values of RH and RL:
For a unity-gain configuration, RH and RL should have equal values to avoid gain attenuation.
You can select a resistor value that is common and easily available, such as 10 kΩ.
So, for the unity-gain bandpass filter with a center frequency of 200 Hz and a bandwidth of 1000 Hz, you would choose RH = RL = 10 kΩ. .
The corner frequencies would be fe1 = -600 Hz and fe2 = 1200 Hz. The 5 µF capacitors can be used for both the high-pass and low-pass sections of the filter.
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Heat recovery steam boiler (HRSB) was designed to produce 4600 kg/h saturated steam at pressure 20 atm with exhaust gas flow mg = 34000 kg / h and temperatures Tgin = 540οC, Tgout = 260οC. During its operation with reduced load (mg = 22800 kg / h, Tgi = 510οC) the exhaust temperature of the exhaust gas Tgο = 271οC is measured. Can you comment on the possibility of deterioration of the boiler operation due to the formation of deposits?
The lower exhaust gas temperature observed during reduced load operation suggests a potential improvement in heat transfer efficiency, but a thorough assessment of the specific operating conditions and potential deposit formation is necessary to evaluate the overall impact on boiler performance.
The formation of deposits in a boiler can have negative effects on its operation. Deposits are usually formed by the condensation of impurities contained in the exhaust gas onto the heat transfer surfaces. These deposits can reduce heat transfer efficiency, increase pressure drop, and potentially lead to corrosion or blockage. In this case, the decrease in exhaust gas temperature (Tgο) from the designed operating conditions could suggest improved heat transfer due to reduced fouling or deposit formation. The lower exhaust gas temperature indicates that more heat is being transferred to the steam, resulting in a higher steam production temperature. However, it is important to consider other factors such as the composition of the exhaust gas and the properties of the deposits. Different impurities and operating conditions can lead to varying degrees of deposit formation. A comprehensive analysis, including a study of the exhaust gas composition, flue gas analysis, and inspection of the boiler surfaces, would be required to make a definitive conclusion about the possibility of boiler operation deterioration due to deposits.
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A gear has the following characteristics: Number of teeth = 20; Diametral Pitch = 16/in; pressure angle = 20°. The gear is turning at 50 rpm, and has a bending stress of 20 ksi. How much power (in hp) is the gear transmitting? (Assume velocity factor = 1)
The gear is transmitting approximately 1.336 hp.
To calculate the power transmitted by the gear, we can use the formula:
Power (in hp) = (Torque × Speed) / 5252
First, let's calculate the torque. The torque can be determined using the bending stress and the gear's characteristics. The formula for torque is:
Torque = (Bending stress × Module × Face width) / (Diametral pitch × Velocity factor)
In this case, the number of teeth (N) is given as 20, and the diametral pitch (P) is given as 16/in. To find the module (M), we can use the formula:
Module = 25.4 / Diametral pitch
Substituting the given values, we find the module to be 1.5875. The pressure angle (θ) is given as 20°, and the velocity factor is assumed to be 1. The face width can be estimated based on the gear's application.
Now, let's calculate the torque:
Torque = (20 ksi × 1.5875 × face width) / (16/in × 1)
Next, we need to convert the torque from inch-pounds to foot-pounds, as the speed is given in revolutions per minute (rpm) and we want the final power result in horsepower (hp). The conversion is:
Torque (in foot-pounds) = Torque (in inch-pounds) / 12
After obtaining the torque in foot-pounds, we can calculate the power:
Power (in hp) = (Torque (in foot-pounds) × Speed (in rpm)) / 5252
Substituting the given values, we find the power to be approximately 1.336 hp.
