Tracer Experiment-Physics-Case Tutorial, Study Guides, Projects, Research of Physics

This is tutorial for case given in it. This was provided by Prof. Karishma Sanyal at Alagappa University. Its main points are: Tracer, Experiment, Fluid, Gamma, Emitting, Detectors, Software, Graphical, Parameter, User, Dispersion, Interface

Typology: Study Guides, Projects, Research

2011/2012

Uploaded on 08/26/2012

lalitkumar
lalitkumar 🇮🇳

4.3

(19)

79 documents

1 / 2

Toggle sidebar

This page cannot be seen from the preview

Don't miss anything!

bg1
Tutorial to CASE 1
1. Problem description
A tracer experiment was made in a straight pipe, more than 30
metres in length and 6 cm in diameter. The fluid was air at ambient
temperature and approximately atmospheric pressure. The tracer,
gamma-emitting 133Xe, was injected by a syringe at the inlet of the
pipe and monitored by two detectors separated by 18.15 metres:
18.15 m
6 cm
Injection 18.15 m
6 cm
Injection
Our objectives are to evaluate the flow rate and the dispersion
coefficient.
2. Running the software
First, click the “Run RTD” item. The graphical user interface
appears.
The data from detectors 1 and 2 are in the case1_1.txt and
case1_2.txt files in the code2 folder; time is in seconds and the
signals have been area-normalised. Select them as the inlet and
outlet signals in the Setup menu. It is a good idea to see what they
look like using Draw/Preview draw/Inlet and outlet. The strange
shape of the inlet signal is due to uneven movement of the syringe
piston during injection. The same shape is visible (though
attenuated) on the signal from detector 2.
Flow in a long pipe can be expected to be one-dimensional
convection plus some amount of dispersion. Axial dispersed plug
flow can therefore be selected in the Setup/Setup parameter menu.
An initial value for tau can be guessed from the pre-visualisation of
the tracer curves. The signals from detectors 1 and 2 are very
similar in height, width and shape, which indicate that the flow
should have little dispersion. Some not too small value for the
Péclet number Pe, say a few tens, should be adequate as an initial
guess. Click on the Yes box to ask for optimisation of these
parameters.
docsity.com
pf2

Partial preview of the text

Download Tracer Experiment-Physics-Case Tutorial and more Study Guides, Projects, Research Physics in PDF only on Docsity!

Tutorial to CASE 1

1. Problem description metres in length and 6 cm in diameter. The fluid was air at ambient^ A tracer experiment was made in a straight pipe, more than 30 temperature and approximately atmospheric pressure. The tracer, gamma-emitting 133 Xe, was injected by a syringe at the inlet of the pipe and monitored by two detectors separated by 18.15 metres:

18.15 m

6 cm Injection (^) 18.15 m

6 cm Injection

coefficient.^ Our objectives are to evaluate the flow rate and the dispersion

2. Running the software appears.^ First, click the “Run RTD” item. The graphical user interface

case1_2.txt^ The data from detectors 1 and 2 are in the files in the code2 folder; time is in seconds and the^ case1_1.txt^ and signals have been area outlet signals in the Setup - normalised. Select them as the inlet and menu. It is a good idea to see what they look like using shape of the inlet signal is due to uneven movement of the syringe Draw/Preview draw/Inlet and outlet. The strange piston attenuated) on the signal from detect during injection. The sameor 2. shape is visible (though

convection plus some amount of dispersion.^ Flow in a long pipe can be expected to be one Axial dispersed plug - dimensional flow An initial value for tau can be guessed from the pre can therefore be selected in the Setup/Setup parameter - visualisation of menu. the tracer curves. The signals from detectors 1 and 2 are very similar in height, width and shape, which indicate that the flow should have little dispersion. Some not too small value for the Péclet number Pe, say a few tens, should be adequate as an initial guess. parameters. Click on the Yes box to ask for optimisation of these

docsity.com

the results using theIt is now possible to launch the Draw menu.^ Solve/Run^ item and visualise

3. Analysis of results and At this stage you should have a set of optimised valuePe as well as an optimised model response curve.s for tau It is possible to answer a few extra questions: o o Is the model adequate?What is the average velocity of air? o What is the flow rate? (The nominal value indicated by a flowmeter was 239 m (^3) /h). o Wh is turbulent.at is the value of the Reynolds number? Check that flow o What literature is thegives value a correlationof the dispersion by G.I. coefficient?Taylor, reading The radius of the pipe andD^ ^10.^1 rv^ ,^ where^ D is^ vthe^ the friction velocity. The latterdispersion^ coefficient,^ r the can be estimated as velocity and f the friction v * factor, one expression of which 0. 5 fU, where U is the average is Is that correlation verified here? f  0. 079 Re^0.^25 , Re being the Reynolds number. o You can also try the perfect mixers in series model. Instead of tau and Pe you will get tau and J. Check whether tau changes close to J/2. according to the model. Check whether Pe is 4. Reference Proc. R. Soc. A223 (1954) 446^ Taylor, G.I., “The dispersion of matter in turbulent pipe flow”-468.

docsity.com