Mixture of Methane, bromotrichloro- + Methane, bromochloro-

Excel

Methane, bromotrichloro-

Name
Methane, bromotrichloro-
InChI
InChI=1S/CBrCl3/c2-1(3,4)5
InChI Key
XNNQFQFUQLJSQT-UHFFFAOYSA-N
Formula
CBrCl3
SMILES
ClC(Cl)(Cl)Br
Mol. Weight (g/mol)
198.27
CAS
75-62-7

Methane, bromochloro-

Name
Methane, bromochloro-
InChI
InChI=1S/CH2BrCl/c2-1-3/h1H2
InChI Key
JPOXNPPZZKNXOV-UHFFFAOYSA-N
Formula
CH2BrCl
SMILES
ClCBr
Mol. Weight (g/mol)
129.38
CAS
74-97-5
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

  1. Mole fraction (2)
  2. ρl - Mass density, kg/m3 (2)
  3. csound,fluid - Speed of Sound, m/s (2)
  4. Vapor or sublimation pressure, kPa (2)

Mole fraction of Methane, bromotrichloro- (1) [ref]

Operational condition: Temperature, K = 308.15 (Liquid)

Mole fraction of Methane, bromotrichloro- (1) - Liquid Mole fraction of Methane, bromotrichloro- (1) - Gas
0.0392 0.0000
0.0881 0.0130
0.1245 0.0252
0.1918 0.0399
0.2536 0.0682
0.3271 0.0920
0.3664 0.1254
0.4174 0.1448
0.4642 0.1703
0.4983 0.1916
0.5625 0.2105
0.6026 0.2497
0.6583 0.2781
0.6859 0.3224
0.7318 0.3450
0.7744 0.3896
0.8383 0.4441
0.8953 0.5394
0.9694 0.6488

Mole fraction of Methane, bromotrichloro- (1) [ref]

Operational condition: Temperature, K = 308.15 (Liquid)

Mole fraction of Methane, bromotrichloro- (1) - Liquid Mole fraction of Methane, bromotrichloro- (1) - Gas
0.0392 0.0000
0.0881 0.0130
0.1245 0.0252
0.1918 0.0399
0.2536 0.0682
0.3271 0.0920
0.3664 0.1254
0.4174 0.1448
0.4642 0.1703
0.4983 0.1916
0.5625 0.2105
0.6026 0.2497
0.6583 0.2781
0.6859 0.3224
0.7318 0.3450
0.7744 0.3896
0.8383 0.4441
0.8953 0.5394
0.9694 0.6488

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Methane, bromotrichloro- (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 1933.23
293.15 0.0520 1938.2
293.15 0.1030 1942.79
293.15 0.1538 1947.34
293.15 0.2031 1951.55
293.15 0.2551 1956.05
293.15 0.3050 1960.19
293.15 0.3522 1963.98
293.15 0.4063 1968.54
293.15 0.4553 1972.41
293.15 0.5058 1976.4
293.15 0.5665 1981.04
293.15 0.6027 1983.79
293.15 0.6567 1987.81
293.15 0.7046 1991.31
293.15 0.7543 1994.91
293.15 0.8025 1998.2
293.15 0.8516 2001.94
293.15 0.8996 2005.35
293.15 0.9228 2007.14
293.15 1.0000 2013.06
298.15 0.0000 1921.71
298.15 0.0520 1926.72
298.15 0.1030 1931.34
298.15 0.1538 1935.88
298.15 0.2031 1940.16
298.15 0.2551 1944.71
298.15 0.3050 1948.82
298.15 0.3522 1952.66
298.15 0.4063 1957.3
298.15 0.4553 1961.2
298.15 0.5058 1965.21
298.15 0.5665 1969.89
298.15 0.6027 1972.67
298.15 0.6567 1976.74
298.15 0.7046 1980.21
298.15 0.7543 1983.88
298.15 0.8025 1987.2
298.15 0.8516 1990.96
298.15 0.8996 1994.38
298.15 0.9228 1996.17
298.15 1.0000 2002.14
303.15 0.0000 1910.15
303.15 0.0520 1915.19
303.15 0.1030 1919.85
303.15 0.1538 1924.46
303.15 0.2031 1928.76
303.15 0.2551 1933.31
303.15 0.3050 1937.49
303.15 0.3522 1941.28
303.15 0.4063 1946.02
303.15 0.4553 1949.96
303.15 0.5058 1954.0
303.15 0.5665 1958.74
303.15 0.6027 1961.52
303.15 0.6567 1965.63
303.15 0.7046 1969.15
303.15 0.7543 1972.83
303.15 0.8025 1976.2
303.15 0.8516 1979.93
303.15 0.8996 1983.39
303.15 0.9228 1985.15
303.15 1.0000 1991.2
308.15 0.0000 1898.51
308.15 0.0520 1903.6
308.15 0.1030 1908.3
308.15 0.1538 1912.93
308.15 0.2031 1917.27
308.15 0.2551 1921.86
308.15 0.3050 1926.18
308.15 0.3522 1929.99
308.15 0.4063 1934.68
308.15 0.4553 1938.65
308.15 0.5058 1942.75
308.15 0.5665 1947.52
308.15 0.6027 1950.31
308.15 0.6567 1954.45
308.15 0.7046 1958.12
308.15 0.7543 1961.75
308.15 0.8025 1965.14
308.15 0.8516 1968.92
308.15 0.8996 1972.42
308.15 0.9228 1974.22
308.15 1.0000 1980.24
313.15 0.0000 1886.82
313.15 0.0520 1891.94
313.15 0.1030 1896.67
313.15 0.1538 1901.44
313.15 0.2031 1905.74
313.15 0.2551 1910.36
313.15 0.3050 1914.72
313.15 0.3522 1918.58
313.15 0.4063 1923.3
313.15 0.4553 1927.29
313.15 0.5058 1931.42
313.15 0.5665 1936.26
313.15 0.6027 1939.1
313.15 0.6567 1943.26
313.15 0.7046 1946.95
313.15 0.7543 1950.61
313.15 0.8025 1954.05
313.15 0.8516 1957.85
313.15 0.8996 1961.38
313.15 0.9228 1963.19
313.15 1.0000 1969.25

