DP FlowFluid Data Sheetcd Flow Fluid Sheet

User Manual: DP-Flow Fluid Data Sheet

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Main Table of Contents
- Flow Table of Contents
  - DP-Flow Fluid Data Sheet (FDS)

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:

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:

Specific Gravity at Flow: ____________________________________________

* Viscosity at Flow: ________________________________________________ Units: ❑ Centipoise ❑ Other:

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:

M.W. / Specific Gravity at Flow: _________________________________________________

Compressibility at Flow: _____________________________________________________

Compressibility at Base: ____________________________________________________

* Viscosity at Flow: _____________________________ Units: ❑ Centipoise ❑ Other: Isentropic Exponent (K):______ 1.4

★

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

CO2

C2H6

C3H8

H2O

H2S

C4H10

C5H12

C8H18

C7H18

C8H18

C9H2O

C10H22

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

________________________________

0 – 100 percent

0 – 12 percent

0 – Dew point

0 – 100 percent

0 – 3.0 percent

0 – 21 percent

0 – 6 percent(1)

0 – 4 percent(2)

0 – 4 percent

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.

DP FlowFluid Data Sheetcd Flow Fluid Sheet

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