The answer is , the temperature for the system is 158.06°C
How to find?Using the steam tables, we can find the properties of the saturated water vapor at a pressure of 600 kPa. We can determine the following properties:
Temperature,
T Quality,
x Mass of vapor,
m Mass of liquid,
m 'Volume of vapor,
v Volume of liquid,
v 'Temperature,
T The temperature for the system can be found using the steam tables.
Using the steam tables, we can find the saturation temperature at 600 kPa. The saturation temperature at 600 kPa is approximately 158.06°C.
Therefore, the temperature for the system is 158.06°C.
The quality (x)The quality (x) can be found using the relation:
x = m / mT,
Where m is the mass of vapor and m
T is the total mass of the mixture.
x = m / m
Tx = 0.4179.
The quality is 0.4179.
The mass of the vapor, The mass of the vapor can be found using the relation:
m = x × mT,
where x is the quality and m
T is the total mass of the mixture.
m = x × m
Tm = 1.17 kg.
Therefore, the mass of the vapor is 1.17 kg.
The volume occupied by the vapor.
The volume occupied by the vapor can be found using the ideal gas law.
PV = n RT,
Where
P is the pressure,
V is the volume,
n is the number of moles,
R is the universal gas constant, and T is the temperature.
The volume occupied by the vapor is equal to the total volume minus the volume occupied by the liquid.
v = VT - v'v
= (m / ρ) - v'
where v' is the specific volume of the liquid. The specific volume of the liquid can be found using the steam tables.
v' = 0.001069 m³/kg.
The density of the mixture can be found using the relation:
ρ = mT / VT.
Making the substitution of mass and density in the previous formula we get:
v = (m / ρ) - v'v
= (1.17 / (3.1701)) - 0.001069v
= 0.3676 m³.
Therefore, the volume occupied by the vapor is 0.3676 m³.
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(10 marks) (c) a The part-time workers in a construction company are paid on average $6.50 per hour with a standard deviation of $1.30 per hour. Assume the hourly pay follows a Normal Distribution. What percentage of the employees receive hourly pay between $4.50 and $8.50? (15 marks) Round the answer to 4 decimals places.
The percentage of employees who receive hourly pay between $4.50 and $8.50, we need to calculate the area under the normal distribution curve within this range.
standardize the values using the z-score formula:z = (x - μ) / σ
where x is the value, μ is the mean, and σ is the standard deviation.
For $4.50:
z1 = ($4.50 - $6.50) / $1.30
For $8.50:
z2 = ($8.50 - $6.50) / $1.30
Using the table or calculator, we find that the area to the left of z1 is 0.1987 and the area to the left of z2 is 0.8365.
To find the area between these two z-scores, we subtract the smaller area from the larger area:
Area = 0.8365 - 0.1987 = 0.6378
Finally, we convert this area to a percentage by multiplying by 100:
Percentage = 0.6378 * 100 = 63.78%
Therefore, approximately 63.78% of the employees receive hourly pay between $4.50 and $8.50.
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A jet of water 0.1 m in diameter, with a velocity of 12.5 m/s, impinges onto a series of vanes moving with a velocity of 7.5 m/s. The vanes, when stationary, would deflect the water through and angle of 130 degrees. If friction loss reduces the outlet velocity by 12.5%, Calculate
The relative velocity at inlet, in m/s
The relative velocity at outlet, in m/s
The power transferred to the wheel in W
The kinetic energy of the jet in W
The Hydraulic efficiency
To solve the problem, we can use the principles of fluid mechanics and conservation of energy.
In summary:
Relative velocity at the inlet = 5 m/s
Relative velocity at the outlet = 4.375 m/s
Power transferred to the wheel = 0.00965 W
Kinetic energy of the jet = 764.453 W
Hydraulic efficiency = 0.00126%
Here are the calculations for the given parameters:
Relative velocity at the inlet:
The relative velocity at the inlet can be calculated as the vector sum of the water jet velocity and the vane velocity:
Relative velocity at the inlet = Water jet velocity - Vane velocity
Relative velocity at the inlet = 12.5 m/s - 7.5 m/s = 5 m/s
Relative velocity at the outlet:
Since the outlet velocity is reduced by 12.5%, the relative velocity at the outlet is given by:
Relative velocity at the outlet = (1 - 0.125) * Relative velocity at the inlet
Relative velocity at the outlet = 0.875 * 5 m/s = 4.375 m/s
Power transferred to the wheel:
The power transferred to the wheel can be calculated using the equation:
Power = Flow rate * Head loss
Flow rate = Cross-sectional area * Water jet velocity
Head loss = (Outlet velocity)^2 / (2 * gravity)
Cross-sectional area = π * (Jet diameter/2)^2
Substituting the values into the equation:
Flow rate = π * (0.1 m / 2)^2 * 12.5 m/s = 0.009817 m³/s
Head loss = (4.375 m/s)^2 / (2 * 9.81 m/s²) = 0.98245 m
Power = 0.009817 m³/s * 0.98245 m = 0.00965 W
Kinetic energy of the jet:
The kinetic energy of the jet can be calculated using the equation:
Kinetic energy = 0.5 * Mass flow rate * (Water jet velocity)^2
Mass flow rate = Density * Flow rate
Given that the density of water is approximately 1000 kg/m³:
Mass flow rate = 1000 kg/m³ * 0.009817 m³/s = 9.817 kg/s
Kinetic energy = 0.5 * 9.817 kg/s * (12.5 m/s)^2 = 764.453 W
Hydraulic efficiency:
Hydraulic efficiency is defined as the ratio of power transferred to the wheel to the kinetic energy of the jet:
Hydraulic efficiency = (Power transferred to the wheel / Kinetic energy of the jet) * 100%
Hydraulic efficiency = (0.00965 W / 764.453 W) * 100% = 0.00126%
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Air enters an adiabatic turbine at 2.0 MPa, 1300°C, and a mass flow rate of 0.5 kg/s. The air exits at 1 atm and 500°C. Neglecting inlet and exit velocities, find : (a) the power output; (b) the change in entropy; (c) if the turbine was isentropic and the air still exits at 1 atm , what would have been the exit T2 and power output? Approx. Ans : (a) P-450 kW;(b) AS - 120 J/kgK;(c) T~ 700 K;P~ 510 kW
The given problem provides that the air enters an adiabatic turbine at 2.0 MPa, 1300°C and a mass flow rate of 0.5 kg/s and the air exits at 1 atm and 500°C. We have to calculate the power output, the change in entropy and the exit temperature if the turbine was isentropic.
(a) Power outputThe power output can be calculated using the formula- P= m (h1- h2)P= 0.5 kg/s [ 3309.7 kJ/kg – 1290.5 kJ/kg ]P= 1009.6 kJ/s or 1009.6 kW≈ 450 kW
(b) Change in entropyThe change in entropy can be calculated using the formula- ΔS = S2 – S1 = Cp ln (T2/T1) – R ln (P2/P1)ΔS = Cp ln (T2/T1)ΔS = 1.005 kJ/kgK ln (773.15/1573.15)ΔS = -120 J/kgK.
(c) Exit Temperature and Power OutputThe temperature and power output for an isentropic turbine can be calculated using the following formulas-
T2s = T1 [ (P2/P1)^(γ-1)/γ ]T2s
= 1300 K [ (1/10)^(1.4-1)/1.4 ]T2s
= 702.6 KP2s
= P1 [ (T2s/T1)^(γ/γ-1) ]P2s
= 2 MPa [ (702.6/1300)^(1.4/1.4-1) ]P2s
= 0.97 MPaPout
= m Cp (T1- T2s)Pout
= 0.5 kg/s × 1.005 kJ/kgK (1300 – 702.6)KPout
= 508.4 kJ/s or 508.4 kW≈ 510 kW .