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Methane, bromotrichloro- (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 1933.23
293.15 0.0520 1938.2
293.15 0.1030 1942.79
293.15 0.1538 1947.34
293.15 0.2031 1951.55
293.15 0.2551 1956.05
293.15 0.3050 1960.19
293.15 0.3522 1963.98
293.15 0.4063 1968.54
293.15 0.4553 1972.41
293.15 0.5058 1976.4
293.15 0.5665 1981.04
293.15 0.6027 1983.79
293.15 0.6567 1987.81
293.15 0.7046 1991.31
293.15 0.7543 1994.91
293.15 0.8025 1998.2
293.15 0.8516 2001.94
293.15 0.8996 2005.35
293.15 0.9228 2007.14
293.15 1.0000 2013.06
298.15 0.0000 1921.71
298.15 0.0520 1926.72
298.15 0.1030 1931.34
298.15 0.1538 1935.88
298.15 0.2031 1940.16
298.15 0.2551 1944.71
298.15 0.3050 1948.82
298.15 0.3522 1952.66
298.15 0.4063 1957.3
298.15 0.4553 1961.2
298.15 0.5058 1965.21
298.15 0.5665 1969.89
298.15 0.6027 1972.67
298.15 0.6567 1976.74
298.15 0.7046 1980.21
298.15 0.7543 1983.88
298.15 0.8025 1987.2
298.15 0.8516 1990.96
298.15 0.8996 1994.38
298.15 0.9228 1996.17
298.15 1.0000 2002.14
303.15 0.0000 1910.15
303.15 0.0520 1915.19
303.15 0.1030 1919.85
303.15 0.1538 1924.46
303.15 0.2031 1928.76
303.15 0.2551 1933.31
303.15 0.3050 1937.49
303.15 0.3522 1941.28
303.15 0.4063 1946.02
303.15 0.4553 1949.96
303.15 0.5058 1954.0
303.15 0.5665 1958.74
303.15 0.6027 1961.52
303.15 0.6567 1965.63
303.15 0.7046 1969.15
303.15 0.7543 1972.83
303.15 0.8025 1976.2
303.15 0.8516 1979.93
303.15 0.8996 1983.39
303.15 0.9228 1985.15
303.15 1.0000 1991.2
308.15 0.0000 1898.51
308.15 0.0520 1903.6
308.15 0.1030 1908.3
308.15 0.1538 1912.93
308.15 0.2031 1917.27
308.15 0.2551 1921.86
308.15 0.3050 1926.18
308.15 0.3522 1929.99
308.15 0.4063 1934.68
308.15 0.4553 1938.65
308.15 0.5058 1942.75
308.15 0.5665 1947.52
308.15 0.6027 1950.31
308.15 0.6567 1954.45
308.15 0.7046 1958.12
308.15 0.7543 1961.75
308.15 0.8025 1965.14
308.15 0.8516 1968.92
308.15 0.8996 1972.42
308.15 0.9228 1974.22
308.15 1.0000 1980.24
313.15 0.0000 1886.82
313.15 0.0520 1891.94
313.15 0.1030 1896.67
313.15 0.1538 1901.44
313.15 0.2031 1905.74
313.15 0.2551 1910.36
313.15 0.3050 1914.72
313.15 0.3522 1918.58
313.15 0.4063 1923.3
313.15 0.4553 1927.29
313.15 0.5058 1931.42
313.15 0.5665 1936.26
313.15 0.6027 1939.1
313.15 0.6567 1943.26
313.15 0.7046 1946.95
313.15 0.7543 1950.61
313.15 0.8025 1954.05
313.15 0.8516 1957.85
313.15 0.8996 1961.38
313.15 0.9228 1963.19
313.15 1.0000 1969.25

