{
  "ANCILLARIES": {
    "hL": {
      "A": [
        -66887.37840747082,
        291.73652206456677,
        -0.2181091848225514,
        -0.0015362875652197962,
        1.0714140611396661e-05,
        -3.640566988137535e-08,
        6.091797307095861e-11,
        -4.1241149982826704e-14
      ],
      "B": [
        1,
        -0.0024986373485216275
      ],
      "Tmax": 395.325,
      "Tmin": 120.0,
      "_note": "coefficients are in increasing order; input in K, output in J/mol; value is enthalpy minus hs_anchor enthalpy",
      "max_abs_error": 330.6602061558506,
      "max_abs_error_units": "J/mol",
      "type": "rational_polynomial"
    },
    "hLV": {
      "A": [
        36055.98008069073,
        -39.629697688492925,
        -1.8752360575236096,
        0.01690686417048871,
        -7.694669613128332e-05,
        1.981423039066895e-07,
        -2.750767123861438e-10,
        1.6192299912661107e-13
      ],
      "B": [
        1,
        -0.0024972889149895514
      ],
      "Tmax": 395.325,
      "Tmin": 120.0,
      "_note": "coefficients are in increasing order; input in K, output in J/mol; value is enthalpy minus hs_anchor enthalpy",
      "max_abs_error": 745.6636833641032,
      "max_abs_error_units": "J/mol",
      "type": "rational_polynomial"
    },
    "pS": {
      "T_r": 395.425,
      "Tmax": 395.42499999999933,
      "Tmin": 120.00000000000001,
      "description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
      "max_abserror_percentage": 0.011933999782232085,
      "n": [
        -5.532034162429256,
        -4.742002285997961,
        4.083301102214,
        -0.8556260869752595,
        -3.759805971191399,
        -5.094637151194883
      ],
      "reducing_value": 3624295.0,
      "t": [
        1.003,
        1.051,
        1.163,
        2.188,
        4.015,
        19.693
      ],
      "type": "pL",
      "using_tau_r": true
    },
    "rhoL": {
      "T_r": 395.425,
      "Tmax": 395.42499999999933,
      "Tmin": 120.00000000000001,
      "description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
      "max_abserror_percentage": 0.24061336574978665,
      "n": [
        9.076759200951095,
        -17.685013904231155,
        59.69226551115479,
        -48.46415018361892,
        0.6023234565910854,
        -1.0939055527121821
      ],
      "reducing_value": 4103.279546177282,
      "t": [
        0.482,
        0.651,
        0.881,
        0.914,
        5.001,
        10.577
      ],
      "type": "rhoLnoexp",
      "using_tau_r": false
    },
    "rhoV": {
      "T_r": 395.425,
      "Tmax": 395.42499999999933,
      "Tmin": 120.00000000000001,
      "description": "rho'' = rhoc*exp(Tc/T*sum(n_i*theta^t_i))",
      "max_abserror_percentage": 0.412713645894236,
      "n": [
        -3.6411060779677857,
        0.3822304251070335,
        -19.603560148262865,
        181.0410898999192,
        -168.52216602298836,
        -2.5180916684231893
      ],
      "reducing_value": 4103.279546177282,
      "t": [
        0.415,
        0.5,
        1.704,
        2.307,
        2.394,
        13.161
      ],
      "type": "rhoV",
      "using_tau_r": true
    },
    "sL": {
      "A": [
        -442.69143178508324,
        4.964636481149071,
        -0.033630347863136026,
        0.00016164634063050705,
        -5.126126415257726e-07,
        1.0043086991519815e-09,
        -1.1025106238746766e-12,
        5.169645731454473e-16
      ],
      "B": [
        1,
        -0.002489541440275261
      ],
      "Tmax": 395.325,
      "Tmin": 120.0,
      "_note": "coefficients are in increasing order; input in K, output in J/mol/K; value is entropy minus hs_anchor entropy",
      "max_abs_error": 0.9540366882595421,
      "max_abs_error_units": "J/mol/K",
      "type": "rational_polynomial"
    },
    "sLV": {
      "A": [
        1301.1817199911154,
        -23.136058272300183,
        0.20520027749999042,
        -0.0010955811926783316,
        3.647452193433386e-06,
        -7.421394987167461e-09,
        8.452876398700314e-12,