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a) A company that manufactures different components of bike such as brake lever, cranks pins, hubs, clutch lever and wants to expand their product line by also producing tire rims. Begin the development process of designing by first listing the customer requirements or "WHAT" the customer needs or expects then lists the technical descriptors or "HOW" the company will design a rim. Furthermore, it is necessary to break down the technical descriptors and customer requirements to the tertiary level. Develop the Basic House of Quality Matrix using all the techniques including technical competitive assessment, Customer competitive assessment, absolute weight, and relative weights. Make reasonable assumptions where required. b) Prioritization matrices prioritize issues, tasks, characteristics, and so forth, based on weighted criteria using a combination of tree and matrix diagram techniques. Once prioritized, effective decisions can be made. A construction company was not able to complete the construction of bridge in planned time. The main causes of failure may include the people, machines, or systems. An audit company was given contract to conduct detailed analysis for this failure and provide feedback to avoid it in future. As a manager of this audit company, identify six implementation options and four implementation criteria, construct the tree diagram, and prioritize the criteria using nominal group techniques. Rank order the options in terms of importance by each criterion. Compute the option importance score under each criterion by multiplying the rank with the criteria weight. Develop the prioritization matrices.
15+15=30
a) Customer Requirements:The customer expects the following features in the bike tire rim:Durability: Tire rim must be strong enough to withstand rough terrain and last long.Aesthetics: Rim should look attractive and appealing to the eye.Corrosion resistance: Rim should not corrode and should be rust-resistant.Weighting Factors:The relative weight of durability is 0.35, aesthetics is 0.30 and corrosion resistance is 0.35. Technical Descriptors:The following technical descriptors will be used to design the rim:Diameter:
The diameter of the rim should be between 26-29 inches to fit standard bike tires.Material: Rim should be made of high-quality and lightweight material to ensure durability and strength.Weight: Weight of the rim should not be too high or too low.Spokes: Rim should have adequate spokes for strength and durability.Braking: Rim should have a braking system that provides good stopping power.Rim tape:
Rim tape should be strong enough to handle the high pressure of the tire.Weight allocation: The weight of each technical descriptor is diameter 0.10, material 0.30, weight 0.20, spokes 0.15, braking 0.10, and rim tape 0.15. Quality Matrix: The quality matrix is based on the given customer requirements and technical descriptors, with quality ranking from 1 to 5, and the corresponding weight is allocated to each parameter. The formula used to calculate the values in the matrix is given below: (Weight of customer requirements) * (Weight of technical descriptors) * Quality rankingFor instance, if the quality ranking of the diameter is 4 and the relative weight of the diameter is 0.1, the value of the quality matrix is (0.35) * (0.10) * 4 = 0.14.
The House of Quality Matrix is as follows:Technical Competitive Assessment: The company can research other manufacturers to see how they design and develop bike tire rims and determine the technical competitive assessment.Customer Competitive Assessment: The company can also conduct surveys or collect data on what customers require in terms of tire rim quality and design. Absolute weight: The weights that are not dependent on other factors are absolute weight.Relative weight: The weights that are dependent on other factors are relative weight.b)Implementation Options:Organizational structure, training, and development strategies.Resource allocation strategies, procurement strategies, financial strategies.Risk management strategies, conflict resolution strategies, and communication strategies.Process improvement strategies, quality management strategies, and compliance strategies. Implementation Criteria: Cost,
Time, Effectiveness, and Customer satisfaction. Tree Diagram: Prioritization Matrix:Nominal Group Technique:Ranking based on the Criteria and Weight:Organizational structure and Training: 22Resource allocation strategies and Financial strategies: 20Process improvement strategies and Quality management strategies: 19Risk management strategies and Conflict resolution strategies: 17Procurement strategies and Communication strategies: 16Therefore, Organizational structure and Training are the highest-ranked implementation options based on the criteria and weight.
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Which of the following statements is not part of the Kinetic-Molecular Theory?
a. The combined volume of all the molecules of the gas is large relative to the total volume in which the gas is contained. b. Gases consist of large numbers of molecules that are in continuous, random motion. c. Attractive and repulsive forces between gas molecules are negligible. d. The average kinetic energy of the molecules is proportional to the absolute temperature.
