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Philippines - Member - New Member Engineering Fields - Control Engineering - New Member Engineering Fields - Instrumentation Engineering - New Member

Join Date: Jun 2007
Location: Philippines
Posts: 85

Flushing Ring

09/15/2008 11:24 PM

Hi guys,

Im doing a data sheet of a Pressure Transmitter with a diaphragm seal, and now Im in the process of choosing the correct type of flushing ring.

What are the factors that I should consider to select the correct flushing ring?

I also have an issue about my options, we are to select from two flushing rings provided by the client, sizes 2" 300/600# and 1.5"" 300/600# flushing rings.

The pressure transmitter Im dealing with now have an isolation valve size 3/4"(I requested to change it to 1", but no approval yet!)

Am I correct if I say that, the flushing ring and the Isolation valve should have the same size, not considering its rating? or should I consider also the rating?

Thanks.

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Active Contributor

Join Date: Jun 2008
Posts: 16
#1

Re: Flushing Ring

09/17/2008 9:32 AM

select the size of the flushing ring to match the process fluids properties.

if it is clean, like steam or sour water or solvents, then yes, you are correct, a 3/4" NPT flushing ring, swaged down to 1/2", and a 1/2" NPTdiaphragm seal will do the job. if it is not, then a 2" flushing ring, 2" flange connection, with a 2" diaphragm seal is a better choice.

the rating should match the piping line class, meaning the main process line. for example, if it is a 2" flange connection and if the line is rated for 600#, you have to select 600#. if it is 300# or less, you can select 300#.

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Join Date: Mar 2008
Location: Houston, Texas
Posts: 101
Good Answers: 6
#2

Re: Flushing Ring

09/17/2008 9:40 AM

The fact that you call this a FLUSHING ring tells me the product has sediments.

In that case will it not be better to have a 2" opening in the pipe than a 3/4" opening

to avoid plugging the tap?

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Active Contributor

Join Date: Jun 2007
Posts: 18
Good Answers: 1
#3

Re: Flushing Ring

09/17/2008 5:21 PM

The isolation valve (not the manifold valves) must meet the primary piping specification and should be increased to the size of the available flushing ("drip, calibration"). A 1 ½ inch ring should be matched with the diaphragm seal, either pancake or flanged. The seals are available in smaller sizes but larger is the proper direction for better response time and minimized temperature change effect. Vendors have programs to calculate the optimization of your seal choice based on plant and process conditions.

Seals are not always used only for chemical or particulate exclusion from the process lead lines, but on level applications the need for reference leg fill fluid maintenance (kept full with known, constant specific gravity) is removed (especially for the poor guy who climbs 30+ mtrs to check).

Pete

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khangnguyenca (1); Pete (Contol Systems) (1); srini (1)

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