yrtgrfeSeagate crystal reports as fou 6 inch for 25 mmscfd (senior)
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This document provides information from an as found report on a gas meter. It includes details on the meter identification, flow rate standards used, gas characterization, system units, calculation type, flow rate, heating value, orifice plate diameter, meter hardware, operating conditions, meter type and materials, characterization method, reference conditions, instrument calibration details, compressibility factors, densities, diameters, gas relative densities, calibration related factors, orifice flow constants, and other relevant gas properties. The report provides a technical summary of the gas meter's configuration and operating parameters in great detail for evaluation.
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yrtgrfeSeagate crystal reports as fou 6 inch for 25 mmscfd (senior)
- 1. As Found Report UnitsAs Found Meter Identification Meter # Field Well Lease Meter Tag Date _/_/__ Time 12:00:00 AM Standards Used Flow Rate Standard AGA3 1992 Compressibility GA8 1992/GPA 2172-96 Gas Characterization Gas Analysis System of Units US Calculation Type Orifice Size Determination Summary $ $ $ $ $ $ Daily -$38.75 US $/Day Monthly -$1,178.65 US $/Month Yearly -$14,143.75 US $/Year Flow Rate Volume Flow Rate at base conditions, Qb 1,041,666.667 scf/hr Volume Flow Rate at base conditions, Qb 25.000 MMscfd Heating Value Net Heating Value, HVNET 902.393 Btu/scf Orifice Plate Diameter Calculated Orifice Plate Diameter, dr 3.717 in Meter Data Hardware Orifice Bore Diameter @ Tr, dr 3.150 in Meter Tube Diameter @ Tr, Dr 6.065 in Beta Ratio 0.519 Operating Conditions Page 1
- 2. As Found Report UnitsAs Found Temperature 80.000 F Flowing Pressure (Gage/Absolute) Gage Atmospheric Pressure 14.730 psia Pressure (Upstream) 406.140 psia Pressure (Downstream) 399.282 psia Differential Pressure 190.000 inh2o Meter Type and Materials Materials Orifice Plate Material Stainless Steel Meter Tube Material Carbon Steel Reference - Temperature Meter Tube Diameter Meas. Temp., Tr 68.000 F Orifice Diameter Meas. Temp., Tr 68.000 F Taps Type of Taps Flange Location of Taps Upstream Characterization Method Mole Percent of Water 0.000 Mole Percent of Helium 0.000 Mole Percent of Methane 83.799 Mole Percent of Ethane 5.587 Mole Percent of Propane 1.117 Mole Percent of I-Butane 0.112 Mole Percent of n-Butane 0.112 Mole Percent of I-Pentane 0.112 Mole Percent of n-Pentane 0.112 Mole Percent of Hexane 0.112 Mole Percent of Heptane 0.000 Mole Percent of Octane 0.000 Mole Percent of Nonane 0.000 Mole Percent of Decane 0.000 Mole Percent of Oxygen 0.000 Mole Percent of Carbon Monoxide 0.000 Mole Percent of Hydrogen 0.000 Mole Percent of Nitrogen 4.469 Mole Percent of Carbon Dioxide 4.469 Mole Percent of Hydrogen Sulfide 0.000 Mole Percent of Argon 0.000 Default Page 2
