Task 2 Trk-1a p7-23a Imananda Fajar Widanto Alvin Rachmanto

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  • 7/26/2019 Task 2 Trk-1a p7-23a Imananda Fajar Widanto Alvin Rachmanto

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    TASK 2

    Alvin Rachmanto (11/312956/TK/37727)

    Imananda Fajar Widanto (11/313655/TK/37986)

    Problem 7-23AA CSTR is being operated at steady state. The cell growth follows the Monod

    growth law without inhibition. The exiting substrate and cell concentrations are measured as afunction of the volumetric flow rate (represented as the dilution rate), and the results are shownbelow. Of course, measurements are not taken until steady state is achieved after each change in

    the flow rate. Neglect substrate consumption for maintenance and the death rate, and assume that

    Yp/c is zero. For run 4, the entering substrate concentration was 50 g/dm3and the volumetric flow

    rate of the substrate was 2 dm3/s.

    Run Cs (g/dm ) D (day-

    ) Cc (g/dm )

    1 1 1 0.9

    2 3 1.5 0.7

    3 4 1.6 0.64 10 1.8 4

    (a) Determine the Monod growth parameters max andKs.

    (b) Estimate the stoichiometric coeficients, Yc/sand Ys/c.

    (c) List ways you can work this problem incorrectly.(d) How could you make this problem more difficult?

    %TUGAS TRK%Alvin Rachmanto /11/312956/TK/37727%Imananda Fajar W /11/313655/TK/37986clcclear

    x = [1/1 1;1/3 1;1/4 1;1/10 1];

    y = [1/1; 1/1.5; 1/1.6; 1/1.8];

    constant = x\y;u = 1/constant(2)Ks = constant(1)*uCsu = linspace(1,10,50);Ds = Csu*u./(Ks + Csu);plot(Csu, Ds)title('Grafik Hubungan Antara Cs vs D')

    xlabel('Cs')ylabel('D')

    Cs0=50;

    Cc=4;D4=1.8;Ycs=Cc/(Cs0-D4*Ks/(u-D4))Ysc=1/Ycs

  • 7/26/2019 Task 2 Trk-1a p7-23a Imananda Fajar Widanto Alvin Rachmanto

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    Hasil RUN

    u = 1.9882

    Ks = 0.9866

    Ycs = 0.0986

    Ysc = 10.1409