calculate the length of a 1 inch diameter 9 geothermal heat exchanger having water flow of above 2 US gpm to deliver 30 kw cooling capacity (6+2) the heat exchanger is buried in coarse 100% sand with density of 100 ib/ft3 with enter water temperature of 80 f ground temp of 110f load factor (fc=1) and cop of 3.5

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Answer 1

The length of a 1 inch diameter 9 geothermal heat exchanger having water flow of above 2 US gpm to deliver 30 kW cooling capacity is 100.26 ft.

Given: Water flow, Q = 2 US gpm= 0.126 LPS

Length of the heat exchanger = ?

Diameter of the heat exchanger = 1 inch = 0.0833 ft

Ground temperature, Tg = 110 °F = 43.33 °C

Water inlet temperature, Tw1 = 80 °F = 26.67 °C

Effective heat transfer load, Qload = 30 kW

Load factor, Fc = 1

Coefficient of Performance, COP = 3.5S and

density, ρ = 100 lb/ft3

Now, Q = (6 + 2) × Qload= 8 × 30= 240 kW

We know that heat flow rate,

Q = (pi/4) x D^2 x L x ρ x Cp x dT/dt

where, pi= 3.14

D = 1 inch

= 0.0833 ft

ρ = 100 lb/ft3

Cp = 1 BTU/lb °FdT/dt

= (Tg - Tw1) / (COP x Fc)

= (43.33 - 26.67) / (3.5 x 1)

= 4.76 ft/hr

= 0.00132 ft/s (convert 4.76 ft/hr to ft/s)

Substituting all the values,

240,000 = (3.14/4) × (0.0833)^2 × L × 100 × 1 × 0.00132L

= 100.26 ft

Therefore, the length of a 1 inch diameter 9 geothermal heat exchanger having water flow of above 2 US gpm to deliver 30 kW cooling capacity is 100.26 ft.

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Related Questions

QUESTION 6 In an ac circuit with an inductive operation at the source terminals, the increase of power factor at the source terminals can be achieved by connecting, O a. a series resistor to the inductive load. O b. a parallel capacitor bank across the source terminals. O c. a parallel inductor bank across the source terminals. O d. a parallel resistor bank across the source terminals.

Answers

The correct option is b. a parallel capacitor bank across the source terminals.

The power factor is an essential parameter for the ac circuit, indicating the relation between real power and the apparent power in the circuit. The power factor shows the efficiency of the system, and a higher power factor shows the system's good efficiency.

The low power factor shows the system's poor efficiency and the energy wastage in the system. Therefore, it is essential to have a high power factor in the system.The inductive operation at the source terminals of the ac circuit can lead to low power factor and increase the inefficiency of the system.

To increase the power factor, the parallel capacitor bank should be connected across the source terminals of the ac circuit. The capacitor bank will add capacitive reactance to the circuit, which will neutralize the inductive reactance present in the circuit.

The capacitive reactance is negative in the phase with respect to the inductive reactance. Therefore, it will reduce the overall inductance of the circuit and, as a result, the overall impedance of the circuit will be reduced, and the power factor will be increased.

To summarize, the parallel capacitor bank across the source terminals of the ac circuit with an inductive operation can increase the power factor of the circuit by adding capacitive reactance to the circuit, which will neutralize the inductive reactance present in the circuit and reduce the overall impedance of the circuit.

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One kilogram of water initially at 160°C, 1.5 bar, undergoes an isothermal, internally reversible compression process to the saturated liquid state. Determine the work and heat transfer, each in kJ. Sketch the process on p-v and T-s coordinates. Associate the work and heat transfer with areas on these diagrams.

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The answer to the given question is,During the isothermal, internally reversible compression process to the saturated liquid state, the heat transfer (Q) is zero.

The work transfer (W) is equal to the negative change in the enthalpy of water (H) as it undergoes this process. At 160°C and 1.5 bar, the water is a compressed liquid. The temperature remains constant during the process. This means that the final state of the water is still compressed liquid, but with a smaller specific volume. The specific volume at 160°C and 1.5 bar is 0.001016 m³/kg.

The specific volume of the saturated liquid at 160°C is 0.001003 m³/kg. The difference is 0.000013 m³/kg, which is the decrease in specific volume. The enthalpy of the compressed liquid is 794.7 kJ/kg. The enthalpy of the saturated liquid at 160°C is 600.9 kJ/kg. The difference is 193.8 kJ/kg, which is the decrease in enthalpy. Therefore, the work transfer W is equal to -193.8 kJ/kg.

The heat transfer Q is equal to zero because the process is internally reversible. On the p-v diagram, the process is represented by a vertical line from 1.5 bar and 0.001016 m³/kg to 1.5 bar and 0.001003 m³/kg. The work transfer is represented by the area of this rectangle: The enthalpy-entropy (T-s) diagram is not necessary to solve the problem.

The conclusion is,The work transfer (W) during the isothermal, internally reversible compression process to the saturated liquid state is equal to -193.8 kJ/kg. The heat transfer (Q) is zero. The process is represented by a vertical line on the p-v diagram, and the work transfer is represented by the area of the rectangle.

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A bar of a steel alloy that exhibits the stress-strain behavior shown in the Animated Figure 6.22 is subjected to a tensile load; the specimen is 375 mm (14.8 in.) long and has a square cross section 5.5 mm (0.22 in.) on a side. (a) Compute the magnitude of the load necessary to produce an elongation of 0.525 mm (0.021 in.). N
(b) What will be the deformation after the load has been released? mm

Answers

The deformation after the load is released will be [Insert numerical value] mm.

What is the magnitude of the load required to produce an elongation of 0.525 mm in a steel alloy bar with specific dimensions and stress-strain behavior?

To compute the magnitude of the load necessary to produce an elongation of 0.525 mm (0.021 in.), we need to use Hooke's Law, which states that stress is proportional to strain.

First, we need to determine the stress (σ) using the formula:

σ = F/A

where F is the force and A is the cross-sectional area of the specimen. Since the cross-section is square, the area can be calculated as:

[tex]A = side^2[/tex]

Given that the side length is 5.5 mm, we have:

[tex]A = (5.5 mm)^2[/tex]

Next, we can calculate the stress:

[tex]σ = F / (5.5 mm)^2[/tex]

Now, we can use the stress-strain curve to determine the magnitude of the load (F) corresponding to the given elongation of 0.525 mm. By referring to the stress-strain curve, we can find the stress value that corresponds to the given strain of 0.525 mm.

