DIFF_PRESS_DP

This function computes the permanent (non-recoverable) pressure loss across a differential-pressure flow meter from upstream and downstream measured pressures, geometry, and meter type. Unlike the instantaneous differential pressure used for flow calculation, this value reflects irreversible energy dissipation.

The quantity is commonly represented as:

\Delta P_{\text{loss}} = f\left(D, D_2, P_1, P_2, C, \text{meter type}\right)

The underlying library applies meter-specific loss correlations, including special handling for orifice, venturi, cone, and wedge geometries.

Excel Usage

=DIFF_PRESS_DP(D, D_two, P_one, P_two, C, dp_meter_type)
  • D (float, required): Upstream internal pipe diameter (m)
  • D_two (float, required): Meter characteristic diameter - orifice hole, venturi throat, cone end, or wedge height (m)
  • P_one (float, required): Static pressure upstream at pressure tap (Pa)
  • P_two (float, required): Static pressure downstream at pressure tap (Pa)
  • C (float, optional, default: 0.6): Coefficient of discharge (required for orifice plates and venturi nozzles) (-)
  • dp_meter_type (str, optional, default: “ISO 5167 orifice”): Type of differential pressure flow meter

Returns (float): Non-recoverable pressure drop of the flow meter (Pa)

Example 1: As-cast venturi tube pressure drop

Inputs:

D D_two P_one P_two dp_meter_type
0.07366 0.05 200000 183000 as cast convergent venturi tube

Excel formula:

=DIFF_PRESS_DP(0.07366, 0.05, 200000, 183000, "as cast convergent venturi tube")

Expected output:

1788.57

Example 2: Cone meter pressure drop

Inputs:

D D_two P_one P_two dp_meter_type
0.25 0.18 1000000 950000 cone meter

Excel formula:

=DIFF_PRESS_DP(0.25, 0.18, 1000000, 950000, "cone meter")

Expected output:

26290

Example 3: Wedge meter pressure drop

Inputs:

D D_two P_one P_two dp_meter_type
0.2 0.14 1000000 950000 wedge meter

Excel formula:

=DIFF_PRESS_DP(0.2, 0.14, 1000000, 950000, "wedge meter")

Expected output:

20344.8

Example 4: Orifice with discharge coefficient

Inputs:

D D_two P_one P_two C dp_meter_type
0.1 0.05 150000 145000 0.61 ISO 5167 orifice

Excel formula:

=DIFF_PRESS_DP(0.1, 0.05, 150000, 145000, 0.61, "ISO 5167 orifice")

Expected output:

3653.64

Python Code

Show Code
from fluids.flow_meter import differential_pressure_meter_dP

def diff_press_dp(D, D_two, P_one, P_two, C=0.6, dp_meter_type='ISO 5167 orifice'):
    """
    Calculate non-recoverable pressure drop across a differential pressure flow meter.

    See: https://fluids.readthedocs.io/fluids.flow_meter.html#fluids.flow_meter.differential_pressure_meter_dP

    This example function is provided as-is without any representation of accuracy.

    Args:
        D (float): Upstream internal pipe diameter (m)
        D_two (float): Meter characteristic diameter - orifice hole, venturi throat, cone end, or wedge height (m)
        P_one (float): Static pressure upstream at pressure tap (Pa)
        P_two (float): Static pressure downstream at pressure tap (Pa)
        C (float, optional): Coefficient of discharge (required for orifice plates and venturi nozzles) (-) Default is 0.6.
        dp_meter_type (str, optional): Type of differential pressure flow meter Valid options: ISO 5167 Orifice, Orifice, Conical Orifice, Eccentric Orifice, Segmental Orifice, Quarter Circle Orifice, ISO 15377 Conical Orifice, ISO 15377 Eccentric Orifice, ISO 15377 Quarter-circle Orifice, Miller Orifice, Miller Conical Orifice, Miller Eccentric Orifice, Miller Segmental Orifice, Miller Quarter Circle Orifice, Hollingshead Orifice, Venturi Nozzle, ISA 1932 Nozzle, Long Radius Nozzle, Machined Convergent Venturi Tube, Rough Welded Convergent Venturi Tube, As Cast Convergent Venturi Tube, Hollingshead Venturi Smooth, Hollingshead Venturi Sharp, Cone Meter, Hollingshead V Cone, Wedge Meter, Hollingshead Wedge, Unspecified Meter. Default is 'ISO 5167 orifice'.

    Returns:
        float: Non-recoverable pressure drop of the flow meter (Pa)
    """
    try:
      if D <= 0:
        return "Error: D (upstream diameter) must be positive."
      if D_two <= 0:
        return "Error: D_two (meter diameter) must be positive."
      result = differential_pressure_meter_dP(
        D=D,
        D2=D_two,
        P1=P_one,
        P2=P_two,
        C=C,
        meter_type=dp_meter_type
      )
      return float(result)
    except Exception as e:
      return f"Error: {str(e)}"

Online Calculator

Upstream internal pipe diameter (m)
Meter characteristic diameter - orifice hole, venturi throat, cone end, or wedge height (m)
Static pressure upstream at pressure tap (Pa)
Static pressure downstream at pressure tap (Pa)
Coefficient of discharge (required for orifice plates and venturi nozzles) (-)
Type of differential pressure flow meter