• Re: Custom ASM2 fractionation model

    I have simulated my model and got DO and C(S_O) in last tank (anoxic tank) in the series is less than 0. The anoxic tank is preceded by aerobic tanks in the series. I didn't change any influent parameters defaults values. I'm wondering the Kla value for two aerobic tanks are 0 and the last tank is 0 as well. The assumed y_S values for PI controller in two consecutive aerobic tanks are 2 and 1 mg/l and I assumed: K_P =-1000, T_I=0.1d, u0=0, umin=0 and umax=1000. Am I right for my assumption or where should i dwell on to improve my simulation results?
    Thanks
    Regards
    Moses
  • Re: Custom ASM2 fractionation model

    Thanks for your help. Its now working better but a bit slow (1 day simulation takes 2 minutes). Whatever pop ups after simulation, i will come back to you.
    Regards
    Moses
  • Re: Custom ASM2 fractionation model

    I have encountered several problems in my simulation results. Please find the attached influent fractionation model and message log details. I tried to check the model if the anticipated sludge and oxygen concentration in the aeration tanks is correct  but I didn't succeed. Can you please advice me where I make a mistake.
    Please note that I didn't have TSS influent flow data and there is hanging outgoing variable (X_TSS), I didn't know what to do with it.
    Regards
    Moses
  • How to create a bypass control system

    Hello,

    I would like to facilitate my model with a bypass control system by which a certain amount of the inflow (above a given value) should bypass the WWTP directly to the recipient while the rest continues through the treatment process. I wonder what kind of controller I shall use in order to set up the system?  How I shall modify the parameters? In other words how can I bypass the excess flow?

    I am modelling an activated sludge WWTP with phosphorus removal (ASM2d).

    Regards,
    Moses
  • Re: How to copy a block from plant layout to microsoft word

    Dear Enrico
    Thanks.
    Regards
    Moses
  • How to copy a block from plant layout to microsoft word

    Hi
    I'm wondering on how to copy the a block from plant layout to the ms-word. I tried to copy the screen from the layout and paste it to ms-word but the quality is not good. Can you please show me the alternative way of copying it to get a better quality structure?
    Regards
    Moses
  • Re: Modelling WWTP to evaluate the influent of stormwater

    Thanks Enrico
    Much appreciated
    Moses
  • Re: Modelling WWTP to evaluate the influent of stormwater

    Dear Enrico and Youri

    I have connected timer and buffer tank (u1 to Q_pump) and then I connect buffer tank to sand filter (pumping Energy to backwash). Am I right for what I have done?
    There is parameters at the timer (T1, T2, u11 and u12). how can I set this parameters?. I'm also wondering on how to include variables in that flow scheme to get on/off backwashing?
    Regards
    Moses
  • Re: Modelling WWTP to evaluate the influent of stormwater

    Dear Enrico and Youri
    Thanks for your assistance. I have succeeded all except sand filter part.
    There is group operational parameter 'backwash' which is unit less. which value should I put there? my backwash pump capacity is 0.33 m3/s.

    I want to start operate backwash once the sand filter is clogged. what equation should I use based on sand filter parameters and how to incorporate it in the model?

    Thanks
    Moses
  • Modelling WWTP to evaluate the influence of stormwater

    Dear MikebyDHI

    I’m using ASM2d to model WWTP with the aim of evaluating the influence of stormwater contribution

    Primary Clarifier

    I dragged primary clarifier (PST_1) from separation block library, there is only Q_flow (m3/d) box to fill in the value. I was expecting to find boxes for area or volume to fill in values as well. Is there something wrong I have done in selecting primary clarifier?

    Aeration basins

    I want to control SRT with the aim of achieving sufficient nitrification. Oxygen level should be controlled by ammonium feedback and set point should vary between 1 to 2mg/l. I have read all your previous comment to Tanya but I have two aerated zones which I represented them in the model as two different tanks in series. How should I do it?

    Sand Filter

    The sand filter is aimed to remove P by using Fe compound. The sand filter has parameters such as area (A), height (m) and backwash. The backwash box has no unit while data I have for backwash flow rate has unit in m3/s. What should I do to make sure that the model recognize the backwash flow unit?

    Also, I want to manipulate filtered flow and unfiltered flow. The variable I have are Q_backwash, Q_In, Q_out_filtered, Q_out_unfiltered,  X_backwash, X_In,  X_out_Filtered, X_out_unfiltered and H.  I have read your comment to Hjrey but the equation does not include particulate (X). I want to include on/off function i.e. when Q_out_filtered flow is zero the Q_backwash pump should start and when it stop the flow should start passing through the sand filter. How can I do it by using my variable parameters?

    Thanks in Advance.
    Moses