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Methane, bromotrichloro- (1) - Liquid Speed of sound, m/s - Liquid
293.15 0.0000 1001.2
293.15 0.0520 992.8
293.15 0.1030 985.2
293.15 0.1538 978.4
293.15 0.2031 972.2
293.15 0.2551 966.1
293.15 0.3050 960.7
293.15 0.3522 956.4
293.15 0.4063 950.8
293.15 0.4553 946.7
293.15 0.5058 942.7
293.15 0.5665 938.2
293.15 0.6027 935.8
293.15 0.6567 932.3
293.15 0.7046 929.6
293.15 0.7543 926.9
293.15 0.8025 924.5
293.15 0.8516 922.3
293.15 0.8996 920.3
293.15 0.9228 919.8
293.15 1.0000 917.1
298.15 0.0000 986.1
298.15 0.0520 977.9
298.15 0.1030 970.4
298.15 0.1538 963.6
298.15 0.2031 957.5
298.15 0.2551 951.6
298.15 0.3050 946.3
298.15 0.3522 942.1
298.15 0.4063 936.7
298.15 0.4553 932.6
298.15 0.5058 928.6
298.15 0.5665 924.2
298.15 0.6027 921.9
298.15 0.6567 918.5
298.15 0.7046 915.8
298.15 0.7543 913.2
298.15 0.8025 910.8
298.15 0.8516 908.7
298.15 0.8996 906.8
298.15 0.9228 906.3
298.15 1.0000 903.6
303.15 0.0000 971.0
303.15 0.0520 962.9
303.15 0.1030 955.5
303.15 0.1538 948.9
303.15 0.2031 942.8
303.15 0.2551 937.0
303.15 0.3050 931.8
303.15 0.3522 927.8
303.15 0.4063 922.4
303.15 0.4553 918.4
303.15 0.5058 914.5
303.15 0.5665 910.3
303.15 0.6027 908.0
303.15 0.6567 904.7
303.15 0.7046 902.0
303.15 0.7543 899.5
303.15 0.8025 897.2
303.15 0.8516 895.1
303.15 0.8996 893.3
303.15 0.9228 892.9
303.15 1.0000 890.2
308.15 0.0000 955.9
308.15 0.0520 947.9
308.15 0.1030 940.7
308.15 0.1538 934.2
308.15 0.2031 928.1
308.15 0.2551 922.6
308.15 0.3050 917.3
308.15 0.3522 913.5
308.15 0.4063 908.2
308.15 0.4553 904.2
308.15 0.5058 900.5
308.15 0.5665 896.4
308.15 0.6027 894.1
308.15 0.6567 891.0
308.15 0.7046 888.3
308.15 0.7543 885.9
308.15 0.8025 883.7
308.15 0.8516 881.6
308.15 0.8996 879.9
308.15 0.9228 879.4
308.15 1.0000 876.8
313.15 0.0000 940.8
313.15 0.0520 933.0
313.15 0.1030 925.9
313.15 0.1538 919.1
313.15 0.2031 913.6
313.15 0.2551 908.1
313.15 0.3050 903.0
313.15 0.3522 898.9
313.15 0.4063 894.0
313.15 0.4553 890.3
313.15 0.5058 886.5
313.15 0.5665 882.6
313.15 0.6027 880.3
313.15 0.6567 877.2
313.15 0.7046 874.7
313.15 0.7543 872.3
313.15 0.8025 870.2
313.15 0.8516 868.3
313.15 0.8996 866.5
313.15 0.9228 865.9
313.15 1.0000 863.6