Once we have the stress value, we can substitute it into the formula to calculate the load:

F = σ * A

To determine the deformation after the load has been released, we need to know the elastic or plastic behavior of the material. If the material is perfectly elastic, it will return to its original shape after the load is released, resulting in no permanent deformation. However, if the material exhibits plastic deformation, it will retain some deformation even after the load is removed.

Without additional information about the material's behavior, it is not possible to determine the deformation after the load has been released.

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A 4 pole, 250 V, dc series motor has a wave- connected armature with 205 conductors. The flux per pole is 25 mWb when the motor is drawing 60 A from the supply. The armature resistance is 0.34 while series field winding resistance is 0.4 2. Calculate the speed under this condition.

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In order to calculate the speed under the given conditions, we can use the following formula:$$E_b=\frac{\phi ZPN}{60A}$$where,Eb is the back emfφ is the flux per poleZ is the number of conductorsP is the number of polesN is the speed of rotation in revolutions per minute

A is the current drawn from the supplyWe are given the following values in the problem statement:Eb = 250 V (as this is a dc series motor)Voltage, V = 250 VFlux per pole, φ = 25 mWbNumber of conductors, Z = 205Armature resistance, Ra = 0.34 ΩField winding resistance,

Rf = 0.42 ΩCurrent, A = 60 APole, P = 4Let's substitute the given values into the formula and solve for the speed, N.$$E_b=\frac{\phi ZPN}{60A}$$$$\frac{E_b*60A}{\phi ZP}=N$$$$N=\frac{V-I_aR_a}{\phi ZP/60}$$

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installation time and eliminates the need for mounting on many types of roofs; the financing and installation of industrial large-scale solar (for example the British Motor Company consisting of 1 606 photovoltaic panels), and the installation of electric vehicle charging stations, in partnership with Rabobank. In the first quarter of 2016, the CEO of SolarCity, Lyndon Rive, reported to shareholders that targets for most initiatives have been exceeded. In terms of MW installed, the target has been exceeded by 19%, the revenue grew by 82% year on year, and $728 million in asset financing has been raised year on year. Furthermore, the CEO also reported on a milestone achieved: the opening of a 100 MW cell-producing plant that will produce cells that exceed the average efficiency by 20%. In addition, with the use of the Zep mounting system, the number of component parts needed to install a module has been reduced from eight to three, the installation time of 16 modules (4 KW) has been reduced to 20 minutes, and the risk of damaging roofs has been reduced as well. To accomplish the mission of SolarCity, teams have to constantly work to enhance scale and efficiency, and tirelessly tear down external barriers to solar. SolarCity has been structured to functionally focus on overcoming each potential barrier in the path of higher penetration of distributed solar: the sales/operations focus is on lowering the upfront costs of solar; the finance teams focus on reducing the cost of capital; research and development (R&D) focus on developing new technology that reduces costs; and the government affairs team works to promote a regulatory policy that supports distributed solar. Policy is the most important initiative to drive higher distributed solar, and small wins have been achieved on the policy front despite the efforts of utility groups to undermine the economics of solar. These wins include energy regulators rejecting fixed charges that penalise distributed solar customers in Mexico, Colorado, Minnesota and Kansas (US). In order to meet the long-term projections, SolarCity has to expand its workforce, increase installation efficiency and exceed the current rate of growth in MW installed. However, there are implementation risks that may lead to a difference between what is projected and actually realised. These risks include: the future level of demand for their solar systems; the availability and timely supply of cost-effective solar panels; the ability to integrate new businesses acquired into existing operations; the effect of changes in rebates/taxes; changes in strategic planning decisions; and the reallocation of internal resources. Overall, solar at the scale envisioned by SolarCity will lead to more competition, as opposed to protecting monopolies, and innovative solutions to meet the world's clean energy needs. Question : Comment on how changes in macro-environment forces affected and influenced SolarCity's decision making in the organisatio

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SolarCity is a company that has gained significant importance in the solar energy sector. The company operates to overcome each possible obstacle in the path of higher penetration of distributed solar. SolarCity has been positively affected by changes in macro-environment forces.

Below are some of the points that provide insights on how changes in macro-environment forces affected and influenced SolarCity's decision making in the organization: Policy - Policy is the most important initiative to drive higher distributed solar.

The government affairs team works to promote a regulatory policy that supports distributed solar. Policy changes have a direct impact on the financials of the company.

As a result, SolarCity is impacted by changes in policy. Small wins have been achieved on the policy front despite the efforts of utility groups to undermine the economics of solar.

Technology - The company is driven by the continuous development of new technology that reduces costs. The R&D team focuses on developing new technology that reduces costs.

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Electric vehicle based on electrical machines and power systems
for human applications, concept design (block diagram).

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Electric vehicles are an alternative to traditional fuel-based vehicles. These electric vehicles have some advantages over fuel-based vehicles, such as being more environmentally friendly and having lower operating costs. This essay discusses electric vehicles based on electrical machines and power systems for human applications, including the concept design .

The block diagram of an electric vehicle-based on electrical machines and power systems consists of several blocks. The battery management system, motor controller, and inverter are the primary blocks. The battery management system is responsible for monitoring and managing the battery system's performance and health. The motor controller regulates the motor's speed and torque, while the inverter converts DC power from the battery to AC power that is used by the motor.

Electric vehicles based on electrical machines and power systems are an efficient and eco-friendly option for human applications. The block diagram of the electric vehicle concept design includes several key components, such as the battery management system, motor controller, and inverter, which work together to power and control the electric vehicle's motor.

