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Mathematical model of continuous and batch (discrete) system combined |
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| Dec11-12, 08:09 AM | #1 |
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Mathematical model of continuous and batch (discrete) system combined
I'm having difficulties trying to establish the best approach to create a mathematical model of a process that has a combined continuous and discrete (batch) element to it. I explain as follows:
The system is a hopper (vessel), open to atmosphere, with dry granular material being fed in by conveyor (i.e. continous), the outlet at bottom of hopper has a valve that opens to discharge granular material initially discharging a lot of material quickly into a container below then a more slow gradual but constant outlet flow as the container is moved forward and filled. The hopper discharge valve then closes and waits a delay time until the next empty container is ready below (meanwhile the hopper is being filled), and the process repeats again. I have tried Integral Mass Balance approach but I don't think this is right. Ideally I need a Laplace transform expression for the system. I know the time values for the valve open discharge and rates of mass flow as well as material in-flow to hopper and hopper volume. If anyone has any ideas on the best way to approach this problem it would be gratefully received. |
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| Dec28-12, 06:40 PM | #2 |
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| Dec31-12, 12:57 AM | #3 |
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Hi Haruspex,
I thought that I'd explained the problem previously? Anyway I'll explain again....I have a container (hopper) with a material infeed that I know (i.e. kg/s). The output from the hopper is controlled by a slide valve opening & closing. The discharge from the hopper goes into a moving container below that travels forwards slowly thus filling the container. Initially, when the slide valve opens there will be a large volume of material discharged from the hopper, then as the container below the hopper moves forwards there will be a constant out flow from the hopper (much less than the initial discharge). I am working on the values of the discharge mass flow flow rates from the hopper. My question is...if I know the hopper in-feed and discharge mass flow rates over time can I construct a Laplace transform to describe the system? and how do I go about this? |
| Dec31-12, 05:25 PM | #4 |
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Mathematical model of continuous and batch (discrete) system combined
I think the simplest model one could reasonably look at is this: Let [itex]V(t)[/itex] be the amount of material in the hopper at time [itex]t[/itex]. Suppose that material falls in to the hopper at a constant rate [itex]k_0 > 0[/itex]. Suppose that the rate at which material is discharged is, when the exit valve is open, [itex]k_0 + k_1V[/itex] with [itex]k_1 > 0[/itex] (chosen on the assumption that, if the hopper is empty when the valve is open, material falls straight through from the conveyor).
Suppose that the valve is closed for [itex]0 < t < T_1[/itex] and open for [itex]T_1 < t < T_2[/itex]. Then the amount of material in the hopper over a single cycle can be modelled by the ordinary differential equation [tex] \frac{\mathrm{d}V}{\mathrm{d}t} = \left\{\begin{array}{r@{\quad}l} k_0 & 0 < t < T_1 \\ -k_1V & T_1 < t < T_2\end{array}\right. [/tex] subject to [itex]V(0) = V_0[/itex]. This equation can be solved analytically to give [tex] V(t) = \left\{\begin{array}{r@{\quad}l} V_0 + k_0t & 0 \leq t \leq T_1 \\ (V_0 + k_0T_1)\exp(-k_1(t - T_1)) & T_1 < t \leq T_2\end{array}\right. [/tex] A drawback of the linear model is that the hopper never completely empties: [itex](V_0 + k_0T_1)\exp(-k_1(t - T_1)) > 0[/itex] for all [itex]T_1 < t \leq T_2[/itex] and all choices of the parameters. However, it is possible to show that the amount of material in the hopper at the end of a cycle tends to a finite limit: Let [itex]V_n = V(nT_2)[/itex] for positive integer [itex]n[/itex]. Then [tex] V_{n+1} = (V_n + k_0T_1)\exp(-k_1(T_2 - T_1)) [/tex] This is a linear recurrence relation, which can be solved to give [tex] V_n = (V_0 - B)a^n + B [/tex] where [tex]a = \exp(-k_1(T_2 - T_1)) \\ B = \frac{k_0T_1\exp(-k_1(T_2 - T_1))}{1 - \exp(-k_1(T_2 - T_1))}[/tex] Since [itex]0 < a < 1[/itex], [itex]V_n \to B[/itex] as [itex]n \to \infty[/itex]. EDIT: one can tune the parameters so that [itex]V(0) = V(T_2) = V_0 \neq 0[/itex]: one must have [tex] k_1(T_2 - T_1) = \ln \left(1 + \frac{k_0T_1}{V_0}\right). [/tex] |
| Dec31-12, 09:43 PM | #5 |
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Hi pasmith,
Many thanks for your explanation. I can't say that I fully understand it, particularly the solving of the 'linear recurrence relation', and I cannot see a way that I can use this information in practice. Looking at the problem from another perspective, if I know the rate of material entering the hopper and also if I know the rate of material discharging from the hopper (initially when the slide valve opens there will be a sudden large discharge rate, then a steady discharge rate which is much less than the initial surge). This information will provide three (3) cases. If I have this data in the form of a graph of hopper material balance (i.e. hopper material vs time) over a cycle of these three cases, can I produce a mathematical model from this data? |
| Jan4-13, 12:15 AM | #6 |
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| Jan4-13, 12:22 AM | #7 |
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