- InChI
- InChI=1S/CH2F2/c2-1-3/h1H2
- InChI Key
- RWRIWBAIICGTTQ-UHFFFAOYSA-N
- Formula
- CH2F2
- SMILES
- FCF
- Molecular Weight1
- 52.02
- CAS
- 75-10-5
- Other Names
-
- CH2F2
- Carbon fluoride hydride
- Freon 32
- Genetron 32
- HFC 32
- Methane, difluoro-
- Methylene difluoride
- Methylene fluoride
- R 32
- R 32 (refrigerant)
- R-32
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°gas : Standard gas enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- ν : Kinematic viscosity (m2/s).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρg : Gas Density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| PAff | 620.50 | kJ/mol | NIST |
| BasG | 589.70 | kJ/mol | NIST |
| ΔcH°gas | -583.08 | kJ/mol | NIST |
| ΔfG° | -432.08 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -452.21 ± 0.92 | kJ/mol | NIST |
| ΔfusH° | 4.51 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 16.19 | kJ/mol | Joback Calculated Property |
| IE | [12.70; 13.27] | eV |
|
| IE | 12.71 | eV | NIST |
| IE | 12.70 | eV | NIST |
| IE | 12.72 | eV | NIST |
| IE | 13.27 | eV | NIST |
| log10WS | -0.44 | Crippen Calculated Property | |
| logPoct/wat | 0.883 | Crippen Calculated Property | |
| McVol | 28.490 | ml/mol | McGowan Calculated Property |
| Pc | [5784.00; 5785.00] | kPa |
|
| Pc | 5785.00 ± 3.00 | kPa | NIST |
| Pc | 5785.00 ± 4.00 | kPa | NIST |
| Pc | 5785.00 ± 9.00 | kPa | NIST |
| Pc | 5784.00 ± 2.50 | kPa | NIST |
| Inp | [183.00; 230.00] |
|
|
| Inp | 230.00 | NIST | |
| Inp | 183.00 | NIST | |
| Inp | 230.00 | NIST | |
| Tboil | [221.00; 221.60] | K |
|
| Tboil | 221.40 | K | NIST |
| Tboil | 221.00 ± 2.00 | K | NIST |
| Tboil | 221.60 ± 0.30 | K | NIST |
| Tboil | 221.60 ± 1.00 | K | NIST |
| Tc | [351.14; 351.29] | K |
|
| Tc | 351.29 ± 0.02 | K | NIST |
| Tc | Outlier 351.14 ± 0.30 | K | NIST |
| Tc | 351.29 ± 0.03 | K | NIST |
| Tc | 351.26 ± 0.05 | K | NIST |
| Tc | 351.25 ± 0.03 | K | NIST |
| Tc | 351.26 ± 0.03 | K | NIST |
| Tfus | 102.21 | K | Joback Calculated Property |
| Vc | 0.128 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [38.23; 50.16] | J/mol×K | [220.82; 355.03] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 38 40 42 44 46 48 50 250 300 350 | ||||
| Cp,gas | 38.23 | J/mol×K | 220.82 | Joback Calculated Property |
| Cp,gas | 40.35 | J/mol×K | 243.19 | Joback Calculated Property |
| Cp,gas | 42.42 | J/mol×K | 265.56 | Joback Calculated Property |
| Cp,gas | 44.43 | J/mol×K | 287.93 | Joback Calculated Property |
| Cp,gas | 46.39 | J/mol×K | 310.29 | Joback Calculated Property |
| Cp,gas | 48.30 | J/mol×K | 332.66 | Joback Calculated Property |
| Cp,gas | 50.16 | J/mol×K | 355.03 | Joback Calculated Property |
| Cp,liquid | [106.65; 164.39] | J/mol×K | [310.00; 340.00] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 110 120 130 140 150 160 170 310 320 330 340 | ||||
| Cp,liquid | 106.65 | J/mol×K | 310.00 | Measure... |
| Cp,liquid | 109.77 | J/mol×K | 315.00 | Measure... |
| Cp,liquid | 113.41 | J/mol×K | 320.00 | Measure... |
| Cp,liquid | 119.65 | J/mol×K | 325.00 | Measure... |
| Cp,liquid | 125.90 | J/mol×K | 330.00 | Measure... |
| Cp,liquid | 138.90 | J/mol×K | 335.00 | Measure... |
| Cp,liquid | 164.39 | J/mol×K | 340.00 | Measure... |
| ΔfusH | [4.36; 4.40] | kJ/mol | [136.40; 136.40] |
|
| ΔfusH | 4.36 | kJ/mol | 136.40 | NIST |
| ΔfusH | 4.40 | kJ/mol | 136.40 | NIST |
| ΔvapH | [19.90; 21.20] | kJ/mol | [197.00; 333.50] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 19.8 20 20.2 20.4 20.6 20.8 21 21.2 200 250 300 | ||||
| ΔvapH | 20.60 | kJ/mol | 197.00 | NIST |
| ΔvapH | 21.20 | kJ/mol | 206.00 | NIST |
| ΔvapH | 21.20 | kJ/mol | 206.50 | NIST |
| ΔvapH | 20.60 | kJ/mol | 216.50 | NIST |
| ΔvapH | 20.30 | kJ/mol | 224.50 | NIST |
| ΔvapH | 19.90 | kJ/mol | 288.50 | NIST |
| ΔvapH | 20.30 | kJ/mol | 333.50 | NIST |
| ν | [7.5000000e-08; 0.0000001] | m2/s | [293.15; 348.18] |
