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Topic: Cyclone for Solid-Gas separation  (Read 5458 times)

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Offline ahmed_saleh

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Cyclone for Solid-Gas separation
« on: June 10, 2008, 01:55:52 AM »
Can anyone advise regarding the following questions about the operating of Cyclones used for Solid-Gas separation:
 
1 - Has the vent stream of the cyclone to be with a downward slope towards the vessel-receiver?  What is the common practice?
 
2 - How sensitive is the separation to the changes in the particle size of the powder?  Any co-relations for that?
 
Thanks for assistance...

Offline technologist

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Re: Cyclone for Solid-Gas separation
« Reply #1 on: June 11, 2008, 02:08:36 AM »
For me it should be backward to facilitate particles drop back to cyclone.

Efficiency varies linearly with the Log(Dp) from 1 to 10 micron size & it is much flatter outside this range. So if particle size increases, the efficiency increases by a factor of log(Dp2/Dp1)...Simple.

For more details consult perry or McCabe Smith.

Offline C6H8O7

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Re: Cyclone for Solid-Gas separation
« Reply #2 on: June 24, 2008, 03:49:47 AM »
That sounds like a fun project.

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