- 3. As Found Report UnitsAs Found Other Absolute viscosity of flowing fluid 0.010268 cP Isentropic Exponent, k 1.300 Reference Conditions - Pressure Base pressure, Pb 14.730 psia Reference Pressure for Relative Density, Pgr 14.730 psia Reference Pressure for Calorimetric Combustion, Ph 14.730 psia Reference Pressure for Calorimetric Density, Pd 14.730 psia Reference Conditions - Temperature Base Temperature, Tb 60.000 F Reference Temperature for Relative Density, Tgr 60.000 F Reference Temperature for Calorimetric Combustion, Th 60.000 F Reference Temperature for Calorimetric Density, Td 60.000 F Instrument Calibration Differential Pressure DeadWeight Calibrator Yes/No No Local Grav. Acc. - Input/Calculate Calculate Acceleration of Gravity used to calibrate the weights, go 32.17400 ft/sec^2 Latitude, L 45.00000 Degrees Elevation, H 0.00000 ft Acceleration due to local gravitational force, gl 32.17405 ft/sec^2 Mercury Manometer Calibration Correction Yes/No No Local Grav. Acc. - Input/Calculate Calculate Mercury Temperature, Tw 60.00000 F Air Temperature, Ta 60.00000 F Latitude, L 45.00000 Degrees Elevation, H 0.00000 ft Acceleration due to local gravitational force, gl 32.17405 ft/sec^2 Static Pressure DeadWeight Calibrator Yes/No No Local Grav. Acc. - Input/Calculate Calculate Acceleration of Gravity used to calibrate the weights, go 32.17400 ft/sec^2 Latitude, L 45.00000 Degrees Elevation, H 0.00000 ft Acceleration due to local gravitational force, gl 32.17405 ft/sec^2 User Input User Input Calibration Factor 1.00000 Water Manometer Calibration Correction Yes/No No Local Grav. Acc. - Input/Calculate Calculate Water Temperature, Tw 60.00000 F Air Temperature, Ta 60.00000 F Page 3
- 4. As Found Report UnitsAs Found Latitude, L 45.00000 Degrees Elevation, H 0.00000 ft Acceleration due to local gravitational force, gl 32.17405 ft/sec^2 Outputs Compressibility Factors Compressibility Factor @ Tf and Pf 0.942749 Compressibility Factor @ Tb and Pb 0.997602 Compressibility Factor at standard conditions 0.997602 Densities Gas density @ Tf and Pf 1.429885 lbm/ft^3 Gas density @ Tb and Pb 0.050894 lbm/ft^3 Gas density at standard conditions 0.050894 lbm/ft^3 Diameters Corrected Orifice Diameter @ Tf, d 3.717453 in Corrected Meter Tube Diameter @ Tf, D 6.065451 in Gas Relative Densities Gas Relative Density at standard conditions 0.665030 Gas Relative Density at base conditions 0.665030 Instrument Calibration Related Factors Mercury Manometer Factor, Fhgm 1.000000 Mercury Manometer Location Factor, Fhgl 1.000000 Mercury Manometer Temperature Factor, Fhgt 1.000000 Water Manometer Air Leg Factor, Fam 1.000000 Water Manometer Location Factor, Fwl 1.000000 Water Manometer Temp Factor, Fwt 1.000000 Differential Pressure Deadweight Factor, Fhwl 1.000000 Static Pressure Deadweight Factor, Fpwl 1.000000 User Input Calibration Factor, Fu 1.000000 FlowRate Fact.=Fhgm*Fhgl*Fhgt*Fam*Fwl*Fwt*Fpwl*Fhwl*Fu 1.000000 Orifice Flow Constants & Factors Discharge Coefficient, Cd 0.604319 Velocity of Approach, Ev 1.079019 Numeric Conversion Factor, Fn 5,042.974665 Orifice Calculation Factor, Fc 0.602560 Orifice Slope Factor, Fsl 0.001759 Expansion Factor, Y 0.994033 Pressure Base Factor, Fpb 1.000000 Temperature Base Factor, Ftb 1.000000 Flowing Temperature Factor, Ftf 0.981295 Relative Density Factor, Fgr 1.226251 Comp. Orif. Flow Factor, C'=Fn(Fc+Fsl)Y*Fpb*Ftb*Ftf*Fgr*Fpv 3,749.848442 Supercompressibility Factor, Fpv 1.028681 Page 4
- 5. As Found Report UnitsAs Found Other Average Gas Velocity 51.326269 ft/sec Reynolds Number - Upstream 5,376,349.629949 Molecular Weight of The Gas 19.222774 Reduced Temperature 1.479510 Reduced Pressure 0.598988 Critical Temperature -94.907343 F Critical Pressure 678.043240 psia Page 5