Mixture of Butane, 1-ethoxy- + Butane, 2-chloro-

Excel

Butane, 1-ethoxy-

Name
Butane, 1-ethoxy-
InChI
InChI=1S/C6H14O/c1-3-5-6-7-4-2/h3-6H2,1-2H3
InChI Key
PZHIWRCQKBBTOW-UHFFFAOYSA-N
Formula
C6H14O
SMILES
CCCCOCC
Mol. Weight (g/mol)
102.17
CAS
628-81-9

Butane, 2-chloro-

Name
Butane, 2-chloro-
InChI
InChI=1S/C4H9Cl/c1-3-4(2)5/h4H,3H2,1-2H3
InChI Key
BSPCSKHALVHRSR-UHFFFAOYSA-N
Formula
C4H9Cl
SMILES
CCC(C)Cl
Mol. Weight (g/mol)
92.57
CAS
78-86-4
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Datasets

  1. Mole fraction (2)
  2. η - Viscosity, Pa*s (2)
  3. Pvap - Vapor or sublimation pressure, kPa (2)
  4. ρl - Mass density, kg/m3 (2)

Mole fraction of Butane, 2-chloro- (2) [ref]

Fixed Measured
Mole fraction of Butane, 2-chloro- (2) - Liquid Temperature, K - Liquid Mole fraction of Butane, 2-chloro- (2) - Gas
0.0669 288.15 0.1728
0.0749 298.15 0.1776
0.0799 308.15 0.1823
0.1331 288.15 0.3017
0.1603 298.15 0.3377
0.1651 308.15 0.3386
0.2259 288.15 0.4689
0.2733 298.15 0.4773
0.2798 308.15 0.4923
0.3315 288.15 0.5894
0.3732 298.15 0.6060
0.3750 308.15 0.6037
0.3943 288.15 0.6791
0.4211 298.15 0.6630
0.4315 308.15 0.6560
0.4823 288.15 0.7319
0.5254 298.15 0.7371
0.5263 308.15 0.7393
0.5645 288.15 0.7958
0.5933 298.15 0.8015
0.6116 308.15 0.7994
0.6529 288.15 0.8500
0.6753 298.15 0.8437
0.6829 308.15 0.8444
0.7430 288.15 0.8884
0.7622 298.15 0.8933
0.7666 308.15 0.8919
0.8209 288.15 0.9330
0.8422 298.15 0.9316
0.8422 308.15 0.9296
0.9084 288.15 0.9666
0.9125 298.15 0.9646
0.9139 308.15 0.9632

Mole fraction of Butane, 2-chloro- (2) [ref]

Fixed Measured
Mole fraction of Butane, 2-chloro- (2) - Liquid Temperature, K - Liquid Mole fraction of Butane, 2-chloro- (2) - Gas
0.0669 288.15 0.1728
0.0749 298.15 0.1776
0.0799 308.15 0.1823
0.1331 288.15 0.3017
0.1603 298.15 0.3377
0.1651 308.15 0.3386
0.2259 288.15 0.4689
0.2733 298.15 0.4773
0.2798 308.15 0.4923
0.3315 288.15 0.5894
0.3732 298.15 0.6060
0.3750 308.15 0.6037
0.3943 288.15 0.6791
0.4211 298.15 0.6630
0.4315 308.15 0.6560
0.4823 288.15 0.7319
0.5254 298.15 0.7371
0.5263 308.15 0.7393
0.5645 288.15 0.7958
0.5933 298.15 0.8015
0.6116 308.15 0.7994
0.6529 288.15 0.8500
0.6753 298.15 0.8437
0.6829 308.15 0.8444
0.7430 288.15 0.8884
0.7622 298.15 0.8933
0.7666 308.15 0.8919
0.8209 288.15 0.9330
0.8422 298.15 0.9316
0.8422 308.15 0.9296
0.9084 288.15 0.9666
0.9125 298.15 0.9646
0.9139 308.15 0.9632

