@@muhammadakbarray4001 i will try , it. If you know the velocity and area of piping you could find the volumetric/ mass flow rate. It might be possible.
@@muhammadakbarray4001 Sorry for a delayed reply. Velocity is depends on the piping size. I believe, if you know the piping size and mass flow, velocity is just apparent.
Whats up, e-Time. it's fairly vivid video. thanks. :)
Went technical... 😂
👌👌
Great job
how about spray dryer & cyclone & scrubber in hysys plus ?
please ,can you help me
How can I enter ejector in aspen hysys
It is necessary
thank you
When i clicked to calculate PSD, the software says "Failed to create PSD from SPS engine". Do you know how to fix it? Thank you
did you define the mesh size properly
@@alimchem8565 there is option for user defined sizes too. I use mean ans standard deviation for calculation.
@@alimchem8565 Add available PSD in the user defined descrete area. OR use mean diameter and standard deviation with log method. Please give a try.
How to simulate spin flash dryer? because air inlet pressure value is -ve draft. But aspen not taking air -ve value.
Let me try, will update you..
thanks sir, this video very supporting me
I struggled to learn Solid handling first that why i made a video to be useful to others, thanks,
@@chrash786 permission to ask sir, whether it can enter the feed inlet velocity on the stream? thanks before sir
@@muhammadakbarray4001 i will try , it. If you know the velocity and area of piping you could find the volumetric/ mass flow rate. It might be possible.
Can variation for velocity inlet sir?
@@muhammadakbarray4001 Sorry for a delayed reply. Velocity is depends on the piping size. I believe, if you know the piping size and mass flow, velocity is just apparent.