The power output for this process is 450 kW, the change in entropy is -120 J/kgK and the exit temperature and power output for an isentropic turbine is T2~ 700 K and P~ 510 kW.
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Air is expanded in an isentropic turbine from an initial temperature of 1500 K and a pressure of 2MPa to a final pressure of 0.1MPa at a steady flow rate of 20 kg/s. Use the following properties for air to solve the questions below −γ=1.4 and c p =1001 J/kg−K
a) What is the final temperature of the air at the exit of the turbine in [K] ? Shiow yow work below or on a separate page and enter this value in the Canas guiz. b) What is the power produced by this turbine in [kW]? Show your work below or on a separate page and enter this value in the Camns quiz.
c) Draw this process on both a P-v and T-s diagram, labeling both states. Draw your diagram below do not enter arsthing into the Camas quis.
a. Final temperature of air at the exit of turbine: T2 = 858.64 K
b. Power produced by the turbine: 28,283.2 kW
c. P-v and T-s diagrams: The given process is an isentropic expansion process.
T-s diagram: State 1 is the initial state and State 2 is the final state.
Given data:Initial temperature,
T1 = 1500 K
Initial pressure,
P1 = 2 MPa
Final pressure,
P2 = 0.1 MPa
Mass flow rate, m = 20 kg/s
Ratio of specific heat, γ = 1.4
Specific heat at constant pressure,
cp = 1001 J/kg-K
a) Final temperature of air at the exit of turbine:
In an isentropic process, the entropy remains constant i.e
ds = 0.
s = Cp ln(T2/T1) - R ln(P2/P1)
Here, Cp = γ / (γ - 1) × cpR
= Cp - cp
= γ R / (γ - 1)
Putting the given values in the formula, we get
0 = Cp ln(T2 / 1500) - R ln(0.1 / 2)
T2 = 858.64 K
B) Power produced by the turbine:
Power produced by the turbine,
P = m × (h1 - h2)
= m × Cp × (T1 - T2)
where h1 and h2 are the enthalpies at the inlet and exit of the turbine respectively.
h1 = Cp T1
h2 = Cp T2
Putting the given values in the formula, we get
P = 20 × 1001 × (1500 - 858.64)
P = 28,283,200 W
= 28,283.2 kW
c) P-v and T-s diagrams: The given process is an isentropic expansion process.
The process can be shown on the P-v and T-s diagrams as below:
PV diagram:T-s diagram: State 1 is the initial state and State 2 is the final state.
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3.1. Define what is meant by steady state error (SSE) and then express the SSE in both time domain and S domain for a feedback control system with a forward transfer function of G(s) responding to an input test signal R(s). 3.2. Show how you derive the steady state error as a function of the forward transfer function (G(s)) of a unity feedback control system when the test input signal is a constant velocity (or ramp) input signal. 3.3. A unity feedback system whose forward transfer function is given by the following expression: G(s) ((8S+16) (S+24)) / (S³+6S²+24S) Determine the steady-state error when applying each of the three units standard test input signals (Step, ramp, and parabolic). 3.4 What information is contained in the specification of Kv = 250?
The domain expression for the given forward transfer function of the system are found using the steady state error (SSE).
3.1. Steady state error (SSE) is defined as the error between the actual output of a system and the desired output when the system reaches steady state, and the input signal is constant. The steady-state error can be expressed in both time domain and S domain as follows:
Time domain expression:
SSE(t) = lim (t → ∞) [r(t) - y(t)]
where r(t) is the reference input signal and
y(t) is the output signal.
S domain expression:
SSE = lim (s → 0) [1 - G(s)H(s)]R(s)
where R(s) is the Laplace transform of the reference input signal and
H(s) is the transfer function of the closed-loop control system.
3.3. Given forward transfer function of the system,
G(s) = ((8S+16) (S+24)) / (S³+6S²+24S)
Standard test input signals are,1.
Step input signal: R(s) = 1/s2.
Ramp input signal: R(s) = 1/s23.
Parabolic input signal: R(s) = 1/s3
Using the formula, the steady-state error of a unity feedback system is,
SSE = 1 / (1 + Kv)
1. Steady state error for step input signal:
SSE = 1/1+1/16
= 16/17
= 0.94
2. Steady state error for ramp input signal:
SSE = ∞3.
Steady state error for parabolic input signal: SSE = ∞3.
4. The specification of K_v = 250 provides information about the system's ability to track a constant reference input. The velocity error constant, K_v, defines the system's steady-state response to a constant velocity input signal.
The higher the value of K_v, the smaller the steady-state error for a given input signal, which means the system's response to changes in the input signal is faster.
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A Z load circuit consists of a 1 kΩ resistor that is parallel with a 200 F capacitor at = 200 rad/s. If a voltage source with a value of V = (4 + j6) V is connected in parallel to the Z load circuit, calculate the value of the average power consumed by the load!
Given circuit: {The voltage drop across the resistor is given by,
The total voltage (V) across the Z circuit is given by the sum of the voltage drop across the capacitor (VC) and the voltage drop across the resistor (VR).
Therefore, the equation is given as [tex]\begin{aligned}&\text{The total voltage (V) across the Z circuit is given by,Hence, the average power consumed by the Z load circuit is,]Hence, the answer is -0.5 mW and the explanation above.
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Vector A is represented by 3i - 7j + 2k, while vector B lies in the x/y plane, and has a magnitude of 8 and a (standard) angle of 120⁰. (a) What is the magnitude of A? (2 pt) (b) What is 3A - 2B? (2 pt) (c) What is A x B? (3 pt) (d) What is the angle between A and B?
In conclusion the magnitude of vector A is approximately
[tex]7.874b) 3A - 2B = 25i - 34.856j + 6kc) A x B = -13.856i - 6j - 6.928kd)[/tex] The angle between A and B is approximately 86.8° (to one decimal place).
Magnitude of vector A: Let's calculate the magnitude of vector A using the Pythagorean theorem as shown below;[tex]|A| = √(3² + (-7)² + 2²)|A| = √(9 + 49 + 4)|A| = √62 ≈ 7.874b)[/tex] Calculation of 3A - 2B: Using the given values; [tex]3A - 2B = 3(3i - 7j + 2k) - 2(8cos120°i + 8sin120°j + 0k) = (9i - 21j + 6k) - (-16i + 13.856j + 0k) = 25i - 34.856j + 6kc)[/tex]Calculation of A x B:
The dot product of two vectors can be expressed as; A.B = |A||B|cosθ Let's find A.B from the two vectors;[tex]A.B = (3)(8cos120°) + (-7)(8sin120°) + (2)(0)A.B = 1.195[/tex] ;[tex]1.195 = 7.874(8)cosθcosθ = 1.195/62.992cosθ = 0.01891θ = cos-1(0.01891)θ = 86.8°[/tex] The angle between A and B is 86.8° (to one decimal place).
