# Species definitions

The following inputs are defined using the `species` prefix.

| Description | Type | Default
--- | --- | --- | ---
solve | Specified name of the species or None to disable the species solver. The name assigned to the species solver is used to specify species inputs. | String | None
diffusivity | Fluid species diffusivity model. `constant` a constant diffusion coefficient is used for all fluid species. | String | None
diffusivity.constant | Constant species diffusivity – required for `constant` diffusivity model | Real | 0
specific_heat | Species specific heat model. This setting only applies if either `fluid.specific_heat = mixture` or `solids.specific_heat = mixture` `constant` a constant specific heat is defined for each species and a mixture specific heat is computed based on the fluid or particle composition. `NASA7-poly` the specific heat of each species is defined by two polynomials that are a function of temperature, then a mixture specific heat is computed based on the fluid or particle composition. One polynomial defines the specific across the low temperature range while the second defines the specific heat across the high temperature range. NASA7 polynomial format: \(c_p(T) = \sum_{i=0}^5 a_iT^i\) | String | None

The following inputs are for each species defined using the `species.[species name]` prefix.

| Description | Type | Default
--- | --- | --- | ---
molecular_weight | Molecular weight of species. Required for mixture molecular weight model and when including chemical reactions. | Real | 0
specific_heat.constant | Constant species specific heat. Required for all fluid (solids) species if the fluid (solids) `specific_heat = mixture` and the specific heat model is `constant` | Real | 0
specific_heat.NASA7.a[i] | Species specific heat polynomial coefficients. Required for all fluid (solids) species if the fluid (solids) `specific_heat = mixture` and the specific heat model is `NASA7-poly` Each polynomial is defined by six coefficients (`a0` .. `a5`), and two values are required for each coefficient. The first value is the low temperature polynomial coefficient (T < 1000K) and the second is the coefficient for the high temperature polynomial (T > 1000K). A total of twelve coefficients are required. | Real |
enthalpy_of_formation | Enthalpy of formation of species. This input is required only when the specific heat model is `constant` and chemical reactions are defined. | Real | 0

## Example inputs

### Fluid species as passive scalars

In the following example, two species are defined and assigned to the fluid. We are required to define the species diffusivity and initial and boundary conditions. The `IncompressibleFluid` constraint is used, and the fluid density and species mass fractions are defined in the initial and boundary conditions. The fluid energy equation is not solved, and because we are not updating fluid density, the local species concentrations do not affect the fluid.

Listing 8 Snippet of inputs defining species as passive tracers. This is not a complete input file.

    mfix.constraint_type = IncompressibleFluid

    mfix.advect_density  = 0
    mfix.advect_enthalpy = 0
    mfix.solve_species   = 1

    # Species model settings
    # -----------------------------------------------------------------------
    species.solve  =  N2  O2

    species.diffusivity = constant
    species.diffusivity.constant  = 1.9e-5

    # Fluid model settings
    # -----------------------------------------------------------------------
    fluid.solve = fluid

    fluid.viscosity          = constant
    fluid.viscosity.constant = 2.0e-5

    fluid.species =  N2  O2

    # Initial Conditions
    # -----------------------------------------------------------------------
    ic.regions = full-domain

    ic.full-domain.fluid.volfrac   =  1.0
    ic.full-domain.fluid.density   =  1.0

    ic.full-domain.fluid.velocity  =  0.0  0.0  0.0

    ic.full-domain.fluid.species.N2   =  0.77
    ic.full-domain.fluid.species.O2   =  0.23

    # Boundary Conditions
    # -----------------------------------------------------------------------
    bc.regions = inlet  outlet

    bc.inlet = mi
    bc.inlet.fluid.volfrac  =  1.0
    bc.inlet.fluid.density  =  1.0

    bc.inlet.fluid.velocity =  1.0e-8  0.0  0.0

    bc.inlet.fluid.species.N2   =  0.77
    bc.inlet.fluid.species.O2   =  0.23

    bc.outlet = po
    bc.outlet.fluid.pressure =  0.

