Separation of CO2 from Flue Gases using Absorber in Aspen HYSYS - Lecture # 22

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  • Опубліковано 17 лис 2024

КОМЕНТАРІ • 68

  • @dibakarsarkar5530
    @dibakarsarkar5530 4 роки тому +2

    Awsm video sir...I clearly understand your simulation sir.... thanks

  • @alicegoncalves867
    @alicegoncalves867 3 роки тому +1

    thank you for saving my life...

  • @usmanismail4130
    @usmanismail4130 Рік тому

    Very detailed.
    Thanks for this

  • @husseinalaamery4960
    @husseinalaamery4960 4 роки тому +4

    Please, Is it possible to define the properties of flue gas directly in aspen plus?

  • @abdullahnasir46
    @abdullahnasir46 8 місяців тому

    wow sir great this is in my FYDP

  • @nadukontnt2583
    @nadukontnt2583 Рік тому +2

    How can u recover the Co2 to recycle it for a syngas production plant
    (For a lower H2/Co ratio)

  • @muhammadhabib5170
    @muhammadhabib5170 3 роки тому +3

    Sir! can you make a tutorial on the pyrolysis of biomass.

  • @hammadshoaib7700
    @hammadshoaib7700 2 роки тому +2

    Can you please share the name of any reference material or book where I can find more detailed explanations of hysys features?

  • @harishr3343
    @harishr3343 Рік тому

    Successfully completed lec 22

  • @shreyaskv4009
    @shreyaskv4009 3 роки тому +2

    can you share the aspen hysis set up link here

  • @muhammadalifridha580
    @muhammadalifridha580 Рік тому +2

    Is this model simulation applicable for cement industry ?

    • @aspenchemchannel
      @aspenchemchannel  Рік тому

      Aspen Plus can be used to model the processes in the cement industry

  • @donchackochan8934
    @donchackochan8934 2 роки тому +1

    Can we make a hybrid model with absorber and membrane??

  • @mohammadsalman5297
    @mohammadsalman5297 6 місяців тому

    very nice, thanks

  • @jaimegutierrezmartinez935
    @jaimegutierrezmartinez935 Рік тому +1

    Hi, how can you know the percentage of flooding of the column?

    • @aspenchemchannel
      @aspenchemchannel  Рік тому

      For this, hydraulic design is required for the system, which is presented in Lecture # 21 on Aspen HYSYS, and Lecture # 55 on Aspen Plus.

  • @namratapawar6761
    @namratapawar6761 6 днів тому

    How to calculate solvent rate??

  • @theophilip3520
    @theophilip3520 3 роки тому

    I have a flue gas of Nitrogen, CO2, water vapor and sulphur dioxide.. how do I absorb only CO2 into water.

  • @nasirkhan3711
    @nasirkhan3711 2 роки тому +2

    I didn't understand why you added H2S and H2O2?

  • @tanajikadam2455
    @tanajikadam2455 2 роки тому

    Is Vaccum pump design in Aspen hysys?

  • @Rivoj_
    @Rivoj_ 2 роки тому

    Thank you bro very clear

  • @usmanismail4130
    @usmanismail4130 Рік тому +2

    Please Sir, the 81% separation achieved is based on what precisely?
    Is it dependent on the input parameter or is there a way we can upscale the % to let's say 92%?

    • @muhammadyasir9056
      @muhammadyasir9056 Рік тому

      Good question, same is my question.
      I'll appreciate your kind response

    • @aspenchemchannel
      @aspenchemchannel  Рік тому +1

      Yes, it can be upscaled, because it's a shortcut design. The separation is achieved because of input in the shortcut column. I hope that addresses your query.

    • @aspenchemchannel
      @aspenchemchannel  Рік тому +1

      Yes, it can be upscaled, because it's a shortcut design. The separation is achieved because of input in the shortcut column. I hope that addresses your query.

    • @muhammadyasir9056
      @muhammadyasir9056 Рік тому

      @@aspenchemchannel that means we can upscale in rigorous design of absorber?

    • @aspenchemchannel
      @aspenchemchannel  Рік тому

      Yes.

  • @moontahafarin9305
    @moontahafarin9305 4 роки тому +1

    Can you please show operation of Flue gas desulpharizer using limestone slurry?

  • @msirdisamia7695
    @msirdisamia7695 4 роки тому +2

    how we can replace package property of acid gas to another property because in my hysys software there is no this property

    • @aspenchemchannel
      @aspenchemchannel  4 роки тому

      You can use Acid gas, in case of older version, and in latest version, can use the package described in the video.

    • @msirdisamia7695
      @msirdisamia7695 4 роки тому

      @@aspenchemchannel Sorry, but you used the acid gas property packag how I can replace this property with another property

    • @aspenchemchannel
      @aspenchemchannel  4 роки тому

      Just click on other property package, and it will be selected.

    • @msirdisamia7695
      @msirdisamia7695 4 роки тому

      @@aspenchemchannel I did not understand please help me

    • @aspenchemchannel
      @aspenchemchannel  4 роки тому

      When you click on e.g., Peng-Robinson, then it gets selected. Right? Similarly, if you want to change to SRK, then click on SRK property package, and it will be selected.