|
|
T(K) Kinematic viscosity (m2/s) 7.00e-8 8.00e-8 9.00e-8 1.00e-7 1.10e-7 1.20e-7 1.30e-7 300 320 340 | ||||
| ν | 0.0000001 | m2/s | 293.15 | Surface... |
| ν | 0.0000001 | m2/s | 303.15 | Surface... |
| ν | 0.0000001 | m2/s | 313.07 | Surface... |
| ν | 9.9800000e-08 | m2/s | 323.15 | Surface... |
| ν | 9.3000000e-08 | m2/s | 333.14 | Surface... |
| ν | 7.9500000e-08 | m2/s | 343.16 | Surface... |
| ν | 7.5000000e-08 | m2/s | 348.18 | Surface... |
| Pvap | [488.10; 5392.00] | kPa | [258.15; 347.89] |
|
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 300 350 | ||||
| Pvap | 488.10 | kPa | 258.15 | Vapor-l... |
| Pvap | 488.10 | kPa | 258.15 | Isother... |
| Pvap | 580.20 | kPa | 263.15 | Vapor-L... |
| Pvap | 624.10 | kPa | 265.15 | Vapor-L... |
| Pvap | 695.40 | kPa | 268.15 | Vapor-L... |
| Pvap | 690.60 | kPa | 268.15 | Vapor-l... |
| Pvap | 814.00 | kPa | 273.15 | Isother... |
| Pvap | 816.80 | kPa | 273.15 | Measure... |
| Pvap | 866.50 | kPa | 275.15 | Vapor-l... |
| Pvap | 866.50 | kPa | 275.15 | Vapor-L... |
| Pvap | 949.60 | kPa | 278.15 | Vapor-L... |
| Pvap | 952.00 | kPa | 278.15 | Vapor-L... |
| Pvap | 1022.00 | kPa | 280.59 | Experim... |
| Pvap | 1109.00 | kPa | 283.05 | Experim... |
| Pvap | 1106.20 | kPa | 283.15 | Vapor-L... |
| Pvap | 1102.20 | kPa | 283.15 | Vapor-L... |
| Pvap | 1107.00 | kPa | 283.15 | Vapor-L... |
| Pvap | 1107.00 | kPa | 283.15 | Vapor-l... |
| Pvap | 1111.80 | kPa | 283.15 | Measure... |
| Pvap | 1107.30 | kPa | 283.15 | Vapor l... |
| Pvap | 1107.30 | kPa | 283.15 | Isother... |
| Pvap | 1111.00 | kPa | 283.19 | Vapor-L... |
| Pvap | 1195.00 | kPa | 285.52 | Experim... |
| Pvap | 1280.00 | kPa | 288.02 | Experim... |
| Pvap | 1281.20 | kPa | 288.15 | Vapor-L... |
| Pvap | 1279.90 | kPa | 288.15 | Vapor-L... |
| Pvap | 1280.60 | kPa | 288.15 | Isother... |
| Pvap | 1286.00 | kPa | 288.21 | Vapor-L... |
| Pvap | 1364.00 | kPa | 290.46 | Experim... |
| Pvap | 1474.00 | kPa | 293.02 | Experim... |
| Pvap | 1474.00 | kPa | 293.15 | Isother... |
| Pvap | 1474.00 | kPa | 293.15 | Vapor l... |
| Pvap | 1475.00 | kPa | 293.15 | Vapor-l... |
| Pvap | 1473.20 | kPa | 293.15 | Vapor-L... |
| Pvap | 1473.20 | kPa | 293.15 | Experim... |
| Pvap | 1475.00 | kPa | 293.15 | Vapor-L... |
| Pvap | 1480.20 | kPa | 293.15 | Measure... |
| Pvap | 1474.60 | kPa | 293.15 | Isother... |
| Pvap | 1473.70 | kPa | 293.16 | Vapor-L... |
| Pvap | 1481.00 | kPa | 293.24 | Vapor-L... |
| Pvap | 1578.00 | kPa | 295.49 | Experim... |
| Pvap | 1684.00 | kPa | 298.01 | Experim... |
| Pvap | 1685.60 | kPa | 298.15 | Vapor-L... |
| Pvap | 1688.40 | kPa | 298.16 | Vapor-L... |
| Pvap | 1689.50 | kPa | 298.17 | Isother... |
| Pvap | 1697.00 | kPa | 298.26 | Vapor-L... |
| Pvap | 1793.00 | kPa | 300.48 | Experim... |
| Pvap | 1918.00 | kPa | 302.94 | Experim... |
| Pvap | 1925.80 | kPa | 303.14 | Isother... |
| Pvap | 1925.30 | kPa | 303.15 | Vapor-L... |
| Pvap | 1928.00 | kPa | 303.15 | Vapor-l... |
| Pvap | 1925.80 | kPa | 303.15 | Vapor l... |
| Pvap | 1930.40 | kPa | 303.15 | Measure... |
| Pvap | 1926.70 | kPa | 303.15 | Experim... |
| Pvap | 1925.00 | kPa | 303.15 | Vapor-L... |
| Pvap | 1935.00 | kPa | 303.27 | Vapor-L... |
| Pvap | 2051.00 | kPa | 305.46 | Experim... |
| Pvap | 2179.00 | kPa | 307.91 | Experim... |
| Pvap | 2188.30 | kPa | 308.15 | Vapor-L... |
| Pvap | 2188.20 | kPa | 308.15 | Isother... |
| Pvap | 2185.20 | kPa | 308.15 | Vapor-L... |
| Pvap | 2197.00 | kPa | 308.28 | Vapor-L... |
| Pvap | 2318.00 | kPa | 310.48 | Experim... |
| Pvap | 2459.00 | kPa | 312.90 | Experim... |
| Pvap | 2476.20 | kPa | 313.15 | Isother... |
| Pvap | 2476.30 | kPa | 313.15 | Experim... |
| Pvap | 2476.00 | kPa | 313.15 | Vapor-L... |
| Pvap | 2469.00 | kPa | 313.15 | Vapor-L... |
| Pvap | 2478.00 | kPa | 313.15 | Measure... |
| Pvap | 2478.00 | kPa | 313.15 | Vapor-l... |
