Mixture of Piperazine + Ammonia + Water

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Piperazine

Name
Piperazine
InChI
InChI=1S/C4H10N2/c1-2-6-4-3-5-1/h5-6H,1-4H2
InChI Key
GLUUGHFHXGJENI-UHFFFAOYSA-N
Formula
C4H10N2
SMILES
C1CNCCN1
Mol. Weight (g/mol)
86.14
CAS
110-85-0

Ammonia

Name
Ammonia
InChI
InChI=1S/H3N/h1H3
InChI Key
QGZKDVFQNNGYKY-UHFFFAOYSA-N
Formula
H3N
SMILES
N
Mol. Weight (g/mol)
17.03
CAS
7664-41-7

Water

Name
Water
InChI
InChI=1S/H2O/h1H2
InChI Key
XLYOFNOQVPJJNP-UHFFFAOYSA-N
Formula
H2O
SMILES
O
Mol. Weight (g/mol)
18.02
CAS
7732-18-5
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Datasets

  1. Partial pressure, kPa (2)
  2. η - Viscosity, Pa*s (2)
  3. ρl - Mass density, kg/m3 (2)

Partial pressure, kPa of Ammonia (2) [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Ammonia (2) - Liquid Mole fraction of Piperazine (1) - Liquid Partial pressure, kPa of Ammonia (2) - Gas
293.65 0.1083 0.0000 10.42
293.75 0.1063 0.0072 10.77
294.15 0.0269 0.0072 2.35
294.75 0.0270 0.0000 2.25
295.05 0.0552 0.0073 5.02
295.65 0.0556 0.0000 4.94
295.65 0.1568 0.0071 20.72
295.65 0.1571 0.0000 19.61
303.65 0.0267 0.0072 3.49
303.65 0.0270 0.0000 3.40
303.75 0.0541 0.0072 8.07
303.85 0.0550 0.0000 7.43
304.35 0.1066 0.0072 17.28
304.35 0.1080 0.0000 16.49
304.35 0.1583 0.0000 30.08
304.55 0.1560 0.0071 33.03
313.15 0.0265 0.0072 5.17
313.15 0.0270 0.0000 5.00
313.15 0.0531 0.0073 11.31
313.15 0.0538 0.0000 10.98
313.15 0.1040 0.0000 24.38
313.15 0.1050 0.0072 27.01
313.45 0.1536 0.0071 46.16
313.75 0.1532 0.0000 45.29

Partial pressure, kPa of Ammonia (2) [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Ammonia (2) - Liquid Mole fraction of Piperazine (1) - Liquid Partial pressure, kPa of Ammonia (2) - Gas
293.65 0.1083 0.0000 10.42
293.75 0.1063 0.0072 10.77
294.15 0.0269 0.0072 2.35
294.75 0.0270 0.0000 2.25
295.05 0.0552 0.0073 5.02
295.65 0.0556 0.0000 4.94
295.65 0.1568 0.0071 20.72
295.65 0.1571 0.0000 19.61
303.65 0.0267 0.0072 3.49
303.65 0.0270 0.0000 3.40
303.75 0.0541 0.0072 8.07
303.85 0.0550 0.0000 7.43
304.35 0.1066 0.0072 17.28
304.35 0.1080 0.0000 16.49
304.35 0.1583 0.0000 30.08
304.55 0.1560 0.0071 33.03
313.15 0.0265 0.0072 5.17
313.15 0.0270 0.0000 5.00
313.15 0.0531 0.0073 11.31
313.15 0.0538 0.0000 10.98
313.15 0.1040 0.0000 24.38
313.15 0.1050 0.0072 27.01
313.45 0.1536 0.0071 46.16
313.75 0.1532 0.0000 45.29