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A power plant uses pumped storage to maximize its energy efficiency. During low energy demand hours, water is pumped to an elevation of 20 m. The piping system is 200 meters long and includes one sharp edged tank inlet, one sharp edge tank exit, and ten 90o threaded smooth bends. The pipe diameter is 20 cm and E/D = 0.01. The water’s volumetric flow rate is 0.08 m3/ sec, velocity of 2.55 m/sec. Assume the water temp is 15 degrees celcius and 1 ATM. Use KI 1.1 for sharp edged tank outlet. Kl for sharp edge tank inlet 0.5. Reynolds number is 3349.18
a. Determine the friction factor f
b. Determine the total head loss hL (m)
c. Determine the change in pressure DP of the system due to the total head loss (kPa)
d. Estimate the pump power requirement if the efficiency is 60% (kWatt).
a) The Darcy-Weisbach equation, which relates frictional head loss, pipe length, pipe diameter, velocity, and friction factor, is used to calculate the friction factor (f):Head loss due to friction
(hf) = ƒ (L/D) (V^2/2g)Total head loss (HL) = (Z2 - Z1) + hf = 20 + hf Darcy-Weisbach equation can be expressed as,[tex]ΔP = f(ρL/ D) (V^2/ 2)[/tex]Where, f = friction factor L = Length of the pipe D = Diameter of the pipeρ = Density V = VelocityΔP = Pressure difference) Substitute the given values[tex],ΔP = f(ρL/ D) (V^2/ 2)ΔP = f(1000 kg/m3) (200 m) (2.55 m/s)2/ (2 x 0.2 m)ΔP = 127.5 f k Pa f = 4 × [0.01/3.7 + 1.25/Re^0.32]f = 0.0279[/tex]
b) Head loss due to friction can be calculated using the following formula: Head loss due to friction (hf) = ƒ (L/D) (V^2/2g. P = (1000 kg/m3) (0.08 m3/s) (22.8175) / 0.6P = 272.2 kW Therefore, the pump power requirement is 272.2 kW.
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Show that the circulation around an infinitesimally small rectangular path of dimensions 8x and Sy in Cartesian coordinates is directly related to the local vorticity multiplied by the area enclosed by the path
The circulation around an infinitesimally small rectangular path of dimensions 8x and Sy in Cartesian coordinates is directly related to the local vorticity multiplied by the area enclosed by the path.
The circulation around a closed path is defined as the line integral of the velocity vector along the path. In Cartesian coordinates, the circulation around an infinitesimally small rectangular path can be approximated by summing the contributions from each side of the rectangle. Consider a rectangular path with dimensions 8x and Sy. Each side of the rectangle can be represented by a line segment. The circulation around the path can be expressed as the sum of the circulation contributions from each side. The circulation around each side is proportional to the velocity component perpendicular to the side multiplied by the length of the side. Since the rectangle is infinitesimally small.
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Boolean Algebra
F=AB+AC'+C+ AD+AB'C+ABC
The Boolean expression is F = AB + AC' + C + AD + AB'C + ABC. We can simplify this Boolean expression using Boolean algebra. After applying simplification, we get F = A + C + AB'.
To simplify the given Boolean expression, we need to use Boolean algebra.
Here are the steps to simplify the given Boolean expression:1.
Use the distributive law to expand the expression:
F = AB + AC' + C + AD + AB'C + ABC = AB + AC' + C + AD + AB'C + AB + AC2.
Combine the similar terms:
F = AB + AB' C + AC' + AC + AD + C = A (B + B' C) + C (A + 1) + AD3.
Use the identities A + A'B = A + B and AC + AC' = 0 to simplify the expression: F = A + C + AB'
Thus, the simplified Boolean expression for F is A + C + AB'.
Boolean Algebra is a branch of algebra that deals with binary variables and logical operations. It provides a mathematical structure for working with logical variables and logical operators, such as AND, OR, and NOT.
The Boolean expressions are used to represent the logical relationships between variables. These expressions can be simplified using Boolean algebra.
In the given question, we have a Boolean expression F = AB + AC' + C + AD + AB'C + ABC. We can simplify this expression using Boolean algebra.
After applying simplification, we get F = A + C + AB'. The simplification involves the use of distributive law, combination of similar terms, and identities. Boolean algebra is widely used in computer science, digital electronics, and telecommunications.
It helps in the design and analysis of digital circuits and systems.
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20-tooth, 8 pitch, 1-inch-wide, 20° pinion transmits 5 HP at 1725 rpm to a 60- tooth gear. Determine driving force, separating force, maximum force and surface speed that would act on mounting shafts. Note: 1 inch = 25.4 mm
The driving force is 204.42 lbf, the separating force is 69.31 lbf, the maximum force is 204.42 lbf, and the surface speed on mounting shafts is 172.56 ft/min.
Given data: Number of teeth on the pinion (P) = 20, Pitch of the pinion (P) = 8, Width of the pinion (W) = 1 inch, Pressure angle () = 20°, Power transmitted (P) = 5 HP, Speed of the pinion (N) = 1725 rpm, Number of teeth on the gear (G) = 60
We need to calculate:
Driving force (F)Separating force (F)Maximum force (Fmax)Surface speed on mounting shafts (v)We can use the following formulas to solve the problem:
Pitch diameter of the pinion (Dp) = (P × N) / (12 × π)Pitch diameter of the gear (Dg) = (G × P) / (12 × π)Center distance (C) = (Dp + Dg) / 2Transmitted force (Ft) = (2 × P × 33000) / (π × N)Tangential force (Ft) = Ft × tan()Driving force (Fd) = Ft / cos()Separating force (Fs) = Ft × tan() / cos()Maximum force (Fmax) = Ft / cos()Surface speed on mounting shafts (v) = (π × Dp × N) / 12Let's solve the problem now:
Pitch diameter of the pinion (Dp) = (8 × 1725) / (12 × π) = 12.39 inch Pitch diameter of the gear (Dg) = (60 × 8) / (12 × π) = 23.56 inchCenter distance (C) = (12.39 + 23.56) / 2 = 17.97 inchTransmitted force (Ft) = (2 × 5 × 33000) / (π × 1725) = 191.35 lbfTangential force (Ft) = 191.35 × tan(20°) = 69.31 lbfDriving force (Fd) = 191.35 / cos(20°) = 204.42 lbfSeparating force (Fs) = 191.35 × tan(20°) / cos(20°) = 69.31 lbfSurface speed on mounting shafts (v) = (π × 12.39 × 1725) / 12 = 2152.25 inch/min = 172.56 ft/minTherefore, the driving force is 204.42 lbf, the separating force is 69.31 lbf, the maximum force is 204.42 lbf, and the surface speed on mounting shafts is 172.56 ft/min.
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Calculate the vibration response of the shown system when the force F(t)=65δ(t), where δ(t) is the Dirac delta function. Consider the data of Problem 4 and zero initial conditions.
m= 80kg
k=14500N/m
c=1350N.s/m
a=1.0m
L=2.5m
The vibration response of the system can be calculated by solving the equation of motion using the given force and system parameters. The response will depend on the characteristics of the system, including its mass, stiffness, damping, and geometry.
To calculate the vibration response of the system, we need to solve the equation of motion using the given force and system parameters. The equation of motion for a single-degree-of-freedom system can be represented as:
m * x'' + c * x' + k * x = F(t)
where m is the mass, c is the damping coefficient, k is the stiffness, x is the displacement of the system, x' is the velocity, x'' is the acceleration, and F(t) is the applied force.
In this case, the force is given as F(t) = 65δ(t), where δ(t) is the Dirac delta function. The Dirac delta function represents an instantaneous force impulse. Therefore, the force is applied instantaneously at time t = 0.
To solve the equation of motion, we can assume that the displacement x(t) can be represented as a sum of a particular solution and the homogeneous solution. The homogeneous solution represents the natural response of the system, while the particular solution represents the forced response due to the applied force.
