4 ай бұрын
Жыл бұрын
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@lucataylor5450 10 күн бұрын
clutch
@willynbintiyanam4942 15 күн бұрын
Can i use pressure swing to separate ethanol & ethyl acetate? The desired product is at least 99.7% purity of ethyl acetate.
@prateekshamishra6545 21 күн бұрын
is this software free??
@MohamadReziAbdulHamid 19 күн бұрын
yes, the software is free to download
@websterbwalyatechnology9789 Ай бұрын
awesome
@websterbwalyatechnology9789 Ай бұрын
wow thanks ...it has helped me alot
@Kandozoo-bn1rg 2 ай бұрын
Can you do a wet fgd process, showing how to remove the gypsum by product.
@GJagadeesh-nu5bj 3 ай бұрын
NYC video some drawings are very hard can u tell me how to start that drawing and end easily
@user-sm9bn4bc9k 3 ай бұрын
my thanks
@user-pc4xh8ed4p 3 ай бұрын
thank you✧*。٩(ˊωˋ*)و✧*。 you're just the savior (´இωஇ`)
@AGnanaprakasam 3 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."
@chem11jaffeerashrafa15 4 ай бұрын
Hi i need a big help regarding aspen hysys pls distillation column not converging 🥲
@Zarnish-fatima485 4 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.
@mc7353 4 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-id4fo 4 ай бұрын
14:34
@Bhavesh-id4fo 4 ай бұрын
15:48
@muhammadnurulhakim9328 5 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-sc1lq 5 ай бұрын
Configuration B Reboiler has also reboiler duty = 42 MW
@Bhavesh-id4fo 5 ай бұрын
To simulate decomposition
@Bhavesh-id4fo 5 ай бұрын
29:30
@waiphyopaing6743 6 ай бұрын
thank you so much ]
@harisenafebriadi 7 ай бұрын
mantap.....
@DaivyDjimbi 7 ай бұрын
can you make all table calculation table in exel
@DaivyDjimbi 8 ай бұрын
nice video, excuse me where can we get This book in PDF learn asp en plus in24 hours
@DaivyDjimbi 8 ай бұрын
Waouuuu Nice video
@user-fe4tw4cm3s 8 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-fe4tw4cm3s 8 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?
@MohamadReziAbdulHamid 8 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-fe4tw4cm3s 8 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
@sitikhadijah9750 8 ай бұрын
Can we just assume the delta Tmin? Or there is calculation for the 25 celcius heat load placement before obtain delta Tmin
@MohamadReziAbdulHamid 8 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
@sitikhadijah9750 8 ай бұрын
@@MohamadReziAbdulHamid Alright thanks for the informative content and the clarification 🙏🏻🙏🏻
@MohamadReziAbdulHamid 8 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.
@ammadjamil1749 4 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.
@levymukopeka5382 8 ай бұрын
Hey,Sir. How can you help me, I want to model a coal dryer simple plant ?
@zulkhahlib325 8 ай бұрын
Can i know what is the pressure at absorber?
@faridlarkem8225 8 ай бұрын
Thanks for sharing, as for the first part, can't wait for the third part.
@levymukopeka5382 8 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?
@MohamadReziAbdulHamid 9 ай бұрын
@17:51 = 4*(150 - 135) = 60 kW (not 20 kW)
@niravrohit3455 9 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
@xiujames636 9 ай бұрын
Great Video. Thank you so much. Do you happen to have an unblocked version of the table that I can access please
@elfin583 9 ай бұрын
@10:00 because the stoichiometric coefficients must be in molar basis.
@faridlarkem8225 9 ай бұрын
Thank you so much, waiting for the second part.
@MohamadReziAbdulHamid 8 ай бұрын
Here is the 2nd part of the video kzbin.info/www/bejne/n6q3aKuor9Z9atk
@brendabaena9339 10 ай бұрын
thanks :)
@prashantsingh2016 11 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.
@adeyeyeisaac7113 11 ай бұрын
Please link to the textbook
@javadjeddizahed1967 11 ай бұрын
Could you please explain how to determine the pressure of HP column?
@farhadeidi8916 11 ай бұрын
very useful conceptual tutorial
@skimkid727 11 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?