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Methane, bromotrichloro- (1) - Liquid Speed of sound, m/s - Liquid
293.15 0.0000 1001.2
293.15 0.0520 992.8
293.15 0.1030 985.2
293.15 0.1538 978.4
293.15 0.2031 972.2
293.15 0.2551 966.1
293.15 0.3050 960.7
293.15 0.3522 956.4
293.15 0.4063 950.8
293.15 0.4553 946.7
293.15 0.5058 942.7
293.15 0.5665 938.2
293.15 0.6027 935.8
293.15 0.6567 932.3
293.15 0.7046 929.6
293.15 0.7543 926.9
293.15 0.8025 924.5
293.15 0.8516 922.3
293.15 0.8996 920.3
293.15 0.9228 919.8
293.15 1.0000 917.1
298.15 0.0000 986.1
298.15 0.0520 977.9
298.15 0.1030 970.4
298.15 0.1538 963.6
298.15 0.2031 957.5
298.15 0.2551 951.6
298.15 0.3050 946.3
298.15 0.3522 942.1
298.15 0.4063 936.7
298.15 0.4553 932.6
298.15 0.5058 928.6
298.15 0.5665 924.2
298.15 0.6027 921.9
298.15 0.6567 918.5
298.15 0.7046 915.8
298.15 0.7543 913.2
298.15 0.8025 910.8
298.15 0.8516 908.7
298.15 0.8996 906.8
298.15 0.9228 906.3
298.15 1.0000 903.6
303.15 0.0000 971.0
303.15 0.0520 962.9
303.15 0.1030 955.5
303.15 0.1538 948.9
303.15 0.2031 942.8
303.15 0.2551 937.0
303.15 0.3050 931.8
303.15 0.3522 927.8
303.15 0.4063 922.4
303.15 0.4553 918.4
303.15 0.5058 914.5
303.15 0.5665 910.3
303.15 0.6027 908.0
303.15 0.6567 904.7
303.15 0.7046 902.0
303.15 0.7543 899.5
303.15 0.8025 897.2
303.15 0.8516 895.1
303.15 0.8996 893.3
303.15 0.9228 892.9
303.15 1.0000 890.2
308.15 0.0000 955.9
308.15 0.0520 947.9
308.15 0.1030 940.7
308.15 0.1538 934.2
308.15 0.2031 928.1
308.15 0.2551 922.6
308.15 0.3050 917.3
308.15 0.3522 913.5
308.15 0.4063 908.2
308.15 0.4553 904.2
308.15 0.5058 900.5
308.15 0.5665 896.4
308.15 0.6027 894.1
308.15 0.6567 891.0
308.15 0.7046 888.3
308.15 0.7543 885.9
308.15 0.8025 883.7
308.15 0.8516 881.6
308.15 0.8996 879.9
308.15 0.9228 879.4
308.15 1.0000 876.8
313.15 0.0000 940.8
313.15 0.0520 933.0
313.15 0.1030 925.9
313.15 0.1538 919.1
313.15 0.2031 913.6
313.15 0.2551 908.1
313.15 0.3050 903.0
313.15 0.3522 898.9
313.15 0.4063 894.0
313.15 0.4553 890.3
313.15 0.5058 886.5
313.15 0.5665 882.6
313.15 0.6027 880.3
313.15 0.6567 877.2
313.15 0.7046 874.7
313.15 0.7543 872.3
313.15 0.8025 870.2
313.15 0.8516 868.3
313.15 0.8996 866.5
313.15 0.9228 865.9
313.15 1.0000 863.6

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 308.15 (Liquid)

Mole fraction of Methane, bromotrichloro- (1) - Liquid Vapor or sublimation pressure, kPa - Gas
0.0392 30.24
0.0881 29.30
0.1245 28.57
0.1918 27.20
0.2536 26.05
0.3271 24.57
0.3664 23.83
0.4174 22.78
0.4642 21.89
0.4983 21.14
0.5625 19.81
0.6026 18.92
0.6583 17.73
0.6859 17.02
0.7318 15.97
0.7744 14.86
0.8383 13.21
0.8953 11.56
0.9694 9.38

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 308.15 (Liquid)

Mole fraction of Methane, bromotrichloro- (1) - Liquid Vapor or sublimation pressure, kPa - Gas
0.0392 30.24
0.0881 29.30
0.1245 28.57
0.1918 27.20
0.2536 26.05
0.3271 24.57
0.3664 23.83
0.4174 22.78
0.4642 21.89
0.4983 21.14
0.5625 19.81
0.6026 18.92
0.6583 17.73
0.6859 17.02
0.7318 15.97
0.7744 14.86
0.8383 13.21
0.8953 11.56
0.9694 9.38

Sources