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Butane, 2-chloro- (2) - Liquid Viscosity, Pa*s - Liquid
283.15 0.0000 0.0005
283.15 0.0525 0.0005
283.15 0.0974 0.0005
283.15 0.2001 0.0005
283.15 0.3027 0.0005
283.15 0.4000 0.0005
283.15 0.5248 0.0005
283.15 0.6016 0.0005
283.15 0.7006 0.0005
283.15 0.7993 0.0005
283.15 0.8997 0.0005
283.15 0.9502 0.0005
283.15 1.0000 0.0005
288.15 0.0000 0.0005
288.15 0.0525 0.0004
288.15 0.0974 0.0004
288.15 0.2001 0.0004
288.15 0.3027 0.0004
288.15 0.4000 0.0004
288.15 0.5248 0.0004
288.15 0.6016 0.0004
288.15 0.7006 0.0004
288.15 0.7993 0.0004
288.15 0.8997 0.0004
288.15 0.9502 0.0004
288.15 1.0000 0.0004
293.15 0.0000 0.0004
293.15 0.0525 0.0004
293.15 0.0974 0.0004
293.15 0.2001 0.0004
293.15 0.3027 0.0004
293.15 0.4000 0.0004
293.15 0.5248 0.0004
293.15 0.6016 0.0004
293.15 0.7006 0.0004
293.15 0.7993 0.0004
293.15 0.8997 0.0004
293.15 0.9502 0.0004
293.15 1.0000 0.0004
298.15 0.0000 0.0004
298.15 0.0525 0.0004
298.15 0.0974 0.0004
298.15 0.2001 0.0004
298.15 0.3027 0.0004
298.15 0.4000 0.0004
298.15 0.5248 0.0004
298.15 0.6016 0.0004
298.15 0.7006 0.0004
298.15 0.7993 0.0004
298.15 0.8997 0.0004
298.15 0.9502 0.0004
298.15 1.0000 0.0004
303.15 0.0000 0.0004
303.15 0.0525 0.0004
303.15 0.0974 0.0004
303.15 0.2001 0.0004
303.15 0.3027 0.0004
303.15 0.4000 0.0004
303.15 0.5248 0.0004
303.15 0.6016 0.0004
303.15 0.7006 0.0004
303.15 0.7993 0.0004
303.15 0.8997 0.0004
303.15 0.9502 0.0004
303.15 1.0000 0.0004
308.15 0.0000 0.0004
308.15 0.0525 0.0004
308.15 0.0974 0.0004
308.15 0.2001 0.0004
308.15 0.3027 0.0004
308.15 0.4000 0.0004
308.15 0.5248 0.0004
308.15 0.6016 0.0004
308.15 0.7006 0.0004
308.15 0.7993 0.0004
308.15 0.8997 0.0004
308.15 0.9502 0.0004
308.15 1.0000 0.0004
313.15 0.0000 0.0003
313.15 0.0525 0.0003
313.15 0.0974 0.0003
313.15 0.2001 0.0003
313.15 0.3027 0.0003
313.15 0.4000 0.0003
313.15 0.5248 0.0003
313.15 0.6016 0.0003
313.15 0.7006 0.0003
313.15 0.7993 0.0003
313.15 0.8997 0.0003
313.15 0.9502 0.0003
313.15 1.0000 0.0003

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Butane, 2-chloro- (2) - Liquid Viscosity, Pa*s - Liquid
283.15 0.0000 0.0005
283.15 0.0525 0.0005
283.15 0.0974 0.0005
283.15 0.2001 0.0005
283.15 0.3027 0.0005
283.15 0.4000 0.0005
283.15 0.5248 0.0005
283.15 0.6016 0.0005
283.15 0.7006 0.0005
283.15 0.7993 0.0005
283.15 0.8997 0.0005
283.15 0.9502 0.0005
283.15 1.0000 0.0005
288.15 0.0000 0.0005
288.15 0.0525 0.0004
288.15 0.0974 0.0004
288.15 0.2001 0.0004
288.15 0.3027 0.0004
288.15 0.4000 0.0004
288.15 0.5248 0.0004
288.15 0.6016 0.0004
288.15 0.7006 0.0004
288.15 0.7993 0.0004
288.15 0.8997 0.0004
288.15 0.9502 0.0004
288.15 1.0000 0.0004
293.15 0.0000 0.0004
293.15 0.0525 0.0004
293.15 0.0974 0.0004
293.15 0.2001 0.0004
293.15 0.3027 0.0004
293.15 0.4000 0.0004
293.15 0.5248 0.0004
293.15 0.6016 0.0004
293.15 0.7006 0.0004
293.15 0.7993 0.0004
293.15 0.8997 0.0004
293.15 0.9502 0.0004
293.15 1.0000 0.0004
298.15 0.0000 0.0004
298.15 0.0525 0.0004
298.15 0.0974 0.0004
298.15 0.2001 0.0004
298.15 0.3027 0.0004
298.15 0.4000 0.0004
298.15 0.5248 0.0004
298.15 0.6016 0.0004
298.15 0.7006 0.0004
298.15 0.7993 0.0004
298.15 0.8997 0.0004
298.15 0.9502 0.0004
298.15 1.0000 0.0004
303.15 0.0000 0.0004
303.15 0.0525 0.0004
303.15 0.0974 0.0004
303.15 0.2001 0.0004
303.15 0.3027 0.0004
303.15 0.4000 0.0004
303.15 0.5248 0.0004
303.15 0.6016 0.0004
303.15 0.7006 0.0004
303.15 0.7993 0.0004
303.15 0.8997 0.0004
303.15 0.9502 0.0004
303.15 1.0000 0.0004
308.15 0.0000 0.0004
308.15 0.0525 0.0004
308.15 0.0974 0.0004
308.15 0.2001 0.0004
308.15 0.3027 0.0004
308.15 0.4000 0.0004
308.15 0.5248 0.0004
308.15 0.6016 0.0004
308.15 0.7006 0.0004
308.15 0.7993 0.0004
308.15 0.8997 0.0004
308.15 0.9502 0.0004
308.15 1.0000 0.0004
313.15 0.0000 0.0003
313.15 0.0525 0.0003
313.15 0.0974 0.0003
313.15 0.2001 0.0003
313.15 0.3027 0.0003
313.15 0.4000 0.0003
313.15 0.5248 0.0003
313.15 0.6016 0.0003
313.15 0.7006 0.0003
313.15 0.7993 0.0003
313.15 0.8997 0.0003
313.15 0.9502 0.0003
313.15 1.0000 0.0003

