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Join Date: Jan 2010
Posts: 1

Interface Float Weight

01/04/2010 5:23 AM

I am facing interface magnetic float level indicator problem. I want to know how the required weight of interface float is determined with calculation methods by using the data below:

Magnetic Interface Float Details:

Equipment: Desalter

Service : Oil/Water

Vessel Operating Pressure : 66 psig

Vessel Operating tempt : 115 DegF

Designed for sp.gr : 0.89 ~ 1.12

Float Material : SS

Empty weight of float : 655.7 gms

Length : 15" (381mm)

Float Diameter: 1 7/8" (47.625 mm)

Pipe Inside Diameter : 2.067" ( 52.5 mm)

Volume of float: 1051.5 in2 (678367 mm2) { Calculated}

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I only know that some formulae using buoyancy is used. Appreciate if someone can help me and also respond to vikkuvikku77@gmail.com

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Guru
United Kingdom - Member - Indeterminate Engineering Fields - Control Engineering - New Member

Join Date: Jan 2007
Location: In the bothy, 7 chains down the line from Dodman's Lane level crossing, in the nation formerly known as Great Britain. Kettle's on.
Posts: 32175
Good Answers: 839
#1

Re: Interface Float weight

01/04/2010 5:47 AM
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Power-User
South Africa - Member -

Join Date: Nov 2008
Location: Johannesburg
Posts: 295
Good Answers: 12
#2

Re: Interface Float Weight

01/05/2010 12:40 AM

Hi there,

Archimedes' principle states that a body wholly or partially immersed in a fluid is buoyed up by a force equal to the weight of the fluid displaced.

A level or density instrument is sensitive to the apparent weight of an immersed displacer.

If the cross-sectional area of the displacer and the density of the liquid are constant, then a unit change in level will result in a reproducible unit change in the apparent weight of the displacer.

The important thing to note is that the displacer must be heavier than the process liquid.

So first of all, you need to work out the total volume of the displacer chamber when filled with the process liquid. If it is a cylinder - Volume = Height x pi x Radius^2

You can then convert that to mass with the SG of the process liquid. (Mass = Volume x Density)

You would then speak to your supplier to select a displacer that is heavier than the process liquid mass that you calculated.

Regards,

Craig

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