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layout="Title" style="Title"><Font executable="false">Heating an Oil Stream Through  Steam-Heated Tanks</Font></Text-field></Input></Group><Group><Input><Text-field alignment="centred" layout="Normal" style="Text">Samir Khan, Adept Scientific
Jason Schattman, Maplesoft, a division of Waterloo Maple Inc.</Text-field></Input></Group><Group><Input><Text-field firstindent="0.0" layout="Author" leftmargin="0.0" linebreak="space" rightmargin="0.0" style="Author"><Font bold="false" encoding="ISO8859-1" executable="false" foreground="[0,0,0]" italic="false" subscript="false" superscript="false" underline="false">\251 </Font><Font bold="false" executable="false" foreground="[0,0,0]" italic="false" subscript="false" superscript="false" underline="false">Maplesoft, a division of Waterloo Maple Inc. and Adept Scientific 2004</Font></Text-field></Input></Group><Group><Input><Text-field layout="Normal" style="Text"/></Input></Group><Group><Input><Text-field alignment="centred"><Image height="350" 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collapsed="true"><Title><Text-field layout="Heading 1" style="Heading 1">Introduction</Text-field></Title><Group><Input><Text-field layout="Normal" style="Text"><Font encoding="ISO8859-1">Oil is to be heated by being pumped through a series of steam-heated tanks. \240This application shows how Maple can be used to design and analyze such a system. \240</Font></Text-field><Text-field layout="Normal" style="Text"/><Text-field layout="Normal" style="Text">In particular, we will derive closed-form formulas for the transient and steady-state temperature of the oil in each tank as a function of time, in terms of the flow rate of the oil (<Font italic="true">W</Font>), the specific heat capacity of the oil (<Font italic="true">Cp</Font>), the mass of the oil in each tank (<Font italic="true">M</Font>), the heat transfer coefficient (<Font italic="true">U</Font>), the heat transfer area (<Font italic="true">A</Font>), the temperature of the cold oil (<Font italic="true">T0</Font>) and the temperature of the steam (<Font italic="true">Ts</Font>).  We will also verify the dimensions of these formulas to get a quick check on the accuracy of the solution.</Text-field><Text-field layout="Normal" style="Text"/><Text-field layout="Normal" style="Text">The following Maple techniques are highlighted:</Text-field><Text-field layout="Normal" style="Text"><Font encoding="UTF-8">\342\200\242  Symbolic solving of systems of ordinary differential equations</Font></Text-field><Text-field layout="Normal" style="Text"><Font encoding="UTF-8">\342\200\242  Management of units and dimensions</Font></Text-field><Text-field layout="Normal" style="Text"><Font encoding="UTF-8">\342\200\242  Manipulation of symbolic expressions to yield further insights into a problem</Font></Text-field><Text-field layout="Normal" style="Text"><Font encoding="UTF-8">\342\200\242  Deployment of the solution as an Excel application through automatic generation of Visual Basic code</Font></Text-field><Text-field layout="Normal" style="Text"><Font encoding="UTF-8">\342\200\242  Deployment </Font>of the solution as a Maplet application</Text-field></Input></Group></Section><Section collapsed="true"><Title><Text-field layout="Heading 1" style="Heading 1">Initialization</Text-field></Title><Group><Input><Text-field layout="Normal" prompt="&gt; " style="Maple Input">restart:
interface( warnlevel = 0 ):
