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Max Dp In Vane Pack.
Started by Isoceles, Feb 19 2016 07:35 AM
diameter vane pack demister separator particule
4 replies to this topic
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#1
Posted 19 February 2016 - 07:35 AM
What is the maximum particle diameter of the gas at the entrance of a vane pack without blockage occurs?
I read that is about 150 microns in GPSA, I'm not sure.
thanks a lot
Isoceles
#2
Posted 19 February 2016 - 09:52 AM
#3
Posted 22 February 2016 - 12:00 PM
Thanks for your answer. I understand that the value of K determines the area I need in vane pack. The deputy does not speak the maximum diameter of the particles that can be in the gas stream.
Quote of the GPSA where recommend a diameter of less than 150 micron particle.
"• Select a separable droplet size and size for the vessel
diameter using Eq 7-1. A droplet size of 150 microns has-been
Typically specified. This May be overly conservative for
vane pack and cyclonic mist extractors, Which Generally
Have gas and liquid Capacities higher than mesh pads. "
Also attached to a guide for the design of separators which recommends trabjar with no particles larger than 150 microns.
"For horizontal separators mist extractor, it is considered that
section secondary gravitational separation or settlement
particles equal to and greater than 150 microns in diameter are removed from
so that the exhaust function optimally without excessive burdens
liquid. Therefore, the terminal velocity is calculated as for
separators without extractor; but it is considered a particle diameter
150 microns for sizing. "
I hope you have understood my question
Thanks ! 

#4
Posted 23 February 2016 - 07:13 AM
Thanks for your answer. I understand that the value of K determines the area I need in vane pack. The deputy does not speak the maximum diameter of the particles that can be in the gas stream.
Quote of the GPSA where recommend a diameter of less than 150 micron particle.
"• Select a separable droplet size and size for the vessel
diameter using Eq 7-1. A droplet size of 150 microns has-been
Typically specified. This May be overly conservative for
vane pack and cyclonic mist extractors, Which Generally
Have gas and liquid Capacities higher than mesh pads. "
Also attached to a guide for the design of separators which recommends trabjar with no particles larger than 150 microns.
"For horizontal separators mist extractor, it is considered that
section secondary gravitational separation or settlement
particles equal to and greater than 150 microns in diameter are removed from
so that the exhaust function optimally without excessive burdens
liquid. Therefore, the terminal velocity is calculated as for
separators without extractor; but it is considered a particle diameter
150 microns for sizing. "
I hope you have understood my question
Thanks ! 

#5
Posted 19 April 2016 - 03:30 AM
Hello, I am Ritixa. Studying Process Engineering and Design...
Recently i am searching for Mist eliminator design and i came across about pressure drop calculation.
Please help me out for better understanding..How to do vane pack design & how to calculate pressure drop across vane pack??????
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