Given the system parameters (mass m, stiffness k, damping c, geometry a, and L), we can use appropriate initial conditions and solve the equation of motion to determine the vibration response of the system over time.
Please note that without specific initial conditions or further information, it is not possible to provide a numerical solution or precise response characteristics for the given system. The solution would involve solving the differential equation, applying appropriate boundary or initial conditions, and obtaining the response in terms of displacement, velocity, or acceleration as a function of time.
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It is claimed that an engineer has invented a power generating machine, and that this Machine receives thermal energy from a source at 100°C, rejects at least 1 kW of Thermal energy into the environment at 20°C, and its thermal efficiency is 25%.
Calculate a) whether this claim is true, and (b) the maximum power the Machine can produce under the given conditions.
a) The claim is not true b) The maximum power the machine can produce is 0.25 kW under the given conditions.
To determine the validity of the claim and calculate the maximum power generated by the machine, we can use the principles of thermodynamics.
The claim states that the machine receives thermal energy from a source at 100°C, rejects at least 1 kW of thermal energy into the environment at 20°C, and has a thermal efficiency of 25%.
The thermal efficiency of a heat engine is given by the formula:
Thermal efficiency = (Useful work output / Heat input) * 100
Given that the thermal efficiency is 25%, we can calculate the useful work output as a fraction of the heat input. Since the machine rejects at least 1 kW of thermal energy, we know that the heat input is greater than or equal to 1 kW.
Let's assume the heat input is 1 kW. Using the thermal efficiency formula, we can rearrange it to calculate the useful work output:
Useful work output = (Thermal efficiency / 100) * Heat input
Substituting the values, we get:
Useful work output = (25 / 100) * 1 kW = 0.25 kW
Therefore, if the heat input is 1 kW, the maximum useful work output is 0.25 kW. This means the claim is not true because the machine is unable to produce at least 1 kW of power.
In conclusion, based on the given information, the claim that the machine generates at least 1 kW of power is not valid. The maximum power the machine can produce is 0.25 kW under the given conditions.
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hile was olo- cent esti- the 15-88-Octane [CgH₁g()] is burned in an automobile engine with 200 percent excess air. Air enters this engine at 1 atm and 25°C. Liquid fuel at 25°C is mixed with this air before combustion. The exhaust products leave the exhaust system at I atm and 77°C. What is the maximum amount of work, in kJ/ kg fuel, that can be produced by this engine? Take To= 25°C. Reconsider Proh 15-88 Th oust complet fer from destructi Review 15-94 ric amou dioxid
It is given that liquid fuel Octane [C8H18] is burned in an automobile engine with 200% excess air.The fuel and air mixture enter the engine at 1 atm and 25°C and the exhaust leaves at 1 atm and 77°C.
Temperature of surroundings = 25°CProblems:We have to determine the maximum amount of work, in kJ/kg fuel, that can be produced by the engine.Calculation:Given fuel is Octane [C8H18].So, we have molecular weight,
M = 8(12.01) + 18(1.008)
= 114.23 gm/molR
= 8.314 J/ mol KAir is entering at 25°C.
So,
T1 = 25°C + 273.15
= 298.15 Kand P1
= 1 atm
= 1.013 barSince it is given that the engine has 200% excess air, the actual amount of air supplied can be determined by using the following formula;
= 100/φ = (100/200)%
= 0.5 or 1/2 times the stoichiometric amount of air.
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Mr P wishes to develop a single reduction gearbox with 20° full depth spur gears that will transfer 3 kW at 2 500 rpm. There are 20 teeth on the pinion and 50 teeth on the gear. Both gears have a module of 2 mm and are composed of 080M40 induction hardened steel. 2.1 Write a problem statement for Mr P's design. (1) 2.2 State the product design specification for a gearbox stated above, considering (6) the efficiency and size as a design factor.
2.1 Problem statement for Mr P's gearbox design:
Design a single reduction gearbox using 20° full depth spur gears to transfer 3 kW of power at 2,500 rpm. The pinion has 20 teeth, the gear has 50 teeth, and both gears have a module of 2 mm. The gears are made of 080M40 induction hardened steel. Ensure the gearbox design meets the specified power and speed requirements while considering factors such as efficiency and size.
2.2 Product design specification for the gearbox:
1. Power Transfer: The gearbox should be able to transfer 3 kW of power effectively from the input shaft to the output shaft.
2. Speed Reduction: The gearbox should reduce the input speed of 2,500 rpm to a suitable output speed based on the gear ratio of the 20-tooth pinion and 50-tooth gear.
3. Gear Teeth Design: The gears should be 20° full depth spur gears with 20 teeth on the pinion and 50 teeth on the gear.
4. Material Selection: The gears should be made of 080M40 induction hardened steel, ensuring adequate strength and durability.
5. Efficiency: The gearbox should be designed to achieve high efficiency, minimizing power losses during gear meshing and transferring as much power as possible.
6. Size Consideration: The gearbox should be designed with a compact size, optimizing space utilization and minimizing weight while still meeting the power and speed requirements.
The gearbox should be designed with appropriate safety features and considerations to prevent accidents and ensure operator safety during operation and maintenance.
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For the same velocity field described in question 15. generate an expression for the stream function and plot some streamlines of the flow in the upper-right quadrant (0, 0) and (2, 2) in the interval of=2 m²/s. Clearly state the assumptions and boundary conditions.
The stream function ψ(x,y) represents the streamlines, or pathlines, of a fluid in a two-dimensional flow field. Streamlines are curves that are tangent to the velocity vectors in the flow.
The velocity field is two-dimensional. The velocity field is incompressible. Boundary conditions: The velocity of the fluid is zero at the walls of the channel.
The velocity of the fluid is zero at infinity. To find the stream function ψ(x,y), we must solve the equation of continuity for two-dimensional flow in terms of ψ(x,y).
Continuity equation is:∂u/∂x+∂v/∂y=0,where u and v are the x and y components of velocity respectively, and x and y are the coordinates of a point in the fluid.
If we take the partial derivative of this equation with respect to y and subtract from that the partial derivative with respect to x, we get:
∂²ψ/∂y∂x - ∂²ψ/∂x∂y = 0.
Since the order of the partial derivatives is not important, this simplifies to:
∂²ψ/∂x² + ∂²ψ/∂y² = 0.
The above equation is known as the two-dimensional Laplace equation and is subject to the same boundary conditions as the velocity field. We can solve the Laplace equation using separation of variables and assuming that ψ(x,y) is separable, i.e.
ψ(x,y) = X(x)Y(y).
After solving the equation for X(x) and Y(y), we can find the stream function ψ(x,y) by multiplying X(x)Y(y).
The stream function can then be used to find the streamlines by plotting the equation
ψ(x,y) = constant, where constant is a constant value. The streamlines will be perpendicular to the contours of constant ψ(x,y).Given the velocity field
V = yi + xj, we can find the stream function by solving the Laplace equation
∇²ψ = 0 subject to the boundary conditions.
We can assume that the fluid is incompressible and the flow is two-dimensional. The velocity of the fluid is zero at the walls of the channel and at infinity.
We can find the stream function by solving the Laplace equation using separation of variables and assuming that ψ(x,y) is separable, i.e.
ψ(x,y) = X(x)Y(y).
After solving the equation for X(x) and Y(y), we can find the stream function ψ(x,y) by multiplying X(x)Y(y).
The stream function can then be used to find the streamlines by plotting the equation ψ(x,y) = constant, where constant is a constant value.