with( CodeGeneration ):</Text-field></Input></Group></Section><Section collapsed="true"><Title><Text-field layout="Heading 1" style="Heading 1">Model</Text-field></Title><Group><Input><Text-field layout="Normal" style="Text">Below is a schematic of the heating system.  Cold oil is pumped through three identical steam-heated tanks at a constant rate.</Text-field></Input></Group><Group><Input><Text-field alignment="centred"><Image height="194" width="558">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</Image></Text-field></Input></Group><Group><Input><Text-field layout="Normal" style="Text">Standard texts on chemical engineering show that the temperature of the oil in each tank can be modeled by the following system of differential equations:</Text-field></Input></Group><Group><Input><Text-field alignment="centred" layout="Normal" style="Text"><Equation input-equation="M*C[p]" style="2D Math">NiMqJkkiTUc2IiIiIiZJIkNHRiU2I0kicEdGJUYm</Equation><Equation input-equation="diff(T[1](t),t)" style="2D Math">NiMtSSVkaWZmR0kqcHJvdGVjdGVkR0YlNiQtJkkiVEc2IjYjIiIiNiNJInRHRipGLg==</Equation> = <Equation input-equation="W*C[p](T[0](t)-T[1](t))+U*A(T[s]-T[1](t))" style="2D Math">NiMsJiomSSJXRzYiIiIiLSZJIkNHRiY2I0kicEdGJjYjLCYtJkkiVEdGJjYjIiIhNiNJInRHRiZGJy0mRjE2I0YnRjQhIiJGJ0YnKiZJIlVHRiZGJy1JIkFHRiY2IywmJkYxNiNJInNHRiZGJ0Y2RjlGJ0Yn</Equation></Text-field></Input></Group><Group><Input><Text-field alignment="centred" layout="Normal" style="Text"><Equation input-equation="M*C[p]" style="2D Math">NiMqJkkiTUc2IiIiIiZJIkNHRiU2I0kicEdGJUYm</Equation><Equation input-equation="diff(T[2](t), t)" style="2D Math">NiMtSSVkaWZmR0kqcHJvdGVjdGVkR0YlNiQtJkkiVEc2IjYjIiIjNiNJInRHRipGLg==</Equation> = <Equation input-equation="W*C[p](T[1](t)-T[2](t))+U*A(T[s]-T[2](t))" style="2D Math">NiMsJiomSSJXRzYiIiIiLSZJIkNHRiY2I0kicEdGJjYjLCYtJkkiVEdGJjYjRic2I0kidEdGJkYnLSZGMTYjIiIjRjMhIiJGJ0YnKiZJIlVHRiZGJy1JIkFHRiY2IywmJkYxNiNJInNHRiZGJ0Y1RjlGJ0Yn</Equation></Text-field></Input></Group><Group><Input><Text-field alignment="centred" layout="Normal" style="Text"><Equation input-equation="M*C[p]" style="2D Math">NiMqJkkiTUc2IiIiIiZJIkNHRiU2I0kicEdGJUYm</Equation><Equation input-equation="diff(T[3](t), t)" style="2D Math">NiMtSSVkaWZmR0kqcHJvdGVjdGVkR0YlNiQtJkkiVEc2IjYjIiIkNiNJInRHRipGLg==</Equation> = <Equation input-equation="W*C[p](T[2](t)-T[3](t))+U*A(T[s]-T[3](t))" style="2D Math">NiMsJiomSSJXRzYiIiIiLSZJIkNHRiY2I0kicEdGJjYjLCYtJkkiVEdGJjYjIiIjNiNJInRHRiZGJy0mRjE2IyIiJEY0ISIiRidGJyomSSJVR0YmRictSSJBR0YmNiMsJiZGMTYjSSJzR0YmRidGNkY6RidGJw==</Equation></Text-field></Input></Group><Group><Input><Text-field layout="Normal" style="Text"/></Input></Group><Text-field layout="Normal" style="Text">where the parameters are defined as follows:
</Text-field><Text-field layout="Normal" style="Text"><Equation input-equation="W" style="2D Math">NiNJIldHNiI=</Equation><Font italic="true">		Flow rate of the oil		</Font><Equation input-equation="kg/s" style="2D Math">NiMqJkkja2dHNiIiIiJJInNHRiUhIiI=</Equation></Text-field><Text-field layout="Normal" style="Text"><Equation input-equation="M" style="2D Math">NiNJIk1HNiI=</Equation><Font italic="true">		Mass of oil in each tank	</Font><Equation input-equation="kg" style="2D Math">NiNJI2tnRzYi</Equation></Text-field><Text-field layout="Normal" style="Text"><Equation input-equation="C[p]" style="2D Math">NiMmSSJDRzYiNiNJInBHRiU=</Equation><Font italic="true">		Specific heat capacity	 	</Font><Equation input-equation="J/(kg*K)" style="2D Math">NiMqJkkiSkc2IiIiIiomSSNrZ0dGJUYmSSJLR0YlRiYhIiI=</Equation></Text-field><Text-field layout="Normal" style="Text"><Equation