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e.g., 24” Gas Export Line
e.g.,6” Gas Line
e.g., 8” Gas Line
e.g., 8” Gas Line
Weymouth Equation
 For Smaller Dia, <=10” &
Shorter Piping of the order
of ‘feet’
 Reynolds number of the
order of > ~11x106
 Moody friction factor is a
function of relative
roughness ()
 Though, P calculated is
over estimated, it is used for
a conservative design
Modified Panhandle
Equation
 For Larger Dia, >10” & long
pipelines (> ~20 miles)
 Reynolds Numbers of the
order of (4x106 to 40x106)
 Moody friction factor is
independent of relative
roughness ()
 Condensation in Pipelines is
not accounted.
AGA Equation
 For Partially Turbulent & Fully
Turbulent flow
 Applicable when internal pipe
roughness is known accurately
 Von Karman Transmission
factor is used instead of
friction factor to estimate P
Spitzglass Equation
 For Smaller Dia, <10”
 Low pressure Vent Lines
 P < 0.1 x Pinlet
General Flow Equation
 For pressures < 7 barg
 Assumes Isothermal Flow.
i.e., no heat transfer
 Pipeline is horizontal
 No mechanical work done by
gas
CHOOSING SINGLE PHASE GAS FLOW CORRELATIONS
References
 Recommended Practice for Design and Installation of Offshore
Production Platform Piping Systems, API Recommended Practice
14E (RP 14E) Fifth Edition, Oct,1991
 Sizing of Gas Pipelines, Mavis Nyarko, International Journal of
Energy Engineering, Dec. 2015, Vol. 4 Iss. 6, PP. 202-205
Notes
 Weymouth Equation is suitable for piping within production
facility (API 14E, 5th Edition)
 API 14E does not suggest applicability of Erosional velocity
criteria for Single Phase flow, but for 2 Phase (Gas/Liquid)

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Single Phase Gas Flow Correlations

  • 1. e.g., 24” Gas Export Line e.g.,6” Gas Line e.g., 8” Gas Line e.g., 8” Gas Line Weymouth Equation  For Smaller Dia, <=10” & Shorter Piping of the order of ‘feet’  Reynolds number of the order of > ~11x106  Moody friction factor is a function of relative roughness ()  Though, P calculated is over estimated, it is used for a conservative design Modified Panhandle Equation  For Larger Dia, >10” & long pipelines (> ~20 miles)  Reynolds Numbers of the order of (4x106 to 40x106)  Moody friction factor is independent of relative roughness ()  Condensation in Pipelines is not accounted. AGA Equation  For Partially Turbulent & Fully Turbulent flow  Applicable when internal pipe roughness is known accurately  Von Karman Transmission factor is used instead of friction factor to estimate P Spitzglass Equation  For Smaller Dia, <10”  Low pressure Vent Lines  P < 0.1 x Pinlet General Flow Equation  For pressures < 7 barg  Assumes Isothermal Flow. i.e., no heat transfer  Pipeline is horizontal  No mechanical work done by gas CHOOSING SINGLE PHASE GAS FLOW CORRELATIONS References  Recommended Practice for Design and Installation of Offshore Production Platform Piping Systems, API Recommended Practice 14E (RP 14E) Fifth Edition, Oct,1991  Sizing of Gas Pipelines, Mavis Nyarko, International Journal of Energy Engineering, Dec. 2015, Vol. 4 Iss. 6, PP. 202-205 Notes  Weymouth Equation is suitable for piping within production facility (API 14E, 5th Edition)  API 14E does not suggest applicability of Erosional velocity criteria for Single Phase flow, but for 2 Phase (Gas/Liquid)