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How can i do this to ionic liquid !

Thank you

I followed the same steps for ionic liquids but I couldn't get the required properties like MULAND-1

Thank you! Great explanation!

Thank you very much for great Aspen Plus lectures!

hi, thanks for the video, can you please recommend how to simulate a system containing reversible and irreversible parallel and series reactions (decomposition)?

"promosm"

Please sir, how can I contact you?

why the value of condenser duty is negative?

W video

thank you :)

Hi, I have created a new model and I got red triangle. Do you know how can I solve it please?

This is a great lecture. Thank you. Please how can I estimate the property of a sample (Cowpea) which may have carbohydrates, protein , fat etc

excellent sir

Wonderful lecture. I learned a lot. Thank you very much Sir.

The dude phase shifted into our reality just to help me with my engineering hw.

I think you should put the duty as zero to get the right combustion temperature. But there will be no more liquid water to separate 🙂

Why the combustion temperture is 50 degree only ?! It is combustion, it should be >1000 degree..

Can you always share the pdf doc, please?

Sir, Plzz share me ur Email Adress Or contact number. I want to learn aspen software from u.

What if we are flashing a stream and we don't know the temperature . Only flash pressure is known..

Hello sir. Would it be possible for you to clarify some of my doubts I'm working on a design project trying to design an FTR unit using rstoic . I have like 48 components and reactions. I can find the selectivity of those components . But how will I put them in aspen? My reaction is co+h2 giving bigger chains alkanes and co2 happening inside the reactor. I know molar flow rates of co and h2 coming inside the reactor. My question is based of selectivity of all components , how do I use this data in aspen plus ? Any help will be appreciated

Sir Can you pls upload that word document?

Isnt it the frequency factor that Aspen Plus is asking for? You entered the reaction rate constant.

hello please i need help , Explain how to fix the following error in ASPEN plus. * WARNING IN THE "STREAM" PARAGRAPH WHICH BEGINSON LINE 66 STREAM NAME: GLUC COMPONENT MOLE FLOWS OF SUBSTREAM: "MIXED" ARE NORMALIZED TO THE TOTAL MOLE FLOW VALUE *WARNING IN THE "STREAM" PARAGRAPH WHICH BEGINSON LINE 70 STREAMNAME SURFA COMPONENT MOLE FLOWS OF SUBSTREAM: "MIXED" ARE NORMALIZED TO THE TOTAL MOLE FLOW VALUE.

Prof. the audio is terrible

Echo :(

Hello. Is there any video in your channel about how to do data regression with the aid of aspen plus?

Wrongly done wanted my 2 hr

Sir , can you please demonstrate a tutorial on vacuum pump and standard pumps in the Aspen plus .

Sir please provide steps for the process 🤜🤛

Teacher, Do you know Aspen Hysys Petroleum Refining modules? Could you do examples about it? Thanks

thank you. you helped me very much

!! what happened at the end ? Wasnt the goal to determine the optimizad values for the volume of each reactor ???! what did you acquied finally ? never showed any change in the reactor volumes !!

Thank you sir !!!

Sir, how can we choose multiple exchangers & compare with single exchanger in the same design.

How to reduce the amount of vapor at the top of the rectification column? The type of trays, their efficiency? I have a lot of top reflux in model the unisim program. I am asking for an answer and best regards.

thank you teacher, I solved my problem thank you so much

Thanks sir. It was really useful.

Thank you Uncle!

Hellow, Thank you for informative video. But I have a question. If absorber is used to remove SOx, How can I calculate the number of stages for radfrac?

Echo is happening. Please look into it if possible.

It was really amazing respected sir! Bundle of thanks sir.

What method (molecular structure or conectivity) do you recommend when we have an anion combined with a cation structure? Thank you

My humble obeissance to The Best Teacher in my life!! :) It is through your blessings that I am what I am today. To have done this class physically in 2008-12 B.Tech. batch is an honour, Sir.

thanks for preparing. it's really helping to me.

Very well explained sir,Thank you.

Sir, How can i estimate zymo(CH1.8O0.5N0.2) ?

Very comprehensive demonstration. Thank you very much!

Very well demonstrated. Thank you sir..