| Pvap | 2475.90 | kPa | 313.15 | Vapor-L... |
| Pvap | 2476.20 | kPa | 313.15 | Vapor l... |
| Pvap | 2485.00 | kPa | 313.30 | Vapor-L... |
| Pvap | 2614.00 | kPa | 315.43 | Experim... |
| Pvap | 2772.00 | kPa | 317.89 | Experim... |
| Pvap | 2791.60 | kPa | 318.14 | Isother... |
| Pvap | 2794.80 | kPa | 318.15 | Vapor-L... |
| Pvap | 2792.00 | kPa | 318.15 | Vapor-L... |
| Pvap | 2801.00 | kPa | 318.28 | Vapor-L... |
| Pvap | 2948.00 | kPa | 320.41 | Experim... |
| Pvap | 3120.00 | kPa | 322.92 | Experim... |
| Pvap | 3142.20 | kPa | 323.14 | Experim... |
| Pvap | 3138.00 | kPa | 323.14 | Isother... |
| Pvap | 3137.60 | kPa | 323.15 | Vapor-L... |
| Pvap | 3137.00 | kPa | 323.15 | Vapor-L... |
| Pvap | 3141.00 | kPa | 323.15 | Vapor-l... |
| Pvap | 3138.00 | kPa | 323.15 | Vapor l... |
| Pvap | 3138.00 | kPa | 323.15 | Vapor-L... |
| Pvap | 3147.00 | kPa | 323.30 | Vapor-L... |
| Pvap | 3303.00 | kPa | 325.42 | Experim... |
| Pvap | 3498.00 | kPa | 327.90 | Experim... |
| Pvap | 3526.00 | kPa | 328.31 | Vapor-L... |
| Pvap | 3694.00 | kPa | 330.35 | Experim... |
| Pvap | 3910.00 | kPa | 332.91 | Experim... |
| Pvap | 3933.00 | kPa | 333.15 | Vapor-l... |
| Pvap | 3933.00 | kPa | 333.15 | Vapor-L... |
| Pvap | 3934.00 | kPa | 333.15 | Vapor-L... |
| Pvap | 4138.00 | kPa | 335.40 | Experim... |
| Pvap | 4370.00 | kPa | 337.93 | Experim... |
| Pvap | 4602.00 | kPa | 340.43 | Experim... |
| Pvap | 4854.00 | kPa | 342.88 | Experim... |
| Pvap | 4884.00 | kPa | 343.15 | Vapor-L... |
| Pvap | 4877.00 | kPa | 343.15 | Vapor-l... |
| Pvap | 4892.00 | kPa | 343.26 | Vapor-L... |
| Pvap | 5117.00 | kPa | 345.40 | Experim... |
| Pvap | 5392.00 | kPa | 347.89 | Experim... |
| γ | [0.00; 0.01] | N/m | [252.74; 332.00] |
|
|
T(K) Surface Tension (N/m) 2.00e-3 4.00e-3 6.00e-3 8.00e-3 0.01 0.01 0.01 260 280 300 320 | ||||
| γ | 0.01 | N/m | 252.74 | Surface... |
| γ | 0.01 | N/m | 252.74 | Surface... |
| γ | 0.01 | N/m | 257.00 | Surface... |
| γ | 0.01 | N/m | 257.00 | Surface... |
| γ | 0.01 | N/m | 260.46 | Surface... |
| γ | 0.01 | N/m | 260.46 | Surface... |
| γ | 0.01 | N/m | 265.04 | Surface... |
| γ | 0.01 | N/m | 265.04 | Surface... |
| γ | 0.01 | N/m | 268.75 | Surface... |
| γ | 0.01 | N/m | 268.75 | Surface... |
| γ | 0.01 | N/m | 273.28 | Surface... |
| γ | 0.01 | N/m | 273.28 | Surface... |
| γ | 0.01 | N/m | 276.85 | Surface... |
| γ | 0.01 | N/m | 276.85 | Surface... |
| γ | 0.01 | N/m | 281.50 | Surface... |
| γ | 0.01 | N/m | 281.50 | Surface... |
| γ | 0.01 | N/m | 285.79 | Surface... |
| γ | 0.01 | N/m | 285.79 | Surface... |
| γ | 0.01 | N/m | 294.05 | Surface... |
| γ | 0.01 | N/m | 294.05 | Surface... |
| γ | 0.01 | N/m | 297.58 | Surface... |
| γ | 0.01 | N/m | 297.58 | Surface... |
| γ | 0.01 | N/m | 301.42 | Surface... |
| γ | 0.01 | N/m | 301.42 | Surface... |
| γ | 0.01 | N/m | 305.30 | Surface... |
| γ | 0.01 | N/m | 305.30 | Surface... |
| γ | 0.01 | N/m | 309.50 | Surface... |
| γ | 0.01 | N/m | 309.50 | Surface... |
| γ | 0.00 | N/m | 315.58 | Surface... |
| γ | 0.00 | N/m | 315.58 | Surface... |
| γ | 0.00 | N/m | 319.38 | Surface... |
| γ | 0.00 | N/m | 319.38 | Surface... |
| γ | 0.00 | N/m | 319.84 | Surface... |
| γ | 0.00 | N/m | 319.84 | Surface... |
| γ | 0.00 | N/m | 323.29 | Surface... |
| γ | 0.00 | N/m | 323.29 | Surface... |
| γ | 0.00 | N/m | 327.23 | Surface... |
| γ | 0.00 | N/m | 327.23 | Surface... |
| γ | 0.00 | N/m | 332.00 | Surface... |
| γ | 0.00 | N/m | 332.00 | Surface... |
Datasets
Molar heat capacity at constant volume, J/K/mol
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Molar heat capacity at constant volume, J/K/mol - Liquid |
| 268.15 | 8268.00 | 49.4742 |
| 268.15 | 8502.00 | 48.7979 |
| 269.15 | 9280.00 | 49.3182 |
| 269.15 | 9512.00 | 49.6823 |
| 270.15 | 10291.00 | 49.4742 |
| 270.15 | 10521.00 | 49.8384 |
| 271.15 | 11302.00 | 49.4222 |
