How to Calibrate variable Head flowmeter (Orifice), here we
dont know High pressure and low pressure then how to apply
pressure on HP and LP side ?
The situation must be an installed, running system, with a receiver that displays a flow rate from the DP pressure signal, because no one just has a DP transmitter across an orifice plate for fun.
Every differential pressure primary flow element is assumed to be zero flow at zero DP. So the DP low side pressure 'zero' will always be zero DP, or when the 3 valve manifold has its process connection valves closed and the equalizing valve open.
The measured DP represents some flow rate on the square rooted curve of the normalized percentage of span.
In order to determine the DP span value, you measure the actual DP and note what the flow rate reads on the receiver (PLC/DCS/recorder/indicator/controller) at that DP.
Then you can calculate what the DP span value is for the max flow rate that receiver is configured for.
The receiver has some configured flow range: 0-500gpm? 0-1,000 bpd? 0-650pm? Find out what it is.
For example, say you measure a DP value of 700mm wc and that 700 mm wc shows a flow rate reading of 264.5 lpm on the receiver.
You have discovered that the receiver is scaled 0-500 lpm for that DP transmitter and the receiver does the square root extraction.
What is the flow rate as percentage of flow span?
264.5 lpm/500 lpm = 52.9% of flow rate span
52.9% normalized is 0.529
Since the flow rate is the square root of the normalized DP span, you need to square the normalized percentage of flow rate to find the equivalent percentage of DP span.
0.529^2 = 0.2798, or 27.98% (~ 28%) of the DP span.
If 700mm is 28% of span, 100% of span is 2500mm wc.
So the DP span for the transmitter is 0 (no flow) to 2500mm wc (max flow).
Carl Ellis
Measure First
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Calculate the maximum pressure drop that can be allowed to occur across a control valve, so that we can prevent cavitation / flashing from occurring. Use the following formula: Δ P allow = Km (P1 – PvapourA) where, Δ P allow - the maximum allowable differential pressure for sizing purposes, or terminal pressure drop; Km- the valve recovery coefficient from the manufacturer’s catalogue; P1 - absolute inlet fluid pressure; PvapourA - absolute fluid vapour pressure at the inlet temperature; Use Atmospheric pressure = 101.3 kPa, P1 = 1200 kPa(g), PvapourA = 4 kPa, KM = 0.72
we are having yokogawa centum cs3000 dcs in our power plant. i need some of the operator guides NOT to appear in HIS0163 AND HIS 0162 but it shoul appear in HIS0164 HOW TO DO IT?
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i am preparing for BARC ,so plz mail me how to prepare for BARC. ALSO IF POSIBLE SOME RELATED QUESTIONS. MY MAIL ID IS khushi_4uall2003@yahoo.co.in
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Hi buddies! my name is sachin and i am working as a electrical and instrumentation engineer in a paper plant. right now i am facing a problem and if someone could help me it will be an immense pleasure to me. i am using AC 800M to synchronise DCS500 drives on paper machine and rewinder.communication is on PROFIBUS and we are using NPBA-01 module to link profibus to DC drives.But these days two of these drives are showing a error named FIELDBUS COMM.TIMED OUT and the drives get tripped.I have changed the NPBA module and PROFIBUS cable.So if anyone can do please help me out with this problem.I'll be highly grateful.
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