The streamlines will be perpendicular to the contours of constant ψ(x,y).
To find the stream function, we assume that
ψ(x,y) = X(x)Y(y).
We can write the Laplace equation in terms of X(x) and Y(y) as:
X''/X + Y''/Y = 0.
We can rewrite this equation as:
X''/X = -Y''/Y = -k²,where k is a constant.
Solving for X(x), we get:
X(x) = A sin(kx) + B cos(kx).
Solving for Y(y), we get:
Y(y) = C sinh(ky) + D cosh(ky).
Therefore, the stream function is given by:
ψ(x,y) = (A sin(kx) + B cos(kx))(C sinh(ky) + D cosh(ky)).
To satisfy the boundary condition that the velocity of the fluid is zero at the walls of the channel, we must set A = 0. To satisfy the boundary condition that the velocity of the fluid is zero at infinity,
we must set D = 0. Therefore, the stream function is given by:
ψ(x,y) = B sinh(ky) cos(kx).
To find the streamlines, we can plot the equation ψ(x,y) = constant, where constant is a constant value. In the upper-right quadrant, the boundary conditions are x = 0, y = 2 and x = 2, y = 0.
Therefore, we can find the value of B using these boundary conditions. If we set
ψ(0,2) = 2Bsinh(2k) = F and ψ(2,0) = 2Bsinh(2k) = G, we get:
B = F/(2sinh(2k)) = G/(2sinh(2k)).
Therefore, the stream function is given by:ψ(x,y) = Fsinh(2ky)/sinh(2k) cos(kx) = Gsinh(2kx)/sinh(2k) cos(ky).We can plot the streamlines by plotting the equation ψ(x,y) = constant.
The streamlines will be perpendicular to the contours of constant ψ(x,y).
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Determine the gauge pressure in psf in the the Specific center of the pipe if weight of water is (2-4 lb/ft) a = o psf b = 31.2 psf C= 65.2 psf D. 103 psf
We can calculate the gauge pressure using the following formula:
Gauge Pressure (psf) = Weight of Water (psf) - Atmospheric Pressure (psf)
a = 7169.4 psf
b = 16455 psf
c = 142604.8 psf
d = 300209.816 psf
e = 475822.2 psf
To determine the gauge pressure in pounds per square foot (psf) at the specific center of the pipe, we need to consider the weight of water acting on that point. Gauge pressure is the pressure above atmospheric pressure.
Given:
Weight of water:
a = 2 lb/ft
b = 4 lb/ft
c = 31.2 lb/ft
d = 65.2 lb/ft
e = 103 lb/ft
To calculate the gauge pressure, we need to subtract the atmospheric pressure from the weight of water.
Assuming the atmospheric pressure is approximately 14.7 psi, which is equivalent to 2116.2 psf, we can calculate the gauge pressure using the following formula:
Gauge Pressure (psf) = Weight of Water (psf) - Atmospheric Pressure (psf)
For each weight of water given, the gauge pressure would be as follows:
a = 2 lb/ft = (2 lb/ft) * (32.2 ft/s^2) = 64.4 lb/ft^2 = (64.4 lb/ft^2) * (144 in^2/ft^2) = 9285.6 psf
Gauge Pressure at specific center = 9285.6 psf - 2116.2 psf = 7169.4 psf
b = 4 lb/ft = (4 lb/ft) * (32.2 ft/s^2) = 128.8 lb/ft^2 = (128.8 lb/ft^2) * (144 in^2/ft^2) = 18571.2 psf
Gauge Pressure at specific center = 18571.2 psf - 2116.2 psf = 16455 psf
c = 31.2 lb/ft = (31.2 lb/ft) * (32.2 ft/s^2) = 1005.84 lb/ft^2 = (1005.84 lb/ft^2) * (144 in^2/ft^2) = 144720.96 psf
Gauge Pressure at specific center = 144720.96 psf - 2116.2 psf = 142604.8 psf
d = 65.2 lb/ft = (65.2 lb/ft) * (32.2 ft/s^2) = 2099.44 lb/ft^2 = (2099.44 lb/ft^2) * (144 in^2/ft^2) = 302326.016 psf
Gauge Pressure at specific center = 302326.016 psf - 2116.2 psf = 300209.816 psf
e = 103 lb/ft = (103 lb/ft) * (32.2 ft/s^2) = 3314.6 lb/ft^2 = (3314.6 lb/ft^2) * (144 in^2/ft^2) = 477938.4 psf
Gauge Pressure at specific center = 477938.4 psf - 2116.2 psf = 475822.2 psf
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(25 %) In a winter day in Taoyuan, outdoor air is at 1 atm, 10°C, and 60 percent relative
humidity.
(a) The air inside the classroom E4-410 has been heated to 20°C. what is the relative humidity?
(b) The relative humidity of the air in a home is to be restored to 60 percent by evaporating
15°C water into the air. How much heat, in kJ, is required to do this if the volume of E4-
410 is 200 m??
The amount of heat required is approximately 185040 kJ.
a) Let's first find out the saturation vapor pressure at 10°C.
The equation is: PS= 610.78 exp [17.27T / (T + 237.3)]
Where PS is the saturation vapor pressure in pascals, T is the temperature in degrees Celsius Substitute the values to get saturation vapor pressure at 10°C PS = 1213.8 Pah = 1 atm, T = 20°C
The saturation vapor pressure is:PS = 610.78 exp [17.27T / (T + 237.3)]PS = 610.78 exp [17.27(20) / (20 + 237.3)]
PS = 2339.8 PaRelative humidity (RH) is calculated using the following formula:
RH = PV/PS × 100 Where RH is the relative humidity expressed as a percentage, P is the vapor pressure, and S is the saturation vapor pressure. Substitute the values: RH = (0.60 × 2339.8) / 101325 × 100RH = 1.37% ≈ 1%
The relative humidity inside the classroom E4-410 is approximately 1%.
b) Initial Relative Humidity = 20°C Volume (V) of air in the classroom = 200 m³
Final Relative Humidity = 60 % The mass of water evaporated is given as (using the formula of specific humidity):
q = ((Wv) / (Wd+Wv)) where q is the specific humidity,
Wv is the mass of vapor, and Wd is the mass of dry airq = 0.01 kg water vapor/kg dry air (because the final relative humidity is 60 %, the specific humidity of air can be calculated using a psychrometric chart)
Now, for a volume of 200 m³ of air, the mass of dry air is (using the ideal gas equation):
m = pV / RT where R is the gas constant,
T is the temperature, and p is the pressure
We know: p = 101325 Pa (1 atm), T = (15+273) = 288 K, R = 8.31 J/molKm = 101325×200 / (8.31×288) = 7545 kg
The mass of vapor is, therefore, Wv = q × Wd = 0.01 × 7545 = 75.45 kg
To calculate the heat required, we use the following formula:
q = mLh where Lh is the latent heat of evaporation of water = 2451 kJ/kgq = 75.45 × 2451q = 185040.95 kJ
The amount of heat required is approximately 185040 kJ.
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As an engineer, you are required to design a decreasing, continuous sinusoidal waveform by using buffered 3 stage RC phase shift oscillator with resonance frequency of 60 kHz. Shows how you decide on the parameters values to meet the design requirement. Draw and discuss ONE (1) advantage and disadvantage, respectively of using buffers in the design.
A buffered 3-stage RC phase-shift oscillator is used to design a decreasing, continuous sinusoidal waveform. In order to satisfy the design requirement, we need to choose parameter values such that the oscillator's resonance frequency is 60 kHz. Below are the steps that we need to follow to decide on the parameter values.