| 271.15 | 11531.00 | 49.5263 |
| 272.15 | 12312.00 | 49.9425 |
| 272.15 | 12421.00 | 50.5667 |
| 272.15 | 12540.00 | 49.0581 |
| 273.15 | 13321.00 | 49.0581 |
| 273.15 | 13429.00 | 49.7864 |
| 273.15 | 13551.00 | 50.2546 |
| 274.15 | 14330.00 | 49.9425 |
| 274.15 | 14438.00 | 49.6303 |
| 274.15 | 14560.00 | 49.3702 |
| 275.15 | 15337.00 | 49.4742 |
| 275.15 | 15444.00 | 49.8384 |
| 275.15 | 15568.00 | 49.4742 |
| 276.15 | 16344.00 | 49.8904 |
| 276.15 | 16452.00 | 49.8384 |
| 276.15 | 16577.00 | 49.7344 |
| 277.15 | 17350.00 | 49.3182 |
| 277.15 | 17457.00 | 49.6303 |
| 277.15 | 17583.00 | 49.9945 |
| 278.15 | 18354.00 | 49.8904 |
| 278.15 | 18462.00 | 50.2546 |
| 278.15 | 18589.00 | 49.4742 |
| 279.15 | 19358.00 | 49.8904 |
| 279.15 | 19465.00 | 49.7864 |
| 279.15 | 19595.00 | 50.1505 |
| 280.15 | 20361.00 | 49.6303 |
| 280.15 | 20468.00 | 50.2026 |
| 280.15 | 20598.00 | 49.9945 |
| 281.15 | 21363.00 | 50.4627 |
| 281.15 | 21470.00 | 49.6303 |
| 281.15 | 21601.00 | 49.8904 |
| 282.15 | 22363.00 | 49.5783 |
| 282.15 | 22472.00 | 50.2546 |
| 282.15 | 22602.00 | 50.0465 |
| 283.15 | 23363.00 | 50.4107 |
| 283.15 | 23473.00 | 50.1505 |
| 283.15 | 23603.00 | 49.9425 |
| 284.15 | 24362.00 | 50.3066 |
| 284.15 | 24472.00 | 49.9425 |
| 284.15 | 24606.00 | 50.2546 |
| 285.15 | 25359.00 | 50.1505 |
| 285.15 | 25470.00 | 50.5147 |
| 285.15 | 25603.00 | 50.2546 |
| 286.15 | 26356.00 | 50.5147 |
| 286.15 | 26466.00 | 50.6188 |
| 286.15 | 26598.00 | 50.2026 |
| 287.15 | 27351.00 | 50.3586 |
| 287.15 | 27461.00 | 50.2026 |
| 287.15 | 27594.00 | 50.3586 |
| 288.15 | 28345.00 | 50.5667 |
| 288.15 | 28454.00 | 50.6188 |
| 288.15 | 28588.00 | 50.4107 |
| 289.15 | 5774.00 | 51.243 |
| 289.15 | 5835.00 | 49.7864 |
| 289.15 | 29338.00 | 50.4627 |
| 289.15 | 29446.00 | 50.7228 |
| 289.15 | 29581.00 | 51.087 |
| 290.15 | 6570.00 | 50.6188 |
| 290.15 | 6631.00 | 50.9309 |
| 291.15 | 7365.00 | 51.139 |
| 291.15 | 7428.00 | 51.191 |
| 292.15 | 8161.00 | 51.243 |
| 292.15 | 8224.00 | 51.139 |
| 293.15 | 8956.00 | 51.3991 |
| 293.15 | 9019.00 | 51.7112 |
| 294.15 | 9752.00 | 51.6592 |
| 294.15 | 9815.00 | 50.8268 |
| 295.15 | 10546.00 | 51.191 |
| 295.15 | 10610.00 | 51.5552 |
| 296.15 | 11341.00 | 51.191 |
| 296.15 | 11405.00 | 51.5032 |
| 297.15 | 12135.00 | 51.6072 |
| 297.15 | 12199.00 | 51.3471 |
| 298.15 | 12929.00 | 51.5032 |
| 298.15 | 12993.00 | 51.9193 |
| 299.15 | 13723.00 | 51.6592 |
| 299.15 | 13787.00 | 51.8153 |
| 300.15 | 14517.00 | 51.6592 |
| 300.15 | 14581.00 | 52.0754 |
| 301.15 | 15309.00 | 52.3355 |
| 301.15 | 15374.00 | 51.9193 |
| 302.15 | 16102.00 | 52.0754 |
| 302.15 | 16167.00 | 52.2315 |
| 303.15 | 16894.00 | 52.1274 |
| 303.15 | 16960.00 | 52.4916 |
| 304.15 | 17685.00 | 52.1274 |
| 304.15 | 17752.00 | 52.5436 |
| 305.15 | 18476.00 | 52.7517 |
| 305.15 | 18543.00 | 52.5956 |
| 306.15 | 19267.00 | 52.7517 |
| 306.15 | 19335.00 | 52.8037 |
| 307.15 | 20125.00 | 52.4916 |
| 308.15 | 20848.00 | 52.9078 |
| 308.15 | 20915.00 | 52.8037 |
| 309.15 | 21639.00 | 52.6997 |
| 309.15 | 21704.00 | 53.324 |
| 310.15 | 22429.00 | 52.8558 |
| 310.15 | 22492.00 | 53.1159 |
| 311.15 | 23217.00 | 53.1679 |
| 311.15 | 23281.00 | 53.6881 |
| 312.15 | 24005.00 | 53.6361 |
| 312.15 | 24068.00 | 53.7922 |
| 313.15 | 24793.00 | 53.5321 |
| 313.15 | 24855.00 | 53.7922 |
| 314.15 | 25579.00 | 53.7922 |
| 314.15 | 25641.00 | 53.428 |
| 315.15 | 26364.00 | 53.5841 |
| 315.15 | 26427.00 | 54.0003 |
| 316.15 | 27149.00 | 53.5321 |
| 316.15 | 27212.00 | 54.6766 |
| 317.15 | 27934.00 | 54.4165 |
| 317.15 | 27996.00 | 54.2084 |
| 318.15 | 28719.00 | 54.1043 |
| 318.15 | 28779.00 | 54.7806 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Gas | Pressure, kPa - Gas | Mass density, kg/m3 - Gas |
| 254.08 | 382.25 | 10.3656 |
| 254.09 | 313.90 | 8.3508 |
| 254.09 | 214.16 | 5.5491 |
| 254.10 | 104.12 | 2.6275 |
| 263.88 | 571.82 | 15.4369 |