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ammonia (2) - Liquid Mole fraction of Piperazine (1) - Liquid Viscosity, Pa*s - Liquid
283.15 0.0108 0.0018 0.0014
283.15 0.0252 0.0018 0.0014
283.15 0.0282 0.0075 0.0016
283.15 0.0500 0.0019 0.0015
283.15 0.0504 0.0075 0.0017
283.15 0.0589 0.0037 0.0015
283.15 0.0592 0.0056 0.0016
283.15 0.0694 0.0074 0.0015
283.15 0.0779 0.0038 0.0016
283.15 0.0798 0.0019 0.0015
283.15 0.1084 0.0057 0.0017
283.15 0.1096 0.0077 0.0018
293.15 0.0108 0.0018 0.0011
293.15 0.0252 0.0018 0.0011
293.15 0.0282 0.0075 0.0012
293.15 0.0500 0.0019 0.0011
293.15 0.0504 0.0075 0.0013
293.15 0.0589 0.0037 0.0012
293.15 0.0592 0.0056 0.0012
293.15 0.0694 0.0074 0.0012
293.15 0.0779 0.0038 0.0012
293.15 0.0798 0.0019 0.0012
293.15 0.1084 0.0057 0.0013
293.15 0.1096 0.0077 0.0014
303.15 0.0108 0.0018 0.0009
303.15 0.0252 0.0018 0.0009
303.15 0.0282 0.0075 0.0010
303.15 0.0500 0.0019 0.0009
303.15 0.0504 0.0075 0.0011
303.15 0.0589 0.0037 0.0010
303.15 0.0592 0.0056 0.0010
303.15 0.0694 0.0074 0.0010
303.15 0.0779 0.0038 0.0010
303.15 0.0798 0.0019 0.0010
303.15 0.1084 0.0057 0.0011
303.15 0.1096 0.0077 0.0011
313.15 0.0108 0.0018 0.0007
313.15 0.0252 0.0018 0.0007
313.15 0.0282 0.0075 0.0008
313.15 0.0500 0.0019 0.0008
313.15 0.0504 0.0075 0.0009
313.15 0.0589 0.0037 0.0008
313.15 0.0592 0.0056 0.0009
313.15 0.0694 0.0074 0.0008
313.15 0.0779 0.0038 0.0008
313.15 0.0798 0.0019 0.0008
313.15 0.1084 0.0057 0.0009
313.15 0.1096 0.0077 0.0009

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ammonia (2) - Liquid Mole fraction of Piperazine (1) - Liquid Viscosity, Pa*s - Liquid
283.15 0.0108 0.0018 0.0014
283.15 0.0252 0.0018 0.0014
283.15 0.0282 0.0075 0.0016
283.15 0.0500 0.0019 0.0015
283.15 0.0504 0.0075 0.0017
283.15 0.0589 0.0037 0.0015
283.15 0.0592 0.0056 0.0016
283.15 0.0694 0.0074 0.0015
283.15 0.0779 0.0038 0.0016
283.15 0.0798 0.0019 0.0015
283.15 0.1084 0.0057 0.0017
283.15 0.1096 0.0077 0.0018
293.15 0.0108 0.0018 0.0011
293.15 0.0252 0.0018 0.0011
293.15 0.0282 0.0075 0.0012
293.15 0.0500 0.0019 0.0011
293.15 0.0504 0.0075 0.0013
293.15 0.0589 0.0037 0.0012
293.15 0.0592 0.0056 0.0012
293.15 0.0694 0.0074 0.0012
293.15 0.0779 0.0038 0.0012
293.15 0.0798 0.0019 0.0012
293.15 0.1084 0.0057 0.0013
293.15 0.1096 0.0077 0.0014
303.15 0.0108 0.0018 0.0009
303.15 0.0252 0.0018 0.0009
303.15 0.0282 0.0075 0.0010
303.15 0.0500 0.0019 0.0009
303.15 0.0504 0.0075 0.0011
303.15 0.0589 0.0037 0.0010
303.15 0.0592 0.0056 0.0010
303.15 0.0694 0.0074 0.0010
303.15 0.0779 0.0038 0.0010
303.15 0.0798 0.0019 0.0010
303.15 0.1084 0.0057 0.0011
303.15 0.1096 0.0077 0.0011
313.15 0.0108 0.0018 0.0007
313.15 0.0252 0.0018 0.0007
313.15 0.0282 0.0075 0.0008
313.15 0.0500 0.0019 0.0008
313.15 0.0504 0.0075 0.0009
313.15 0.0589 0.0037 0.0008
313.15 0.0592 0.0056 0.0009
313.15 0.0694 0.0074 0.0008
313.15 0.0779 0.0038 0.0008
313.15 0.0798 0.0019 0.0008
313.15 0.1084 0.0057 0.0009
313.15 0.1096 0.0077 0.0009