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A steam power plant operates on an ideal reheat regenerative Rankine cycle with two turbine stages, one closed feed water heater and one open feed water heater. Steam is superheated and supplied to the high-pressure turbine at 200 bar and 700 °C. Steam exits at 30 bar and a fraction of it is bled to a closed feed water heater. The remaining steam is reheated in the boiler to 600 °C before entering the low-pressure turbine. During expansion in the low pressure turbine, another fraction of the steam is bled off at a pressure of 2 bar to the open feed water heater. The remaining steam is expanded to the condenser pressure of 0.2 bar. Saturated liquid water leaving the condenser is pumped to the pressure of the open feed heater. Water leaving this is then pumped through the closed feed heater and mixed with the pumped cross flow bled steam. The whole of the water is returned to the boiler and super heater and the cycle is repeated.
i) Starting with state 1 at the entrance to the high-pressure turbine, draw a fully annotated schematic diagram of the steam power plant, and a sketch an accompanying temperature - specific entropy diagram.
ii) Plot on the supplied enthalpy – entropy steam chart (Mollier diagram) states 1 to 5 and the process lines for steam expansion through the high-pressure turbine, reheat through the boiler, and expansion to the condenser pressure. Clearly mark on the chart all state properties. Ensure that you include the annotated steam chart along with your solutions to obtain relevant marks for the above question part.
iii) Determine the fractions of steam extracted from the turbines and bled to the feed heaters. State all assumptions used and show all calculation steps.
iv) Calculate the thermal efficiency of the plant and the specific steam consumption, clearly stating all assumptions.
v) Explain why the thermal efficiency of the steam cycles may be increased through use of regenerative feed heaters. Make use of suitable sketches and clearly identify the main thermodynamic reasons

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A fully annotated schematic diagram of the steam power plant is as follows: Figure 1: Schematic diagram of a steam power plantThe accompanying temperature - specific entropy diagram.

Temperature-specific entropy diagramed) The enthalpy – entropy steam chart (Mollier diagram) is shown below: :Enthalpy – entropy steam chart (Mollier diagram) States 1 to 5 and the process lines for steam expansion through the high-pressure turbine, reheat through the boiler, and expansion to the condenser pressure are plotted on the diagram, as shown below:

Process lines for steam expansion through the high-pressure turbine, reheat through the boiler, and expansion to the condenser pressure) The mass balance for the feed heaters is shown below: Let the mass flow rate of steam entering the high-pressure turbine be the mass flow rate of steam extracted from the high-pressure turbine and sent to the closed feed water heater is 0.05m.

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A cantilever beam 4 m long deflects by 16 mm at its free end due to a uniformly distributed load of 25 kN/m throughout its length. What force P (kN) should be applied at the mid-length of the beam for zero displacement at the free end?

Answers

The force P that should be applied at the mid-length of the cantilever beam is 8.33 kN.

To determine the force P required at the mid-length of the cantilever beam for zero displacement at the free end, we can use the principle of superposition.

Calculate the deflection at the free end due to the distributed load.

Given that the beam is 4 m long and deflects by 16 mm at the free end, we can use the formula for the deflection of a cantilever beam under a uniformly distributed load:

δ = (5 * w * L^4) / (384 * E * I)

where δ is the deflection at the free end, w is the distributed load, L is the length of the beam, E is the Young's modulus of the material, and I is the moment of inertia of the beam's cross-sectional shape.

Substituting the given values, we have:

0.016 m = (5 * 25 kN/m * 4^4) / (384 * E * I)

Calculate the deflection at the free end due to the applied force P.

Since we want zero displacement at the free end, the deflection caused by the force P at the mid-length of the beam should be equal to the deflection caused by the distributed load.

Using the same formula as in step 1, we can express this as:

δ = (5 * P * (L/2)^4) / (384 * E * I)

Equate the two deflection equations and solve for P.

Setting the two deflection equations equal to each other, we have:

(5 * 25 kN/m * 4^4) / (384 * E * I) = (5 * P * (4/2)^4) / (384 * E * I)

Simplifying, we find:

P = (25 kN/m * 4^4 * 2^4) / 4^4 = 8.33 kN

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The characteristic equation of a system is S⁴ +25³ +25² +3S+ K = 0 Determine the range of the parameter K such that the system is stable.

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The range of the parameter K for system stability is K > -125.

To determine the stability of the system, we need to analyze the characteristic equation. The characteristic equation of the system is given as S⁴ + 25³ + 25² + 3S + K = 0. Stability of a system is determined by the roots of its characteristic equation.

For the system to be stable, all the roots of the characteristic equation must have negative real parts. In this case, the system has a quartic characteristic equation, and we need to consider the coefficients and the parameter K.

The coefficient of the S⁴ term is 1, which implies that the system has a leading coefficient of 1, indicating the presence of a stable pole at the origin. The coefficient of the S³ term is 25³, the coefficient of the S² term is 25², and the coefficient of the S term is 3. These coefficients alone do not affect the stability of the system.

The parameter K plays a crucial role in determining stability. For the system to be stable, the values of K should be such that all the roots of the characteristic equation have negative real parts. To achieve this, we can analyze the value of K in relation to the other coefficients.

Since K is a constant term, it does not affect the real parts of the roots. However, to maintain stability, the value of K should be chosen in such a way that it does not cause any roots to have positive real parts. Therefore, for stability, K must be greater than the sum of the coefficients of the S term and the constant term, which is -125. Hence, the range of the parameter K for system stability is K > -125.

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Steam in the condenser of a power plant is to be condensed at a temperature of 30 °C with cooling water from a nearby lake, which enters the tubes of the condenser at 14 °C and leaves at 22 °C. The surface area of the tubes is 45 m², and the overall heat transfer coefficient is 2100 W/m² C. Calculate the heat transfer rate in the condenser assuming parallel flow in the condenser.

Answers

The heat transfer rate in the condenser is 8,880 kW assuming parallel flow in the condenser.

Given information:

Temperature of steam = 30 °C

Temperature of inlet cooling water = 14 °C

Temperature of outlet cooling water = 22 °C

Surface area of the tubes = 45 m²

Overall heat transfer coefficient = 2100 W/m² C

Heat transfer rate is given by the following relation,

Q = U A ΔTlog mean

Q = Heat transfer rate = ?

U = Overall heat transfer coefficient = 2100 W/m² C (given)

A = Surface area of the tubes = 45 m² (given)

ΔTlog mean = Logarithmic Mean

Temperature Difference = T1 - t2/t1 - T2

For parallel flow arrangement, the formula to calculate ΔTlog mean is given by,

ΔTlog mean = {(T1 - t2) - (t1 - T2)} / ln {(T1 - t2) / (t1 - T2)}

Where,

T1 = Inlet temperature of steam

t2 = Outlet temperature of cooling water.

t1 = Inlet temperature of cooling water

T2 = Outlet temperature of steam.

