Difference between revisions of "Isothermal reactor design - 2013"

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| vimeoID3 = 59196489
| vimeoID3 = 59196489
| vimeoID4 = 59455740
| vimeoID4 = 59455740
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| vimeoID5 = 59734705
| course_notes_PDF =  
| course_notes_PDF =  
| course_notes_alt = Course notes
| course_notes_alt = Course notes

Revision as of 14:11, 15 February 2013

Class date(s): 04 February to 14 February
Download video: Link (plays in Google Chrome) [291 M]

Download video: Link (plays in Google Chrome) [304 M]

Download video: Link (plays in Google Chrome) [393 M]

Download video: Link (plays in Google Chrome) [M]

Download video: Link (plays in Google Chrome) [243 M]

  • F2011: Chapter 5 and 6
  • F2006: Chapter 4

04 February 2013 (05A)

06 February 2013 (05B)

07 February 2013 (05C)

to see the effect on pressure drop in the packed bed.

11 February 2013 (06A)

  • Audio and video recording of the class
  • Polymath code to solve the example in class
Example 5.6 |POLVER05_0 |1
# Differential equations

d(y) / d(W) = -alpha/(2*y) * (1+eps*X) 
y(0) = 1.0
d(X) / d(W) = -rAdash / FA0 
X(0) = 0


# Constants
FA0   = 0.1362  # [mol/s]
kdash = 0.0074  # [mol/(kg catalyst . s)]
alpha = 0.0367  # [1/kg]
eps   = -0.15   # [-]

# Algebraic equations
rAdash = -kdash * (1-X)/(1+eps*X) * y
flow_ratio = (1 + eps*X)/y

# Initial and final values for independent variable:
W(0) = 0
W(f) = 20

14 February 2013 (06C): midterm review