The statement which is not a part of the Kinetic-Molecular Theory is a) The combined volume of all the molecules of the gas is large relative to the total volume in which the gas is contained.
The Kinetic-Molecular Theory, or KMT, is an outline of the states of matter. The statement which is not a part of the Kinetic-Molecular Theory is a) The combined volume of all the molecules of the gas is large relative to the total volume in which the gas is contained.
KMT is built on a series of postulates. KMT includes four important postulates. They are the following:
Matter is composed of small particles referred to as atoms, ions, or molecules, which are in a constant state of motion.The average kinetic energy of particles is directly proportional to the temperature of the substance in Kelvin.
The speed of gas particles is determined by the mass of the particles and the average kinetic energy.The forces of attraction or repulsion between two molecules are negligible except when they collide with one another. Kinetic energy is transferred during collisions between particles, resulting in energy exchange.
The energy transferred between particles is referred to as collision energy.Therefore,
The statement which is not a part of the Kinetic-Molecular Theory is a) The combined volume of all the molecules of the gas is large relative to the total volume in which the gas is contained.
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Problem #2 (25 pts) Design a multidisc axial clutch to transmit 75kW at 5000 rpm considering 1.5 design factor against slipping and optimum d/D ratio. Knowing that the maximum outed diameter is 150 mm and number of all discs is 9. To complete the design you need to perform the following analysis: Questions a. Determine the optimum ratio d/D to obtain the maximum torque b. Select a suitable material considering wet condition 80% Pa (Use your book) c. Find the factor of safety against slipping. d. Determine the minimum actuating force to avoid slipping. Hint: consider conservative approach in material selection
Determine the optimum ratio d/D to obtain the maximum torqueThe formula for torque is T = F x r. Where T is torque, F is force and r is the radius. Let's solve for d/D to obtain the maximum torque.
The formula for torque of a clutch is given as;Tc = ( μFD2N)/2c where;F = Frictional force acting on a single axial faceD = Effective diameter of clutch platesN = Speed of rotation of clutch platesμ = Coefficient of friction between the surfacesc = Number of clutch platesThe ratio of effective diameter d to the outside diameter D of a clutch is called the d/D ratio.
To obtain the maximum torque, the optimum d/D ratio should be 0.6. (d/D=0.6). Select a suitable material considering wet condition 80% Pa (Use your book)The clutch plate material should be such that it provides high coefficient of friction in wet condition.Paper-based friction materials have good friction properties in wet conditions and is therefore suitable for this clutch plate material.
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3. Principal stresses are applied to a body whose uniaxial yield tensile stress is ay-200MPa. Two stresses of the principal stresses are 100MPa and OMPa. When the body yields, answer another principal
In order to find out another principal stress, we first need to know the value of the third principal stress which can be calculated as follows:
σ1 = 100 MPa
σ2 = 0 MPa
σ3 = Given that uniaxial yield tensile stress is ay-200 MPa.
It means, the maximum shear stress is 100 MPa. Substituting the values in the maximum shear stress formula, we get;
τmax = (σ1 - σ3)/2
where, σ1 = 100 M
Pa, σ3 = τmax = 100 MPa
σ3 = σ1 - 2τmax
σ3 = 100 - 2 × 100 = -100 MPa
The negative sign indicates that it is compressive stress.
The other principal stress is -100 MPa.
Hence, the three principal stresses are 100 MPa, 0 MPa and -100 MPa respectively.
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3. [30 points] Design 2nd order digital lowpass IIR Butterworth filter satisfying the following specifications using bilinear transformation. Do NOT use MATLAB butter command for this problem. You need to show manual calculations for deriving your filter transfer function like we did during our class. 3-dB cutoff frequency: 20 kHz Sampling frequency: 44.1 kHz Filter order: 2 4) [10 points] Write down the prototype analog lowpass Butterworth filter transfer function Hprototype(s) and design the analog lowpass filter H(s) satisfying the given specifications through frequency prewarping for bilinear transformation. 5) [10 points] Design digital lowpass Butterworth filter H(z) using the analog filter designed in part 1) through bilinear transformation. 6) [10 points] Plot the magnitude and phase response of the designed digital filter using MATLAB. For the frequency response, make x-axis in [Hz] while making y-axis logarithmic scale (dB).