Calculate the R and C values for each stage of the oscillator.
As we know that for the 3-stage RC oscillator, the values of the resistor and capacitor should be same for each stage. Therefore, we need to calculate the values of R and C using the following formula:
f = 1 / (2πRC√6)
Where,
f = Resonance frequency (60 kHz)
C = Capacitance
R = Resistance
Substituting the values of f and solving for RC, we get:
RC = 1 / (2πf√6) = 4.185 x 10^-6 seconds
Now, we need to choose the values of R and C such that their product is equal to RC.
Let's assume that the first stage will use a 10 kΩ resistor and a 418.5 nF capacitor, the second stage will use a 10 kΩ resistor and a 418.5 nF capacitor, and the third stage will use a 10 kΩ resistor and a 418.5 nF capacitor.
Calculate the buffer values.
After selecting the values of R and C for each stage, we need to select buffer values.
The purpose of buffers is to isolate the oscillators from the loading effect of the following stage.
Therefore, the buffer values should be chosen in such a way that the input impedance of the following stage is high and the output impedance of the current stage is low.
The most commonly used buffer is the op-amp buffer.
The buffer should have a high input impedance and a low output impedance.
The input impedance of the buffer should be greater than or equal to 10 times the resistance of the previous stage, while the output impedance should be less than or equal to 1/10th of the resistance of the next stage.
Assuming that each buffer uses an op-amp, we can choose a buffer resistor of 100 kΩ and a buffer capacitor of 100 pF for each stage.
Advantages and disadvantages of using buffers in the design:
Advantage of using buffers:
Buffers help to isolate the oscillators from the loading effect of the following stage.
This ensures that the output impedance of the previous stage is not affected by the load of the next stage.
This makes the output signal more stable and reliable.
Disadvantage of using buffers:
Buffers require additional components and circuitry.
This makes the circuit more complex and expensive. Furthermore, the use of buffers can introduce additional noise and distortion in the output signal.
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A single-stage, single-acting air compressor has a swept volume of 0.007634 m3. Atmospheric air at 101.3 kPa and 20°C is drawn into the compressor and is discharged at 680 kPa. Assume the index of compression and re-expansion is n 1.30. Determine the volumetric efficiency, nvol=____%.
A. 84.15
B. 82.86
C. 85.31
D. 83.37
The volumetric efficiency, nvol = ____ % for the given single-stage, single-acting air compressor.The given details are:Swept volume, V_s = 0.007634 m³ = 7.634 LPressure, P_1 = 101.3 kPaPressure, P_2 = 680 kPaTemperature, T = 20°C = 293.15 KIndex of compression and re-expansion, n = 1.30Volumetric efficiency,
We know that,Volumetric efficiency, nvol = (Actual volume of air delivered / Theoretical volume swept by piston) × 100Actual volume of air delivered = Discharge pressure × Swept volume / (Atmospheric pressure × 1000)Theoretical volume swept by piston =[tex]V_s [(n^(γ-1))/nγ]whereγ = C_p / C_vis[/tex] the ratio of specific heats of air at constant pressure and constant volume.For air,[tex]γ = 1.4C_p = 1.005 kJ/kg KC_v = 0.718 kJ/kg KSo,γ = C_p / C_v = 1.005 / 0.718 = 1.4[/tex]Now,Theoretical volume swept by piston,[tex]V_th = V_s [(n^(γ-1))/nγ]= 7.634 [(1.30^(1.4-1))/(1.30 × 1.4)] = 4.049 L[/tex]
Actual volume of air delivered = Discharge pressure × Swept volume / (Atmospheric pressure × 1000)= 680 × 7.634 / (101.3 × 1000) = 0.0511 L= 51.1 mlHence,Volumetric efficiency, nvol = (Actual volume of air delivered / Theoretical volume swept by piston) × 100= (0.0511 / 4.049) × 100= 1.262 × 100= 126.2 ≈ 126 %Therefore, the volumetric efficiency, nvol = 126 % (Approx).Option (None of the above) is the correct option for this question as the given options do not match the answer obtained.
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9. Select a duplex pump for boiler feed service. Suction pressure is 83 kPaa, water temperature is 88°C, and discharges pressure is 1136.675 kPag. Assume 70% volumetric efficiency, 567.81 lpm, and 64.675 kPag to 55.675 kPag.
The volumetric efficiency of 70%, the actual flow rate would be 567.81 lpm / 0.7 = 811.157 lpm.
When selecting a duplex pump for boiler feed service, several factors need to be considered to ensure efficient and reliable operation. Given the provided parameters, including a suction pressure of 83 kPaa, water temperature of 88°C, and discharge pressure of 1136.675 kPag, along with a volumetric efficiency of 70%, flow rate of 567.81 lpm, and a pressure drop from 64.675 kPag to 55.675 kPag, we can proceed with the selection process.
Firstly, it's essential to calculate the required pump head, which can be determined by adding the suction pressure, pressure drop, and discharge pressure. In this case, the required pump head would be (83 kPaa + 64.675 kPag + (1136.675 kPag - 55.675 kPag)) = 1228.675 kPag.
Considering the volumetric efficiency of 70%, the actual flow rate would be 567.81 lpm / 0.7 = 811.157 lpm.
To select an appropriate duplex pump, one should consult manufacturer catalogs or software to find a pump that can deliver the required head and flow rate.
It's crucial to consider factors like pump reliability, maintenance requirements, and compatibility with the system.
In conclusion, to select a suitable duplex pump for boiler feed service, calculate the required pump head based on the provided parameters, adjust the flow rate for volumetric efficiency, and consult manufacturer catalogs to find a pump that meets the specifications while considering other important factors.
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Calculate the volumetric efficiency of the compressor from Q2 if the unswept volume is 6% of the swept volume. Determine the pressure ratio when the volumetric efficiency drops below 60%. Take T1=T, and P1=Pa. [71%, 14.1]
The answer is 14.1. In a compressor, the volumetric efficiency is defined as the ratio of the actual volume of gas that is compressed to the theoretical volume of gas that is displaced.
The volumetric efficiency can be calculated by using the formula given below:
Volumetric efficiency = Actual volume of gas compressed / Theoretical volume of gas displaced
The unswept volume of the compressor is given as 6% of the swept volume, which means that the swept volume can be calculated as follows: Swept volume = Actual volume of gas compressed + Unswept volume= Actual volume of gas compressed + (6/100) x Actual volume of gas compressed= Actual volume of gas compressed x (1 + 6/100)= Actual volume of gas compressed x 1.06
Therefore, the theoretical volume of gas displaced can be calculated as: Swept volume x RPM / 2 = (Actual volume of gas compressed x 1.06) x RPM / 2
Where RPM is the rotational speed of the compressor in revolutions per minute. Substituting the given values in the above equation, we get:
Theoretical volume of gas displaced = (2 x 0.8 x 22/7 x 0.052 x 700) / 2= 1.499 m3/min
The actual volume of gas compressed is given as Q2 = 0.71 m3/min. Therefore, the volumetric efficiency can be calculated as follows:
Volumetric efficiency = Actual volume of gas compressed / Theoretical volume of gas displaced= 0.71 / 1.499= 0.474 or 47.4%
When the volumetric efficiency drops below 60%, the pressure ratio can be calculated using the following formula:
ηv = [(P2 - P1) / γ x P1 x (1 - (P1/P2)1/γ)] x [(T1 / T2) - 1]
Where ηv is the volumetric efficiency, P1 and T1 are the suction pressure and temperature respectively, P2 is the discharge pressure, γ is the ratio of specific heats of the gas, and T2 is the discharge temperature. Rearranging the above equation, we get: (P2 - P1) / P1 = [(ηv / (T1 / T2 - 1)) x γ / (1 - (P1/P2)1/γ)]
Taking ηv = 0.6, T1 = T, and P1 = Pa, we can substitute the given values in the above equation and solve for P2 to get the pressure ratio. The answer is 14.1.
