Problem 21.13. Only do parts (a) and (b). can be used to generate the fol-21.13 The function f(x) = 2elowing table of unequally spaced data:x | 0 0 0.050.150.25 0.35 0.475 0.6f(x) 2 1.8555 1.5970 1.3746 1.1831 0.9808 0.8131Evaluate the integral from a = 0 to b = 0.6 using (a) analyticalmeans, (b) the trapezoidal rule, and (c) a combination of the trap-ezoidal and Simpson's rules; employ Simpson's rules whereverpossible to obtain the highest accuracy. For (b) and (c), compute

Part (a): Analytical Evaluation We need to evaluate the integral of f(x)=2e−1.5x from a = 0 to b =…

Answered: can be used to generate the fol- 21.13…

Elements Of Electromagnetics

7th Edition

ISBN:9780190698614

Author:Sadiku, Matthew N. O.

Publisher:Sadiku, Matthew N. O.

ChapterMA: Math Assessment

Section: Chapter Questions

Problem 1.1MA

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I have the answers but I want to know the steps. blank1 = 1.764 , blank2 = -2.18 , blank3= 43.307 , blank4 = 1.764
I have the answers but I want to know the steps with calculation to reach these answers. blank1 = 1.764 , blank2 = -2.18 , blank3= 43.307 , blank4 = 1.764
Table Error function (erf) values erf (z) erf (2 erf (z) 0.55 0.5033 13 0.9340 0.025 0.0282 O 60 0.6039 14 0.9523 0.05 0.0564 0.05 0 6420 15 0.9001 0.10 0.1125 0.70 0 6778 0.9703 16 0.15 0.1080 0.75 0.7112 1.7 0.9838 0 20 0.2227 080 07421 18 0.0091 025 0 2703 0.85 0.7707 1.9 0.0028 0.30 0.3290 0.90 0.7969 20 0.9953 0.35 03704 0.95 0.8200 22 0.9981 040 0.4284 O 8427 O 8802 1.0 24 0.9903 0.45 0.4755 11 2.6 0.0098 0 50 0.5205 12 0.9103 28 0 9990 A 1010 steel is to be carburized using a gas atmosphere that produces 1.0% Cat the surface of the steel. The case depth is defined as the distance below the surface that contains at least 0.5% Č. If carburizing is done at 1000 C, determine the time required to produce a case depth of 0 234 mm. For the diffusion of Garbon in FCC iron Q - 137.7 kJ/mol and Do = 0.23 x 10 m²/s. The gas constant is R- 8.314 J/(mol - K). Assume that the diffusion coefficient D remains constant and the concentrations of the diffusing atoms at the surface (c.) and at…
Please i need it ASAP
a) b) c) Use composite Simpson's rule to estimate xe*dx with n=4. Subsequently, find the absolute error. dy dx Given 3y + 2x, where y(0) = 1 and h = 0.2. Approximate the solution for the differential equation for one iteration only by using Runge Kutta method of order two. Set up the Gauss-Siedel iterative equations the following linear system: 6x₁-3x₂ = 2 -x₁ + 3x₂ + x3 =1 x₂ + 4x₂ = 3 (Do not solve)
Calculate the value of the first order derivative at the point x=0.2 with a single finite difference formula using all the following values. 0.1 0.2 0.3 0.4 f(x) 0.000 000 0.078 348 0.138 910 0.192 916 0.244981
What's the mean of the following points? x = [-3 3 4 2 -1 1 4 5] Type your answer...
A webassign.net/web/Student/Assignment-Responses/last?dep=28040811 Consider the following. Z = 2 Sketch a graph of the plane. 10 10 0. 5. 5. 10 10 10 10 10 10 rz 0. 5. 10 10 10 10 O Type here to search
Had to place entire problem on here because it was confusing experts. Thank you for your help.
How do you calculate the instantaneous velocity from a velocity vs time graph? Eg. From the image below, Calculate the instantaneous velocity of V(4) at t(4),etc.
Read the questions carefully and answer with complete solution and units. Use the steam tables provided and use 4 decimal places for solving. Final answers shown are in 2 decimal places. Draw the T-S diagrams properly with respect to the saturation line A steam power plant uses the ideal Reheat-Regenerative Rankine cycle where the steam enters the high-pressure turbine at 4 MPa and 300C. It partially expands to 600 kPa where some steam is extracted for feedwater heating while the rest is reheated to the same temperature. After expanding again, it enters the condenser at 10 kPa. Sketch the schematic diagram and the TS diagram with labeled points, and solve for mass taken for feedwater heating, Qa, Qr, Wt, Wp, Wnet, thermal efficiency, and Steam rate. Neglect the condensate pump work. 20.01%, 2667.841,1715.52,955.97, 3.74,952.32¹,3 35.69%, 3.78- kg kg kg kg kWh I

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