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IRWIN 9e 2_38
Course: EEE 202, Fall 2009School: ASU
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ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
ASU - EEE - 202
European Business School - FIN - 123
Rice - CHE - 470
Problem 1Overall Material Balance:dn d(V) = = i Fi F dt dt ( Fi F ) = 0 dV d +V = i Fi F dt dt(S1.1)Assuming constant density and reactor volume, equation (S1.1) yields:Fi F = 0(S1.2)Therefore, the input and output flow rates are equal at each po
Rice - CHE - 470
CHBE 470 Process Dynamics and Control Fall 2007 Homework Set 4 Assigned: Wednesday, September 26 Due: Wednesday, October 3Note: Please staple your papers and include your name in the first page Use table 7.1 from textbook wherever you find appropriate Pr
Rice - CHE - 470
CHBE 470 - Control Design Problem Maleic Anhydride Plant Homework #9 - Due November 30, 2007 The feed preparation and reaction section of a Maleic Anhydride plant is shown in the following sketch. In this exercise, you will design controls for this plant.
Rice - CHE - 470
Problem 1Overall Material Balance:dn d(V) = = i Fi F dt dt ( Fi F ) = 0 dV d +V = i Fi F dt dt(S1.1)Assuming constant density and reactor volume, equation (S1.1) yields:Fi F = 0(S1.2)Therefore, the input and output flow rates are equal at each po
Rice - CHE - 470
Problem 1 Overall Material Balance:dn d(V) d(Ah) = = = i Fi F dt dt dtAdh d + Ah = i Fi F dt dt(S1.1)In absence of chemical reactions and at constant temperature and pressure, the density of the fluid liquid in the tank can be assumed constant. There
Rice - CHE - 470
Problem 1 From table 7.1 in the textbook, the Laplace transform of y(t)=te-t is: L te t = y(s) = 1 (s + 1) 2 (S1.1)Moreover, the Laplace transform of the unit-impulse (t) is:L [ (t) ] = u(s) = 1(S1.2)Since u(t)=0 all the time but at t=to, assuming tha
Rice - CHE - 470
Problem 1 a) For noninteracting capacities with linear resistances subject to a unit-step change in the input of the first tank, the material balance can be written as follows:A1R1A2R 2dy1 + y1 = R1u(t) dtdy 2 R + y 2 = 2 y1 dt R1(S1.1)(S1.2)subjec
Rice - CHE - 470
Problem 1ySP (s) +k = 1.65 (s + 1)(2s + 1)y(s)The closed loop transfer function can be written as follows:8 y(s) 8 89 (s + 1)(2s + 1) G CL (s) = = =2 = 2 8 ySP (s) 1 + 2s + 3s + 9 2 9s + 1 3s + 1 (s + 1)(2s + 1) Thus, comparing (S1.1) to the standar
Rice - CHE - 470
Problem 1controller valve tank 11 0.2s + 0.4s + 12ySP (s)k C (1 + 3 s)y(s)1Measuring device2Figure 1The characteristic equation for the closed loop in figure 1 can be written as follows:1 + G OL (s) = 1 +2k C (1 + 3 s) 0.2s 2 + 0.4s + 1(S1.1
Rice - CHE - 470
Problem 1 a) The transfer function of this process can be expressed as the product of three first order lag transfer functions. The AR and phase angles of a general 1st order lag are:AR =K +12 2and = tan 1 ()(S1.1)Thus, applying the principle of sup
Rice - CHE - 470
Rice - CHE - 470
Rice - CHE - 470
Rice - CHE - 470
Rice - CHE - 470
Umea University - PHYSICS - thermo b
Umea University - PHYSICS - thermo b
Umea University - PHYSICS - thermo b
Umea University - PHYSICS - thermo b
Umea University - PHYSICS - thermo b
Umea University - PHYSICS - thermo b
Umea University - PHYSICS - thermo b