Jump to content



Featured Articles

Check out the latest featured articles.

File Library

Check out the latest downloads available in the File Library.

New Article

Product Viscosity vs. Shear

Featured File

Vertical Tank Selection

New Blog Entry

Low Flow in Pipes- posted in Ankur's blog

2

Calculating Max Flow Through An Orifice

orifice

2 replies to this topic
Share this topic:
| More

#1 Process EngrPsh

Process EngrPsh

    Brand New Member

  • Members
  • 8 posts

Posted 19 June 2019 - 06:50 PM

hi guys,

 

Could you help me in solving the below:

 

Max Flow through the orifice = ?

Fluid = Gaseous Oxygen (Pure Oxy)

Upstream Pressure = 300 Bar

Downstream Pressure = 14.3 Bar

Required flow = 62.3 m3/hr

Orifice Diameter = 04 mm

Just curious to know if we could maintain the required flow without choking the orifice?

 

Thanks for your help



#2 breizh

breizh

    Gold Member

  • ChE Plus Subscriber
  • 4,233 posts

Posted 19 June 2019 - 07:51 PM

Hi,

Let you consider the search engine in this forum .

In addition I've attached  document to support your work .

 

Good luck

Breizh

Attached Files


Edited by breizh, 19 June 2019 - 08:03 PM.


#3 astro

astro

    Gold Member

  • Members
  • 76 posts

Posted 19 June 2019 - 11:30 PM

To quote Lt. Commander Montgomery Christopher Jorgensen Scott, "Ya canna change the laws of physics".
 
Based on the pressure differential you're quoting, I'd need some convincing that choked flow can be avoided across a single orifice. It would be doable using a multi-staged approach. This is one way of designing a silencer, to avoid critical flow and the noise that is generated. Is this the reason for your question? Or something else?
 
One of the references that breizh has pointed you to makes reference to this paper that, in my case, furthered my understanding on the subject significantly:
Ward-Smith, A.J., Critical Flowmetering: The Characteristics of Cylindrical Nozzles with Sharp Upstream Edges, Int. J. Heat & Fluid Flow, Vol 1, No. 3, pp.123-132, Sep 1979.
 
Abstract:
"A detailed study of the influence of axial length on the critical discharge coefficient of cylindrical orifices with sharp upstream edges is reported. Systematic consideration is given to the full range of geometries from the thin plate orifice up to the largest thickness/diameter (t/d) ratios of practical interest. A simple theoretical approach is used together with a more complete description of the physical nature of the flow. 
 
A range of orifice geometries is identified for which the critical discharge coefficient is independent of Reynolds number and t/d. Cylindrical nozzles in this range are particularly suited to critical flowmetering. They are simple to manufacture. Some new measurements are reported and these, together with existing experimental data, are shown to be consistent with the present analysis."
 
Ward-Smith performed a meta-study drawing on 6 other researchers results in the development of his findings. One of the takeaways from the paper that resonated with me can be captured by the following commentary:
"The theory ... therefore indicates that for choking to occur in knife-edged orifices the critical discharge coefficient must approach a value of unity."
"These results indicate that for practical purposes choking does not occur in nozzles with these small values of t/d."
So, while critical flow is theoretically possible with a thin plate (it appears to me that) there's currently no reliable way of mathematically characterising thin plate RO behaviour. This is borne out by the commentary in the AFT paper.
 
The flip-side to this commentary, is that if you know you're going to be dealing with critical flow through a restriction orifice, make sure that you're working with a "thick" plate so that you'll have confidence in the size that you calculate.





Similar Topics