By substituting the given values in the above equation,

ΔTlog mean = {30 - 22 - (14 - 30)} / ln {(30 - 22) / (14 - 30)} = 9.11 °C

Heat transfer rate,

Q = U A ΔTlog mean

Q = 2100 × 45 × 9.11Q = 8,88277.5 ≈ 8,880 kW

Thus, the heat transfer rate in the condenser is 8,880 kW assuming parallel flow in the condenser.

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An ideal Rankine Cycle operates between the same two pressures as the Carnot Cycle above. Calculate the cycle efficiency, the specific net work out and the specific heat supplied to the boiler. Neglect the power needed to drive the feed pump and assume the turbine operates isentropically.

Answers

The cycle efficiency, the specific net work out, and the specific heat supplied to the boiler are 94.52%, 3288.1 kJ/kg, and 3288.1 kJ/kg respectively.

An ideal Rankine cycle operates between the same two pressures as the Carnot Cycle above. We are supposed to calculate the cycle efficiency, the specific net work out, and the specific heat supplied to the boiler. We will neglect the power needed to drive the feed pump and assume the turbine operates isentropically.

The thermal efficiency of the ideal Rankine cycle can be expressed as the ratio of the net work output of the cycle to the heat supplied to the cycle.

W = Q1 - Q2 ... (1)

The formula to calculate the efficiency of the ideal Rankine cycle can be given as:

η = W / Q1... (2)

where,Q1 = heat supplied to the boiler

Q2 = heat rejected from the condenser to the cooling water

The following points must be noted before the efficiency calculation:

The given Rankine Cycle is ideal. We are to neglect the power needed to drive the feed pump. The turbine operates isentropically. The working fluid in the Rankine cycle is water .The water entering the boiler is saturated liquid at state 1.The water exiting the condenser is saturated liquid at state 2.

An ideal Rankine Cycle operates between the same two pressures as the Carnot Cycle above.

Therefore, the temperature of the steam entering the turbine is 500°C (773 K) as calculated in the Carnot cycle.

The enthalpy of the saturated liquid at state 1 is 125.6 kJ/kg. The enthalpy of the steam at state 3 can be found out using the steam tables. At 773 K, the enthalpy of the steam is 3479.9 kJ/kg. The enthalpy of the saturated liquid at state 2 can be found out using the steam tables. At 45°C, the enthalpy of the steam is 191.8 kJ/kg.

Let the mass flow rate of steam be m kg/s .We know that the net work output of the cycle is the difference between the enthalpy of the steam entering the turbine and the enthalpy of the saturated liquid exiting the condenser multiplied by the mass flow rate of steam.

W = m (h3 – h2)

From the energy balance of the cycle, we know that the heat supplied to the cycle is equal to the net work output of the cycle plus the heat rejected to the cooling water.

Q1 = m (h3 – h2) + Q2

Substituting (1) in the above equation, we get;

Q1 = W + Q2Q1 = m (h3 – h2) + Q2

From (2), the efficiency of the Rankine cycle

isη = W / Q1Therefore,η = m (h3 – h2) / [m (h3 – h2) + Q2]

The heat rejected to the cooling water is equal to the heat supplied to the cycle minus the net work output of the cycle.Q2 = Q1 - W

Substituting the values of the enthalpies of the states in the above equations, we get;

h2 = 191.8 kJ/kgh3 = 3479.9 kJ/kgη = 1 – (191.8 / 3479.9) = 0.9452 = 94.52%

The cycle efficiency of the ideal Rankine Cycle is 94.52%.

The work output of the cycle is given by the equation ;W = m (h3 – h2)W = m (3479.9 – 191.8)W = m (3288.1)

Specific net work output of the cycle = W / m = 3288.1 kJ/kg

The specific heat supplied to the boiler is Q1 / m = (h3 - h2) = 3288.1 kJ/kg.

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1 22 Problem 4: Revolute-Prismatic Manipulator (25 points). Consider the two-link manipulator shown in 0 0 Fig. 4 with di 0. Link 1 has an inertia tensor given by о ту о and mass mi. Assume that link 2 0 01). has all its mass, m2, located at a point at the end-effector. Derive the dynamic equations for the manipulator. Assume that gravity is directed along –zo. Hint: Recall that moment of inertia of a point mass is the body frame is zero. ] d2 21 02 01 22 21 YY1 22 Y Y2 De di 20 Yo 00 To

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The dynamic equations for the given two-link manipulator can be derived by considering the inertia tensors, masses, and the location of the mass at the end-effector of link 2.

To derive the dynamic equations for the two-link manipulator, we need to consider the kinetic and potential energy of the system. The kinetic energy is determined by the motion of the manipulator, while the potential energy is influenced by the gravitational force.

In this case, we have two links in the manipulator. Link 1 has an inertia tensor given by о ту о and a mass m1. Link 2 has all its mass, m2, located at the end-effector point. To derive the dynamic equations, we need to compute the Lagrangian, which is the difference between the kinetic and potential energy of the system.

The Lagrangian of the system can be expressed as:

L = T - V,

where T represents the total kinetic energy and V represents the total potential energy.

The kinetic energy T can be calculated as the sum of the kinetic energies of each link. For link 1, the kinetic energy is given by:

T1 = 0.5 * m1 * v1^2 + 0.5 * w1^T * о * w1,

where v1 is the linear velocity of link 1 and w1 is the angular velocity of link 1.

Similarly, for link 2, since all its mass is located at the end-effector, the kinetic energy can be simplified as:

T2 = 0.5 * m2 * v2^2 + 0.5 * w2^T * о * w2,

where v2 is the linear velocity of the end-effector and w2 is the angular velocity of the end-effector.

The potential energy V is determined by the gravitational force acting on the system. Assuming gravity is directed along –zo, the potential energy can be written as:

V = (m1 * g * r1z) + (m2 * g * r2z),

where g is the acceleration due to gravity and r1z and r2z are the z-components of the positions of the center of mass of link 1 and the end-effector, respectively.

By calculating the Lagrangian L = T - V and applying the Euler-Lagrange equations, we can derive the dynamic equations for the manipulator.

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Question 1 Not yet answered Marked out of 4.00 A Proportional-Derivative (PD) controller may reduce the stability of the system. Select one: O True O False

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Proportional-Derivative (PD) controller is one of the most commonly used types of controllers in control theory. It provides excellent accuracy in controlling the system, but it may reduce the stability of the system when the controller is not set correctly. So, the given statement is True.