| 263.88 | 506.07 | 13.4247 |
| 263.88 | 401.96 | 10.3885 |
| 263.88 | 306.27 | 7.74 |
| 263.88 | 204.78 | 5.0609 |
| 263.88 | 107.72 | 2.6075 |
| 263.89 | 71.43 | 1.7159 |
| 273.74 | 824.10 | 22.3391 |
| 273.73 | 817.04 | 22.1108 |
| 273.74 | 771.81 | 20.6433 |
| 273.73 | 711.85 | 18.7582 |
| 273.74 | 614.63 | 15.8288 |
| 273.73 | 513.88 | 12.9426 |
| 273.74 | 416.77 | 10.2856 |
| 273.73 | 312.85 | 7.5636 |
| 273.74 | 224.38 | 5.3352 |
| 273.73 | 101.73 | 2.3681 |
| 283.54 | 1013.18 | 26.9253 |
| 283.54 | 1013.16 | 26.9235 |
| 283.55 | 911.64 | 23.6652 |
| 283.53 | 812.63 | 20.6499 |
| 283.52 | 710.61 | 17.6856 |
| 283.52 | 614.51 | 15.0118 |
| 283.54 | 502.33 | 12.0197 |
| 283.52 | 412.99 | 9.7269 |
| 283.53 | 312.42 | 7.2368 |
| 283.53 | 213.32 | 4.8632 |
| 283.53 | 101.75 | 2.2806 |
| 293.33 | 1397.32 | 37.8678 |
| 293.33 | 1265.09 | 33.2531 |
| 293.34 | 1161.47 | 29.864 |
| 293.34 | 1066.35 | 26.9025 |
| 293.34 | 968.81 | 23.9856 |
| 293.34 | 866.25 | 21.0499 |
| 293.34 | 760.28 | 18.1362 |
| 293.32 | 656.65 | 15.3945 |
| 293.32 | 546.17 | 12.5808 |
| 293.32 | 432.29 | 9.7863 |
| 293.37 | 323.39 | 7.2059 |
| 293.38 | 219.26 | 4.8156 |
| 293.32 | 107.46 | 2.3235 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Gas | Pressure, kPa - Gas | Mass density, kg/m3 - Gas |
| 313.15 | 201.80 | 4.12 |
| 313.15 | 201.90 | 4.121 |
| 313.15 | 490.80 | 10.342 |
| 313.15 | 791.00 | 17.277 |
| 313.15 | 996.60 | 22.355 |
| 313.15 | 1203.30 | 27.77 |
| 313.15 | 1396.50 | 33.159 |
| 313.15 | 1602.90 | 39.331 |
| 313.15 | 1801.80 | 45.76 |
| 313.15 | 1801.90 | 45.748 |
| 313.15 | 1998.10 | 52.687 |
| 313.15 | 2103.60 | 56.702 |
| 313.15 | 2201.50 | 60.637 |
| 313.15 | 2251.00 | 62.72 |
| 313.15 | 2298.10 | 64.762 |
| 313.15 | 2355.70 | 67.348 |
| 313.15 | 2355.80 | 67.343 |
| 313.15 | 2402.70 | 69.541 |
| 313.15 | 2403.00 | 69.545 |
| 313.15 | 2435.00 | 71.084 |
| 313.15 | 2435.10 | 71.095 |
| 313.15 | 2450.50 | 71.838 |
| 313.15 | 2450.60 | 71.855 |
| 313.15 | 2472.00 | 72.903 |
| 313.15 | 490.80 | 10.336 |
| 313.15 | 791.00 | 17.275 |
| 313.15 | 996.60 | 22.349 |
| 313.15 | 1203.30 | 27.759 |
| 313.15 | 1396.50 | 33.148 |
| 313.15 | 1602.90 | 39.322 |
| 313.15 | 1998.10 | 52.676 |
| 313.15 | 2103.60 | 56.692 |
| 313.15 | 2201.50 | 60.629 |
| 313.15 | 2251.00 | 62.711 |
| 313.15 | 2298.10 | 64.748 |
| 313.15 | 2472.00 | 72.918 |
| 323.15 | 207.90 | 4.101 |
| 323.15 | 499.20 | 10.125 |
| 323.15 | 801.10 | 16.793 |
| 323.15 | 801.20 | 16.794 |
| 323.15 | 998.30 | 21.387 |
| 323.15 | 1095.20 | 23.732 |
| 323.15 | 1200.30 | 26.337 |
| 323.15 | 1200.40 | 26.341 |
| 323.15 | 1397.40 | 31.424 |
| 323.15 | 1590.60 | 36.664 |
| 323.15 | 1797.20 | 42.644 |
| 323.15 | 2004.90 | 49.091 |
| 323.15 | 2200.60 | 55.637 |
| 323.15 | 2402.30 | 62.99 |
| 323.15 | 2596.10 | 70.738 |
| 323.15 | 2699.00 | 75.19 |
| 323.15 | 2699.10 | 75.207 |
| 323.15 | 2799.00 | 79.805 |
| 323.15 | 2802.90 | 80.005 |
| 323.15 | 2900.60 | 84.82 |
| 323.15 | 2901.20 | 84.882 |
| 323.15 | 2947.00 | 87.258 |
| 323.15 | 2960.30 | 87.971 |
| 323.15 | 3002.20 | 90.24 |
| 323.15 | 3002.30 | 90.261 |
| 323.15 | 3010.20 | 90.716 |
| 323.15 | 3041.10 | 92.478 |
| 323.15 | 3041.20 | 92.495 |
| 323.15 | 3074.60 | 94.445 |
| 323.15 | 3099.50 | 95.942 |
| 323.15 | 3125.50 | 97.558 |
| 323.15 | 3125.60 | 97.549 |
| 323.15 | 3134.20 | 98.084 |
| 323.15 | 207.90 | 4.103 |
| 323.15 | 499.20 | 10.143 |
| 323.15 | 998.30 | 21.393 |
| 323.15 | 1397.40 | 31.416 |
| 323.15 | 1590.60 | 36.67 |
| 323.15 | 1797.20 | 42.658 |
| 323.15 | 2004.90 | 49.105 |
| 323.15 | 2200.60 | 55.653 |
| 323.15 | 2402.30 | 62.978 |
| 323.15 | 2596.10 | 70.733 |
| 323.15 | 2799.00 | 79.816 |
| 323.15 | 2802.90 | 80.017 |
| 323.15 | 2900.60 | 84.839 |
| 323.15 | 2901.20 | 84.872 |
| 323.15 | 2947.00 | 87.244 |
| 323.15 | 2960.30 | 87.99 |
| 323.15 | 3010.20 | 90.73 |
| 323.15 | 3074.60 | 94.453 |
