Modelling and scientific computing

From Process Model Formulation and Solution: 3E4
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Course slides

<pdfreflow> class_date = 13 September 2010 (slides 1 to 8) button_label = Create my course notes! show_page_layout = 1 show_frame_option = 1 pdf_file = A-Modelling-12-Sept-2010.pdf </pdfreflow>


<pdfreflow> class_date = 15 September 2010 (slides 9 to 15) button_label = Create my course notes! show_page_layout = 1 show_frame_option = 1 pdf_file = A-Modelling-15-Sept-2010.pdf </pdfreflow>


<pdfreflow> class_date = 16 September 2010 (slides 16 to 19)
20 September 2010 (slides 20 to the end) button_label = Create my course notes! show_page_layout = 1 show_frame_option = 1 pdf_file = A-Modelling-20-Sept-2010.pdf </pdfreflow>


Practice questions

  1. From the Hangos and Cameron reference, (available here] - accessible from McMaster computers only)
    • Work through example 2.4.1 on page 33
    • Exercise A 2.1 and A 2.2 on page 37
    • Exercise A 2.4: which controlling mechanisms would you consider?
  2. Homework problem, similar to the case presented on slide 18, except
    • Use two inlet streams F1 and F2, and assume they are volumetric flow rates
    • An irreversible reaction occurs, A+3Br2C
    • The reaction rate for A = rA=kCACB3
    1. Derive the time-varying component mass balance for species B.
      • VdCBdt=F1inCB,1in+F2inCB,2inFoutCB+03kCACB3
    2. What is the steady state value of CB? Can it be calculated without knowing the steady state value of CA?
      • F1inCB,1in+F2inCB,2inFoutCB3kCACB3 - we require the steady state value of CA, denoted as CA, to calculate CB.

More exercises to come