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Cone Meters
v2.1
Mass or gross volume flowrate calculation for cone type meters
This is essentially the ISO 5167 standard modified for the geometry and characteristics of a cone meter.
Configuration
Option
Setting
Fluid Type
Gas
Liquid
Primary Flowrate
Gross Volume
Mass
Edition
24509-54 Rev 3.2
24509-54 Rev 2.5
ISO 5167-5:2016
V-Cone Model
Standard
Wafer
Temperature Transmitter Location
Recovery Point
Downstream
Upstream
Temperature Correction Method
Isentropic Exponent
ISO TR 9464
Density Location
Recovery Point
Downstream
Upstream
Temperature Exponent Method
Calculated
User Entered
Discharge Coefficient
Fixed
Interpolated
Contains Drain Hole
No
Yes
Energy Flowrate Calculated from
Std. Vol. Flowrate
Mass Flowrate
Inputs
Field
Units
Value
Differential Pressure
mbar
bar
Pa
Upstream Pressure (p1)
mbar
mbar g
bar
bar g
Pa
Pa g
kPa
kPa g
MPa
MPa g
GPa
GPa g
psi
psi g
inH2O @ 60°F
Recovery Point Temperature (t3)
°C
°F
K
°R
Pipe Diameter
mm
cm
m
km
in
ft
Pipe Coefficient of Expansion
mm/mm/°C
mm/mm/°F
mm/mm/K
mm/mm/°R
m/m/°C
m/m/°F
m/m/K
m/m/°R
Pipe Calibration Temperature
°C
°F
K
°R
Cone Diameter
mm
cm
m
km
in
ft
Cone Coefficient of Expansion
mm/mm/°C
mm/mm/°F
mm/mm/K
mm/mm/°R
m/m/°C
m/m/°F
m/m/K
m/m/°R
Cone Calibration Temperature
°C
°F
K
°R
Upstream Density
kg/m³
g/m³
mg/m³
lb/ft³
Isentropic Exponent
-
Fluid Viscosity
mPa.s
Pa.s
cP
P
pdl.s/ft²
rhe
Standard Density
kg/Sm³
g/Sm³
mg/Sm³
lb/Sft³
Superior Real Volume Based CV
MJ/Sm³
Discharge Coefficient
-
Intermediates
Field Name
Value
Iterations
0
Results
Description
Units
Actual
Temperature Exponent
-
Beta Ratio
-
Temperature Corrected Pipe Diameter
mm
cm
m
km
in
ft
Temperature Corrected Device Diameter
mm
cm
m
km
in
ft
Beta Ratio (Corrected)
-
Adiabatic Expansion Factor
-
Thermal Expansion Factor
-
Flow Coefficient
-
Permanent Pressure Loss
mbar
bar
Pa
Downstream Pressure (p2)
mbar
mbar g
bar
bar g
Pa
Pa g
kPa
kPa g
MPa
MPa g
GPa
GPa g
psi
psi g
inH2O @ 60°F
Recovered Pressure (p3)
mbar
mbar g
bar
bar g
Pa
Pa g
kPa
kPa g
MPa
MPa g
GPa
GPa g
psi
psi g
inH2O @ 60°F
Upstream Temperature (t1)
°C
°F
K
°R
Downstream Temperature (t2)
°C
°F
K
°R
Mass Flowrate
kg/s
kg/h
kg/d
t/s
t/h
t/d
lb/h
lb/s
lb/d
long ton/s
long ton/h
long ton/d
short ton/s
short ton/h
short ton/d
Gross Volume Flowrate
m³/s
m³/h
m³/d
km³/s
km³/h
km³/d
bbl/s
bbl/h
bbl/d
bbl(UK)/s
bbl(UK)/h
bbl(UK)/d
bbl(US)/s
bbl(US)/h
bbl(US)/d
Standard Volume Flowrate
Sm³/s
Sm³/h
Sm³/d
kSm³/s
kSm³/h
kSm³/d
Sbbl/s
Sbbl/h
Sbbl/d
Sbbl(UK)/s
Sbbl(UK)/h
Sbbl(UK)/d
Sbbl(US)/s
Sbbl(US)/h
Sbbl(US)/d
scf/s
scf/h
scf/d
kscf/s
kscf/h
kscf/d
MMscf/s
MMscf/h
MMscf/d
Energy Flowrate
J/s
J/h
J/d
MJ/s
MJ/h
MJ/d
GJ/s
GJ/h
GJ/d
TJ/s
TJ/h
TJ/d
PROJECT CODE:
STREAM ID:
TEST NUMBER:
TEST CONDUCTED BY:
TEST WITNESSED BY:
ADDITIONAL WITNESS:
ADDITIONAL WITNESS:
ADDITIONAL WITNESS:
ADDITIONAL WITNESS:
COMMENTS:
TEST DATE:
03/03/2021 20:27:09