CHE555 Assignment 1 Mac 2015

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CHE555 2015 1 FACULTY OF CHEMICAL ENGINEERING CHE 555 NUMERICAL METHODS & OPTIMIZATION ASSIGNMENT 1 ANSWER ALL QUESTIONS This is a group assignment (3 members) which has to be submitted within 1 week after receiving the assignment. Standardize all the calculation up to 4 decimal points. QUESTION 1 PO1, CO1, C3 An isothermic reaction is carried out adiabatically and the CSTR reactor design algorithm is shown as below: The reaction is second order in A. The feed which is equimolar in a solvent and A, and its enters the reactor at a total volumetric flow rate, v 0 of 10 dm 3 /min with the initial concentration of A being 4 M. The rate constant, k given as 0.1 dm 3 /mol.min at 380 K. Determine the conversion can be achieved in 600 dm 3 CSTR by using the following methods: a) Graphically b) False position method with initial guesses of X l =0.6 and X u =0.9 c) Secant method with initial estimates of X -1 = 0.6 and X 0 , =0.9 Iterate until the approximate error falls below 1 %. Find the absolute relative approximate error at the end of each iteration. (20 marks) QUESTION 2 PO1, CO2, C4 A liquid-liquid extraction is used to extract nickel from the aqueous solution into an organic solution. Table 1 shows the experimental data from the extraction process. Table 1 Extraction of Nickel Ni in aqueous phase, a (g/l) 4 8 12 16 20 Ni in organic phase, g (g/l) 6.3 12 15.5 18.3 21.5 Where g is the amount of nickel in the organic solution and a is the amounts of nickel in the aqueous solution. Identify the best type of polynomial that fit to these data and determine its polynomial

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Transcript of CHE555 Assignment 1 Mac 2015

  • CHE555 2015

    1 FACULTY OF CHEMICAL ENGINEERING

    CHE 555 NUMERICAL METHODS & OPTIMIZATION

    ASSIGNMENT 1

    ANSWER ALL QUESTIONS

    This is a group assignment (3 members) which has to be submitted within 1 week after receiving the

    assignment. Standardize all the calculation up to 4 decimal points.

    QUESTION 1

    PO1, CO1, C3

    An isothermic reaction is carried out adiabatically and the CSTR reactor design algorithm is shown as

    below:

    The reaction is second order in A. The feed which is equimolar in a solvent and A, and its enters the

    reactor at a total volumetric flow rate, v0 of 10 dm3/min with the initial concentration of A being 4 M.

    The rate constant, k given as 0.1 dm3/mol.min at 380 K. Determine the conversion can be achieved in

    600 dm3 CSTR by using the following methods:

    a) Graphically

    b) False position method with initial guesses of Xl =0.6 and Xu =0.9

    c) Secant method with initial estimates of X-1 = 0.6 and X0, =0.9

    Iterate until the approximate error falls below 1 %. Find the absolute relative approximate error at the

    end of each iteration.

    (20 marks)

    QUESTION 2

    PO1, CO2, C4

    A liquid-liquid extraction is used to extract nickel from the aqueous solution into an organic solution.

    Table 1 shows the experimental data from the extraction process.

    Table 1 Extraction of Nickel

    Ni in aqueous phase, a (g/l) 4 8 12 16 20

    Ni in organic phase, g (g/l) 6.3 12 15.5 18.3 21.5

    Where g is the amount of nickel in the organic solution and a is the amounts of nickel in the aqueous

    solution. Identify the best type of polynomial that fit to these data and determine its polynomial

  • CHE555 2015

    2 FACULTY OF CHEMICAL ENGINEERING

    equation. Then estimate the amount of nickel in the organic solution when 25 g/l of nickel is in the

    aqueous solution.

    (20 marks)

    QUESTION 3

    PO4, C03, C4

    Compare answer from Question 2 with the answer from Excel and Matlab. Write the details command

    (Excel and Matlab) and result of this problem.