Raai2015
Chemical
- Jun 21, 2008
- 61
Hi all , We have the boiler desuperheater control by Multiple nozzle desuperheater valve. I got a offer from two reupted supplier. Below are some details on design case.
Spray flow : 3,11tph
Spec density : 0,95
Cv @ 80% opening : 6,78
Dp offered : 0,3 bar
On the above i calcualted the DP , it was around 0.2 bar. Below are some opinions needed.
1, Both the suppliers give DP across the load same 0,3bar but with different CV --> My view is Different Cv (different opening) results in different DP in principle. May be they specify the max 0.3 bar in all load cases.
2, Interesting for me : this kind of valve (multiple nozzle) suppliers requires atleast 5 bar above the steam line. I was under impression 5 bar will the DP across the multiple nozzle valve. When they have 0,3bar DP across then why do they every time require 5 bar DP atleast?
3, I read somewhere , weber number is the indication of atomization and it needs to be above 12. Does anybody have calcualtion (Dr google is not much helpfull this time) of weber number?
Spray flow : 3,11tph
Spec density : 0,95
Cv @ 80% opening : 6,78
Dp offered : 0,3 bar
On the above i calcualted the DP , it was around 0.2 bar. Below are some opinions needed.
1, Both the suppliers give DP across the load same 0,3bar but with different CV --> My view is Different Cv (different opening) results in different DP in principle. May be they specify the max 0.3 bar in all load cases.
2, Interesting for me : this kind of valve (multiple nozzle) suppliers requires atleast 5 bar above the steam line. I was under impression 5 bar will the DP across the multiple nozzle valve. When they have 0,3bar DP across then why do they every time require 5 bar DP atleast?
3, I read somewhere , weber number is the indication of atomization and it needs to be above 12. Does anybody have calcualtion (Dr google is not much helpfull this time) of weber number?