| 323.15 | 3099.50 | 95.952 |
| 323.15 | 499.20 | 10.143 |
| 323.15 | 499.20 | 10.132 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Fluid (supercritical or subcritical phases) | Pressure, kPa - Fluid (supercritical or subcritical phases) | Mass density, kg/m3 - Fluid (supercritical or subcritical phases) |
| 313.16 | 3353.70 | 900.17 |
| 316.15 | 4967.10 | 899.97 |
| 319.15 | 6571.40 | 899.77 |
| 322.15 | 8162.40 | 899.57 |
| 328.16 | 11399.70 | 899.19 |
| 334.15 | 14753.40 | 898.82 |
| 337.15 | 16580.50 | 898.63 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.54 | 3000.00 | 1027.1 |
| 283.54 | 5000.00 | 1035.42 |
| 283.55 | 10000.00 | 1054.01 |
| 283.55 | 15000.00 | 1070.11 |
| 283.55 | 20000.00 | 1084.45 |
| 283.55 | 25000.00 | 1097.41 |
| 283.56 | 30000.00 | 1109.29 |
| 283.56 | 40000.00 | 1130.47 |
| 283.56 | 60000.00 | 1165.73 |
| 283.56 | 80000.00 | 1194.77 |
| 283.55 | 100000.00 | 1219.47 |
| 293.49 | 3000.00 | 989.19 |
| 293.49 | 5000.00 | 999.53 |
| 293.49 | 10000.00 | 1021.69 |
| 293.48 | 15000.00 | 1040.44 |
| 293.49 | 20000.00 | 1056.75 |
| 293.49 | 25000.00 | 1071.31 |
| 293.49 | 30000.00 | 1084.43 |
| 293.49 | 40000.00 | 1107.67 |
| 293.49 | 60000.00 | 1145.64 |
| 293.50 | 80000.00 | 1176.55 |
| 293.50 | 100000.00 | 1202.49 |
| 303.43 | 3000.00 | 946.84 |
| 303.43 | 5000.00 | 960.0 |
| 303.42 | 10000.00 | 987.14 |
| 303.42 | 15000.00 | 1009.19 |
| 303.43 | 20000.00 | 1027.86 |
| 303.43 | 25000.00 | 1044.2 |
| 303.44 | 30000.00 | 1058.82 |
| 303.43 | 40000.00 | 1084.3 |
| 303.44 | 60000.00 | 1125.22 |
| 303.45 | 80000.00 | 1157.85 |
| 303.44 | 100000.00 | 1185.37 |
| 313.35 | 3000.00 | 898.97 |
| 313.36 | 5000.00 | 916.76 |
| 313.35 | 10000.00 | 951.05 |
| 313.36 | 15000.00 | 977.36 |
| 313.36 | 20000.00 | 999.0 |
| 313.37 | 25000.00 | 1017.48 |
| 313.36 | 30000.00 | 1033.81 |
| 313.36 | 40000.00 | 1061.8 |
| 313.37 | 60000.00 | 1105.9 |
| 313.36 | 80000.00 | 1140.76 |
| 313.36 | 100000.00 | 1169.51 |
| 323.26 | 5000.00 | 864.36 |
| 323.25 | 10000.00 | 909.88 |
| 323.25 | 15000.00 | 941.66 |
| 323.25 | 20000.00 | 966.72 |
| 323.25 | 25000.00 | 987.67 |
| 323.25 | 30000.00 | 1005.85 |
| 323.25 | 40000.00 | 1036.43 |
| 323.25 | 60000.00 | 1083.93 |
| 323.25 | 80000.00 | 1120.89 |
| 323.25 | 100000.00 | 1151.14 |
| 333.14 | 10000.00 | 865.89 |
| 333.14 | 15000.00 | 905.11 |
| 333.15 | 20000.00 | 934.53 |
| 333.15 | 25000.00 | 958.47 |
| 333.15 | 30000.00 | 978.86 |
| 333.15 | 40000.00 | 1012.65 |
| 333.15 | 60000.00 | 1063.95 |
| 333.15 | 80000.00 | 1103.15 |
| 333.15 | 100000.00 | 1134.94 |
| 343.00 | 10000.00 | 815.42 |
| 342.99 | 15000.00 | 866.16 |
| 343.00 | 20000.00 | 901.33 |
| 343.00 | 25000.00 | 928.7 |
| 343.00 | 30000.00 | 951.59 |
| 343.00 | 40000.00 | 988.88 |
| 343.01 | 60000.00 | 1044.01 |
| 343.01 | 80000.00 | 1085.29 |
| 343.01 | 100000.00 | 1118.63 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.05; 5893.28] | kPa | [137.00; 351.60] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.88243e+01 | |||
| Coefficient B | -4.29952e+03 | |||
| Coefficient C | -1.03475e+01 | |||
| Coefficient D | 2.22293e-05 | |||
| Temperature range, min. | 137.00 | |||
| Temperature range, max. | 351.60 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 200 300 | ||||
| Pvap | 0.05 | kPa | 137.00 | Calculated Property |
| Pvap | 1.10 | kPa | 160.84 | Calculated Property |
| Pvap | 10.00 | kPa | 184.69 | Calculated Property |
| Pvap | 50.21 | kPa | 208.53 | Calculated Property |
| Pvap | 171.62 | kPa | 232.38 | Calculated Property |
| Pvap | 452.75 | kPa | 256.22 | Calculated Property |
| Pvap | 999.76 | kPa | 280.07 | Calculated Property |
| Pvap | 1950.92 | kPa | 303.91 | Calculated Property |
| Pvap | 3493.00 | kPa | 327.76 | Calculated Property |
| Pvap | 5893.28 | kPa | 351.60 | Calculated Property |
Similar Compounds
Find more compounds similar to Difluoromethane.
