Gas phase:
| (9–3) | 
     is the mean gas density and 
 is the mean gas heat capacity at constant pressure. 
 and 
 are the temperature and the volume of the gas mixture and 
 is the enthalpy of gas species 
 at gas-phase temperature 
. 
 is the total number of bulk phases. 
 is the total heat addition to the gas phase from external sources and
     
 is the heat transfer rate from the bulk-phase 
 to the gas phase. Note that the latter also includes the enthalpy brought into
    the gas-phase from bulk-phase 
 due to the interphase interactions which are assumed to be happening at the
    temperature of the bulk phase (see Heat Transfer
    ). The first summation term corresponds to the effective
    inflow rate of the gas-phase enthalpy where 
, 
, and 
 indicate mass-inflow rate, enthalpy at the inlet temperature, and enthalpy at
    the gas-phase temperature in the reactor of gas-phase species 
, respectively. Note that the summation over all the inlets (when/if there are
    multiple inlets) is implied. This summation term is non-zero (applicable) only for the open
    reactor model.
Bulk phase:
| (9–4) | 
In Equation 9–4, molar basis is used and the ~
    accent indicates that the quantities are in molar units. The first summation on the right-hand
    side of the equation corresponds to the effective inflow rate of enthalpy for bulk-phase
      and summation over multiple inlets is implied.  
 is the total number of bulk phases, whereas  
 is the temperature and 
 the volume of the bulk-phase 
. The enthalpy of bulk species 
 in bulk-phase 
 at temperature 
 is indicated by 
. 
 is the total heat addition to the bulk phase 
 from external sources. 
 is the heat transfer rate from the bulk phase 
 to the bulk phase 
. As in the case for the gas phase, the interphase heat transfer includes the
    enthalpy gain/loss due to mass transfer. This mass transfer is assumed to be occurring at a
    corresponding phase temperature (see Heat Transfer
    ).). In this release of Ansys Chemkin, the effect of
     dPdt term (in the case of the given volume closed
    reactor) and enthalpy inflow term due to surface species attached to the bulk phase (in the case
    of open reactor) is ignored.