Ideality of a CSTR - PowerPoint PPT Presentation

About This Presentation
Title:

Ideality of a CSTR

Description:

Property of Beehive Engineering. Ideality of a CSTR. Jordan H. Nelson ... Introduction General CSTR Information. Three Questions. Experimental Conclusions ... – PowerPoint PPT presentation

Number of Views:752
Avg rating:3.0/5.0
Slides: 33
Provided by: cheU4
Learn more at: https://my.che.utah.edu
Category:

less

Transcript and Presenter's Notes

Title: Ideality of a CSTR


1
Ideality of a CSTR
Jordan H. Nelson
2
Brief Overview
Introduction General CSTR Information
Three Questions
Experimental Conclusions
3
Schematic of the CSTR
Item Description
1 Mixing Point
2 Mixing Point
3 Mixing Point
4 Mixing Points
5 Water Bath Inlet and Outlet
6 Four Wall Mounted Baffles
7 Mixer Drive
8 Marine Type Impeller
9 CSTR Vessel
10 Water Bath Vessel
4
3 Questions ?
  • Where is the best mixing in the CSTR?
  • What is tmean and how does it compare to tideal?
  • What configuration of PFR-CSTR will produce the
    greatest conversion?

5
Where is the Best Mixing?
  • Impeller selection
  • Food Dye Test
  • Dead Zones
  • Impeller Speed

6
Flow Patterns of different impellers
Rushton Impeller
Marine Impeller
7
tMean vs tIdeal ?
  • tMean Measured mean residence time
  • The amount of time a molecule spends in the
    reactor
  • tIdeal Ideal residence time is calculated from
    the following equation

8
Experiment
  • Fill reactor with low concentration salt
    (baseline)
  • Spike reactor at most ideal mixing
  • Create spike concentration at least one order of
    magnitude larger than baseline
  • Measure change in conductivity over time
  • Run experiment at different impeller speeds

9
Yikes!
Plot of Concentration vs Time with Error
10
Measured Concentration over time in the CSTR.
11
RTD Function E(t)
  • Measured concentrations are used to create the
    residence time distribution function

12
Plot of an ideal residence time distribution
function
13
Residence time distributions
14
Mean Residence Time
  • Using E(t) the following equations produce the
    mean residence time

15
Comparison of Residence Times
RPM Mean Residence Time Standard Deviation Sigma Sigma/Tau
15 357.57 11.58 206.87 0.58
30 358.14 11.58 206.35 0.58
Ideal CSTR 466.97 5.90    
16
Loss of Data
  • Over an hour of data was lost from Opto 22
  • Calculation of Reynolds number over 4000
    (Turbulent)
  • Equation applies to a baffled CSTR
  • RPM speed of 300 obtained full turbulence

17
CSTR-PFR Configurations ?
  • Schematic of arrangements
  • Levenspiel Plot
  • Conduct saponification reaction in the reactor at
    different RPMs
  • Use Equimolar flow rates and concentrations of
    reactants
  • Quench reaction with a HCl and titrate with NaOH

18
Series Reactor with CSTR Before PFR.
19
Series Reactor with PFR Before CSTR.
20
(No Transcript)
21
CSTR-PFR Configurations ?
  • Schematic of arrangements
  • Levenspiel Plot
  • Conduct saponification reaction in the reactor at
    different RPMs
  • Use Equimolar flow rates and concentrations of
    reactants
  • Quench reaction with a HCl and titrate with NaOH

22
Measured Conversion for PFR-CSTR Configuration
Speed (RPM) Conversion () Conversion Error ()
30 19.7 /- 4.30
60 21.7 /- 3.91
200 21.2 /- 4.00
400 24.3 /- 3.48
875 24.7 /- 3.41
23
Measured Conversion for CSTR-PFR Configuration
Speed (RPM) Conversion ()   Conversion Error ()
30 21.5 /- 3.94
60 21.2 /- 4.00
200 21.4 /- 3.97
400 20.9 /- 4.06
875 21.5 /- 3.94
24
3 Questions ?
  • Where is the best mixing in the CSTR?
  • What is tmean and how does it compare to tideal?
  • What configuration of PFR-CSTR will produce the
    greatest conversion?

25
Conclusions
  • Better mixing for a Rushton impeller is below the
    impeller
  • The reactor is far from ideal at low impeller
    speeds
  • The PFR-CSTR arrangement provided better
    conversions
  • Run the PFR-CSTR reactor at RPMs of higher than
    300

26
Opportunities
  • Run the experiment again to obtain the lost
    residence time values
  • Run the saponification reaction at higher
    temperatures
  • Exit sampling stream should be at the bottom of
    the reactor

27
Acknowledgements
  • Taryn Herrera
  • Robert Bohman
  • Michael Vanderhooft
  • Dr. Francis V. Hanson
  • Dr. Misha Skliar

28
  • REFERENCES
  • De Nevers, Noel, Fluid Mechanics, McGraw Hill,
    New York N.Y. (2005)
  • Fogler, H. Scott, Elements of Chemical Reaction
    Engineering, Prentice Hall, Upper Saddle River,
    N.J. (1999)
  • Havorka, R.B., and Kendall H.B. Tubular Reactor
    at Low Flow Rates. Chemical Engineering
    Progress, Vol. 56. No. 8 (1960).
  • Ring, Terry A, Choi, Byung S., Wan, Bin., Phyliw,
    Susan., and Dhanasekharan, Kumar. Residence Time
    Distributions in a Stirred Tank-Comparison of CFD
    Predictions with Experiments. Industrial and
    Engineering Chemistry. (2003).
  • Ring, Terry A, Choi, Byung S., Wan, Bin., Phyliw,
    Susan., and Dhanasekharan, Kumar. Predicting
    Residence Time Distribution using Fluent Fluent
    Magazine. (2003).

29
What to expect from your CSTR.
30
Question?
31
Design Equations
32
Design Equations
Write a Comment
User Comments (0)
About PowerShow.com