DP FlowFluid Data Sheetcd Flow Fluid Sheet
User Manual: DP-Flow Fluid Data Sheet
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Page Count: 4
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Catalog 2002 – 2003
Flow-105
This form identifies custom fluids that are not in the Rosemount Fluid Database. Complete this form for the
following DP Flowmeters (if applicable):
• Annubar Flowmeter Series
• Model 405P Compact Orifice
• Model 1195 Integral Orifice, ProPlate Flowmeter, Mass ProPlate Flowmeter
For technical assistance in filling out this CDS, call your local Rosemount representative. Complete this form to
define a custom fluid. The ★symbol identifies the default value.
NOTE
This form is not required if using the Rosemount Fluid Database.
* = Required Item
★ = Default
Customer Information
Customer: Contact Name:
Customer Phone: Customer Fax:
Customer PO:
Fluid Properties
❑ Custom Liquid– Complete Table ❑ Liquid
❑ Custom Gas– Complete Table ❑ Gas
❑ Custom Natural Gas– Complete Table ❑ Natural Gas
For Rosemount Use Only
S.O.: LI
CHAMP: DATE:
ADMIN:
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Catalog 2002 – 2003
Flow-106
TABLE 1. Custom Liquid Worksheet
* = Required Item
★ = Default
Mass Liquid Density and Viscosity Information
1. Fill in the following operating temperatures
a) _________________________ min
b) _________________________ [1/3 (max - min))] + min
c) _________________________ [2/3 (max - min))] + min
d) _________________________ max
2. Transfer the values from the above section to the numbered lines below.
3. Check one Density box, then enter the values for each temperature and the standard density.
4. Check one Viscosity box, then enter values for each temperature. (At least one viscosity value is required).
Density
❑ Density in lbs/CuFt
❑ Density in kg/CuM
Viscosity
❑ Viscosity in centipoise
❑ Viscosity in lbs/ft sec
❑ Viscosity in pascal sec
Temperature Temperature
a) _____________ min a) _____________ min.
b) _____________ [1/3 (max - min))] + min b) _____________ [1/3 (max - min))] + min
c) _____________ [2/3 (max - min))] + min c) _____________ [2/3 (max - min))] + min
d) _____________ max d) _____________ max
Base density: __________________________________________________________
(at base reference conditions specified)
Volumetric Liquid Density and Viscosity Information
* Density at Flow: _________________________________________________ Units: ❑ lb/ft3❑ Kg/m3❑ Other:
OR
Specific Gravity at Flow: ____________________________________________
* Viscosity at Flow: ________________________________________________ Units: ❑ Centipoise ❑ Other:
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Catalog 2002 – 2003
Flow-107
TABLE 2. Custom Gas Worksheet
* = Required Item
★ = Default
Mass Gas Compressibility and Viscosity Information
1. Fill in the following operating pressures and operating temperatures
Operating Pressures Operating Temperatures
a) _____________ min e) _____________ min
b) _____________ [1/3 (max - min))] + min f) _____________ [1/2 (max - min))] + min
