Re: [foxboro] Natural Gas Temp & Pressure compensation
- From: "Wilson, Brad" <brad.wilson@xxxxxxxxxxxxxxxx>
- To: <foxboro@xxxxxxxxxxxxx>
- Date: Thu, 28 Feb 2008 14:38:11 -0500
At the temps & pressures you're talking about, the scaling is linear.
Temperature is direct, pressure is inverse. Just be sure to use absolute
temperature (deg F + 460) and PSIA.
compensated flow =3D flow * (T-act/T-ref) * (P-ref/P-act)
T-ref is usually 60 F & P-ref is usually 0 psig (14.7 psia)
Brad Wilson
brad.wilson@xxxxxxxxxxxxxxxx
Invensys Process Systems, Inc
1090 King Georges Post Rd, Suite 204
Edison, NJ 08837
-----Original Message-----
From: foxboro-bounce@xxxxxxxxxxxxx [mailto:foxboro-bounce@xxxxxxxxxxxxx]
On Behalf Of David Johnson
Sent: Thursday, February 28, 2008 2:04 PM
To: Foxboro@xxxxxxxxxxxxx
Subject: [foxboro] Natural Gas Temp & Pressure compensation
Hello all,
I was wondering if someone had the formula in their back pocket for =
taking a DP on a natural gas line and converting it to a compensated
flow.
I have a DP orifice plate that is scaled from 0-235 " water. This, I =
am told corresponds to 0-2000 CFM.
I have a PT scaled from 0-130 PSI
I have a TT scaled from 0-300 deg F.
So a DP of 100" H2O at 80 Deg F and 100 PSI is ??????SCFM.
So can one of you Chemical Engineers lend a hand?
Thanks,
David
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