In general, a PD controller is designed to provide faster response to changes in error and to reduce the steady-state error. However, in some cases, a PD controller may be too sensitive to changes in error and produce unstable responses. This instability is caused by the derivative term, which amplifies high-frequency noise in the error signal. As a result, the system may oscillate or even become unstable. To overcome this, it is important to tune the controller gains carefully. A good controller tuning will ensure that the controller responds optimally to changes in error while maintaining stability.

This is usually done using various methods such as Ziegler-Nichols method, Cohen-Coon method, and many more. In conclusion, a PD controller can reduce the stability of the system if not tuned correctly.

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32 marks) Al. (a) (1) Agricultural robots are are capable of assisting farmers with a wide range of operations. They have the capability to analyze, contemplate, and carry out a multitude of functions, and they can be programmed to grow and evolve to match the needs of various tasks. Suppose you are the manager of a design team which aims at designing an Agricultural robot for a small scale farm field, about 10 m X 10 m, discuss how you approach the problem and work out a design specification table for your design. (6 marks) (ii) With reference to the specification in (i), propose a design with hand sketch. Label all components and explain how to evaluate the performance of your design. Construct a block diagram to show the connections between different components. (6 marks)

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Agricultural robots are machines that are programmed to carry out a range of tasks on a farm. They are capable of analyzing, assessing, and  programmed to evolve and adapt to suit the needs of various tasks.

Given a small-scale farm field of about 10m x 10m, this article discusses how to approach the problem and develop a design specification table for your design. A design specification table outlines the specific requirements for a design project.

Here are the steps that can be followed to develop a design specification table for the agricultural robot: Identify the design problem. The design problem is that there is a need for an agricultural robot to carry out tasks on a small-scale farm field. The robot should be designed to meet the needs of the farmers and be able to carry out the tasks efficiently.

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When using the flexure formula for a beam, the maximum normal stress occurs where ?
Group of answer choices
A. at a point on the cross-sectional area farthest away from the neutral axis
B. at a point on the cross-sectional area closest to the neutral axis
C. right on the neutral axis
D. halfway between the neutral axis and the edge of the beam

Answers

The maximum normal stress occurs at a point on the cross-sectional area farthest away from the neutral axis.

Option A is correct. When a beam is subjected to bending, the top fibers of the beam are compressed while the bottom fibers are stretched. The neutral axis is the location within the beam where there is no change in length during bending. As we move away from the neutral axis, the distance between the fibers increases, leading to higher strains and stresses. Therefore, the point on the cross-sectional area farthest away from the neutral axis experiences the maximum normal stress. This is important to consider when analyzing the structural integrity and strength of beams under bending loads.

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QUESTION 2 Copy of A power plant was analysed based on Carnot cycle, the evaporator supplie 459 kJ of heat per cycle at 442°C and condenser cooling fluid was maintained at 33°C. Determine the amount of heat rejected in the condenser? Provide answer to no decimal place and insert the unit symbol in kilo.... 1 °C is 273K in this question if required.

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To determine the amount of heat rejected in the condenser of a power plant operating on the Carnot cycle, we need to use the temperature difference between the evaporator and the condenser.

Given:
Temperature at the evaporator (T₁) = 442°C
Temperature at the condenser (T₂) = 33°C

To convert these temperatures to Kelvin, we add 273 to each value:
T₁ = 442 + 273 = 715 K
T₂ = 33 + 273 = 306 K

The amount of heat rejected in the condenser can be calculated using the formula:

Q = Qₕ - Qₗ

Where:
Q = Amount of heat rejected in the condenser
Qₕ = Heat supplied by the evaporator (459 kJ)
Qₗ = Heat absorbed by the condenser

Since the Carnot cycle is a reversible cycle, the heat rejected in the condenser is equal to the heat absorbed by the evaporator. Therefore:

Q = Qₕ - Qₗ = 459 kJ

So the amount of heat rejected in the condenser is 459 kilojoules (kJ)

Use Matlab to create the required Bode plots. 1) Design a lead compensator for the system below. The ramp error constant should be K) = 20 and the phase margin should be greater than or equal to 50°. Hand in your uncompensated Bode plot and your compensated Bode plot.
G(s) = 4/s(s+2)
solution
G(s) = 40.16 s+4.39/s+17.64

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To make the Bode plots for the given system using MATLAB as well as the design a lead compensator, one can use the code given below

What is the MATLAB?

MATLAB is a computer program made for scientists and engineers to study and design things that help make the world better. MATLAB's main component is its language, which is based on matrices and allows for easy expression of mathematical computations.

Therefore, the computer program tends to creates the G_uncompensated transfer function using the special numbers. After that, it creates a graph called the Bode plot using a tool called the bode function. It also gives the graph a name.

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A reciprocating compressor draws in 500 cubic feet per minute of air whose density is 0.079lb/cu ft and discharges it with a density of 0.304lb/ cu ft. At suction, p1=15psia; at discharge , p 2 ​ = 80 psia. The increase in the specific internal energy is 33.8 Btu and the heat transferred from the air by cooling is 13Btu/lb. Determine the work on the air in Btu/min and in hp. Neglect change in kinetic energy.

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The work on the air is approximately 22.24 Btu/min and 0.037 hp.

To determine the work on the air in Btu/min and in horsepower (hp), we can use the following equations and steps:

1. Calculate the mass flow rate (m_dot) of air using the given volumetric flow rate (Q_dot) and air density (ρ):

  m_dot = Q_dot * ρ

  Here, Q_dot = 500 cubic feet per minute and ρ = 0.079 lb/cu ft.

  Substituting these values, we get:

  m_dot = 500 * 0.079 = 39.5 lb/min

2. Determine the change in specific internal energy (Δu) using the given increase in specific internal energy (Δu_in) and mass flow rate (m_dot):

  Δu = Δu_in * m_dot

  Here, Δu_in = 33.8 Btu and m_dot = 39.5 lb/min.

  Substituting these values, we get:

  Δu = 33.8 * 39.5 = 1334.3 Btu/min

3. Calculate the work done on the air (W_dot) using the change in specific internal energy (Δu) and mass flow rate (m_dot):

  W_dot = Δu / 60

  Since the given units are in Btu/min, we divide by 60 to convert it to Btu/s.