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Mole fraction of Butane, 2-chloro- (2) - Liquid Temperature, K - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0669 288.15 5.11
0.0749 298.15 8.61
0.0799 308.15 13.86
0.1331 288.15 5.79
0.1603 298.15 9.79
0.1651 308.15 15.78
0.2259 288.15 6.59
0.2733 298.15 11.20
0.2798 308.15 17.69
0.3315 288.15 7.60
0.3732 298.15 12.51
0.3750 308.15 19.55
0.3943 288.15 8.21
0.4211 298.15 13.21
0.4315 308.15 20.45
0.4823 288.15 9.05
0.5254 298.15 14.63
0.5263 308.15 22.49
0.5645 288.15 9.84
0.5933 298.15 15.74
0.6116 308.15 24.15
0.6529 288.15 10.50
0.6753 298.15 16.66
0.6829 308.15 25.50
0.7430 288.15 11.21
0.7622 298.15 17.75
0.7666 308.15 27.12
0.8209 288.15 11.79
0.8422 298.15 18.66
0.8422 308.15 28.50
0.9084 288.15 12.59
0.9125 298.15 19.73
0.9139 308.15 29.93

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Mole fraction of Butane, 2-chloro- (2) - Liquid Temperature, K - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0669 288.15 5.11
0.0749 298.15 8.61
0.0799 308.15 13.86
0.1331 288.15 5.79
0.1603 298.15 9.79
0.1651 308.15 15.78
0.2259 288.15 6.59
0.2733 298.15 11.20
0.2798 308.15 17.69
0.3315 288.15 7.60
0.3732 298.15 12.51
0.3750 308.15 19.55
0.3943 288.15 8.21
0.4211 298.15 13.21
0.4315 308.15 20.45
0.4823 288.15 9.05
0.5254 298.15 14.63
0.5263 308.15 22.49
0.5645 288.15 9.84
0.5933 298.15 15.74
0.6116 308.15 24.15
0.6529 288.15 10.50
0.6753 298.15 16.66
0.6829 308.15 25.50
0.7430 288.15 11.21
0.7622 298.15 17.75
0.7666 308.15 27.12
0.8209 288.15 11.79
0.8422 298.15 18.66
0.8422 308.15 28.50
0.9084 288.15 12.59
0.9125 298.15 19.73
0.9139 308.15 29.93

