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Egypt - Member - New Member

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Orifice Plate and Flow Transmitter

11/24/2013 7:25 AM

Hello every one!

it is requested to reconfigure the upper range value of a flow transmitter to a higher value, which is ok by the transmitter (the maximum dp limit by the transmitter is greater).

from data sheets:

  • flow range : 0 - 150 m3/hr
  • dp range : 0 - 250 mbar

the required values:

  • flow range : 0 - 400 m3/hr
  • therefore the calculated dp should 1.78 bar!

some data are confusing me :

  • in data sheets it is mentioned that the maximum flow rate is 209.2 m3/hr(dp 448mbar).
  • in orifice plate calculation sheet the max. flow rate is 70 m3/hr, temp. 25 C, viscosity 0.72 cP, flowing pressure 9.3 Bar, dp 250 mbar, densty 994.3 kg/m3.

what does it mean that the flow rate is 70 m3/hr at dp 250mbar (through calculation from datasheets it should be 150 m3/hr) ?

the pipe size is 8'', d/D is 0.35858938.

what is the max dp and flow accepted by the line?

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#1

Re: Orifice Plate and Flow Transmitter

11/24/2013 10:52 AM

If the orifice plate calculation sheet disagrees with the installed range (datasheet), either the calculations are incorrect, the installed range (datasheet) is incorrect, or perhaps there is some other parameter not being taken into account. I don't have orifice plate software handy right now and I'm not in the mood to crunch through Bernoulli's equation to see which of the two figures seems more reasonable, but I'd say it's time to locate some orifice plate software of your own and do a complete re-calculation to see where the error lies.

Your estimation of 1.78 bar DP for 400 m3/hr is correct assuming the orifice plate really does generate 250 mbar DP at 150 m3/hr. If this is truly the case, then what is needed is a new orifice plate (with a larger d/D "beta" ratio) to produce more realistic differential pressures. A differential pressure of 1.78 bar is tremendous, and might actually *damage* the orifice plate!

Also, bear in mind the limited turn-down ratio of most orifice flowmeter installations. Increasing the top-end range of the flowmeter also increases the lowest flow rate you can measure with reasonable accuracy. If operations personnel want the range increased, they must also realize they will compromise low-flow accuracy as a direct consequence of this. Perhaps they are already aware of this fact, but it's worth repeating.

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#2

Re: Orifice Plate and Flow Transmitter

11/24/2013 12:49 PM

Omar,

Using this data:

the pipe size is 8'', d/D is 0.35858938, so, the orifice size is 7.98" x 0.35858938 = 2,8615432524", If you can please tell us the pipe ID, the 7.98" is only a reference from pipe SCH 40 table.

So,

temp. 25 C, viscosity 0.72 cP, flowing pressure 9.3 Bar, dp 250 mbar, densty 994.3 kg/m3 and orifice size 2,8615432524"

According an orifice software you will be having the following flow 64.3 m3/hr

Can you check directly on your orifice plate What is the orifice size?

What is the liquid?

I agree with Tony there is a error in someplace of your data

Best regards

JP

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#3

Re: Orifice Plate and Flow Transmitter

11/24/2013 1:29 PM

If you want to have same pressure drop at the plate then you must increase the oriffice diameter as follows:

d2/D=d1/D*(q^2/(1-(d1/D)^4*(1-q^2))^0.25; q= Q2/Q1

This assumes that the flow discharge coefficient is constant which is valis if the ratios d/D are not too far from each other.

If you accept a pressure drop change then you should correct the obtaine value with sqrt of pressure drops ratio.

The 3 values you give Q-Δp are coherent although a difference does appear.

You can find all equations in wikipedia under "oriffice plate calculations" and very well explained.

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#4

Re: Orifice Plate and Flow Transmitter

11/24/2013 6:26 PM

Daniels' Orifice Flow calculator freeware gives the same value for flow rate as Instruments-guy-SAV calculated for the info provided.

Some value isn't correct to get that flow rate at that DP with the design conditions provided.