  • @oghoghosamwajuihian5643
    @oghoghosamwajuihian5643 3 роки тому

    What can I do if majority of the N2 and O2 are exiting at the bottom ?

  • @hannahmichaelareyes6172
    @hannahmichaelareyes6172 2 роки тому

    Hi! Is it possible for the flue gas to contain water at 65 C? Won’t it be in liquid form? Thanks

  • @dithinmathew4386
    @dithinmathew4386 Рік тому

    Hi Dr. Muhammad Haris, Is it possible to design a membrane using ASPEN HYSYS to separate CO2 from a gaseous mixture.

  • @rahultangade2721
    @rahultangade2721 3 роки тому +1

    I have gas flow in nm3/hr how to feed it in material stream?

    • @aspenchemchannel
      @aspenchemchannel  3 роки тому +1

      Its a volumetric flowrate. Instead of specifying molar flow, specify volumetric flow

    • @rahultangade2721
      @rahultangade2721 3 роки тому

      @@aspenchemchannel thanks for replying

  • @mnssefnubi4913
    @mnssefnubi4913 2 роки тому

    This methode can separate CO2 from H2

  • @quangmiketran1562
    @quangmiketran1562 3 роки тому

    Excuse me sir, can we do this in Aspen Plus, or do you have a video for it? Also, what is the preferred method for it please? like SRK or Peng-Robinson? Thank you very much

    • @aspenchemchannel
      @aspenchemchannel  3 роки тому

      Yes. We can do this in Aspen Plus. I haven't made video on it yet. The property package selected in the video will remain the same.

    • @quangmiketran1562
      @quangmiketran1562 3 роки тому

      @@aspenchemchannel sir I did one and it worked. So I used the Elec Wizard and method ENRTL-RK to design the CO2 desorption system. The reboiler duty is around 6.13-13 kW and I set my reflux ratio to somewhere 0.5-0.8. Then to reverse the reaction and recover MEA, I had a flask to act as a condenser and reduce the temp at the vapor outlet of the desorber (rad frac, 2 stages). The recycle has a purge like 0.02 and then add a makeup for MEA solution. Also to mention I have a 0.3wt% solution of MEA. Thanks for the video again sir, it gave me an idea where to start!

  • @Rania-rn7ov
    @Rania-rn7ov 4 роки тому

    What can i use instead "acid gas"?? I have the old hysys
    Is it ok if i do it with peng robinson ?

    • @aspenchemchannel
      @aspenchemchannel  4 роки тому

      Yes. Acid gas in previous versions. No, peng robinson cannot be used, as it's an amine process.

    • @Rania-rn7ov
      @Rania-rn7ov 4 роки тому

      I don't have this property package in my hysys, what should i use ?

  • @Rania-rn7ov
    @Rania-rn7ov 4 роки тому

    Plzz tell me just with which another property package i can do this simulation ? I DON'T HAVE "acid gaz" nor "other property"
    Plz answer me i really need it

  • @sreenathvishnu
    @sreenathvishnu 3 роки тому

    is it possible to model a membrane seperation in aspen

    • @aspenchemchannel
      @aspenchemchannel  3 роки тому

      Yes. However, first the model should be prepared in the Aspen Custom Modeler, and then imported to Aspen Plus.

  • @Fatima-bx9zq
    @Fatima-bx9zq 3 роки тому

    hi, can you make a video for ethylene/ethane separation by Ba-ETS-4 by adsorption Aspen HYSYS

    • @aspenchemchannel
      @aspenchemchannel  3 роки тому

      Adsorption is not possible in Aspen Hysys. The phenomena of adsorption can only be depicted by using component splitter, a short cut method.

  • @tariqs.111
    @tariqs.111 3 роки тому

    Are there any alternatives to AspenHYSYS or any free trial for this software?

    • @aspenchemchannel
      @aspenchemchannel  3 роки тому

      This software is available free of cost.

    • @tariqs.111
      @tariqs.111 3 роки тому

      @@aspenchemchannel Where can I get this software? I didn't see any download link from the website.

    • @aspenchemchannel
      @aspenchemchannel  3 роки тому

      getintopc.com

    • @sachinpanwar8086
      @sachinpanwar8086 3 роки тому

      @@aspenchemchannel ohh. this is really bad for Aspen tech since this tool is available free of cost.

  • @ML_VLOG_official
    @ML_VLOG_official 2 роки тому

    Can i get its model file so i run it directly

  • @Rania-rn7ov
    @Rania-rn7ov 4 роки тому

    Is it possible with NRTL ??

    • @aspenchemchannel
      @aspenchemchannel  4 роки тому

      NRTL means non-random two liquids. So, as per definition, and obviously looking at the model, this property package cannot be used.

    • @Rania-rn7ov
      @Rania-rn7ov 4 роки тому

      @@aspenchemchannel in my hysys there's no "acid gas" not even "other property" so i can't do this simulation ??

  • @fatmayamani5658
    @fatmayamani5658 2 роки тому

    ممكن باقي الحلقة