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Division 2.2.4.3 SSV-CVS system

United Kingdom

Original text. Later amendments are not shown.

The diluted exhaust gas mass over the cycle m ed [kg/test] shall be calculated by means of equation (7-39), if the temperature of the diluted exhaust gas is kept within ± 11 K over the cycle by using a heat exchanger:

m ed = 1,293 · qV SSV · Δt (7-39)

Where:

1,293 kg/m3
  • air density at 273,15 K and 101,325 kPa

  • Δt
  • cycle time [s]

  • qV SSV
  • air flow rate at standard conditions (101,325 kPa, 273,15 K) [m3/s]

  • with

    q V SSV = A 0 60 d 2 v C d P p 1 T r 1,4286 p − r 1,7143 p × 1 1 − r 4 D r 1,4286 p (7-40)

    Where:

    A 0
  • collection of constants and units conversions = 0,0056940 m 3 min × K 1 2 kPa × 1 mm 2

  • d V
  • diameter of the SSV throat [mm]

  • C d
  • discharge coefficient of the SSV [-]

  • p p
  • absolute pressure at venturi inlet [kPa]

  • T in
  • temperature at the venturi inlet [K]

  • r p
  • ratio of the SSV throat to inlet absolute static pressure, 1 − Δ P P a [-]

  • r D
  • ratio of the SSV throat diameter to the inlet pipe inner diameter d D [-]

  • If a system with flow compensation is used (i.e. without heat exchanger), the mass of the diluted exhaust gas m ed, i [kg] during the time interval shall be calculated by means of equation (7-41):

    m ed, i = 1,293 · qV SSV · Δt i (7-41)

    Where:

    1,293 kg/m3
  • air density at 273,15 K and 101,325 kPa

  • Δti
  • time interval [s]

  • qV SSV
  • volumetric flow rate of the SSV [m3/s]