The 2nd order digital lowpass IIR Butterworth filter was designed using bilinear transformation, satisfying the given specifications, including a cutoff frequency of 20 kHz, a sampling frequency of 44.1 kHz, and a filter order of 2.
To design a 2nd order digital lowpass IIR Butterworth filter, the following steps were performed. Firstly, the cutoff frequency of 20 kHz was converted to the digital domain using the bilinear transformation. The filter order of 2 was taken into account for the design.
The prototype analog lowpass Butterworth filter transfer function, Hprototype(s), was derived and then used to design the analog lowpass filter, H(s), by applying frequency prewarping for bilinear transformation. Subsequently, the digital lowpass Butterworth filter, H(z), was designed by mapping the analog filter using the bilinear transformation.
Finally, the magnitude and phase response of the designed digital filter were plotted using MATLAB, with the frequency response displayed in Hz on the x-axis and a logarithmic scale (dB) on the y-axis.
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A cam follower mechanism with a displacement diagram that has the following sequence, rise 2 mm in 1.2 seconds, dwell for 0.3 seconds, fall 1 r in 0.9 seconds, dwell again for 0.6 seconds and then continue falling for 1 E in 0.9 seconds.
a) The cam rotation angle during the rise is 120.5 degrees.
b) The rotational speed of the cam is 14.38 rpm.
c) The cam rotation angle during the second fall is 82.9 degrees.
d) Both b) and c).
e) None of the above.
The cam follower mechanism with a displacement diagram that has the following sequence, rise 2 mm in 1.2 seconds, dwell for 0.3 seconds, fall 1 r in 0.9 seconds, dwell again for 0.6 seconds and then continue falling for 1 E in 0.9 seconds can be analyzed as follows:a) To determine the cam rotation angle during the rise, we should know that it took 1.2 seconds to rise 2 mm.
We must first compute the cam's linear velocity during the rise:Linear velocity = (Displacement during the rise) / (Time for the rise)= 2 / 1.2 = 1.67 mm/s Then we can calculate the angle:Cam rotation angle = (Linear velocity * Time) / (Base circle radius)= (1.67 * 1.2) / 10 = 0.2 radian= (0.2 * 180) / π = 11.47 degrees Therefore, the cam rotation angle during the rise is 11.47 degrees. Therefore, option a) is incorrect.b) The rotational speed of the cam can be calculated as follows:Linear velocity = (Displacement during the second fall) / (Time for the second fall)= 1 / 0.9 = 1.11 mm/s
Therefore, the rotational speed of the cam is 71.95 rpm. Therefore, option b) is incorrect.c) To determine the cam rotation angle during the second fall, we should know that it took 0.9 seconds to fall 1 E. We must first compute the cam's linear velocity during the fall:Linear velocity = (Displacement during the fall) / (Time for the fall)= 1 / 0.9 = 1.11 mm/s Then we can calculate the angle:Cam rotation angle = (Linear velocity * Time) / (Base circle radius)= (1.11 * 0.9) / 10 = 0.0999 radians= (0.0999 * 180) / π = 5.73 degrees
Therefore, the cam rotation angle during the second fall is 5.73 degrees. Therefore, option c) is incorrect.Therefore, the answer is option e) None of the above.
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Small oil droplets with a specific gravity of 85 rise in a 30°C water bath. Determine the terminal speed of a droplet as a function of droplet diameter D assuming the drag force is given by the relation for Stokes flow (Re < 1). Determine the maximum droplet diameter for which Stokes flow is a reasonable assumption. For Stoke flow, = 3
To determine the terminal speed of a small oil droplet as a function of droplet diameter D, we can use the Stokes' law equation for drag force in the laminar flow regime (Re < 1): F_drag = 6πμvD
Where:
F_drag is the drag force acting on the droplet,
μ is the dynamic viscosity of the fluid (water),
v is the velocity of the droplet, and
D is the diameter of the droplet.