  Substituting the value of Δu, we get:

  W_dot = 1334.3 / 60 = 22.24 Btu/s

4. Convert the work done to horsepower (hp):

  1 hp = 550 ft-lbf/s

  1 Btu/s = 778 ft-lbf/s

  W_hp = W_dot / (778 * 550)

  Substituting the value of W_dot, we get:

  W_hp = 22.24 / (778 * 550) = 0.037 hp

Therefore, the work on the air is approximately 22.24 Btu/min and 0.037 hp.

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6.13 A BJT is specified to have Is = 5 × 10-¹5 A and ß that falls in the range of 50 to 200. If the transistor is operated in the active mode with UBE set to 0.700 V, find the expected range of ic, ib, and ie.

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We need to find the expected range of ic, ib, and ie, if the transistor is operated in the active mode with UBE set to 0.700 V.

The equation for the currents flowing in the active mode is given as follows:

Ic = βIBIe = Ic + IB

Let’s take the lower limit of β as[tex]50.β = 50 = > IB = IC/50β = 50 = > IE = IC(50 + 1) = 51IC[/tex]

We know, Ic = Is (e^(VBE/VT) - 1),

whereIs  = 5 × 10^-15 A, VT = 26 mV at room temperature (25°C)VBE = UBE = 0.700 V

When β = 50,

we get I B = IC/50 = (5 × 10^-15 A)/50 = 1 × 10^-16 A and IE = IC(50 + 1) = 51IC = 51 × IC

Now, substituting these values in the equation for Ic,

we get[tex]IC = Is (e^(VBE/VT) - 1)IC = 5 × 10^-15 (e^(0.700/0.026) - 1) = 1.55 mA[/tex] (approx)

The expected range of ie is 0 to 1.58 mA (approx).

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a) An amplifier system without feedback has the following specifications: Open loop gain: 90 Input impedance: 25kΩ Output impedance: 5kΩ (i) If the amplifier system employs negative feedback and the close loop gain is 9.5, calculate the system feedback factor, β. (ii) Suppose the negative feedback topology used for the amplifier system in Q3(a)(i) is a current shunt feedback, determine the amplifier, input impedance and output impedance of the amplifier with feedback.

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Therefore, the feedback amplifier has an input impedance of 2.09 kΩ and an output impedance of 184.3 Ω.

A feedback amplifier is a type of electronic amplifier that utilizes feedback to regulate the response of the amplifier. This method, also known as negative feedback, entails feeding some of the output back to the input in a phase-reversed form. The fundamental principle is to decrease the gain of the amplifier to a reasonable value while maintaining stability and decreasing distortion.

In an amplifier system without feedback, the open loop gain is 90, input impedance is 25 kΩ, and output impedance is 5 kΩ.

The close loop gain of the amplifier is 9.5.

The feedback factor β of the amplifier can be determined as follows:

β = A / (1 + AB)

Here, A is the open-loop gain, and B is the feedback factor.

β = 90 / (1 + 90 * (9.5 - 1))

= 0.0836 (or 8.36%)

To find out the input impedance of the feedback amplifier, the input impedance of the original amplifier must be multiplied by the feedback factor.

Rin = β * R

= 0.0836 * 25 kΩ

= 2.09 kΩ

The output impedance of the feedback amplifier can be calculated using the following formula:

Rout = R / (1 + AB)

= 5 kΩ / (1 + 90 * (9.5 - 1))

= 184.3 Ω

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A blood specimen has a hydrogen ion concentration of 40 nmol/liter and a partial pressure of carbon dioxide (PCO2) of 60 mmHg. Calculate the hydrogen ion concentration. Predict the type of acid-base abnormality that the patient exhibits

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A blood specimen with a hydrogen ion concentration of 40 nmol/L and a partial pressure of carbon dioxide (PCO2) of 60 mmHg is indicative of respiratory acidosis.

The normal range for hydrogen ion concentration is 35-45 nmol/L.A decrease in pH or hydrogen ion concentration is known as acidemia. Acidemia can result from a variety of causes, including metabolic or respiratory disorders. Respiratory acidosis is a disorder caused by increased PCO2 levels due to decreased alveolar ventilation or increased CO2 production, resulting in acidemia.

When CO2 levels rise, hydrogen ion concentrations increase, leading to acidemia. The HCO3- level, which is responsible for buffering metabolic acids, is typically normal. Increased HCO3- levels and decreased H+ levels result in alkalemia. HCO3- levels and H+ levels decrease in metabolic acidosis.

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What advantages does the piezoresistive sensor have over the common (metal) electrical resistance strain gage? What are some disadvantages?

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Piezoresistive sensors are solid-state devices that detect changes in resistance when a force is applied. It is a type of strain gauge that is made from a semiconductor material such as silicon, germanium, or gallium arsenide. When a force is applied to the sensor, the resistance changes. This change is then detected and can be used to measure the force applied to the sensor.

There are several advantages to using piezoresistive sensors over the common (metal) electrical resistance strain gauge. One of the main advantages is that piezoresistive sensors are more sensitive to changes in force. They can detect smaller changes in force, making them ideal for applications where precision is important. Another advantage of piezoresistive sensors is that they are more stable over a wider range of temperatures than metal strain gauges. This makes them ideal for use in applications where the temperature may vary significantly. Additionally, piezoresistive sensors are smaller and more lightweight than metal strain gauges, making them easier to install and use.However, there are also some disadvantages to using piezoresistive sensors. One of the main disadvantages is that they are more expensive than metal strain gauges. This can make them less suitable for applications where cost is a concern. Additionally, piezoresistive sensors are more fragile than metal strain gauges and can be damaged if they are subjected to excessive force. This can limit their use in some applications. In conclusion, piezoresistive sensors have many advantages over common (metal) electrical resistance strain gauges. They are more sensitive, stable over a wider range of temperatures, and smaller and more lightweight. However, they are more expensive and fragile, which can limit their use in some applications.

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The Master Productiom Schedule is an aggregated production plan developed during the SOP process O True False

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The given statement "The Master Production Schedule is an aggregated production plan developed during the SOP process" is True.

The Master Production Schedule (MPS) is a collection of data that organizes manufacturing plans for a particular period of time. The MPS consists of a list of all of the goods that are planned to be manufactured, as well as the dates on which they are planned to be manufactured.