Mixtures
- Difluoromethane + Ethane, pentafluoro-
- Difluoromethane + Norflurane
- 1-Butene + Difluoromethane
- Difluoromethane + Ethane, 1,1-difluoro-
- Propane + Difluoromethane
- Difluoromethane + Propene
- Difluoromethane + Dimethyl ether
- Difluoromethane + Butane
- Difluoromethane + Nitrous oxide
- Ethane, 1,1,1-trifluoro- + Difluoromethane + Ethane, pentafluoro-
- Difluoromethane + Ethane, fluoro-
- Difluoromethane + Ethane, fluoro- + Ethane, pentafluoro-
- Difluoromethane + Methyl Alcohol
- Difluoromethane + Ethanol
- Difluoromethane + 1-Propanol
- Difluoromethane + 1-Butanol
- Benzene + Difluoromethane
- Difluoromethane + Toluene
- Difluoromethane + Benzene, 1,3-dimethyl-
- Difluoromethane + Mesitylene
Find more mixtures with Difluoromethane.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- An Experimental Study of the pV T x Properties for Binary Mixtures of HFC-32 and HFC-125 from 258 to 354 K at Pressures up to 16.9 MPa1
- Burnett Measurements and Virial Coefficients for the R32+N2O System
- Viscosity of Alternative Refrigerants R407C and R407E in the Vapor Phase from 298.15 to 423.15K
- Isochoric Specific Heat Capacity of Difluoromethane (R32) and a Mixture of 51.11mass% Difluoromethane (R32) + 48.89mass% Pentafluoroethane (R125)
- Study on Isochoric Specific Heat Capacity of Liquid R-410A and HFE-347pcf2
- PVTx measurements for N2O+CH3F, N2O+CH2F2, and N2O+ CHF3 binary systems
- Vapor liquid equilibrium data for the difluoromethane (R32) dimethyl ether (RE170) system at temperatures from 283.03 to 363.21K and pressures up to 5.5MPa
- An experimental study of PVTx properties in the gas phase for binary mixtures of HFC-161 and HFC-32
- Vapor liquid equilibria and critical loci of binary and ternary systems composed of CH2F2, C2HF5 and C2H2F4
- Measurements of gas phase PVTx properties for the ternary HFC-161/125/32 system
- Vapor-liquid equilibrium of difluoromethane +1,1,1,2-tetrafluoroethane systems over a temperature range from 258.15 to 343.15K
- Vapor liquid equilibrium measurements and correlations for the binary mixture of difluoromethane + isobutane and the ternary mixture of propane + isobutane + difluoromethane
- Vapor-liquid equilibrium measurement and modeling for the difluoromethane + pentafluoroethane + propane ternary mixture
- Isothermal vapor-liquid equilibrium data for the binary mixture difluoromethane (HFC-32)+ ethyl fluoride (HFC-161) over a temperature range from 253.15 to 303.15 K
- Solubility of HFCs in lower alcohols
- Solubility of hydrofluorocarbons in aromatic solvents and alcohols: Experimental data and modeling with CPA EoS
- Vapor-liquid equilibria of difluoromethane + N,N-dimethylacetamide, difluoromethane + dimethylether diethylene glycol and 1,1-difluoroethane + dimethylether diethylene glycol systems
- Isothermal vapor-liquid equilibrium measurements and assessments of 1,1,1,3,3,3-hexafluoropropane+N,N-dimethylformamide/N-methyl-2-pyrrolidone working pairs for absorption power cycles
- Isothermal vapor liquid equilibrium measurements for difluoromethane (R32) + trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
- Vapor liquid equilibrium measurements for difluoromethane (R32) + 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) and fluoroethane (R161) + 2,3,3,3-tetrafluoroprop-1-ene (R1234yf)
- Gaseous PvTx measurements of HFO-1234yf + HFC-32 binary mixture by single-sinker magnetic suspension densimeter
- Experimental measurements of saturated vapor pressure and isothermal vapor-liquid equilibria for 1,1,1,2-Tetrafluoroethane (HFC-134a) + 3,3,3-trifluoropropene (HFO-1243zf) binary system
- Experimental vapour liquid equilibrium data and modeling for binary mixtures of 1-butene with 1,1,2,3,3,3-hexafluoro-1-propene, 2,2,3-trifluoro-3-(trifluoromethyl)oxirane, or difluoromethane
- Solubilities of hydrofluorocarbons in ionic liquids: Experimental and modelling study
- Apparatus based on a compact single-sinker densimeter and measurements of the (p,.rho.,T) relation of difluoromethane
- Solubility of hydrofluorocarbons in phosphonium-based ionic liquids: Experimental and modelling study
- Liquid viscosity of low-GWP refrigerant mixtures (R32 + R1234yf) and (R125 + R1234yf)
- Volumetric properties of binary mixtures of {difluoromethane (R32) + trans-1,3,3,3-tetrafluoropropene (R1234ze(E))} at temperatures from 283.15 K to 363.15 K and pressures up to 100 MPa
- Diffusion coefficients and Henry's constants of hydrofluorocarbons in [HMIM][Tf2N], [HMIM][TfO], and [HMIM][BF4]
- Vapor liquid equilibria for binary mixtures of difluoromethane (R32) + fluoroethane (R161) and fluoroethane (R161) + trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
