Problem 2. A chemical constituent flows between three well-mixed tanks, also called reactors, as depicted in Figure below. Steady-state mass balances can be written for a substance that reacts with first- order kinetics. For example, the mass balance in reactor 1 is where Qin volumetric inflow to reactor 1 (L/min), cin inflow mass concentration to reactor 1 (g/L), Qij volumetric flow from reactor i to reactor j (L/min), c = concentration in reactor i (g/L), k first-order decay rate (min), and V₁ = volume of reactor i (L). (a) Write the mass balances for reactors 2 and 3. (b) If k = 0.1 min, write the mass balances for all three reactors as a system of linear algebraic equations. (c) Compute the LU factorization for this system. (d) Use the LU factorization to compute the matrix inverse. (e) Use the matrix inverse to address the following questions: Q-10 -200 (i) What are the steady-state concentrations in the three reactors? 021-22 (ii) If the inflow in the second reactor is set to zero, what is the resulting reduction in the concentration in reactor 1? 12-5 V₁-100 V-150 Q13-117 10-110 Sia - 10 (iii) If the inflow concentration to reactor 1 is doubled, and the inflow concentration to reactor 2 is halved, what will be the concentration in reactor 3?

Database System Concepts
7th Edition
ISBN:9780078022159
Author:Abraham Silberschatz Professor, Henry F. Korth, S. Sudarshan
Publisher:Abraham Silberschatz Professor, Henry F. Korth, S. Sudarshan
Chapter1: Introduction
Section: Chapter Questions
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Python Programming. Do not use Matlab.

Problem 2. A chemical constituent flows between three well-mixed tanks, also called reactors, as
depicted in Figure below. Steady-state mass balances can be written for a substance that reacts with first-
order kinetics. For example, the mass balance in reactor 1 is
where Qin volumetric inflow to reactor 1 (L/min), cin inflow mass concentration to reactor 1 (g/L), Qij
volumetric flow from reactor i to reactor j (L/min), c = concentration in reactor i (g/L), k first-order
decay rate (min), and V₁ = volume of reactor i (L).
(a) Write the mass balances for reactors 2 and 3.
(b) If k = 0.1 min, write the mass balances for all three reactors as a system of linear algebraic equations.
(c) Compute the LU factorization for this system.
(d) Use the LU factorization to compute the matrix
inverse.
(e) Use the matrix inverse to address the following
questions:
Q-10
-200
(i) What are the steady-state concentrations in the
three reactors?
021-22
(ii) If the inflow in the second reactor is set to zero,
what is the resulting reduction in the concentration in
reactor 1?
12-5
V₁-100
V-150
Q13-117
10-110
Sia - 10
(iii) If the inflow concentration to reactor 1 is
doubled, and the inflow concentration to reactor 2 is halved, what will be the concentration in reactor 3?
Transcribed Image Text:Problem 2. A chemical constituent flows between three well-mixed tanks, also called reactors, as depicted in Figure below. Steady-state mass balances can be written for a substance that reacts with first- order kinetics. For example, the mass balance in reactor 1 is where Qin volumetric inflow to reactor 1 (L/min), cin inflow mass concentration to reactor 1 (g/L), Qij volumetric flow from reactor i to reactor j (L/min), c = concentration in reactor i (g/L), k first-order decay rate (min), and V₁ = volume of reactor i (L). (a) Write the mass balances for reactors 2 and 3. (b) If k = 0.1 min, write the mass balances for all three reactors as a system of linear algebraic equations. (c) Compute the LU factorization for this system. (d) Use the LU factorization to compute the matrix inverse. (e) Use the matrix inverse to address the following questions: Q-10 -200 (i) What are the steady-state concentrations in the three reactors? 021-22 (ii) If the inflow in the second reactor is set to zero, what is the resulting reduction in the concentration in reactor 1? 12-5 V₁-100 V-150 Q13-117 10-110 Sia - 10 (iii) If the inflow concentration to reactor 1 is doubled, and the inflow concentration to reactor 2 is halved, what will be the concentration in reactor 3?
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