The MPS is used to guarantee that there are no significant delays in the production process and that manufacturing and inventory costs are minimized. The MPS is essential because it enables planners to adjust their schedules, materials, and resources to suit current market demand and modifications to the supply chain.

The MPS is developed as part of the Sales and Operations Planning (SOP) process.

The SOP is a periodic process that brings together all aspects of the firm, including production, finance, sales, and marketing, to agree on a unified plan for the future.

As a result, the MPS is generated at the conclusion of the SOP procedure and is influenced by the overall business plan, market predictions, and any resource or capacity limitations that were identified throughout the SOP process.

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Explain, in your own words (You will get zero for copying from friends or elsewhere): • The key considerations in fatigue analysis that makes it different from static load analysis. • Include examples where static load analysis is not enough to determine the suitability of a part for a specific application and how fatigue analysis changes your technical opinion. • How does fatigue analysis help value (cost cutting) engineering of component designs? • Is there value in also understanding metallurgy when doing fatigue analysis? Why? • Include references where applicable.

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Fatigue analysis can help with value engineering of component designs by identifying potential failure modes and allowing engineers to optimize designs to minimize the risk of fatigue failure.

When it comes to analyzing the fatigue of a particular component or part, there are a few key considerations that make it different from static load analysis.

While static load analysis involves looking at the stress and strain of a part or structure under a single, constant load, fatigue analysis involves understanding how the part will perform over time when subjected to repeated loads or cycles.

This is important because even if a part appears to be strong enough to withstand a single load, it may not be able to hold up over time if it is subjected to repeated stress.

For example, let's say you are designing a bicycle frame. If you only perform a static load analysis on the frame, you may be able to determine how much weight it can hold without breaking.

However, if you don't also perform a fatigue analysis, you may not realize that the frame will eventually fail after being exposed to thousands of cycles of stress from normal use.

Fatigue analysis can help with value engineering of component designs by identifying potential failure modes and allowing engineers to optimize designs to minimize the risk of fatigue failure.

By considering factors such as the materials used, the design of the part, and the loads it will be subjected to over time, engineers can create more robust and durable designs that can withstand repeated use without failure.

Understanding metallurgy is also important when performing fatigue analysis because the properties of a material can have a significant impact on its ability to withstand repeated loads.

By understanding the microstructure of a material and how it responds to different types of stress, engineers can make more informed decisions about which materials to use in their designs.

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A 2 hp gearmotor is rotating at 200 rpm, cw, and driving a mixing agitator, which approximately 60 rpm. Select an appropriate chain and commercially available sprockets. Also, determine the actual velocity of the driven sheave and the chain speed. Also, determine an appropriate center distance and determine the number of chain links required.

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Given: 2 hp gearmotor, Rotating speed= 200 rpm, Mix agitator speed= 60 rpm. Now, we need to select an appropriate chain and commercially available sprockets and determine the actual velocity of the driven sheave and the chain speed and find an appropriate center distance and determine the number of chain links required.

Now, the chain speed will be equal to the linear velocity of the pitch diameter of the sprocket that the chain is wrapped around. Let's solve for each step one by one Chain and Sprockets selectionUsing the formula We can find the number of teeth of both gears and use it to determine the pitch diameter of the sprocket. Let T2 be the agitator sprocket and T1 be the motor sprocket.The sprocket with the lesser number of teeth should be selected as the motor sprocket so as to increase the chain's wrap.

For an appropriate center distance, pitch diameter of the sprocket should be selected as below Where, The diameter of sprocket 2 can now be calculated as: Thus, the recommended chain will be a 40 pitch chain.Step 2: Actual velocity of driven sheaveThe actual velocity of driven sheave can be calculated using the formula Where,V2 = actual velocity of the driven sheave

N1 = motor speed

N2 = agitator speed

D = diameter of the driven sheave

We know that

D2 = 849.3mm

and

N1 = 200 rpm

and

N2 = 60 rpm

V2 = π × 849.3 × (200/60) = 8,924.9 mm/min

Number of chain links The number of chain links required can be calculated using the formula Approximately 1366 chain links are required.

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Find the poles of the system represented in the following state-space form. x(t) = [5/-2] [-8/-1]x(t) + [3]u(t) y(t) = [5  0] x(t) A) s₁ = -5, S₂ = 1 B) s₁ = -3, S₂ = 7 C) s₁ = 5, S₂-1 D) s₁ = 3, S₂ = -7 E) s₁ = -5, S₂ = 4

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The state-space equation is shown below:x(t) = [5/-2] [-8/-1]x(t) + [3]u(t)y(t) = [5 0] x(t)To find the poles of the system represented in the given state-space form, the characteristic equation needs to be determined.

For a system in a state-space form, the characteristic equation is defined as:|sI-A| = 0Here, A is a matrix with dimensions n x n, and sI is an identity matrix with dimensions n x n multiplied by the Laplace transform variable s. We have A = [-8/-1] [5/-2] and sI = [s 0] [0 s]So, sI - A = [s+1 0] [0 s+2] - [-8/-1] [5/-2]= [s+1 0] [0 s+2] + [8/1] [-5/2]Now, the determinant of the matrix sI-A is given by:(s+1) (s+2) - [(8/1) * (5/2)]=>(s+1) (s+2) - 20= s² + 3s - 18The characteristic equation of the system is s² + 3s - 18 = 0.We know that for a second-order system, the poles of the system are given by the roots of the characteristic equation.

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Which of the following is an example of non-destructive testing and inspection? a Ultrasonic testing and inspection b Visual testing and inspection c All of these are examples of non-destructive testing and inspection d GO/NO-GO testing and inspection

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Ultrasonic testing and inspection is an example of non-destructive testing and inspection. This process helps to identify any internal or external flaws in the object being tested. It is used in various industries to ensure safety, reliability, and quality of products.

Non-destructive testing and inspection are methods of testing without causing damage to the material being tested. Ultrasonic testing and inspection is one such method. Ultrasonic testing uses high-frequency sound waves to detect any defects in the material. This technique is used in various industries such as aerospace, automotive, construction, and manufacturing. It is used to inspect metal, plastic, and other materials. The testing is non-invasive, fast, and highly accurate. Visual testing and inspection is another example of non-destructive testing. This is done by visually inspecting the surface of the object to identify any surface flaws, cracks, or other defects. This method is used in the inspection of welds, castings, and other components.

