% 11.+11:04) العنوانDrive the modeling process equation the filling a tank, which explained in thefollowing figure. By applied the transfer function for controlling on the tank filling1/P1۱/۱Find I-fincostron|||AOI =T☑M

Answered: % 11. + 11:04 ) العنوان Drive the…

Principles of Heat Transfer (Activate Learning with these NEW titles from Engineering!)

8th Edition

ISBN:9781305387102

Author:Kreith, Frank; Manglik, Raj M.

Publisher:Kreith, Frank; Manglik, Raj M.

Chapter4: Numerical Analysis Of Heat Conduction

Section: Chapter Questions

Problem 4.6P

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'p' (liquid density 'A' (tank cross sectional area) 'Qin' (Input Flow Rate) "Que P 'R' (restriction coefficient) '' (head of liquid) dh Qin = A + dt Figure 1 The single tank system (Figure 1) has been modelled by the first order differential equation given as equation. The equation describes the relationship between the input flow rate entering the tank and the head of liquid in the tank. ph R 5 m equation The following constants are provided: R = 40 Kpa s m², 4 = 10 m², p= 1001 kg m², and g = 9.81 m s A pump is suddenly switched on and provides a step input flow rate of 0.5 m³s¹. (1) Using Laplace Transforms, solve equation and provide an expression to show how the level in the tank will vary in time after the step input has been applied.
hey can i get help with these two questions please. thank you.
ZVA @ e SIM a A moodle1.du.edu.om Solve the second order homogeneous differential equation y " -6y'-7y = 0 with intial values y(0) = 0; y'(0) = 1 %3D Maximum file size: 200MB, maximum number of files: 1 Files II
Please solve this question in mechatronics
b. Using Simulink, simulate the transfer function airflow response, Q(t) (air entering respiratory system) for a sine wave input pressure Pao(t)= 2.5 cm·H2O (i.e. 5 cm·H2O peak-to-peak) at 15 breaths min' (or 0.25 Hz) for each lung model. Use the following parameters: -1 i. RC model: R= 1cm·H2O's L' and C=0.2 L·cm·H2O¯ RIC model: R= 1cm·H2O's·L', C= 0.2 L·cm·H2O¯ , and I= 0.01 cm·H2O L-s² Two-compartment model: R. = lcm H2O's L', Rp1,2 = 0.5 cm·H2O•s·L', Cp1,2=0.2 L·cm·H2O', and I= 0.01 cm H2O·L-•s² Mead model: R. = 1cm·H2O•s L', Rp = 0.5 cm:H2O•s·L', C1 =0.2 L·cm·H2O', Cw=0.2 L·cm·H2O-', C, =0.005 L·cm·H2O', and I= 0.01 cm H2O·L-1·s² ii. iii. iv.
The Johnson & Royce model of a distillation column is driven by the inputs of steam flow and its flow rate; the output measurement is the temperature change. The state-space model is given by: -2 x = [¯²¯¯¯7 | x + | | | u; y = [0_1]x - the system defining the model of the distillation column is a. Asymptotically stable O b. Unstable Oc. Marginally stable Od. Indeterminate in relation to its stability
B9
find trasfer function Y(s)/R(s) if kc is 5 and plant is 1/(0.5s+1). input r(t) is a unit-step function
Help me with this ASAP. Thank you! Find the Following: 1. Natural angular velocity 2.Damped angular velocity 3. Equation of motion x(t). Assume Initial conditions for displacement and velocity 4. Graph 2 cycles of the vibrating system. You can use third party app for this.
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