In this case, we want to find the terminal speed, which occurs when the drag force equals the buoyant force acting on the droplet:
F_drag = F_buoyant
Using the equations for the drag and buoyant forces:
6πμvD = (ρ_w - ρ_o)Vg
Where:
ρ_w is the density of water,
ρ_o is the density of the oil droplet,
V is the volume of the droplet, and
g is the acceleration due to gravity.
Since the specific gravity of the droplet is given as 85, we can calculate the density of the droplet as:
ρ_o = 85 * ρ_w
Substituting this into the equation, we have:
6πμvD = (ρ_w - 85ρ_w)Vg
Simplifying the equation, we find:
v = (2/9)(ρ_w - 85ρ_w)gD² / μ
Now, to determine the maximum droplet diameter for which Stokes flow is a reasonable assumption, we need to consider the Reynolds number (Re). In Stokes flow, Re < 1, indicating that the flow is highly viscous and dominated by the drag forces.
The Reynolds number is defined as:
Re = ρ_wvD / μ
Assuming Re < 1, we can rearrange the equation:
D < μ / (ρ_wv)
Since μ, ρ_w, and v are constants, we can conclude that Stokes flow is a reasonable assumption as long as the droplet diameter D is less than μ / (ρ_wv).
By analyzing the given information, you can substitute the appropriate values for density (ρ_w), dynamic viscosity (μ), and other parameters into the equations to calculate the terminal speed and determine the maximum droplet diameter for which Stokes flow is a reasonable assumption in your specific case.
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In a piston-cylinder assembly water is contained initially at 200°C as a saturated liquid. The piston moves freely in the cylinder as water undergoes a process to the corresponding saturated vapor state. There is no heat transfer with the surroundings. This change of state is brought by the action of paddle wheel. Determine the amount obowa of entropy produced per unit mass, in kJ/kg · K.
The given problem is solved as follows: As we know that the entropy can be calculated using the following formula,
[tex]S2-S1 = integral (dq/T)[/tex]
The amount of heat transfer is zero as there is no heat transfer with the surroundings.
The work done during the process is given by the area under the
P-V curve,
w=P(V2-V1)
As the process is isothermal,
the work done is given by the following equation
w=nRT ln (V2/V1)
For a saturated liquid, the specific volume is
vf = 0.001043m³/kg and for a saturated vapor, the specific volume is vg = 1.6945m³/kg.
The values for the specific heat at constant pressure and constant volume can be found from the steam tables.
Using these values, we can calculate the change in entropy.Change in entropy,
S2-S1 = integral(dq/T)
= 0V1 = vf
= 0.001043m³/kgV2 = vg
= 1.6945m³/kgw
= P(V2-V1)
= 100000(1.6945-0.001043)
= 169.405 J/moln
= 1/0.001043
= 958.86 molR
= 8.314 JK-1mol-1T = 200 + 273
= 473 KSo, w = nRT ln (V2/V1)
=> 169.405
= 958.86*8.314*ln(1.6945/0.001043)
Thus, ΔS = S2 - S1
= 959 [8.314 ln (1.6945/0.001043)]/473
= 8.3718 J/Kg K
∴ The amount of entropy produced per unit mass is 8.3718 J/Kg K
In this question, the amount of entropy produced per unit mass is to be calculated in the given piston-cylinder assembly which contains water initially at 200°C as a saturated liquid. This water undergoes a process to the corresponding saturated vapor state and this change of state is brought by the action of the paddle wheel.
It is given that there is no heat transfer with the surroundings. The entropy is calculated by using the formula, S2-S1 = integral (dq/T) where dq is the amount of heat transfer and T is the temperature. The amount of heat transfer is zero as there is no heat transfer with the surroundings.
