Good one. I am a beginner. I understood and implemented your examples quite easily. Well, my purpose of learning these simulations is to finally simulate a system consisting of solar energy and Rankaine cycle. I am postdoc candidate. If you want to collaborate with me, you are welcome. Your expertise in Hysys will be asset for me.
Sir can you please guide me how to do simulation for middle vessel batch distillation column, I am getting tear stream issues and liquid head error in both radfrac... please help me
Hello kind Sir, thank you very much for your tutorials! I would like to ask you if the Aspen Process Economic Analyzer tends to trigger warnings when using a simple heater like in the example: I've tried to input all the information in a case I am working on, but no matter in what environment I use them the problem persists. The Main solver works and the streams and equipment are in the right color but I'm afraid I might be specifying the heater incorrectly/insufficiently
Probably, you are not specifying utility for the heater/cooler, or if specified, didn't link it with the block. Accordingly, economic evaluation is providing an error.
At the ending part, why did you place composition of ethane as 1 and methane as 0? Can you throw more light on degree of freedom because in the question, the degree of freedom is 2 for the first question and you used 4 degrees of freedom.
Nice video... very well explained I am also trying to model a heater, but in my case I know the heater Duty and need to calculate the outlet temperature. My trouble is Hysys is not automatically taking the flow from inlet stream to outlet (outlet is not getting auto updated with respect to inlet stream), can you suggest what could be the solution Thanks in advance
Sir, If you could probably provide the questions statements in description or as a link so we can also save them with our aspen files. That would be great
Sir I have a suggestion regarding the youtube lectures, you should use a software which displays the keys you press or mouse clicks It would be really helpful
Good one. I am a beginner. I understood and implemented your examples quite easily. Well, my purpose of learning these simulations is to finally simulate a system consisting of solar energy and Rankaine cycle. I am postdoc candidate. If you want to collaborate with me, you are welcome. Your expertise in Hysys will be asset for me.
This lecture is very informative and contains many things to learn.
Excellent lectures Dr. Haris. I am following you lectures to learn.
Thank you! I hope that you are enjoying the lectures. Please share your valuable feedback for the improvements.
@@aspenchemchannel Welcome... you are already doing a perfect job....
Very interesting, I like the way you explained everything, is easy to understand and I hope you to upload more videos with exercise as this one.
Thank you for the kind words ☺️
very nice initiative sir. enjoying and learning from your tutorials
Thanks Jyotimay. Please do watch other videos, and provide your kind feedback. 😄
Thank you Prof. Very clear explanations
You are welcome
Good work 👏
Complete series on both Aspen plus or hysys😊
Very useful tutorial ✌
Thanks Abdur Rehman. Please do share the feedback for improvement.
Sir can you please guide me how to do simulation for middle vessel batch distillation column, I am getting tear stream issues and liquid head error in both radfrac... please help me
Super explanation. thanks
Hello kind Sir, thank you very much for your tutorials! I would like to ask you if the Aspen Process Economic Analyzer tends to trigger warnings when using a simple heater like in the example: I've tried to input all the information in a case I am working on, but no matter in what environment I use them the problem persists. The Main solver works and the streams and equipment are in the right color but I'm afraid I might be specifying the heater incorrectly/insufficiently
Probably, you are not specifying utility for the heater/cooler, or if specified, didn't link it with the block. Accordingly, economic evaluation is providing an error.
HELLO?
I am looking for how to simulate the TVC (Thermal Vapor Compression Desalination).
BEST REGARDS.
Hello @Aspentech thank you for sharing.
I want to ask, why did you put 1 value in vapor in the mixer simulation worksheet??
Plz explain in comments
At the ending part, why did you place composition of ethane as 1 and methane as 0?
Can you throw more light on degree of freedom because in the question, the degree of freedom is 2 for the first question and you used 4 degrees of freedom.
Hello Sir thanks for the wonderful tutorials. Its very clear & precise. Please Sir can you do a video on multi-stage compressor sizing & selection.
Sure. But for this, you may need to wait a bit, as I am moving to distillation.
@@aspenchemchannel ok Will gladly wait
Hello sir Do you provide personal training ?
Thank you
Superbb!!
Thanks Fahad
Please do share feedback for improvement.
Pls sir share the word file which use this video so we can forther simulation. Question
Sure
Nice video... very well explained
I am also trying to model a heater, but in my case I know the heater Duty and need to calculate the outlet temperature.
My trouble is Hysys is not automatically taking the flow from inlet stream to outlet (outlet is not getting auto updated with respect to inlet stream), can you suggest what could be the solution
Thanks in advance
Please make sure that active button is pressed, and simulation not on hold.
@@aspenchemchannel Thanks a lot!! I am new to HYSYS, so missed it
thank you bro
Great 💯
Thanks Ahsan. Please do share the feedback for improvement
Sir, If you could probably provide the questions statements in description or as a link so we can also save them with our aspen files.
That would be great
@@ahsanwaqar9951 Sure.
Good
thankyou
Thank you Moiz for appreciation.
Sir I have a suggestion regarding the youtube lectures, you should use a software which displays the keys you press or mouse clicks
It would be really helpful
Ok dear. I will try.
May I know how to get the software?
It's given in the description of this video.
Hi sir, why did u put your flowrate as 100kg/s everytime?
Hi. This was just an example to demonstrate the use of different unit operations in Aspen.