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Butane, 2-chloro- (2) - Liquid Mass density, kg/m3 - Liquid
283.15 0.0000 759.632
283.15 0.0525 765.075
283.15 0.0974 769.762
283.15 0.2001 780.678
283.15 0.3027 791.975
283.15 0.4000 803.128
283.15 0.5248 818.168
283.15 0.6016 827.85
283.15 0.7006 840.875
283.15 0.7993 854.496
283.15 0.8997 869.038
283.15 0.9502 876.678
283.15 1.0000 884.34
288.15 0.0000 754.838
288.15 0.0525 760.242
288.15 0.0974 764.897
288.15 0.2001 775.744
288.15 0.3027 786.952
288.15 0.4000 798.037
288.15 0.5248 812.98
288.15 0.6016 822.613
288.15 0.7006 835.554
288.15 0.7993 849.096
288.15 0.8997 863.543
288.15 0.9502 871.137
288.15 1.0000 878.756
293.15 0.0000 750.018
293.15 0.0525 755.382
293.15 0.0974 760.006
293.15 0.2001 770.778
293.15 0.3027 781.909
293.15 0.4000 792.91
293.15 0.5248 807.76
293.15 0.6016 817.343
293.15 0.7006 830.202
293.15 0.7993 843.651
293.15 0.8997 858.003
293.15 0.9502 865.523
293.15 1.0000 873.13
298.15 0.0000 745.173
298.15 0.0525 750.495
298.15 0.0974 755.081
298.15 0.2001 765.789
298.15 0.3027 776.837
298.15 0.4000 787.763
298.15 0.5248 802.529
298.15 0.6016 812.044
298.15 0.7006 824.819
298.15 0.7993 838.178
298.15 0.8997 852.437
298.15 0.9502 859.908
298.15 1.0000 867.474
303.15 0.0000 740.3
303.15 0.0525 745.579
303.15 0.0974 750.131
303.15 0.2001 760.765
303.15 0.3027 771.741
303.15 0.4000 782.594
303.15 0.5248 797.247
303.15 0.6016 806.71
303.15 0.7006 819.404
303.15 0.7993 832.663
303.15 0.8997 846.826
303.15 0.9502 854.248
303.15 1.0000 861.779
308.15 0.0000 735.393
308.15 0.0525 740.632
308.15 0.0974 745.146
308.15 0.2001 755.706
308.15 0.3027 766.603
308.15 0.4000 777.385
308.15 0.5248 791.941
308.15 0.6016 801.337
308.15 0.7006 813.943
308.15 0.7993 827.116
308.15 0.8997 841.188
308.15 0.9502 848.552
308.15 1.0000 856.044
313.15 0.0000 730.451
313.15 0.0525 735.646
313.15 0.0974 740.124
313.15 0.2001 750.603
313.15 0.3027 761.432
313.15 0.4000 772.132
313.15 0.5248 786.597
313.15 0.6016 795.924
313.15 0.7006 808.443
313.15 0.7993 821.529
313.15 0.8997 835.498
313.15 0.9502 842.814
313.15 1.0000 850.266

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Butane, 2-chloro- (2) - Liquid Mass density, kg/m3 - Liquid
283.15 0.0000 759.632
283.15 0.0525 765.075
283.15 0.0974 769.762
283.15 0.2001 780.678
283.15 0.3027 791.975
283.15 0.4000 803.128
283.15 0.5248 818.168
283.15 0.6016 827.85
283.15 0.7006 840.875
283.15 0.7993 854.496
283.15 0.8997 869.038
283.15 0.9502 876.678
283.15 1.0000 884.34
288.15 0.0000 754.838
288.15 0.0525 760.242
288.15 0.0974 764.897
288.15 0.2001 775.744
288.15 0.3027 786.952
288.15 0.4000 798.037
288.15 0.5248 812.98
288.15 0.6016 822.613
288.15 0.7006 835.554
288.15 0.7993 849.096
288.15 0.8997 863.543
288.15 0.9502 871.137
288.15 1.0000 878.756
293.15 0.0000 750.018
293.15 0.0525 755.382
293.15 0.0974 760.006
293.15 0.2001 770.778
293.15 0.3027 781.909
293.15 0.4000 792.91
293.15 0.5248 807.76
293.15 0.6016 817.343
293.15 0.7006 830.202
293.15 0.7993 843.651
293.15 0.8997 858.003
293.15 0.9502 865.523
293.15 1.0000 873.13
298.15 0.0000 745.173
298.15 0.0525 750.495
298.15 0.0974 755.081
298.15 0.2001 765.789
298.15 0.3027 776.837
298.15 0.4000 787.763
298.15 0.5248 802.529
298.15 0.6016 812.044
298.15 0.7006 824.819
298.15 0.7993 838.178
298.15 0.8997 852.437
298.15 0.9502 859.908
298.15 1.0000 867.474
303.15 0.0000 740.3
303.15 0.0525 745.579
303.15 0.0974 750.131
303.15 0.2001 760.765
303.15 0.3027 771.741
303.15 0.4000 782.594
303.15 0.5248 797.247
303.15 0.6016 806.71
303.15 0.7006 819.404
303.15 0.7993 832.663
303.15 0.8997 846.826
303.15 0.9502 854.248
303.15 1.0000 861.779
308.15 0.0000 735.393
308.15 0.0525 740.632
308.15 0.0974 745.146
308.15 0.2001 755.706
308.15 0.3027 766.603
308.15 0.4000 777.385
308.15 0.5248 791.941
308.15 0.6016 801.337
308.15 0.7006 813.943
308.15 0.7993 827.116
308.15 0.8997 841.188
308.15 0.9502 848.552
308.15 1.0000 856.044
313.15 0.0000 730.451
313.15 0.0525 735.646
313.15 0.0974 740.124
313.15 0.2001 750.603
313.15 0.3027 761.432
313.15 0.4000 772.132
313.15 0.5248 786.597
313.15 0.6016 795.924
313.15 0.7006 808.443
313.15 0.7993 821.529
313.15 0.8997 835.498
313.15 0.9502 842.814
313.15 1.0000 850.266

Sources