NaClFluidProperties

Fluid properties for NaCl

NaCl fluid properties as a function of pressure (Pa) and temperature (K).

note

Only solid state (halite) properties are currently implemented to use in brine formulation

Properties for halite given by Driesner (2007), apart from thermal conductivity, which is calculated using the data of Urqhart and Bauer (2015). Critical values are taken from Anderko and Pitzer (1992).

Properties of NaCl

Property	value
Molar mass	0.058443 kg/mol
Critical temperature	3841.15 K
Critical pressure	18.2 MPa
Critical density	108.43 kg/m $var element = document.getElementById("moose-equation-ec05fd2e-3851-4386-8b6e-fdc1524068c2");katex.render("^3", element, {displayMode:false,throwOnError:false,macros:{"\\eqc":"\\,,","\\eqp":"\\,.","\\pd":"\\frac{\\partial #1}{\\partial #2}","\\pr":"\\left(#1\\right)","\\ddt":"\\frac{d #1}{d t}"}});$
Triple point temperature	1073.85 K
Triple point pressure	50 Pa

Range of validity

The NaClFluidProperties UserObject is valid for the solid phase region only

Input Parameters

T_initial_guess400Temperature initial guess for Newton Method variable set conversion
Default:400
C++ Type:double
Unit:(no unit assumed)
Controllable:No
Description:Temperature initial guess for Newton Method variable set conversion
max_newton_its100Maximum number of Newton iterations for variable set conversions
Default:100
C++ Type:unsigned int
Controllable:No
Description:Maximum number of Newton iterations for variable set conversions
p_initial_guess200000Pressure initial guess for Newton Method variable set conversion
Default:200000
C++ Type:double
Unit:(no unit assumed)
Controllable:No
Description:Pressure initial guess for Newton Method variable set conversion
tolerance1e-08Tolerance for 2D Newton variable set conversion
Default:1e-08
C++ Type:double
Unit:(no unit assumed)
Controllable:No
Description:Tolerance for 2D Newton variable set conversion

Variable Set Conversions Newton Solve Parameters

allow_imperfect_jacobiansFalsetrue to allow unimplemented property derivative terms to be set to zero for the AD API
Default:False
C++ Type:bool
Controllable:No
Description:true to allow unimplemented property derivative terms to be set to zero for the AD API
control_tagsAdds user-defined labels for accessing object parameters via control logic.
C++ Type:std::vector<std::string>
Controllable:No
Description:Adds user-defined labels for accessing object parameters via control logic.
enableTrueSet the enabled status of the MooseObject.
Default:True
C++ Type:bool
Controllable:Yes
Description:Set the enabled status of the MooseObject.
fp_typesingle-phase-fpType of the fluid property object
Default:single-phase-fp
C++ Type:FPType
Controllable:No
Description:Type of the fluid property object

Advanced Parameters

prop_getter_suffixAn optional suffix parameter that can be appended to any attempt to retrieve/get material properties. The suffix will be prepended with a '_' character.
C++ Type:MaterialPropertyName
Unit:(no unit assumed)
Controllable:No
Description:An optional suffix parameter that can be appended to any attempt to retrieve/get material properties. The suffix will be prepended with a '_' character.
use_interpolated_stateFalseFor the old and older state use projected material properties interpolated at the quadrature points. To set up projection use the ProjectedStatefulMaterialStorageAction.
Default:False
C++ Type:bool
Controllable:No
Description:For the old and older state use projected material properties interpolated at the quadrature points. To set up projection use the ProjectedStatefulMaterialStorageAction.

Material Property Retrieval Parameters

References

A. Anderko and K. S. Pitzer. Equation of state for pure sodium chloride. Fluid Phase Equilibria, 79:103–112, 1992.

@article{anderko1992,
    author = "Anderko, A. and Pitzer, K. S.",
    title = "Equation of state for pure sodium chloride",
    journal = "Fluid Phase Equilibria",
    volume = "79",
    pages = "103--112",
    year = "1992"
}

T. Driesner. The system H$_2$O-NaCl. Part II: Correlations for molar volume, enthalpy, and isobaric heat capacity from 0 to 1000 C, 1 to 5000 bar, and 0 to 1 X$_NaCl$. Geochimica et Cosmochimica Acta, 71:4902–4919, 2007.

@article{driesner2007b,
    author = "Driesner, T.",
    title = "{The system H$\_2$O-NaCl. Part II: Correlations for molar volume, enthalpy, and isobaric heat capacity from 0 to 1000 C, 1 to 5000 bar, and 0 to 1 X$\_{NaCl}$}",
    journal = "Geochimica et Cosmochimica Acta",
    volume = "71",
    pages = "4902--4919",
    year = "2007"
}

A. Urqhart and S. Bauer. Experimental determination of single-crystal halite thermal conductivity, diffusivity and specific heat from -75 C to 300 C. Int. J. Rock Mech. and Mining Sci., 78:350–352, 2015.

@article{urqhart2015,
    author = "Urqhart, A. and Bauer, S.",
    title = "{Experimental determination of single-crystal halite thermal conductivity, diffusivity and specific heat from -75 C to 300 C}",
    journal = "Int. J. Rock Mech. and Mining Sci.",
    volume = "78",
    pages = "350--352",
    year = "2015"
}

Properties of NaCl
Range of validity
Input Parameters
References