c) _____________ [2/3 (max - min))] + min g) _____________ max
d) _____________ max h) _____________ [1/3 (max - min))] + min
i) _____________ [2/3 (max - min))] + min
2. Transfer the values from the above section to the numbered lines below
3. Check one Density/Compressibility box, then enter the 12 values for each pressure/temperature range.
4. Check one Viscosity box, then enter values for each temperature. (At least one viscosity value is required).
5. Enter values for molecular weight, isentropic exponent, and standard density (or standard compressibility).
Density
❑ Density in lbs/CuFt
❑ Density in kg/CuM
❑ Compressibility
Viscosity
❑ Viscosity in centipoise
❑ Viscosity in lbs/ft sec
❑ Viscosity in pascal sec
Pressure Temperature Temperature
1) ____________ 5) _____________________________ 5) ________________________________________
2) ____________ 5) _____________________________ 8) ________________________________________
3) ____________ 5) _____________________________ 9) ________________________________________
4) ____________ 5) _____________________________ 7) ________________________________________
1) ____________ 6) _____________________________
2) ____________ 6) _____________________________ Molecular Weight: _________________________
3) ____________ 6) _____________________________ Isentropic Exponent: _______________________ 1.4 ★
4) ____________ 6) _____________________________
1) ____________ 7) _____________________________
2) ____________ 7) _____________________________
3) ____________ 7) _____________________________
4) ____________ 7) _____________________________
Standard density/compressibility: __________________________________________________________
Volumetric Gas Compressibility and Viscosity Information
* Density at Flow: ______________________________ Units: ❑ lb/ft3❑ Kg/m3❑ Other:
OR
M.W. / Specific Gravity at Flow: _________________________________________________
Compressibility at Flow: _____________________________________________________
Compressibility at Base: ____________________________________________________
* Viscosity at Flow: _____________________________ Units: ❑ Centipoise ❑ Other: Isentropic Exponent (K):______ 1.4
★
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Catalog 2002 – 2003
Flow-108
TABLE 3. Natural Gas Worksheet
NOTE
The minimum requirement for the Volumetric options is highlighted gray on page Flow-108.
* = Required Item
★ = Default
Compressibility Factor Information
Choose desired character4ization method and only enter values for that method.
❑ Detail Characterization Method (AGA8 1992) Mole Valid Range
CH4
N2
CO2
C2H6
C3H8
H2O
H2S
H2
CO
O2
C4H10
C4H10
C5H12
C5H12
C8H18
C7H18
C8H18
C9H2O
C10H22
He
Ar
Methane mole percent
Nitrogen mole percent
Carbon Dioxide mole percent
Ethane mole percent
Propane mole percent
Water mole percent
Hydrogen Sulfide mole percent
Hydrogen mole percent
Carbon monoxide mole percent
Oxygen mole percent
i-Butane mole percent
n-Butane mole percent
i-Pentane mole percent
n-Pentane mole percent
Hexane mole percent
n-Heptane mole percent
n-Octane mole percent
n-Nonane mole percent
n-Decane mole percent
Helium mole percent
Argon mole percent
________________________________
________________________________
________________________________
________________________________
________________________________
________________________________
________________________________
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________________________________
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________________________________
________________________________
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%
%
%
%
%
%
%
%
%
%
%
%
%
%
%
%
%
%
%
%
%
0 – 100 percent
0 – 100 percent
0 – 100 percent
0 – 100 percent
0 – 12 percent
0 – Dew point
0 – 100 percent
0 – 100 percent
0 – 3.0 percent
0 – 21 percent
0 – 6 percent(1)
0 – 6 percent(1)
0 – 4 percent(2)
0 – 4 percent
0 – Dew Point
0 – Dew Point
0 – Dew Point
0 – Dew Point
0 – Dew Point
0 – 3.0percent
0 – 1.0 percent
❑ Gross Characterization Method, Option Code 1 (AGA8 Gr-Hv-CO2)Mole Valid Range
Specific Gravity at 14.73 psia and 60 °F ________________________________ 0.554 – 0.87
Volumetric gross heating value at base conditions
Carbon Dioxide mole percent
Hydrogen mole percent
Carbon Monoxide mole percent
________________________________
________________________________
________________________________
________________________________
BTU/SCF
%
%
%
477 – 1150 BTU/SCF
0 – 30 percent
0 – 10 percent
0 – 3.0 percent
❑ Gross Characterization Method, Option Code 2 (AGA8 Gr-CO2-N2)Mole Valid Range
Specific Gravity at 14.73 psia and 60 °F
Carbon Dioxide mole percent
Nitrogen mole percent
Hydrogen mole percent
Carbon Monoxide mole percent
________________________________
________________________________
________________________________
________________________________
________________________________
%
%
%
%
%
0.554 – 0.87
0 – 30 percent
0 – 50 percent
0 – 10 percent
0 – 3.0 percent
(1) The summaries of i-Butane and n-Butane cannot exceed 6 percent.
(2) The summaries of i-Pentane and n-Pentane cannot exceed 4 percent.