Modeling Salt Mixing in a Chemical Plant: Finding Eigenvalues and Equilibria

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Homework Help Overview

The discussion revolves around a mathematical model for salt mixing in a chemical plant with three tanks. The problem involves differential equations representing the flow and mixing of saltwater in the tanks, with specific parameters such as tank volumes and flow rates provided. Participants are tasked with finding eigenvalues and eigenvectors, as well as determining equilibrium states of the system.

Discussion Character

  • Mixed

Approaches and Questions Raised

  • Participants discuss the formulation of the differential equations and the corresponding coefficient matrix. There are attempts to find eigenvalues and eigenvectors, with some expressing confusion about the process. Questions arise regarding the behavior of tanks 2 and 3 and their relevance to the overall system.

Discussion Status

Some participants are actively engaging with the mathematical aspects of the problem, while others express confusion about the setup and whether the question fits the forum's guidelines for homework help. There is no explicit consensus on the interpretation of the problem or the direction of the discussion.

Contextual Notes

Participants note potential issues with the clarity of the problem, particularly regarding the flow dynamics in tanks 2 and 3. There is also a concern about the appropriateness of the question for the forum, suggesting it may be perceived as a typical homework problem.

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A chemical plant with 3 tanks in succession with mizing of reactants and products. Brine tanks = fresh water flows into tank, mixed brine from tank 1 to tank 2, then tank 2 into tank 3, and out of tank 3.

Let xi(t) = lbs of salt in tank i at time t for i=1,2,3

Assume each flow rate is in gal/min

dx1/dt = (rate in) - (rate out) = 0 lbs/min - (r gal/min)*(x1 lbs / V1 gal)

dx1/dt = (-r / V1)*x1

dx2/dt = (r / V1)*x1 - (r / V2)*x2

dx3/dt = (r / V2)*x2 - (r / V3)*x3

To simplify the variables:

x1(t) = x x2(t) = y x3(t) = z

Let x1(t),y1(t),z1(t) = lbs of salt in tank 1 after t minutes

Suppose V1 = 20 gal, V2= 40 gal, and V3 = 50 gal and r = 10 gal/min with initial amounts of salt in each tank:

x(0) = 15 lbs, y(0) = 0 lbs, z(0) = 0 lbs

(a) Write the mathematical model in the form of dŷ/dt = Aŷ and find the 3x3 coefficient matrix A.

ŷ = vector y notation

I did this part and got dx/dt = -1/2x dy/dt = 1/2x-1/4y dz/dt = 1/4y - 1/5z

coefficient matrix: | 1/2 - λ 0 0 |

| 1/2 -1/4-λ 0 |

| 0 1/4 -1/5-λ|

b) Show hand work in finding the eigen values, by solving det(A-λI)=0, and eigenvectors of A.

I got Eigenvalues: λ1 = -1/2 λ2 = -1/4 λ3 = -1/5, but I am having trouble getting the eigen vectors



E = NOATION FOR EIGENVECTOR

c) Fidn the general solution as a linear combination of eigen solutions:

ŷ(t) = c1e^(λ1t)*E1 + c2e^(λ2t)*E2 + c3e^(λ3t)*E3



(d) find the formulas for x(t), y(t), and z(t), the maountf of salt in each tank after t minutes using theinitial data



(e) Find all equilibrium of the DE system dŷ/dt = Aŷ and describe their type (spiral or sink or real source, etc)
 
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I am puzzled as to what happens in tanks 2 and 3. If solution simple flows in and then out, with no additional water or solution, the whole problem is just what comes out of tank1. Tanks 2 and 3 might as well be a single outflow pipe.
 
I'm also confused, but for a different reason.

This sure sounds to me like a "homework style" question. I'm not a regular here, but shouldn't it be redirected to one of the homework forums?
 
chogg said:
I'm also confused, but for a different reason.

This sure sounds to me like a "homework style" question. I'm not a regular here, but shouldn't it be redirected to one of the homework forums?

Done.
 

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