Modelling and scientific computing

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 18)
20 September 2010 (slides 19 to the end) button_label = Create my course notes! show_page_layout = 1 show_frame_option = 1 pdf_file = A-Modelling-15-Sept-2010.pdf </pdfreflow>

Practice questions

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?
• Homework problem, similar to the case presented on slide 18, except
  • Use two inlet streams \(F_1\) and \(F_1\), and assume they are volumetric flow rates
  • An irreversible reaction occurs, \(\sf A + 3B \stackrel{r}{\rightarrow} 2C\)
  • The reaction rate for A = \(\sf -r_A = -kC_\text{A} C_\text{B}^3\)
  1. Derive the time-varying component mass balance for species B.
  2. What is the steady state value of \(\sf C_B\)? Can it be calculated without knowing the steady state value of \(C_A\)?

More exercises to come