Mixing two streams

Since reactors can have multiple inlets and outlets, they can be used to implement mixers, splitters, etc. In this example, air and methane are mixed in stoichiometric proportions. Due to the low temperature, no reactions occur. Note that the air stream and the methane stream use different reaction mechanisms, with different numbers of species and reactions. When gas flows from one reactor or reservoir to another one with a different reaction mechanism, species are matched by name. If the upstream reactor contains a species that is not present in the downstream reaction mechanism, it will be ignored. In general, reaction mechanisms for downstream reactors should contain all species that might be present in any upstream reactor.

Compare this approach for the transient problem to the method used for the steady-state problem in mixing.py.

Requires: cantera >= 2.5.0

Tags: Python thermodynamics reactor network mixture

 gri30:

      temperature   300 K
         pressure   1.0133e+05 Pa
          density   1.1361 kg/m^3
 mean mol. weight   27.968 kg/kmol
  phase of matter   gas

                         1 kg             1 kmol
                    ---------------   ---------------
         enthalpy        -2.047e+05        -5.725e+06  J
  internal energy       -2.9388e+05       -8.2194e+06  J
          entropy            7158.8        2.0022e+05  J/K
   Gibbs function       -2.3523e+06       -6.5791e+07  J
heat capacity c_p            1057.5             29578  J/K
heat capacity c_v            760.26             21263  J/K

                     mass frac. Y      mole frac. X     chem. pot. / RT
                    ---------------   ---------------   ---------------
               O2           0.22164           0.19373           -26.315
              CH4           0.04445          0.077491            -54.88
               N2           0.72073           0.71956           -23.362
               AR          0.013177         0.0092251           -23.296
    [  +49 minor]       -4.9702e-29       -8.6629e-29

import cantera as ct

# Use air for stream a.
gas_a = ct.Solution('air.yaml')
gas_a.TPX = 300.0, ct.one_atm, 'O2:0.21, N2:0.78, AR:0.01'
rho_a = gas_a.density


# Use GRI-Mech 3.0 for stream b (methane) and for the mixer. If it is desired
# to have a pure mixer, with no chemistry, use instead a reaction mechanism
# for gas_b that has no reactions.
gas_b = ct.Solution('gri30.yaml')
gas_b.TPX = 300.0, ct.one_atm, 'CH4:1'
rho_b = gas_b.density

# Create reservoirs for the two inlet streams and for the outlet stream.  The
# upsteam reservoirs could be replaced by reactors, which might themselves be
# connected to reactors further upstream. The outlet reservoir could be
# replaced with a reactor with no outlet, if it is desired to integrate the
# composition leaving the mixer in time, or by an arbitrary network of
# downstream reactors.
res_a = ct.Reservoir(gas_a)
res_b = ct.Reservoir(gas_b)
downstream = ct.Reservoir(gas_b)

# Create a reactor for the mixer. A reactor is required instead of a
# reservoir, since the state will change with time if the inlet mass flow
# rates change or if there is chemistry occurring.
gas_b.TPX = 300.0, ct.one_atm, 'O2:0.21, N2:0.78, AR:0.01'
mixer = ct.IdealGasReactor(gas_b)

# create two mass flow controllers connecting the upstream reservoirs to the
# mixer, and set their mass flow rates to values corresponding to
# stoichiometric combustion.
mfc1 = ct.MassFlowController(res_a, mixer, mdot=rho_a*2.5/0.21)
mfc2 = ct.MassFlowController(res_b, mixer, mdot=rho_b*1.0)

# connect the mixer to the downstream reservoir with a valve.
outlet = ct.Valve(mixer, downstream, K=10.0)

sim = ct.ReactorNet([mixer])

# Since the mixer is a reactor, we need to integrate in time to reach steady
# state
sim.advance_to_steady_state()

# view the state of the gas in the mixer
print(mixer.thermo.report())