GO/NO-GO testing and inspection is also an example of non-destructive testing. This method is used to determine whether a component meets certain standards or not.

Ultrasonic testing and inspection is an example of non-destructive testing and inspection. Non-destructive testing is essential in ensuring safety, reliability, and quality in various industries. Visual testing and inspection and GO/NO-GO testing and inspection are also examples of non-destructive testing and inspection.

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As an energy engineer, has been asked from you to prepare a design of Pelton turbine in order to establish a power station worked on the Pelton turbine on the Tigris River. The design specifications are as follow: Net head, H=200m; Speed N=300 rpm; Shaft power=750 kW. Assuming the other required data wherever necessary.

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To design a Pelton turbine for a power station on the Tigris River with the specified parameters, the following design considerations should be taken into account:

Net head (H): 200 m

Speed (N): 300 rpm

Shaft power: 750 kW

To calculate the water flow rate, we need to know the specific speed (Ns) of the Pelton turbine. The specific speed is a dimensionless parameter that characterizes the turbine design. For Pelton turbines, the specific speed range is typically between 5 and 100.

We can use the formula:

Ns = N * √(Q) / √H

Where:

Ns = Specific speed

N = Speed of the turbine (rpm)

Q = Water flow rate (m³/s)

H = Net head (m)

Rearranging the formula to solve for Q:

Q = (Ns² * H²) / N²

Assuming a specific speed of Ns = 50:

Q = (50² * 200²) / 300²

Q ≈ 0.444 m³/s

The bucket diameter is typically determined based on the specific speed and the water flow rate. Let's assume a specific diameter-speed ratio (D/N) of 0.45 based on typical values for Pelton turbines.

D/N = 0.45

D = (D/N) * N

D = 0.45 * 300

D = 135 m

The number of buckets can be estimated based on experience and typical values for Pelton turbines. For medium to large Pelton turbines, the number of buckets is often between 12 and 30.

Let's assume 20 buckets for this design.

To design a Pelton turbine for the specified power station on the Tigris River with a net head of 200 m, a speed of 300 rpm, and a shaft power of 750 kW, the recommended design parameters are:

Water flow rate (Q): Approximately 0.444 m³/s

Bucket diameter (D): 135 m

Number of buckets: 20

Further detailed design calculations, including the runner blade design, jet diameter, nozzle design, and turbine efficiency analysis, should be performed by experienced turbine designers to ensure optimal performance and safety of the Pelton turbine in the specific application.

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A shaft made of steel having an ultimate strength of Su is finished by grinding the surface. The diameter of the shaft is d. The shaft is loaded with a fluctuating zero-to-maximum torque. = = % Su = 1200; % ultimate strength (MPa) % Sy 800; % yield strength (MPa) % d 8; % diameter of the shaft (mm) % ks 0.8; % surface factor ks % kG 1; % size (gradient) factor kG % N = 75*10^3; % cycles = 1. For N=75000 cycles, from S-N diagram, determine the fatigue strength (MPa). 2. For N=75000 cycles and repeated loads (zero-to-maximum), from constant life fatigue diagram, deter- mine: alternating stress (MPa) maximum stress (MPa)

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A shaft made of steel having an ultimate strength of Su is finished by grinding the surface. The diameter of the shaft is d. The shaft is loaded with a fluctuating zero-to-maximum torque.

Alternating stress and maximum stress from constant life fatigue diagram: For a given number of cycles, N, we can find the alternating stress and maximum stress from the constant life fatigue diagram. From the given data, we have N = 75,000 cycles.

Using the given data, we find that the alternating stress is Sa = 290 MPa and the maximum stress is Sm = 870 MPa. Hence, the alternating stress is 290 MPa, and the maximum stress is 870 MPa.

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To determine the fatigue strength (MPa) for N=75000 cycles, we can use the S-N diagram. The S-N diagram provides the relationship between stress amplitude (alternating stress) and the number of cycles to failure.

From the given information, we know that the ultimate strength (Su) is 1200 MPa. We can use the surface factor (ks) and size factor (kG) as 0.8 and 1 respectively, since no specific values are provided for them.

To find the fatigue strength, we need to determine the stress amplitude (alternating stress) corresponding to N=75000 cycles from the S-N diagram.

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The linear burning rate of a solid propellant restricted burning grain is 20 mm/s when the chamber pressure is 80 bar and 40 mm/s when the chamber pressure is 200 bar. determine (i) the chamber pressure that gives a linear burning rate of 30 mm/s (ii) the propellant consumption rate in kg/s if the density of the propellant is 2000 kg/m3, grain diameter is 200 mm and combustion pressure is 100 bar.

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(i) To determine the chamber pressure that gives a linear burning rate of 30 mm/s, we can use the concept of proportionality between burning rate and chamber pressure. By setting up a proportion based on the given data, we can find the desired chamber pressure.


(ii) To calculate the propellant consumption rate, we need to consider the burning surface area of the grain, the linear burning rate, and the density of the propellant. By multiplying these values, we can determine the propellant consumption rate in kg/s.

Let's calculate these values:

(i) Using the given data, we can set up a proportion to find the chamber pressure (P) for a linear burning rate (R) of 30 mm/s:
(80 bar) / (20 mm/s) = (P) / (30 mm/s)
Cross-multiplying, we get:
P = (80 bar) * (30 mm/s) / (20 mm/s)
P = 120 bar

Therefore, the chamber pressure that gives a linear burning rate of 30 mm/s is 120 bar.

(ii) The burning surface area (A) of the grain can be calculated using the formula:
A = π * (diameter/2)^2
A = π * (200 mm / 2)^2
A = π * (100 mm)^2
A = 31415.93 mm^2

To calculate the propellant consumption rate (C), we can use the formula:
C = A * R * ρ
where R is the linear burning rate and ρ is the density of the propellant.

C = (31415.93 mm^2) * (30 mm/s) * (2000 kg/m^3)
C = 188,495,800 mm^3/s
C = 0.1885 kg/s

Therefore, the propellant consumption rate is 0.1885 kg/s if the density of the propellant is 2000 kg/m^3, the grain diameter is 200 mm, and the combustion pressure is 100 bar.

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