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hey thanks for sharing this simulation, i tried to run the exact same simulation nut I'm getting error that most of the structure has not been defined and the calculated Mw of TRIPA-01 is 807.3344 while the available one is 807.3200. I'm using aspen v11, kindly help me out regarding this matter. thanks in anticipation.

Thank you always!

Hi I sent you an email. I would be very grateful if you would share the files for that video - geometry, mesh, etc.

Could you share the reference for the SOE model equations?

how can I know how much the reboiler duty? I'm currently studying in aspen plus. Thank you for your VDO and your answer.

Could you tell me if it possible to estimated a fractional conversion of component CO? You writed on video that fractional conversion is later determined by Fortran subroutine. I did this simulation (from this video) and I don't know, where is fractional conversion of component CO individual reactions.I will be grateful for your answer.

Hello can you send me the link or info on where you find the stoichio and percent conversions? Thank you!

thank you for video!

Hello KG Engineering, I really appreciate your videos on youtube and Linkedin as well. Keep it up. I want study Amine Absorption in Hysys. Also, in rate based modeling, in Promax/Protreat we put actual tray nos...SO how this is done in hysys rate based modelsing?? plz help

THANK YOU !

Again thak you for share this content. One question, Do you think that it's possible to simulate the Bio-OIL as non-conventional component since there is no available data about composition and only there is available overall yields? I suppose that will be necessary more data about properties of bio-oil yo simulate the condensation phase, but I am not sure if it is possible. Do you have any content similar like that?

ASPEN V14 provides a local case of alkaline electrolyzed water. Could you explain it to us? Thank you very much

The generator does not produce any refrigerant (water vapour) at 100°C and 7.90 Kpa. How to overcome this problem please help sir

Hello sir i want to download the simulation how can i do payment

I have donated two times to get the files, but it was empty. Have you deleted it?

Have you considered carrying out a simulation of HTC in liquid phase?

Please, can You tell me how did you calculate the distillate to feed ratio?

hello , i am wondering why did you stopped the recording three times and start again ?

you dont support payments from india?

Hello sir, could you tell me how you determined the height of the tower? I calculated the diameter on my own but I'm confused about the height. If you could explain it to me I would be very grateful.

sir, why B4 is not in turbine model?

pq tanto anuncios sapo y la ctm

Great thank you for sharing. I have a questions, any reason for not consider BIO-OIL fir this simulation? or this is based on the source you use to model the process?

could you please specify the reference that you used?

Hey, nice video I will try to follow. Could you do one for chemical looping reforming for hydrogen production?

hello sir, while you are calculating Vcell ,why you used current density insted of current ? thank you

nice work🤩🤩. could you please do other simulations in this paper 🙏 or give some tips on those

Could you do the plastic pyrolysis process please?

Ladies and gentlemen, "COMPONENT 'BIOMASS' IN SUBSTREAM 'NC' HAS ZERO FLOWRATE IN THE OUTLET STREAM. FRACTIONAL CONVERSION HAS BEEN MODIFIED BY A FACTOR OF '1.000000'" is just a warning. You and Aspen can calculate the decimals with very little difference. Perhaps the decimal point is 1.0000002 rather than 1. Ignore this error if it is 1.0000. This is just a warning you need to be check, not error to run. If the value is less than 1.000, such as 0.98 or 0.99, proceed with your stoichiometric calculations. You can close the toggle of warning on the flow sheet on the menu if you want.

Are you able to provide the source material for this simulation? Thank you and have a nice day

After giving the combustion reactions and all the other inputs as stated by you in the video, still amount of carbon is left in outlet stream after 1st PFR where combustion reactions are given, but in your video no carbon is left? I tried doing it over but same problem occurs. Please help.

Thank you for the wonderful vedio! I have a confusion at 16:09, the calculation of the fractional conversion of H2O. [H2O conversion (about 0.09) X MW of H2O (18.015)]/[0.65*900] should be near 0.00275, but the result shows 2.75. Even if the value was expressed as percentage, it would be 0.275. I cannot understand what happend.

could you put the line of the ppt here in the description ?

Thanks for the tutorial. It will help a lot.

Hello, can you do aspen plus simulation on sorption enhance steam methane reforming ? 🥹

Buenas noches Estoy en un proyecto para la pirolisis de la biomasa de la yuca en aspen plus. Ya tengo la caracterizacion de la biomasa, pero necesito informacion cinetica y l estequimetria de las reacciones, si me suscribo al canal me podria ayudar a entender la estequiometria de la biomasa?

Hi, thanks for the video! What about longer hydrocarbon chains though? >C13. Aren‘t they also produced in the process and dont they also make up a significant amount? In your new video you are using distillation to separate Fischer tropsch products and you are also including long hydrocarbon chains like waxes. Why do this if you dont have any? Thank you very much in advance!

i still dont understand in the calculator part. can you give a definition or a brief explanation? and why not directly use PYRO (RGibs). and if a want to define the size of the particle, where can i input the value? (the size of the particles are same in the simulation)

Hello, it was great video. May i ask where to find this simulation in a reference? I went through the journal you mentioned to some who asked but the simulation there is different

I got two error when I tried doing the same: 1- M-BAL LOOP DID NOT CONVERGE IN 50 ITERATIONS. CHECK STOICHIOMETRY/MOLECULAR WEIGHTS. 2- ERROR OCCURRED DURING RFLASH ROUTINE CALCULATION. Do you know why did I got that? Thank you

Hello

Thanks for uploading it. I was in need of it, thank you

bad mesh

for reynolds number of 90000 is it better to model it as k-w?

The video was very helpful. What paper was the simulation based on? I would like to check the results against the paper.

This is so helpful.. Can you please provide some sources for literature review..

Nice one..should have shown some pfd or process description

its clear-cut explanation sir, thank you. but how do we connect this to CSTR using PID controller?

how can i contact u. i need ur suggestion ( pyrolysis of waste tire with aspen plus v11 ). email pls