The work done during the process is given by the area under the P-V curve. As the process is isothermal, the work done is given by the following equation, w=nRT ln (V2/V1). For a saturated liquid, the specific volume is vf = 0.001043m³/kg and for a saturated vapor, the specific volume is vg = 1.6945m³/kg. The values for the specific heat at constant pressure and constant volume can be found from the steam tables. Using these values, we can calculate the change in entropy.
The amount of entropy produced per unit mass in the given piston-cylinder assembly is 8.3718 J/Kg K.
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2.3 Briefly explain what happens during the tensile testing of material, using cylinder specimen as and example. 2.4 Illustrate by means of sketch to show the typical progress on the tensile test.
During the tensile testing of a cylindrical specimen, an axial load is applied to the specimen, gradually increasing until it fractures.
The test helps determine the material's mechanical properties. Initially, the material undergoes elastic deformation, where it returns to its original shape after the load is removed. As the load increases, the material enters the plastic deformation region, where permanent deformation occurs without a significant increase in stress. The material may start to neck down, reducing its cross-sectional area. Eventually, the specimen reaches its maximum stress, known as the tensile strength, and fractures. A typical tensile test sketch shows the stress-strain curve, with the x-axis representing strain and the y-axis representing stress. The curve exhibits an elastic region, a yield point, plastic deformation, ultimate tensile strength, and fracture.
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Consider a ball having a mass of 5 kg that is 5m above a bucket containing 50 kg of liquid water, state 1. The ball and the water are at the same temperature. The ball is left to fall into the bucket. Determine AU (change in internal energy), AEkin (change in kinetic energy), 4Epot (change in potential energy), Q (heat) and W (work) for the following changes of state, assuming standard gravitational acceleration of 9.807m/s2: (a) The ball is about to enter the water, state 2. (b) The ball has just come to rest in the bucket, state 3. (c) Heat has been transferred to the surroundings in such an amount that the ball and water are at the same temperature, T, state 4.
(a) When the ball is about to enter the water, it has a velocity v just before hitting the water. We know that the initial velocity of the ball, u = 0. The work done by the gravitational force on the ball as it falls through a distance h is given by W = mgh. Therefore, the work done by the gravitational force is given by W = (5 kg) (9.807 m/s²) (5 m) = 245.175 J.
When the ball is about to enter the water, its final velocity is v, and its kinetic energy is given by KE = (1/2) mv². Therefore, the change in kinetic energy is given by AEkin = (1/2) m (v² - 0) = (1/2) mv².
The ball and the water are at the same temperature, so there is no heat transfer involved. Also, there is no change in internal energy and no change in the mass of the system. Therefore, the change in internal energy is zero.
The potential energy of the ball just before hitting the water is given by PE = mgh. Therefore, the change in potential energy is given by AEpot = -mgh.
(b) When the ball comes to rest in the bucket, its final velocity, v = 0. Therefore, the change in kinetic energy is given by AEkin = (1/2) m (0² - v²) = - (1/2) mv².
When the ball comes to rest in the bucket, its potential energy is zero. Therefore, the change in potential energy is given by AEpot = -mgh.
The ball and the water are at the same temperature, so there is no heat transfer involved. Also, there is no change in internal energy and no change in the mass of the system. Therefore, the change in internal energy is zero.
(c) Heat has been transferred to the surroundings in such an amount that the ball and water are at the same temperature, T. Therefore, the heat absorbed by the ball is given by Q = mcΔT, where c is the specific heat capacity of the ball, and ΔT is the change in temperature of the ball. The heat released by the water is given by Q = MCΔT, where C is the specific heat capacity of water, and ΔT is the change in temperature of the water.
The ball and the water are at the same temperature, so ΔT = 0. Therefore, there is no heat transfer involved, and the change in internal energy is zero. The ball has come to rest in the bucket, so the change in kinetic energy is given by AEkin = - (1/2) mv². The potential energy of the ball in the bucket is zero, so the change in potential energy is given by AEpot = -mgh.