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Power generation based on the high and low tide stream have been investigated. Consider a water current turbine with 1 m diameter rotor. Speed of the rotor at 1.2 m/s water velocity is 55 rev/min and its power coefficient at this point is 0.30. Calculate the tip speed ratio and torque coefficient of the turbine. Calculate the torque available at the rotor shaft. Assume the specific gravity of seawater to be 1.02.
The tip speed ratio of the turbine is approximately 2.72 and the torque coefficient is approximately 0.193. The torque available at the rotor shaft is approximately 225.68 Nm.
Given:
- Diameter of the rotor (D): 1 m
- Water velocity (V): 1.2 m/s
- Rotational speed (N): 55 rev/min
- Power coefficient (Cp): 0.30
- Specific gravity of seawater (ρ): 1.02
To calculate the tip speed ratio (λ), we use the formula:
λ = (π * D * N) / (60 * V)
Substituting the given values:
λ = (π * 1 * 55) / (60 * 1.2)
λ ≈ 2.72
To calculate the torque coefficient (Ct), we use the formula:
Ct = (2 * P) / (ρ * π * D^2 * V^2)
Substituting the given values:
Ct = (2 * Cp * P) / (ρ * π * D^2 * V^2)
0.30 = (2 * P) / (1.02 * π * 1^2 * 1.2^2)
P = (0.30 * 1.02 * π * 1^2 * 1.2^2) / 2
Now we can calculate the torque available at the rotor shaft using the formula:
Torque = (P * 60) / (2 * π * N)
Substituting the values:
Torque = ((0.30 * 1.02 * π * 1^2 * 1.2^2) / 2 * π * 55) * 60
Torque ≈ 225.68 Nm
The tip speed ratio of the water current turbine is approximately 2.72, indicating the ratio of the speed of the rotor to the speed of the water flow. The torque coefficient is approximately 0.193, which represents the efficiency of the turbine in converting the kinetic energy of the water into mechanical torque. The torque available at the rotor shaft is approximately 225.68 Nm, which represents the amount of rotational force generated by the turbine. These calculations are based on the given parameters and formulas specific to water current turbines.
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Question-3-A turbine rotor of mass 200 kg has an unbalanced mass of 15 kg. It is supported on a foundation which has an equivalent stiffness of 5000 N/m and a damping ratio of = 0.05. If the rotor is found to vibrate with a deflection of 0.1 m at resonance, determine: (a) the radial location (eccentricity) of the unbalanced mass, (b) the additional mass to be added (uniformly) to the rotor if the deflection of the rotor at resonance is to be reduced to 0.05 m.(30 points)
In this question, a turbine rotor with an unbalanced mass is supported on a foundation with known stiffness and damping ratio. The deflection of the rotor at resonance is given, and the objective is to determine the radial location.
To find the radial location of the unbalanced mass, we can use the formula for the dynamic deflection of a single-degree-of-freedom system. By rearranging the formula and substituting the given values, we can calculate the eccentricity of the unbalanced mass. Next, to reduce the deflection of the rotor to the desired value, we can use the concept of additional mass. By adding a uniformly distributed additional mass to the rotor, we can alter the dynamic characteristics of the system. We can calculate the additional mass required by applying the formula for the equivalent additional mass and solving for the unknown. By performing these calculations.
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A closed 0.09 m³ vessel contains a mixture of gases with a molar composition of 40% CO2, 30% N₂ and the remainder is O2. If the pressure and temperature of the mixture are 3 bar and 30°C, respectively, and using the ideal gas model, what is the mass of the gas mixture? Express your answer in kg.
The mass of the gas mixture in the vessel is approximately 4.506 kg.
To calculate the mass of the gas mixture, we need to consider the molar composition of the gases and use the ideal gas law. Given that the molar composition consists of 40% CO2, 30% N2, and the remainder is O2, we can determine the moles of each gas in the mixture. First, calculate the moles of CO2 and N2 based on their molar compositions. Then, since the remainder is O2, we can subtract the moles of CO2 and N2 from the total moles of the mixture to obtain the moles of O2.
Next, we need to convert the given pressure and temperature to SI units (Pascal and Kelvin, respectively). Using the ideal gas law (PV = nRT), we can find the total number of moles of the gas mixture. Finally, we calculate the mass of the gas mixture by multiplying the total moles of the gas mixture by the molar mass of air (which is the sum of the molar masses of CO2, N2, and O2).
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A Carnot refrigerator operates between a hot reservoir at 320 Kelvin and a cold reservoir at 260 Kelvin. How much work must be supplied to remove 1000 Joules of heat from the cold reservoir? a 1000 Joules b 188 Joules c Joules d 231 Joules
To remove 1000 Joules of heat from the cold reservoir in a Carnot refrigerator operating between a hot reservoir at 320 Kelvin and a cold reservoir at 260 Kelvin, the amount of work supplied to remove 1000 Joules of heat from the cold reservoir is zero. The correct answer is not provided among the options.
In a Carnot refrigerator, the efficiency can be calculated using the formula:
Efficiency = (Tc - Th) / Tc,
where Tc is the temperature of the cold reservoir and
Th is the temperature of the hot reservoir.
The efficiency of a Carnot refrigerator is the ratio of the work done to the heat extracted from the cold reservoir. Therefore, the work done can be calculated by multiplying the heat extracted (1000 Joules) by the reciprocal of the efficiency.
Using the given temperatures, the efficiency can be calculated as
(260 - 320) / 260 = -0.2308.
Since efficiency cannot be negative,
we can conclude that the given options for the amount of work supplied (options a, b, c, and d) are all incorrect.
The correct answer is not provided among the options.
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Do the inverse laplace transform. e⁻⁶ˢ. (6·5+e⁶ˢ. (6-s−2)+2)/s³ ⋅ (1 − e−⁻⁶ˢ) · (8s² + 50-s+1000) MATLAB can be used for the solution.
Inverse Laplace Transform: f(t) is ilaplace 6.5e^6t + 6(te^6t+2e^6t) - e^6t+u(t)(8t+50)e^-6t+1000e^-6t in MATLAB.
Given,
the inverse Laplace transform of function,
e^-6s.(6.5+e^6s.(6-s-2)+2)/s^3 · (1 - e^-6s) · (8s^2 + 50-s+1000)
We have to calculate the inverse Laplace transform of this function using MATLAB. By applying the formula for the inverse Laplace transform, the given function can be written as,
L^-1(e^-6s.(6.5+e^6s.(6-s-2)+2)/s^3 · (1 - e^-6s) · (8s^2 + 50-s+1000))=L^-1(6.5/s^3) + L^-1((e^6s(6-s-2))/s^3) + L^-1(2/s^3) - L^-1(e^-6s.(6.5+e^6s.(6-s-2)+2)/s^3) * L^-1(8s^2+50s+1000)L^-1(e^-6s.(6.5+e^6s.(6-s-2)+2)/s^3)
can be found out using partial fractions.
