Can i use pressure swing to separate ethanol & ethyl acetate? The desired product is at least 99.7% purity of ethyl acetate.
@prateekshamishra654521 күн бұрын
is this software free??
@MohamadReziAbdulHamid19 күн бұрын
yes, the software is free to download
@websterbwalyatechnology9789Ай бұрын
awesome
@websterbwalyatechnology9789Ай бұрын
wow thanks ...it has helped me alot
@Kandozoo-bn1rg2 ай бұрын
Can you do a wet fgd process, showing how to remove the gypsum by product.
@GJagadeesh-nu5bj3 ай бұрын
NYC video some drawings are very hard can u tell me how to start that drawing and end easily
@user-sm9bn4bc9k3 ай бұрын
my thanks
@user-pc4xh8ed4p3 ай бұрын
thank you✧*。٩(ˊωˋ*)و✧*。 you're just the savior (´இωஇ`)
@AGnanaprakasam3 ай бұрын
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."
@chem11jaffeerashrafa154 ай бұрын
Hi i need a big help regarding aspen hysys pls distillation column not converging 🥲
@Zarnish-fatima4854 ай бұрын
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 KZbinrs 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.
@mc73534 ай бұрын
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
@Bhavesh-id4fo4 ай бұрын
14:34
@Bhavesh-id4fo4 ай бұрын
15:48
@muhammadnurulhakim93285 ай бұрын
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 !!
@VaibhavSawant-sc1lq5 ай бұрын
Configuration B Reboiler has also reboiler duty = 42 MW
@Bhavesh-id4fo5 ай бұрын
To simulate decomposition
@Bhavesh-id4fo5 ай бұрын
29:30
@waiphyopaing67436 ай бұрын
thank you so much ]
@harisenafebriadi7 ай бұрын
mantap.....
@DaivyDjimbi7 ай бұрын
can you make all table calculation table in exel
@DaivyDjimbi8 ай бұрын
nice video, excuse me where can we get This book in PDF learn asp en plus in24 hours
@DaivyDjimbi8 ай бұрын
Waouuuu Nice video
@user-fe4tw4cm3s8 ай бұрын
thank you for sharing. could you tell me how to show or check the enthalpy of each stream above/below pinch point
@user-fe4tw4cm3s8 ай бұрын
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?
@MohamadReziAbdulHamid8 ай бұрын
I don't think can show the enthalpy value above and below stream. Can check under view perhaps. If you move ur cursor it only show enthalpy of stream Tinitial - Tfinal. Not exactly what you want. If u solve the heat X the program can tell u enthalpy of the stream. Cost parameter can refer to design book - it depend on many things. For heat-X often it is a, b, c parameter and the equation usually like this: $ = A + B*Area^C. Hope this helps
@user-fe4tw4cm3s8 ай бұрын
@@MohamadReziAbdulHamid thank you for replying! I'm looking forward to your next video. maybe you can make a video about heat network modification in a retrofit project
@sitikhadijah97508 ай бұрын
Can we just assume the delta Tmin? Or there is calculation for the 25 celcius heat load placement before obtain delta Tmin
@MohamadReziAbdulHamid8 ай бұрын
You can use any delta Tmin as long as it is greater than zero..in fact, different processing will have different recommended delta Tmin. For example, low temperature/cryogenics will use small deltaT min. In my case i just simply use 10oC
@sitikhadijah97508 ай бұрын
@@MohamadReziAbdulHamid Alright thanks for the informative content and the clarification 🙏🏻🙏🏻
@MohamadReziAbdulHamid8 ай бұрын
@@sitikhadijah9750 Just want to add...if u decide to choose different deltaTmin..for example 5oC. You just need to shift your hot composite curve such that the 'neck/pinch' is 5oC. Changing delta Tmin will change heat recovery n utility usage...of course if go detail - heat-x area, no of unit etc.
@ammadjamil17494 ай бұрын
My POV, the recommended value for delta t min is shown in graphs (Cost or Area vs Delta T min) in textbook (PINCH ANALYSIS FOR ENERGY AND CARBON FOOTPRINT REDUCTION) is around 10 to 20. This typically will give maximum efficiency with little to no drawbacks. Hope that helps.
@levymukopeka53828 ай бұрын
Hey,Sir. How can you help me, I want to model a coal dryer simple plant ?
@zulkhahlib3258 ай бұрын
Can i know what is the pressure at absorber?
@faridlarkem82258 ай бұрын
Thanks for sharing, as for the first part, can't wait for the third part.
@levymukopeka53828 ай бұрын
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?
@MohamadReziAbdulHamid9 ай бұрын
@17:51 = 4*(150 - 135) = 60 kW (not 20 kW)
@niravrohit34559 ай бұрын
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
@xiujames6369 ай бұрын
Great Video. Thank you so much. Do you happen to have an unblocked version of the table that I can access please
@elfin5839 ай бұрын
@10:00 because the stoichiometric coefficients must be in molar basis.
@faridlarkem82259 ай бұрын
Thank you so much, waiting for the second part.
@MohamadReziAbdulHamid8 ай бұрын
Here is the 2nd part of the video kzbin.info/www/bejne/n6q3aKuor9Z9atk
@brendabaena933910 ай бұрын
thanks :)
@prashantsingh201611 ай бұрын
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.
@adeyeyeisaac711311 ай бұрын
Please link to the textbook
@javadjeddizahed196711 ай бұрын
Could you please explain how to determine the pressure of HP column?
@farhadeidi891611 ай бұрын
very useful conceptual tutorial
@skimkid72711 ай бұрын
You just saved my life lol great intro
@MohamadReziAbdulHamid Жыл бұрын
2011, 2035, 2012 are line numbers btw. DESIGN: 11,032 kPag/FV@343C/-29C probably design pressure under full vacuum at temperature
@ehsansharif3677 Жыл бұрын
GREAT EXPLANATION BY YOU MAN
@monakhamisi3555 Жыл бұрын
hi i have nonconventional solid how to define the Stoichiometric coefficients for drying
@moaaz2928 Жыл бұрын
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.
@kries6928 Жыл бұрын
poggers video
@usamasaeed5842 Жыл бұрын
Hi kindly elaborate why solids temperature is decreasing wrt length of dryer?