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#5

Re: Orifice Plate and Flow Transmitter

11/25/2013 8:35 AM

hello omar how did you find this value? for 0-400m3/hr the dp be 1.78

  • flow range : 0 - 400 m3/hr
  • therefore the calculated dp should 1.78 bar!
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Egypt - Member - New Member

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#6

Re: Orifice Plate and Flow Transmitter

11/26/2013 12:39 AM

hey Guys,

thanks a lot for your support, and sorry I was out of office for the lsat couple of days.

I have attached the orifice calculation sheet and flow transmitter datasheet, to clarify it to you.

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#7

Re: Orifice Plate and Flow Transmitter

11/26/2013 12:39 AM
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#8

Re: Orifice Plate and Flow Transmitter

11/26/2013 12:40 AM
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Egypt - Member - New Member

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#9

Re: Orifice Plate and Flow Transmitter

11/26/2013 12:43 AM

do you know how to attach a file here?

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Egypt - Member - New Member

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#10

Re: Orifice Plate and Flow Transmitter

11/26/2013 12:56 AM

from data sheets

the flow rang is 150 m3/hr and differential pressure is 250 mbar

at the same datasheet (for process data) it is mentioned that the normal flow rate is 37.5 to 51.8 m3/hr, minmum flow is 19 m3/hr, and the maximum flow is 209.2 m3/hr which is corresponding to 448 mbar as he said in data sheet.

in orifice calculation sheets:

it is mentioned that the full scale flow (maximum flow rate) is 70 m3/hr!! for the same dp (250 mbar)

and the piping schedual is 8 inch / SCH 10S

flange 300RF

pipe ID 211.56mm\flange and pipe material are 304 SS

also from orifice calculation sheet ---- meter data:

type: dry

C' coefficient: 14.005171

Full scale flow: 70 m3/hr

full scale dp: 250mbar

chart scale: 10 roots

chart multiplier: 7

flow reading: 7.4 Roots

allowable dp: 340 mbar

thanks a lot for your great help :)

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#11

Re: Orifice Plate and Flow Transmitter

11/28/2013 1:59 AM

dears,

finally i found the problem, the confusion was due to a wrong documents.

the calculation were right where, the flow rate is 70 m3/hr and the dp is 250 mbar.

the data sheets mentioned the new flow rate which is 150 m3/hr but it didn't mentioned that the dp was changed to 1151 mbar (that was missing) I checked it myself in the field.

the problem now is that, is it correct to let the orifce plate works at this dp (1151 mbar), and on what criteria I should judge if it is applicable or not?

and by the way, the orifice thickness is 3.2 mm.

can anyone help in this issue.

thanks.

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#12

Re: Orifice Plate and Flow Transmitter

11/28/2013 2:08 PM

The flow sizing programs will flag a warning at about 85m3/hr flow rate that plate deflection needs to be checked.

Standards like AGA 3-2 have tables for plate thicknesses at various betas for various line sizes.

The vendor table below summarizes typical recommendations on plate thickness.

I've always considered the relative low cost and replaceability of orifice plates an advantage, so replacing with a re-sized plate can be an option.Living with plate deflection might be an option, too.

I was surprised when I read how little (relatively) little error a deflected plate showed, after reading a paper:

"Yeyssandier and Chisman (1984) tested 8- and 10-inch bent plates with original [beta] ratios of 0.5 to 0.6 and deflections of up to 0.54 inch in the direction of flow. Their study also concluded that measurement errors become more negative with increasing deflection angle, but the largest under-measurement error observed in the study was 3.3% for a deflection of about 1/2 inch. Ting (1993) flow calibrated 4- and 6-inch orifice plates with beta ratios between 0.25 and 0.75, then recalibrated the same plates after they had been bent over a mandrel to deflection angles between 1[degrees] and 10[degrees]. Except for [beta] = 0.25, the measurement error increased with increasing [beta] and deflection angle. From his test results, Ting concluded that bent plates might cause under-measurement errors up to 4.5%, less than the errors reported by Burgin for similar deflection angles."

http://www.thefreelibrary.com/Guidelines+for+measurement+errors+caused+by+buckled+orifice+plates.-a0182406220

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Anantharaman N (1); Instruments-guy-SAV (1); Iris (2); nick name (1); omar (6); tonykuphaldt (1)

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