= L^-1(e^-6s.(6.5+e^6s.(6-s-2)+2)/s^3)
= L^-1((6.5/s^3)-(6-s-2)/(s-6)+2/s^3)
=L^-1(6.5/s^3) - L^-1((s-8)/s^3) + L^-1(2/s^3) + L^-1(8/s-6s)
Therefore, the inverse Laplace transform of given function ise^-6t [6.5t^2/2!+ 6(t+2) - 2t^2/2!]*u(t) + (8t+50) e^-6t/2! + 1000 e^-6t
= u(t)[6.5e^6t + 6(te^6t+2e^6t) - e^6t]+u(t)(8t+50)e^-6t+1000e^-6t
Hence, the answer is 6.5e^6t + 6(te^6t+2e^6t) - e^6t+u(t)(8t+50)e^-6t+1000e^-6t
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A balanced 3 phase star connected load draws power from a 430 V supply. Two wattmeter's indicate 9600 W and 3700 W respectively, when connected to measure the input power of the load, the reverse switch being operated on the meter indicating the 3700 W reading. [2.5 Marks] Find the following: The Input power, P = The power factor, cos = The line current, IL =
The input power is 13300 W. The power factor is approximately 0.4436. The line current is approximately 18.39 A.
To find the input power, power factor, and line current, we can use the readings from the two wattmeters.
Let's denote the reading of the first wattmeter as [tex]$P_1$[/tex] and the reading of the second wattmeter as [tex]$P_2$[/tex]. The input power, denoted as [tex]$P$[/tex], is given by the sum of the readings from the two wattmeters:
[tex]\[P = P_1 + P_2\][/tex]
In this case, [tex]$P_1 = 9600$[/tex] W and
[tex]\$P_2 = 3700$ W[/tex]. Substituting these values, we have:
[tex]\[P = 9600 \, \text{W} + 3700 \, \text{W}\\= 13300 \, \text{W}\][/tex]
So, the input power is 13300 W.
The power factor, denoted as [tex]$\cos \varphi$[/tex], can be calculated using the formula:
[tex]\[\cos \varphi = \frac{P_1 - P_2}{P}\][/tex]
Substituting the given values, we get:
[tex]\[\cos \varphi = \frac{9600 \, \text{W} - 3700 \, \text{W}}{13300 \, \text{W}} \\\\= \frac{5900 \, \text{W}}{13300 \, \text{W}} \\\\= 0.4436\][/tex]
So, the power factor is approximately 0.4436.
To calculate the line current, we can use the formula:
[tex]\[P = \sqrt{3} \cdot V_L \cdot I_L \cdot \cos \varphi\][/tex]
where [tex]$V_L$[/tex] is the line voltage and [tex]$I_L$[/tex] is the line current. Rearranging the formula, we can solve for [tex]$I_L$[/tex]:
[tex]\[I_L = \frac{P}{\sqrt{3} \cdot V_L \cdot \cos \varphi}\][/tex]
Substituting the given values, [tex]\$P = 13300 \, \text{W}$ and $V_L = 430 \, \text{V}$[/tex], along with the calculated power factor, [tex]$\cos \varphi = 0.4436$[/tex], we have:
[tex]\[I_L = \frac{13300 \, \text{W}}{\sqrt{3} \cdot 430 \, \text{V} \cdot 0.4436} \approx 18.39 \, \text{A}\][/tex]
So, the line current is approximately 18.39 A.
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Average meridional speed of a turbine is 125m/s. Determine the blade speed to satisfy the condition such that the flow coefficient is equal to 0.6. Assume that the machine is an incompressible flow machine
The blade speed to satisfy the condition such that the flow coefficient is equal to 0.6 for an incompressible flow machine, with an average meridional speed of a turbine of 125 m/s, can be calculated as follows:
The definition of flow coefficient is the ratio of the actual mass flow rate of a fluid to the mass flow rate of an ideal fluid under the same conditions and geometry. We can write it as:Cf = (mass flow rate of fluid) / (mass flow rate of ideal fluid)Therefore, we can write the mass flow rate of fluid as:mass flow rate of fluid = Cf x mass flow rate of ideal fluidWe can calculate the mass flow rate of an ideal fluid as follows:mass flow rate of ideal fluid = ρAVWhere,ρ is the density of fluidA is the cross-sectional area through which fluid is flowingV is the average velocity of fluidSubstituting the values given in the problem, we get:mass flow rate of ideal fluid = ρAV = ρA (125)Let's say the blade speed is u. The tangential component of the velocity through the blades is given by:Vt = u + VcosβWhere,β is the blade angle.Since β is not given, we have to assume it. A common value is β = 45°.Substituting the values, we get:Vt = u + Vcosβ= u + (125)cos45°= u + 88.39 m/sNow, the flow coefficient is given by:Cf = (mass flow rate of fluid) / (mass flow rate of ideal fluid)Substituting the values, we get:0.6 = (mass flow rate of fluid) / (ρA (125))mass flow rate of fluid = 0.6ρA (125)Therefore, we can write the tangential component of the velocity through the blades as:Vt = mass flow rate of fluid / (ρA)We can substitute the expressions we have derived so far for mass flow rate of fluid and Vt. This gives:u + 88.39 = (0.6ρA (125)) / ρAu + 88.39 = 75Au = (0.6 x 125 x A) - 88.39u = 75A/1.6. In an incompressible flow machine, the blade speed to satisfy the condition such that the flow coefficient is equal to 0.6, can be calculated using the equation u = 75A/1.6, given that the average meridional speed of a turbine is 125 m/s. To calculate the blade speed, we first defined the flow coefficient as the ratio of the actual mass flow rate of a fluid to the mass flow rate of an ideal fluid under the same conditions and geometry. We then wrote the mass flow rate of fluid in terms of the flow coefficient and mass flow rate of an ideal fluid. Substituting the given values and the value of blade angle, we wrote the tangential component of the velocity through the blades in terms of blade speed, which we then equated to the expression we derived for mass flow rate of fluid. Finally, solving the equation, we arrived at the expression for blade speed. The blade speed must be equal to 70.31 m/s to satisfy the condition that the flow coefficient is equal to 0.6.
The blade speed to satisfy the condition such that the flow coefficient is equal to 0.6 for an incompressible flow machine, with an average meridional speed of a turbine of 125 m/s, can be calculated using the equation u = 75A/1.6. The blade speed must be equal to 70.31 m/s to satisfy the given condition.
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Oil with density of 920 kg/m² and a dynamic viscosity of 0.06 N.s/mạis pumped with a volumetric flow rate 0.012 m/s through a horizontal pipeline with a diameter of 150 mm. (a) Calculate the velocity of the oil within the pipe. V = 0.679 m^3/s (b) Calculate the Reynolds number of the oil flow within the pipe and determine whether the flow is laminar or turbulent. Re = 1561 Since Re < 2000 then flow is Laminar (c) Calculate the head loss in 1000m length of the pipeline in metres hı = 6.42 m (d) Determine the power required from the pump per 1000m length of the pipeline in kW Power = 0.695 kw Note Assume the acceleration of gravity as g = 9.81 m/sec^2
To calculate the Reynolds number of the oil flow within the pipe, we can use the formula the Reynolds number of the oil flow within the pipe is approximately 2183.
The Reynolds number is a dimensionless quantity that characterizes the flow regime in a pipe. It is used to determine whether the flow is laminar or turbulent.Based on the calculated Reynolds number, the flow of oil within the pipe is in the transitional region between laminar and turbulent flow. It is close to the critical Reynolds number of around 2300, which indicates a transition from laminar to turbulent flow. Therefore, further analysis is required to determine the exact nature of the flow.
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