        -4.1287274609476215e-15
      ],
      "B": [
        1,
        -0.002464387299890532
      ],
      "Tmax": 395.325,
      "Tmin": 120.0,
      "_note": "coefficients are in increasing order; input in K, output in J/mol/K; value is entropy minus hs_anchor entropy",
      "max_abs_error": 2.6116792652106025,
      "max_abs_error_units": "J/mol/K",
      "type": "rational_polynomial"
    },
    "surface_tension": {
      "BibTeX": "Mulero-JPCRD-2012",
      "Tc": 395.425,
      "a": [
        0.05175
      ],
      "description": "sigma = sum(a_i*(1-T/Tc)^n_i)",
      "n": [
        1.197
      ]
    }
  },
  "EOS": [
    {
      "BibTeX_CP0": "",
      "BibTeX_EOS": "deVries-ICR-1995",
      "STATES": {
        "hs_anchor": {
          "T": 434.96750000000003,
          "T_units": "K",
          "hmolar": 58393.30275454103,
          "hmolar_units": "J/mol",
          "p": 6063856.182495852,
          "p_units": "Pa",
          "rhomolar": 3692.951591559554,
          "rhomolar_units": "mol/m^3",
          "smolar": 221.4864314659426,
          "smolar_units": "J/mol/K"
        },
        "reducing": {
          "T": 395.425,
          "T_units": "K",
          "hmolar": 51702.03879706071,
          "hmolar_units": "J/mol",
          "p": 3624295,
          "p_units": "Pa",
          "rhomolar": 4103.279546177282,
          "rhomolar_units": "mol/m^3",
          "smolar": 206.85527832672045,
          "smolar_units": "J/mol/K"
        },
        "sat_min_liquid": {
          "T": 120.0,
          "T_units": "K",
          "hmolar": 6701.784158335417,
          "hmolar_units": "J/mol",
          "p": 0.026738623617928323,
          "p_units": "Pa",
          "rhomolar": 13575.607811207094,
          "rhomolar_units": "mol/m^3",
          "smolar": 27.106870278931343,
          "smolar_units": "J/mol/K"
        },
        "sat_min_vapor": {
          "T": 120.0,
          "T_units": "K",
          "hmolar": 37724.91375665319,
          "hmolar_units": "J/mol",
          "p": 0.02673846118338111,
          "p_units": "Pa",
          "rhomolar": 2.6799128836333592e-05,
          "rhomolar_units": "mol/m^3",
          "smolar": 285.6329247088121,
          "smolar_units": "J/mol/K"
        }
      },
      "T_max": 470,
      "T_max_units": "K",
      "Ttriple": 75,
      "Ttriple_units": "K",
      "acentric": 0.2880950842214292,
      "acentric_units": "-",
      "alpha0": [
        {
          "a1": -11.669406,
          "a2": 9.8760443,
          "type": "IdealGasHelmholtzLead"
        },
        {
          "a": 2.175638,
          "type": "IdealGasHelmholtzLogTau"
        },
        {
          "n": [
            -7.389735,
            0.8736831,
            -0.1115133
          ],
          "t": [
            -1,
            -2,
            -3
          ],
          "type": "IdealGasHelmholtzPower"
        },
        {
          "a1": -0.000144036507408073,
          "a2": 7.30088431548676e-05,
          "reference": "IIR",
          "type": "IdealGasHelmholtzEnthalpyEntropyOffset"
        }
      ],
      "alphar": [
        {
          "d": [
            1,
            1,
            1,
            2,
            2,
            3,
            5,
            6,
            8,
            2,
            12,
            1,
            1,
            1,
            1,
            15,
            3,
            3,
            4,
            9
          ],
          "l": [
            0,
            0,
            0,
            0,
            0,
            0,
            0,
            0,
            0,
            1,
            1,
            2,
            2,
            2,
            2,
            2,
            3,
            3,
            4,
            4
          ],
          "n": [
            -0.01262962,
            2.168373,
            -3.330033,
            0.1610361,
            -9.666145e-05,
            0.0119131,
            -0.002880217,
            0.001681346,
            1.594968e-05,
            0.1289674,
            1.182213e-05,
            -0.4713997,
