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Process Simulations
เข้าร่วมเมื่อ 3 มิ.ย. 2021
Welcome to All. In this channel you will learn important process simulation software for free with interesting and effective way. The targeted software will be Aspen HYSYS, Aspen Plus, Aspen Adsorption, Aspen Energy Analyzer, Aspen EDR, Ansys FLUENT, COMSOL and many more.
Hope you will enjoy
Hope you will enjoy
How to Use EndNote
This is a basic video which describes the usage of EndNote at very basic level.
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Aspen Adsorption Intermediate Flowsheet
มุมมอง 3.3K3 ปีที่แล้ว
In this video, you will learn how to create the the intermediate flowsheet in Aspen Adsorption
Aspen Adsorption Full Flowsheet Part2
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This is the part 2 of understanding the full flowsheet in Aspen Adsorption
Aspen Adsorption_FullFlowsheet_Part1
มุมมอง 6K3 ปีที่แล้ว
This is the part 1 of understanding the full flowsheet in Aspen Adsorption
03_Plots and Running Simulations in Aspen Adsorption
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In this video, viewers will learn how to develop different plots and how to execute the simulations in Aspen Adsorption software
02_Creating Simple Flowsheet in Aspen Adsorption
มุมมอง 15K3 ปีที่แล้ว
In this video the viewers will learn how to create a simple flowsheet in Aspen Adsorption software.
01_Component List Creation in Aspen Adsorption
มุมมอง 10K3 ปีที่แล้ว
In this video the creation of component list in Aspen Adsorption software will be taught by Aspen Official Trainers.
Thankyou very much!
I'm sorry! Were did you found number of IP(1,"N2"), IP(1,"O2"), IP(2,"N2"), IP(2,"N2")? I tried to found this information in "HELP" but there were no numbers. Thant you for answer!
Using extended Langmuir 1 as assumed Isotherm while configuring the bed, you will see IP(1,x) to IP(2, x) value prompts in the specify table.
@@chineduakuma4484 don't think that's what he was asking for. he was wondering where you get those actual values
Hello. Thank u so much for this playlist! Tell me please why is "intra-particle voidage" parameter value 0?
Thank you so much for this playlist for Aspen Adsorption. Kindly could you provide your email ? I need to contact you to discuss in deep for Aspen program. I appreciate what you did in these videos.
Hi. If your simulation is below 1 Initial Variable, click on the "Specification Analysis" option. This option indicates: "Recommended changes to specifications" in Presets/Initials, Y_First_Node("N2") equals 1 change "Free" for "Initial". Regards,
hello ma'am, wanted to know what is the significance of the gas interacting bed in the simulation?
I followed same procedure. But I am not able to run the initialization. No prompt is coming on run command. From bottom if I click error its shown as "your simulation is underspecified by one variable. Inorder to make it green if I change the product variable of flow as "initial'' or pressure as '''initial', then initialization run command is prompted. But if I run then error showing as initialization failed at time zero. From bottom if I selected the error button then its shown as "your simulation is badly posed structurally because a subset of equations is not independent"'. Please help
I have similar issues here, using V12.
I have the same issue using V11. Please any solution to that?
If someone's getting errors, in the second 3:26, the feed pressure you have to set to make it work is 3.045 bar, also for the pressure in the TD2, this section seems to be cut from the published video in the second 5:22, the correct pressure you need to set is 3.0447 bar.
Thank You!
Do you have an email where I can contact you?
Please need help here
Hiii thanks a lot for your video its great and also I have a quick question I triedo to simulated with CH4, CO2;H2 with zeolitas , however in the system its appear error "A sub-group in the decomposition failed to solve" initialized time 0 :( I dont if its ok to put in the compositions of the product CH4-0 h2-0 and CO2-1 :( Any help would be great
Hii and thanks a lot for this video , I just have a question its about cyclic steady state I dont understand what its mean and Why its better to use de library Gas_dynamic, I really apreciated if you can help me or provide any information .
TD1.P is not appearing in the "Event driven" options?
hi, have u solve this issue? im facing the same
Hello! I have followed your simulation step by step but in the end (when I ''free'' the product pressure variable) my simulation is under by 1 Initial variable. Can you suggest what might be the problem? Thank you in advance!! (I am running the simulation in Aspen Adsorption V11)
Hi! I don't know if you have figured out your problem yet, however, I was having the same problem and I was able to solve this by going to the bed configuration and then the presets/initials and set the Y_First_Node('N2") to initial rather than free
@@CarlosHernandez-pk3gd , Hi! Thanks for your advice. I've changed Y_First_Node('N2") to initial rather than free and the square at the bottom turned green. But when i try to run initialization, an "Initialization failed at time 0" error appears. May be you know what the problem is? Thanks in advance!
Hi guys I am using aspen adsorption for wastewater treatment. Can you share your knowledge with me regarding to operation of aspen adsorption. Thanks.
did you figure out the solution?
@@АнастасияЖигалова-й2ы Did you figure out the solution to this problem?
Ms. Can you send me the file u created please?
I need also
Hey there, Thanks for these tutorials. Can you please do some about using the ion exchange model in Aspen Adsorption.