input-equation="U" style="2D Math">NiNJIlVHNiI=</Equation><Font italic="true">		Heat transfer coefficient	</Font><Equation input-equation="W/(m^2*K)" style="2D Math">NiMqJkkiV0c2IiIiIiomSSJtR0YlIiIjSSJLR0YlRiYhIiI=</Equation></Text-field><Text-field layout="Normal" style="Text"><Equation input-equation="A" style="2D Math">NiNJIkFHNiI=</Equation><Font italic="true">		Heat transfer area		</Font><Equation input-equation="m^2" style="2D Math">NiMqJEkibUc2IiIiIw==</Equation></Text-field><Text-field layout="Normal" style="Text"><Equation input-equation="T[0]" style="2D Math">NiMmSSJURzYiNiMiIiE=</Equation><Font italic="true">		Temperature of cold oil stream 	</Font><Equation input-equation="C" style="2D Math">NiNJIkNHNiI=</Equation></Text-field><Text-field layout="Normal" style="Text"><Equation input-equation="T[1](t)" style="2D Math">NiMtJkkiVEc2IjYjIiIiNiNJInRHRiY=</Equation> <Equation input-equation="T[2](t)" style="2D Math">NiMtJkkiVEc2IjYjIiIjNiNJInRHRiY=</Equation> <Equation input-equation="T[3](t)" style="2D Math">NiMtJkkiVEc2IjYjIiIkNiNJInRHRiY=</Equation>	<Font italic="true">Transient temperatures 	</Font><Equation input-equation="C" style="2D Math">NiNJIkNHNiI=</Equation></Text-field><Text-field layout="Normal" style="Text"><Equation input-equation="T[s]" style="2D Math">NiMmSSJURzYiNiNJInNHRiU=</Equation><Font italic="true">		Temperature of steam		</Font><Equation input-equation="C" style="2D Math">NiNJIkNHNiI=</Equation></Text-field><Text-field layout="Normal" style="Text"/><Group><Input><Text-field layout="Normal" style="Text">We first enter this model into Maple</Text-field></Input></Group><Section collapsed="true"><Title><Text-field layout="Heading 2" style="Heading 2">Temperature in Tank 1</Text-field></Title><Group><Input><Text-field layout="Normal" prompt="&gt; " style="Maple Input">eq1 :=  M*Cp * diff(T1(t),t) = W*Cp*(T0-T1(t)) + U*A*(Ts-T1(t));</Text-field></Input></Group></Section><Section collapsed="true"><Title><Text-field layout="Heading 2" style="Heading 2">Temperature in Tank 2</Text-field></Title><Group><Input><Text-field layout="Normal" prompt="&gt; " style="Maple Input">eq2 := M*Cp * diff(T2(t),t) = W*Cp*(T1(t)-T2(t))+U*A*(Ts-T2(t));</Text-field></Input></Group></Section><Section><Title><Text-field layout="Heading 2" style="Heading 2">Temperature in Tank 3</Text-field></Title><Group><Input><Text-field layout="Normal" prompt="&gt; " style="Maple Input">eq3 := M*Cp * diff(T3(t),t) = W*Cp*(T2(t)-T3(t))+U*A*(Ts-T3(t));</Text-field></Input></Group></Section><Section><Title><Text-field layout="Heading 2" style="Heading 2">Initial conditions</Text-field></Title><Group><Input><Text-field layout="Normal" prompt="&gt; " style="Maple Input">Initial := T1(0) = T0, T2(0) = T0, T3(0) = T0;</Text-field></Input></Group></Section></Section><Section collapsed="true"><Title><Text-field layout="Heading 1" style="Heading 1">Solve</Text-field></Title><Group><Input><Text-field layout="Normal" style="Text">We can now easily solve the model equations symbolically in one step.</Text-field></Input></Group><Group><Input><Text-field layout="Normal" prompt="&gt; " style="Maple Input">sols := dsolve( {eq1, eq2, eq3, Initial}, parametric );</Text-field></Input></Group></Section><Section collapsed="true"><Title><Text-field layout="Heading 1" style="Heading 1">Test</Text-field></Title><Text-field layout="Normal" style="Text">Maple has given us the explicit formulas describing the transient change in temperature in each tank.  It's now easier to investigate the natural consequences of the model equations.  