            -0.2412873,
            0.6868066,
            -0.08621095,
            4.728645e-06,
            0.01487933,
            -0.03001338,
            0.001849606,
            0.0004126073
          ],
          "t": [
            2,
            0.5,
            1,
            0.5,
            2.5,
            -1,
            1,
            0,
            -0.5,
            1.5,
            1,
            2.5,
            -0.25,
            1,
            5,
            2,
            15,
            20,
            15,
            45
          ],
          "type": "ResidualHelmholtzPower"
        }
      ],
      "gas_constant": 8.314471,
      "gas_constant_units": "J/mol/K",
      "molar_mass": 0.1364762,
      "molar_mass_units": "kg/mol",
      "p_max": 40000000,
      "p_max_units": "Pa",
      "pseudo_pure": false
    }
  ],
  "INFO": {
    "2DPNG_URL": "http://www.chemspider.com/ImagesHandler.ashx?id=16841",
    "ALIASES": [],
    "CAS": "2837-89-0",
    "CHEMSPIDER_ID": 16841,
    "ENVIRONMENTAL": {
      "ASHRAE34": "A1",
      "FH": 1,
      "GWP100": 609.0,
      "GWP20": 2070.0,
      "GWP500": 185.0,
      "HH": 1,
      "Name": "R124",
      "ODP": 0.022,
      "PH": 0
    },
    "FORMULA": "C_{2}Cl_{1}F_{4}H_{1}",
    "INCHI_KEY": "BOUGCJDAQLKBQH-UHFFFAOYSA-N",
    "INCHI_STRING": "InChI=1S/C2HClF4/c3-1(4)2(5,6)7/h1H",
    "NAME": "R124",
    "REFPROP_NAME": "R124",
    "SMILES": "C(C(F)(F)F)(F)Cl"
  },
  "STATES": {
    "critical": {
      "T": 395.425,
      "T_units": "K",
      "hmolar": 51696.2811525728,
      "hmolar_units": "J/mol",
      "p": 3624295.0,
      "p_units": "Pa",
      "rhomolar": 4103.279546177282,
      "rhomolar_units": "mol/m^3",
      "smolar": 206.84238695903932,
      "smolar_units": "J/mol/K"
    },
    "triple_liquid": {
      "T": 120.0,
      "T_units": "K",
      "hmolar": 6701.784158335417,
      "hmolar_units": "J/mol",
      "p": 0.026738623617928323,
      "p_units": "Pa",
      "rhomolar": 13575.607811207094,
      "rhomolar_units": "mol/m^3",
      "smolar": 27.106870278931343,
      "smolar_units": "J/mol/K"
    },
    "triple_vapor": {
      "T": 120.0,
      "T_units": "K",
      "hmolar": 37724.91375665319,
      "hmolar_units": "J/mol",
      "p": 0.02673846118338111,
      "p_units": "Pa",
      "rhomolar": 2.6799128836333592e-05,
      "rhomolar_units": "mol/m^3",
      "smolar": 285.6329247088121,
      "smolar_units": "J/mol/K"
    }
  },
  "TRANSPORT": {
    "conductivity": {
      "BibTeX": "Huber-IECR-2003",
      "f_int": {
        "T_reducing": 1.0,
        "T_reducing_units": "K",
        "a": [
          0.0011769,
          6.78397e-07
        ],
        "t": [
          0,
          1
        ]
      },
      "psi": {
        "a": [
          1.0898,
          -0.0154229
        ],
        "rhomolar_reducing": 4103.0,
        "rhomolar_reducing_units": "mol/m^3",
        "t": [
          0,
          1
        ]
      },
      "q_D": 1999999999.9999998,
      "q_D_units": "m",
      "reference_fluid": "Propane",
      "type": "ECS"
    },
    "viscosity": [
      {
        "BibTeX": "Bell-PURDUE-2016-ETA",
        "C": 0.99792,
        "c_liq": [
          0.6100913843,
          0.4508958312,
          -0.017063,
          0.000564
        ],
        "c_vap": [
          0.0,
          1.2,
          -0.308598,
          0.035317
        ],
        "rhosr_critical": -53640.36876934566,
        "type": "rhosr-CS",
        "x_crossover": 2
      },
      {
        "BibTeX": "Huber-IECR-2003",
        "epsilon_over_k": 275.8,
        "epsilon_over_k_units": "K",
        "psi": {
          "a": [
            1.04253,
            0.00138528,
            0.0
          ],
          "rhomolar_reducing": 4103.0,
          "rhomolar_reducing_units": "mol/m^3",
          "t": [
            0,
            1,
            2
          ]
        },
        "reference_fluid": "Propane",
        "sigma_eta": 5.501000000000001e-10,
        "sigma_eta_units": "m",
        "type": "ECS"
      }
    ]
  }
}