วีดีโอ

clutch

Can i use pressure swing to separate ethanol & ethyl acetate? The desired product is at least 99.7% purity of ethyl acetate.

is this software free??

awesome

wow thanks ...it has helped me alot

Can you do a wet fgd process, showing how to remove the gypsum by product.

NYC video some drawings are very hard can u tell me how to start that drawing and end easily

my thanks

thank you✧*。٩(ˊωˋ*)و✧*。 you're just the savior (´இωஇ`)

When feeding kinetic data, it requires concentration exponents. The following error is popping up: "REAC-DATA not complete: REACNO = 1. At least one exponent for the reactant must be specified."

Hi i need a big help regarding aspen hysys pls distillation column not converging 🥲

Your videos are more informative iI am really thankful to you, I was really so worried about Aspen plus and there is no proper guidance it took 2 months to find your video and channel, this kind of informative and true TH-camrs should be promoted and suggested at the top or searching bar, I am really very thankful to you my you more success in your career and you life and split more easiness for other beginners like your this work.

thank you for this video its really helpful i was struggling to find anything on the internet about this and explaining in detail like u did so thank you very much

14:34

15:48

Thank you so much. Just a little suggestion, Sir. As I know the magnitude of DT Min is not so arbitrary, to decide whether it shall be 5 degC or 10 deg C. There is a minimum value of it. If you set the DT min too low, you will end up with having only cold end network as your video (network that only require cold utilities, it is undesirable in design point of view). Anyway, I am also new in this field. Your video help me a lot to understand about aspen energy analyzer interface. Thank you !!

Configuration B Reboiler has also reboiler duty = 42 MW

To simulate decomposition

29:30

thank you so much ]

mantap.....

can you make all table calculation table in exel

nice video, excuse me where can we get This book in PDF learn asp en plus in24 hours

Waouuuu Nice video

thank you for sharing. could you tell me how to show or check the enthalpy of each stream above/below pinch point

Hi thank you for your sharing, I have some questions,1/ how to make aspen energy analyzer show the enthalpy value of each stream above/below the pinch?2/ how to identify the cost parameter?

Can we just assume the delta Tmin? Or there is calculation for the 25 celcius heat load placement before obtain delta Tmin

Hey,Sir. How can you help me, I want to model a coal dryer simple plant ?

Can i know what is the pressure at absorber?

Thanks for sharing, as for the first part, can't wait for the third part.

hey, can you help me out. i want to design a coal dryer , our coal contains a lot of moisture , how can you help me?

@17:51 = 4*(150 - 135) = 60 kW (not 20 kW)

Awesome...thank you very much I trying this simulation from 2 month.....again thanks ...keep it ...can you start series for petroleum refining all process on Aspen plus....cdu,fccu, hydrogen manufacturing,hydrotreater....can you recommend any course that help me for this simulation

Great Video. Thank you so much. Do you happen to have an unblocked version of the table that I can access please

@10:00 because the stoichiometric coefficients must be in molar basis.

Thank you so much, waiting for the second part.

thanks :)

Very nice explanation. In addition I like to request to manage subtitles in such way that it can be stopped. Many times it becomes impossible to read original text in back ground specially equations.

Please link to the textbook

Could you please explain how to determine the pressure of HP column?

very useful conceptual tutorial

You just saved my life lol great intro

2011, 2035, 2012 are line numbers btw. DESIGN: 11,032 kPag/FV@343C/-29C probably design pressure under full vacuum at temperature

GREAT EXPLANATION BY YOU MAN

hi i have nonconventional solid how to define the Stoichiometric coefficients for drying

I am using HCOALGEN and DCHARTIGT to define my biomass. I added the HCOMB coming from calorimeter experiment (19 MJ/KG). However, the value I got in ASPEN is (-3.5). I wanted to study the effect of energy content change on the process... However, whatever number I write, it does not affect on the process yield or Syngas in gasification. Is that logical? I will truly appreciate your help.

poggers video