Before we proceed, we should check that the formulas make dimensional sense.  Maple provides built-in support for units management to make this task fast and easy.</Text-field><Section collapsed="true"><Title><Text-field layout="Heading 2" style="Heading 2">Verify the units and dimensions</Text-field></Title><Group><Input><Text-field layout="Normal" prompt="&gt; " style="Maple Input">t1 := eval(T1(t), sols);
t2 := eval(T2(t), sols);
t3 := eval(T3(t), sols);
with( Units[Standard] ):</Text-field></Input></Group><Group><Input><Text-field layout="Normal" style="Text">
Here are some sample values for the parameters <Font italic="true">W, M, Cp, U, A, T0 </Font>and<Font italic="true"> Ts </Font><Font bold="true">with units attached</Font>.</Text-field></Input></Group><Group><Input><Text-field layout="Normal" prompt="&gt; " style="Maple Input">sampleValues := [
W  = 100 * Unit(kg/s), 
M  = 1000 * Unit(kg), 
Cp = 2 * Unit(J/(kg*K)), 
U  = 10 * Unit(W/(m^2*K)), 
A  = 1 * Unit(m^2), 
T0 = 10 * Unit(degC), 
Ts = 250 * Unit(degC), 
t  = t * Unit(s) ];</Text-field></Input></Group><Group><Input><Text-field layout="Normal" style="Text"/><Text-field layout="Normal" style="Text">Here is the formula for the temperature in Tank 1 evaluated at these sample values.  <Font bold="true">Note that the dimensions reduce to temperature (Kelvin (K)), as expected</Font>.  This gives us an extra measure of confidence that Maple's solution to the model equations is correct.</Text-field></Input></Group><Group><Input><Text-field layout="Normal" prompt="&gt; " style="Maple Input">T1(t) := eval( t1, sampleValues );</Text-field></Input></Group><Group><Input><Text-field layout="Normal" style="Text">
And the temperature in Tank 2:</Text-field></Input></Group><Group><Input><Text-field layout="Normal" prompt="&gt; " style="Maple Input">T2(t) := eval( t2, sampleValues );</Text-field></Input></Group><Group><Input><Text-field layout="Normal" style="Text">
And the temperature in Tank 3:</Text-field></Input></Group><Group><Input><Text-field layout="Normal" prompt="&gt; " style="Maple Input">T3(t) := eval( t3, sampleValues );</Text-field></Input></Group><Group><Input><Text-field layout="Normal" prompt="&gt; " style="Maple Input">plot([convert(T1(t), unit_free), convert(T2(t), unit_free),convert(T3(t), unit_free)], t=0..60, color=[red,blue,black], thickness=2, labels=["Time", "Temperature (K)"], labeldirections=[HORIZONTAL, VERTICAL], legend=["Tank 1", "Tank 2", "Tank 3"], 
title="Transient Temperatures vs. Time");
</Text-field></Input></Group></Section><Group><Input><Text-field layout="Normal" style="Text">Next we wish to see what happens in the steady state.  That is, what temperature does the oil stream converge to when it is fully heated?  Maple will again help us derive symbolic formulas that will yield further insight into the problem.  In particular, <Font bold="true">we will be able to predict the steady-state temperature in a system with <Font italic="true">any number of tanks</Font>, not just three</Font>.</Text-field></Input></Group><Section><Title><Text-field layout="Heading 2" style="Heading 2">Steady-state temperature in Tank 1</Text-field></Title><Group><Input><Text-field layout="Normal" style="Text">We can extract an expression describing the steady-state temperature in Tank 1 by finding the limit of T<Font subscript="true">1</Font>(t) as t approaches infinity assuming all parameters are positive.</Text-field></Input></Group><Group><Input><Text-field layout="Normal" prompt="&gt; " style="Maple Input">limit(t1, t = infinity) assuming positive:
convert(%, parfrac, U);</Text-field></Input></Group><Group><Input><Text-field layout="Normal" style="Text">We can find the steady-state temperature in the other two tanks following a similar process.</Text-field></Input></Group></Section><Section><Title><Text-field layout="Heading 2" style="Heading 2">Steady-state temperature in Tank 2</Text-field></Title><Group><Input><Text-field layout="Normal" prompt="&gt; " style="Maple Input">limit(t2, t = infinity) assuming positive:
convert(%, parfrac, U);</Text-field></Input></Group></Section><Section><Title><Text-field layout="Heading 2" style="Heading 2">Steady-state temperature in Tank 3</Text-field></Title><Group><Input><Text-field layout="Normal" prompt="&gt; " style="Maple Input">limit(t3, t = infinity) assuming positive:
convert(%, parfrac, U);</Text-field></Input></Group></Section><Section><Title><Text-field layout="Heading 2" style="Heading 2">Steady-state temperature in Tank N</Text-field></Title><Group><Input><Text-field layout="Normal" style="Text">From the formulas above, we can infer that the steady-state temperature in the <Font italic="true">n</Font>th tank is: </Text-field><Text-field layout="Normal" style="Text"/></Input><Input><Text-field alignment="centred" style="Text"><Equation input-equation="Ts+W^n*Cp^n*(-Ts+T0)/(W*Cp+U*A)^n" style="2D Math">NiMsJkkjVHNHNiIiIiIqKilJIldHRiVJIm5HRiVGJilJI0NwR0YlRipGJiwmRiQhIiJJI1QwR0YlRiZGJiksJiomRilGJkYsRiZGJiomSSJVR0YlRiZJIkFHRiVGJkYmRipGLkYm</Equation> </Text-field></Input></Group><Group><Input><Text-field layout="Normal" style="Text"/><Text-field layout="Normal" style="Text">This formula gives us considerable predictive power.  We now know how a system of any number of tanks will perform in the steady state, without having to build any prototypes or do any more modeling.</Text-field></Input></Group></Section></Section><Section collapsed="true"><Title><Text-field layout="Heading 1" style="Heading 1">Deploy</Text-field></Title><Group><Input><Text-field layout="Normal" style="Text">We have used Maple to solve the problem as stated.  The final challenge is to put that solution into the hands of the people who can benefit from it.  Maple provides numerous options for such deployment.  We show two of them below.</Text-field></Input></Group><Section collapsed="true"><Title><Text-field layout="Heading 2" style="Heading 2">Deployment as a Maplet application</Text-field></Title><Group><Input><Text-field layout="Normal" style="Text">First, we deploy this solution as a Maplet application.  It provides a point-and-click interface in which users can experiment with how the system behaves in response to different parameter values.  Users don't need to know any Maple commands.or even the theory behind the physical process.

If you are viewing this as a live Maple worksheet, <Hyperlink bold="false" executable="false" italic="false" linktarget="Maplet:./OilStream.maplet" style="Hyperlink" subscript="false" superscript="false">click here to run this Maplet application</Hyperlink> .</Text-field></Input></Group><Group><Input><Text-field alignment="centred"><Image height="581" 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collapsed="true"><Title><Text-field layout="Heading 2" style="Heading 2">Deployment to Excel using Visual Basic code generation</Text-field></Title><Group><Input><Text-field layout="Normal" style="Text">Next, we will use <Font bold="true">Maple's automatic code generation</Font> to convert the formulas to Visual Basic code.  We can then copy and paste this code into an Excel macro, so that <Font bold="true">anyone with Excel on their desktop can make use of the solution we have derived</Font>.</Text-field><Text-field layout="Normal" style="Text"/></Input></Group><Section><Title><Text-field layout="Heading 3" style="Heading 3">Visual Basic code for T<Font style="Heading 2" subscript="true">1</Font><Font style="Heading 2">(t)</Font></Text-field></Title><Group><Input><Text-field layout="Normal" prompt="&gt; " style="Maple Input">VisualBasic(simplify(t1), resultname = temp_1, coercetypes= false, optimize);</Text-field></Input></Group></Section><Section><Title><Text-field layout="Heading 3" style="Heading 3"><Font executable="false">Visual Basic code for T<Font style="Heading 2" subscript="true">2</Font><Font style="Heading 2">(t)</Font></Font></Text-field></Title><Group><Input><Text-field layout="Normal" prompt="&gt; " style="Maple Input">VisualBasic(simplify(t2), resultname = temp_2, coercetypes= false, optimize);</Text-field></Input></Group></Section><Section><Title><Text-field layout="Heading 3" style="Heading 3"><Font executable="false">Visual Basic</Font> code for T<Font style="Heading 2" subscript="true">3</Font><Font style="Heading 2">(t)</Font></Text-field></Title><Group><Input><Text-field layout="Normal" prompt="&gt; " style="Maple Input">VisualBasic(simplify(t3), resultname = temp_3, coercetypes= false, optimize);</Text-field></Input></Group></Section></Section></Section><Text-field layout="Normal" style="Text"/><Group><Input><Text-field layout="Normal" style="Text"><Font italic="true">Legal Notice: The copyright for this application is owned by Maplesoft. The application is intended to demonstrate the use of Maplesoft products to solve a particular problem. It has been made available for product evaluation purposes only and may not be used in any other context without the express permission of Maplesoft.</Font>
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