- Vapor phase pvTx measurements of binary mixtures of difluoromethane (R32) and 2,3,3,3-tetrafluoroprop-1-ene (R1234yf)
- Experimental measurements and correlation of isothermal vapor-liquid equilibria for HFC-32 + HFO-1234ze (E) and HFC-134a + HFO-1234ze (E) binary systems
- Investigation on the Vapor-Liquid Equilibrium for the Ternary Mixture HFC-32 + HFC-125 + HFC-161 at Temperatures from 265.15 K to 303.15 K
- Experimental Clathrate Hydrate Dissociation Data for Systems Comprising Refrigerant + CaCl2 Aqueous Solutions
- Surface Tension and Liquid Viscosity of R32+R1234yf and R32 + R1234ze
- Isothermal Vapor Liquid Equilibrium of HFC-161 + DMETrEG within the Temperature Range of 293.15 353.15 K and Comparison for HFC-161 Combined with Different Absorbents
- Vapor-Liquid Equilibria for the Binary and Ternary Systems of Difluoromethane (R32), 1,1-Difluoroethane (R152a), and 2,3,3,3-Tetrafluoroprop-1-ene (R1234yf)
- Isothermal Vapor-Liquid Equilibrium of the Absorption Working Pairs (HFC-32 + DMETrEG, HFC-32 + NMP) at Temperatures from 293.15 to 343.15 K
- Vapor-Liquid Equilibrium Data for the Azeotropic Difluoromethane + Propane System at Temperatures from 294.83 to 343.26 K and Pressures up to 5.4 MPa
- Vapor-Liquid Equilibria for the Binary System Difluoromethane (HFC-32) + Propane (HC-290) at Seven Temperatures [(268.15, 278.15, 283.15, 288.15, 298.15, 308.15, and 318.15) K]
- Surface Tension Measurements of Difluoromethane(R-32) and the Binary Mixture Difluoromethane(R-32) + 1,1,1,2-tetrafluoroethane(R-134a) from (253 to 333) K
- Isothermal Vapor-Liquid Equilibrium and Excess Enthalpy Data for the Binary Systems Propylene oxide + 2-Methylpentane and Difluoromethane (R32) + Pentafluoroethane (R125)
- Surface Tension of Difluoromethane (R-32) + 1,1,1,2,3,3,3-Heptafluoropropane (R-227ea) from (253 to 333) K
- PVTx Properties in the Gas Phase for Difluoromethane (HFC-32) + Pentafluoroethane (HFC-125)
- Measurement of Vapor-Liquid Equilibria for the Binary Mixture Difluoromethane (HFC-32) + Propylene (R-1270)
- Isothermal VLE Measurements for Difluoromethane + Dimethylether and an Evaluation of Hydrogen Bonding
- Vapor-Liquid Equilibria of the Binary n-Butane (HC-600) + Difluoromethane (HFC-32), + Pentafluoroethane (HFC-125), + 1,1,1,2-Tetrafluoroethane (HFC-134a) Mixture Systems
- Vapor-Liquid Equilibrium for the Difluoromethane (R32) + n-Butane (R600) System
- Specific Heat Capacity at Constant Volume for R125 and R410A at Temperatures from (300 to 400) K and Pressures to 20 MPa
- Solubility and Diffusivity of Difluoromethane in Room-Temperature Ionic Liquids
- Vapor-Liquid Equilibria of the Difluoromethane + Dimethyl Ether and 1,1,1,2-Tetrafluoroethane + Dimethyl Ether Systems
- Acoustic Determination of Thermophysical Properties and Critical Parameters for R410A and Critical Line of xCO2 + (1 - x)R410A
- Vapor-Liquid Equilibrium Study of an Absorption Heat Transformer Working Fluid of (HFC-32 + DMF)
- Vapor Liquid Equilibrium Measurements of Difluoromethane + [Emim]OTf, Difluoromethane + [Bmim]OTf, Difluoroethane + [Emim]OTf, and Difluoroethane + [Bmim]OTf Systems
- Experimental Measurements and Thermodynamic Modeling of the Dissociation Conditions of Clathrate Hydrates for (Refrigerant + NaCl + Water) Systems
- Solubility of Hydrofluorocarbons in Halobenzene Solvents
- Measurement and Correlation of Isothermal Vapor Liquid Equilibrium of 1,1,1,3,3-Pentafluoropropane + N,N-Dimethylacetamide and 1,1,1,3,3,3-Hexafluoropropane + N,N-Dimethylacetamide/Diethylene Glycol Dimethyl Ether Systems
- Vapor Liquid Equilibrium of Three Hydrofluorocarbons with [HMIM][Tf2N]
- Vapor-Liquid Equilibrium Data for the Binary Mixture Difluoromethane (HFC-32) + Pentafluoroethane (HFC-125) of an Alternative Refrigerant
- PVTx Properties of Gaseous Mixtures of Difluoromethane and 1,1,1,2,3,3,3-Heptafluoropropane
- PVT Property Measurements for R143a, R125, and R32 in the Gaseous Phase
- PVTx Property Measurements for Difluoromethane + Pentafluoroethane (R32 + R125) in the Gaseous Phase
- Measurements of the Surface Tension for the R290 + R32 Mixture
- Measurements of the Isobaric Specific Heat Capacity for 1,1,1-Trifluoroethane (R143a), Pentafluoroethane (R125), and Difluoromethane (R32) in the Liquid Phase
- Kinematic Viscosity of R410A and R407C Refrigerant-Oil Mixtures in the Saturated Liquid Phase with Lubricant Mass Fraction in the Range of (0 to 0.0001)
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
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