Відео

Thank you for sharing :)

Thank you for sharing great information. Is there a similar application to reduce the number of probabilities in another situation (such as 4 or 5 when the conditions are more than 2) to reduce the number of probabilities?

Thank you for sharing this valuable lesson 👍

I have been looking for this peace of knowledge for quate sometime now, come across with it it has real served. Thank you.

Thanks!

This explanation was thorough and concise. Thank you sir.

Hello, Sir. Your video is really helpful, may I have the pdf document you're using on this video? Thanks.

was not it overall heat transfer cooefficient???

Simply Excellent ❣❣❣❣❣💖

How can i get calculation PDF and hysys fiel???

Thank you very much, sir for this helpful video. But is there a similar video that treats Economic analyzer for Aspen plus sir as I need it for my design project. Thank you sir

OK GOOD

Very helpful, thank you!!

Merci monsieur ❤❤❤❤

good presentation and explaination

I guess All lectures pertaining to course has not been uploaded. Sir Please if you can upload all remaining topics as outlined.

What is the difference between the Diesel product and the AGO product? as far as I understand they are interchangeable terms

Dr. Zaman you elaborated effectively. Great help Thankyou very Much

I've searched through a wide range of videos, by far this is the best and most straightforward video of the bunch. Thank you so much for posting it!

Круто

@drzamansajid Sir is this your email address that mentioned in video? I emailed you if that's your email address

What is the name of the source?

Hi, excelent video. I want to know where i can fin the paper that you use for the example?

Thank you. It is a nice explanation.

It's different. It's Excellent.

Dear Dr.Zaman, Thank you for the video, it's very helpful. What should we do if an equipment does not exist in the APEA library? In my case, I am simulating an electrolysis process and I don't know how to include the electrolyzer in the economic alnalysis.

Hi, thanks for your video. normally a stream contains multiple components (reactor effluent), how to define price of each component in that case as aspen offers to define stream price only!

Where is the heck "Bayesian Network"?!!

Great Work Dr Zaman, it helped alot. If possible please send me this Hsys file.

Can we get graphs of this optimization problem in Aspen?

Good I find it useful

Thank you very much for the video, your series of videos is truly excellent. Please note that when you added the additional trays to the column, you did not readjust their efficiency to 75%. Thus you have a top product benzene composition of 95%, not 97%. I had to go to 24 trays to get 97% benzene in the distillate.

are there chinese version?

Great video!!! Thanks for posting this! I have a question though: for the weather example, if we have "observations" for the probability of raining or not given today is a cloudy day, could we define P(Cloud) as the prior probability and P(Could|Rain) as the posterior probability? To ask it in a more general way, does the definition of prior/posterior probability depend on the nature of the problem or the information/observation we are given?

Thanks so much. It's so helpful

Hii sir. I had run the simulation almost 2 times, but while running it says diseal stream data is insufficient

Thank you Dr. Sajid for the lecture. If I want to edit the excell spreadsheet (in this case i want to add some project cost componen e.g. offsite facilities CAPEX or add VAT), will the result generate automatically ( in this case for NPV, IRR)? I assume that excell spreadsheets are linked function.

Thank you for explanation

Thank you dr Dr I am emailing you regarding the Aspen hysys file can you share me as soon as possible

Hello Sir, Your videos are really great; I have much appreciation and a lot of respect for you. I am learning GeNie by using your video. My data set contains both discrete and continuous variables at the same time. When I try to run my model using a PC algorithm, it says it does not support it. Can you please guide me here?

Thank you so much for this lecture. It was really helpful. Is there any lecture of you that analyzes more than one outcome with multiple input variables?

thank a lot

Thanks for the video ! when u add the add the water stream at the begining the composition is given in mole fraction ? shouldn't it be given in mass fraction as mass flow rate is given?

It's ok thx, but when the level reaches the SP value the level stabilizes because the LIC is manipulating the water outlet valve , it would have been nice that you showed also the water valve; And also, as you set the tank level at 0% at the start you should have set the outlet water valve at 0% at the start, should have been more realistic.

Hi, I would need a help. i have to simulate in Aspen Plus a thermal storage tank (it is a packed bed), would you have any idea of how to do that? Thank you

Hello Dr. Zaman, first of all thank you for your valuable video. I have a question that if I want to create a new simulation or rescale this simulation to a different crude oil flow rate, how do I decide the side draws flow rates and pump around rates?

Can you, please, explain if it is possible to change the plant location? Even if you choose different template (Chinese/EU metric), it gives Plant Location: North America.

"ERROR> 'HE - 6' THICKNESS CALCULATED EXCEEDS 25 PCT OF PORT DIAMETER Thickness CALC: 6.250 INCHES" , ERROR> 'GC - 2' INLET TEMPERATURE IS OUT OF RANGE , how can i fix this errors?

Hi, I want to ask If you want to compare the design results with actual data for the desalter tool, what do you need to pay attention to? and is it possible to find out the results of the reduced salt content in this hysys design?

Waiting palm oil simulation process with aspen plus