### Fluid as mixture

In this example, the fluid is treated as a mixture of two species and the `IdealGasOpenSystem` constraint is used. Because we are solving the energy equation, the fluid thermal conductivity is provided and the specific heats for both species are needed. The species specific heat model is set to `NASA7-poly`; therefore 12 coefficients (6 low-temperature range coefficients and 6 high-temperature range coefficients) are defined for each species. Additionally, species molecular weights are provided to compute the mixture molecular weights needed to evaluate the ideal-gas equation of state.

Fluid temperature is specified by the initial and boundary conditions, and unlike the previous example, density is no longer provided. Instead, the ideal gas equation of state is used to compute density from temperature, fluid composition, and the thermodynamic pressure. The thermodynamic pressure is taken as the outflow boundary condition pressure which is set here to 1 atmosphere.

Listing 9 Snippet of inputs defining fluid as a mixture with `NASA7-poly` specific heat model. This is not a complete input file.

    mfix.constraint_type = IdealGasOpenSystem

    mfix.advect_density  = 1
    mfix.solve_species   = 1
    mfix.advect_enthalpy = 1

    # Species model settings
    # -----------------------------------------------------------------------
    species.solve  =  N2  O2

    species.diffusivity = constant
    species.diffusivity.constant  = 1.9e-5

    species.O2.molecular_weight = 31.99880e-3
    species.N2.molecular_weight = 28.01340e-3

    species.specific_heat = NASA7-poly

    # Oxygen
    species.O2.molecular_weight = 31.99880e-3
    species.O2.specific_heat.NASA7.a0    =  3.78245636E+00    3.66096065E+00
    species.O2.specific_heat.NASA7.a1    = -2.99673416E-03    6.56365811E-04
    species.O2.specific_heat.NASA7.a2    =  9.84730201E-06   -1.41149627E-07
    species.O2.specific_heat.NASA7.a3    = -9.68129509E-09    2.05797935E-11
    species.O2.specific_heat.NASA7.a4    =  3.24372837E-12   -1.29913436E-15
    species.O2.specific_heat.NASA7.a5    = -1.06394356E+03   -1.21597718E+03

    # Nitrogen
    species.N2.molecular_weight = 28.01340e-3
    species.N2.specific_heat.NASA7.a0    =  3.53100528E+00    2.95257637E+00
    species.N2.specific_heat.NASA7.a1    = -1.23660988E-04    1.39690040E-03
    species.N2.specific_heat.NASA7.a2    = -5.02999433E-07   -4.92631603E-07
    species.N2.specific_heat.NASA7.a3    =  2.43530612E-09    7.86010195E-11
    species.N2.specific_heat.NASA7.a4    = -1.40881235E-12   -4.60755204E-15
    species.N2.specific_heat.NASA7.a5    = -1.04697628E+03   -9.23948688E+02

    # Fluid model settings
    # -----------------------------------------------------------------------
    fluid.solve = fluid

    fluid.viscosity          = constant
    fluid.viscosity.constant = 2.0e-5

    fluid.thermal_conductivity = constant
    fluid.thermal_conductivity.constant = 0.026

    fluid.specific_heat = mixture

    fluid.species =  N2  O2

    # Initial Conditions
    # -----------------------------------------------------------------------
    ic.regions = full-domain

    ic.full-domain.fluid.volfrac   =  1.0

    ic.full-domain.fluid.velocity  =  0.0  0.0  0.0

    ic.full-domain.fluid.species.N2  =  0.77
    ic.full-domain.fluid.species.O2  =  0.23

    ic.full-domain.fluid.temperature = 300.0

    # Boundary Conditions
    # -----------------------------------------------------------------------
    bc.regions = inlet  outlet

    bc.inlet = mi
    bc.inlet.fluid.volfrac  =  1.0

    bc.inlet.fluid.velocity =  1.0e-8  0.0  0.0

    bc.inlet.fluid.species.N2   = 0.77
    bc.inlet.fluid.species.O2   = 0.23

    bc.inlet.fluid.temperature = 300.0

    bc.outlet = po
    bc.outlet.fluid.pressure =  101325.