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ammonia (2) - Liquid Mole fraction of Piperazine (1) - Liquid Mass density, kg/m3 - Liquid
283.15 0.0069 0.0074 998.64
283.15 0.0108 0.0018 995.68
283.15 0.0252 0.0018 989.92
283.15 0.0282 0.0074 990.37
283.15 0.0500 0.0019 980.65
283.15 0.0504 0.0075 982.73
283.15 0.0529 0.0056 978.83
283.15 0.0589 0.0037 978.46
283.15 0.0779 0.0038 971.08
283.15 0.0798 0.0019 969.31
283.15 0.1084 0.0057 960.34
283.15 0.1096 0.0077 962.49
293.15 0.0069 0.0074 996.92
293.15 0.0108 0.0018 994.0
293.15 0.0252 0.0018 988.0
293.15 0.0282 0.0074 988.28
293.15 0.0500 0.0019 978.34
293.15 0.0504 0.0075 980.29
293.15 0.0529 0.0056 976.27
293.15 0.0589 0.0037 975.93
293.15 0.0779 0.0038 968.23
293.15 0.0798 0.0019 966.36
293.15 0.1084 0.0057 956.82
293.15 0.1096 0.0077 959.01
303.15 0.0069 0.0074 994.24
303.15 0.0108 0.0018 991.35
303.15 0.0252 0.0018 985.19
303.15 0.0282 0.0074 985.31
303.15 0.0500 0.0019 975.22
303.15 0.0504 0.0075 977.06
303.15 0.0529 0.0056 972.95
303.15 0.0589 0.0037 972.7
303.15 0.0779 0.0038 964.72
303.15 0.0798 0.0019 962.89
303.15 0.1084 0.0057 952.81
303.15 0.1096 0.0077 954.85
313.15 0.0069 0.0074 990.7
313.15 0.0108 0.0018 987.82
313.15 0.0252 0.0018 981.53
313.15 0.0282 0.0074 981.54
313.15 0.0500 0.0019 971.41
313.15 0.0504 0.0075 973.03
313.15 0.0529 0.0056 968.94
313.15 0.0589 0.0037 968.25
313.15 0.0779 0.0038 960.47
313.15 0.0798 0.0019 958.43
313.15 0.1084 0.0057 948.08
313.15 0.1096 0.0077 949.92
323.15 0.0069 0.0074 986.43
323.15 0.0108 0.0018 982.54
323.15 0.0252 0.0018 977.17
323.15 0.0282 0.0074 977.1
323.15 0.0500 0.0019 966.96
323.15 0.0504 0.0075 968.5
323.15 0.0529 0.0056 964.2
323.15 0.0589 0.0037 964.03
323.15 0.0779 0.0038 955.62
323.15 0.0798 0.0019 953.79
323.15 0.1084 0.0057 942.89
323.15 0.1096 0.0077 944.95

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ammonia (2) - Liquid Mole fraction of Piperazine (1) - Liquid Mass density, kg/m3 - Liquid
283.15 0.0069 0.0074 998.64
283.15 0.0108 0.0018 995.68
283.15 0.0252 0.0018 989.92
283.15 0.0282 0.0074 990.37
283.15 0.0500 0.0019 980.65
283.15 0.0504 0.0075 982.73
283.15 0.0529 0.0056 978.83
283.15 0.0589 0.0037 978.46
283.15 0.0779 0.0038 971.08
283.15 0.0798 0.0019 969.31
283.15 0.1084 0.0057 960.34
283.15 0.1096 0.0077 962.49
293.15 0.0069 0.0074 996.92
293.15 0.0108 0.0018 994.0
293.15 0.0252 0.0018 988.0
293.15 0.0282 0.0074 988.28
293.15 0.0500 0.0019 978.34
293.15 0.0504 0.0075 980.29
293.15 0.0529 0.0056 976.27
293.15 0.0589 0.0037 975.93
293.15 0.0779 0.0038 968.23
293.15 0.0798 0.0019 966.36
293.15 0.1084 0.0057 956.82
293.15 0.1096 0.0077 959.01
303.15 0.0069 0.0074 994.24
303.15 0.0108 0.0018 991.35
303.15 0.0252 0.0018 985.19
303.15 0.0282 0.0074 985.31
303.15 0.0500 0.0019 975.22
303.15 0.0504 0.0075 977.06
303.15 0.0529 0.0056 972.95
303.15 0.0589 0.0037 972.7
303.15 0.0779 0.0038 964.72
303.15 0.0798 0.0019 962.89
303.15 0.1084 0.0057 952.81
303.15 0.1096 0.0077 954.85
313.15 0.0069 0.0074 990.7
313.15 0.0108 0.0018 987.82
313.15 0.0252 0.0018 981.53
313.15 0.0282 0.0074 981.54
313.15 0.0500 0.0019 971.41
313.15 0.0504 0.0075 973.03
313.15 0.0529 0.0056 968.94
313.15 0.0589 0.0037 968.25
313.15 0.0779 0.0038 960.47
313.15 0.0798 0.0019 958.43
313.15 0.1084 0.0057 948.08
313.15 0.1096 0.0077 949.92
323.15 0.0069 0.0074 986.43
323.15 0.0108 0.0018 982.54
323.15 0.0252 0.0018 977.17
323.15 0.0282 0.0074 977.1
323.15 0.0500 0.0019 966.96
323.15 0.0504 0.0075 968.5
323.15 0.0529 0.0056 964.2
323.15 0.0589 0.0037 964.03
323.15 0.0779 0.0038 955.62
323.15 0.0798 0.0019 953.79
323.15 0.1084 0.0057 942.89
323.15 0.1096 0.0077 944.95

Sources