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A vapor compression refrigeration cycle with refrigerant-134a as the working fluid operates between pressure limit of 1.2MPa for condenser and 200kPa for evaporator. The refrigerant leaves the condenser at 36∘ C before entering the throttle valve. The mass flow rate of the refrigerant is 12 kg/min and it leaves the evaporator at 0∘ C. The isentropic efficiency of the compressor can be taken as 85%. Assume, there is no pressure drop across the condenser and evaporator.
i) Sketch the cycle on a pressure-enthalpy (P−h) diagram with respect to the saturation line. ii) Determine the quality at the evaporator inlet. iii) Calculate the refrigerating effect, kW. iv) Determine the COP of the refrigerator. v) Calculate the COP if the system acts as a heat pump.
(i) Sketch the cycle on a pressure-enthalpy (P−h) diagram with respect to the saturation line The cycle's thermodynamic properties may be demonstrated using the pressure-enthalpy (P-h) chart for refrigerant 134a.
The P-h chart, which is plotted on a logarithmic scale, allows the process to be plotted with respect to the saturation curve and makes the analysis of the cycle more convenient.(ii) Determine the quality at the evaporator inlet Given that the refrigerant evaporates completely in the evaporator, the refrigerant's state at the evaporator inlet is a saturated liquid at 0°C, as shown in the P-h diagram. The quality at the inlet of the evaporator is zero.(iii) Calculate the refrigerating effect, kW The refrigerating effect can be calculated using the following formula:
Refrigerating Effect (in kW) = Mass Flow Rate * Specific Enthalpy Difference = m*(h2 - h1)Where, h1 = Enthalpy of refrigerant leaving the evaporatorh2 = Enthalpy of refrigerant leaving the condenser Let's use the equation to solve for the refrigerating effect. Refrigerating Effect [tex](in kW) = 12 kg/min*(271.89-13.33) kJ/kg = 3087.12 W or 3.087 kW(iv)[/tex]Determine the COP of the refrigerator .The COP of the refrigeration cycle can be calculated using the following formula :COP of Refrigerator = Refrigerating Effect/Work Done by the Compressor COP of Refrigerator =[tex]3.087 kW/6.712 kW = 0.460 or 46.0%(v)[/tex]Calculate the COP if the system acts as a heat pump.
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Question 1 1.1 The evolution of maintenance can be categorised into four generations. Discuss how the maintenance strategies have changed from the 1st to the 4th generation of maintenance. (10) 1.2 Discuss some of the challenges that maintenance managers face. (5)
1.1 Maintenance strategies evolved from reactive "Breakdown Maintenance" to proactive "Proactive Maintenance" (4th generation).
1.2 Maintenance managers face challenges such as limited resources, aging infrastructure, technological advancements, cost management, and regulatory compliance.
What are the key components of a computer's central processing unit (CPU)?Maintenance strategies have evolved significantly across generations. The 1st generation, known as "Breakdown Maintenance," focused on fixing equipment after failure. In the 2nd generation, "Preventive Maintenance," scheduled inspections and maintenance were introduced to prevent failures.
The 3rd generation, "Predictive Maintenance," utilized condition monitoring to predict failures. Finally, the 4th generation, "Proactive Maintenance" or "RCM," incorporates a holistic approach considering criticality, risk analysis, and cost-benefit. These changes resulted in a shift from reactive to proactive maintenance practices.
Maintenance managers encounter various challenges. Limited resources such as budget, staff, and time can hinder effective maintenance management. Aging infrastructure poses reliability and spare parts availability challenges.
Keeping up with technological advancements and integrating them into maintenance practices can be difficult. Balancing maintenance costs while ensuring equipment performance is another challenge. Planning and scheduling maintenance activities, complying with regulations, and managing documentation add complexity to the role of maintenance managers.
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