Mixture of Phenol, 2-methoxy- + Tetrahydrofuran

Excel

Phenol, 2-methoxy-

Name
Phenol, 2-methoxy-
InChI
InChI=1S/C7H8O2/c1-9-7-5-3-2-4-6(7)8/h2-5,8H,1H3
InChI Key
LHGVFZTZFXWLCP-UHFFFAOYSA-N
Formula
C7H8O2
SMILES
COc1ccccc1O
Mol. Weight (g/mol)
124.14
CAS
90-05-1

Tetrahydrofuran

Name
Tetrahydrofuran
InChI
InChI=1S/C4H8O/c1-2-4-5-3-1/h1-4H2
InChI Key
WYURNTSHIVDZCO-UHFFFAOYSA-N
Formula
C4H8O
SMILES
C1CCOC1
Mol. Weight (g/mol)
72.11
CAS
109-99-9
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Datasets

  1. Activity coefficient (2)

Activity coefficient of Tetrahydrofuran (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydrofuran (2) - Liquid Activity coefficient of Tetrahydrofuran (2) - Liquid
298.15 0.0895 0.2830
298.15 0.0938 0.2870
298.15 0.0979 0.2870
298.15 0.1932 0.3580
298.15 0.1946 0.3600
298.15 0.1939 0.3620
298.15 0.2940 0.4530
298.15 0.2911 0.4500
298.15 0.2905 0.4530
298.15 0.3818 0.5540
298.15 0.3899 0.5480
298.15 0.3886 0.5610
298.15 0.4958 0.6940
298.15 0.5193 0.7200
298.15 0.5103 0.7100
298.15 0.6503 0.8590
298.15 0.6266 0.8360
298.15 0.6240 0.8350
298.15 0.7131 0.9060
298.15 0.7306 0.9150
298.15 0.7087 0.9070
298.15 0.8006 0.9580
298.15 0.8069 0.9560
298.15 0.8035 0.9670
298.15 0.8994 0.9910
298.15 0.9108 0.9930
298.15 0.8979 0.9870
308.15 0.1010 0.3480
308.15 0.0980 0.3470
308.15 0.1005 0.3440
308.15 0.1918 0.4200
308.15 0.1955 0.4260
308.15 0.1966 0.4150
308.15 0.2944 0.4960
308.15 0.3013 0.5050
308.15 0.2935 0.4960
308.15 0.3952 0.5970
308.15 0.3846 0.5890
308.15 0.3829 0.5910
308.15 0.4720 0.6850
308.15 0.4830 0.6920
308.15 0.4941 0.7060
308.15 0.6132 0.8240
308.15 0.6043 0.8160
308.15 0.6086 0.8190
308.15 0.6966 0.8880
308.15 0.7051 0.8980
308.15 0.7167 0.8940
308.15 0.7946 0.9460
308.15 0.7962 0.9480
308.15 0.7983 0.9490
308.15 0.8529 0.9770
308.15 0.8891 0.9800
308.15 0.8935 0.9840
318.15 0.0947 0.3730
318.15 0.0978 0.3790
318.15 0.0812 0.3690
318.15 0.1923 0.4380
318.15 0.1939 0.4360
318.15 0.1907 0.4330
318.15 0.2930 0.5020
318.15 0.2922 0.5080
318.15 0.2914 0.5130
318.15 0.3767 0.5870
318.15 0.3905 0.6000
318.15 0.3843 0.5960
318.15 0.4863 0.7010
318.15 0.4939 0.7140
318.15 0.4939 0.7110
318.15 0.5980 0.8020
318.15 0.5895 0.7820
318.15 0.6001 0.8080
318.15 0.6888 0.8730
318.15 0.7050 0.8840
318.15 0.7028 0.8810
318.15 0.7979 0.9350
318.15 0.8003 0.9420
318.15 0.7919 0.9300
318.15 0.8938 0.9800
318.15 0.8907 0.9700
318.15 0.9005 0.9750

Activity coefficient of Tetrahydrofuran (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydrofuran (2) - Liquid Activity coefficient of Tetrahydrofuran (2) - Liquid
298.15 0.0895 0.2830
298.15 0.0938 0.2870
298.15 0.0979 0.2870
298.15 0.1932 0.3580
298.15 0.1946 0.3600
298.15 0.1939 0.3620
298.15 0.2940 0.4530
298.15 0.2911 0.4500
298.15 0.2905 0.4530
298.15 0.3818 0.5540
298.15 0.3899 0.5480
298.15 0.3886 0.5610
298.15 0.4958 0.6940
298.15 0.5193 0.7200
298.15 0.5103 0.7100
298.15 0.6503 0.8590
298.15 0.6266 0.8360
298.15 0.6240 0.8350
298.15 0.7131 0.9060
298.15 0.7306 0.9150
298.15 0.7087 0.9070
298.15 0.8006 0.9580
298.15 0.8069 0.9560
298.15 0.8035 0.9670
298.15 0.8994 0.9910
298.15 0.9108 0.9930
298.15 0.8979 0.9870
308.15 0.1010 0.3480
308.15 0.0980 0.3470
308.15 0.1005 0.3440
308.15 0.1918 0.4200
308.15 0.1955 0.4260
308.15 0.1966 0.4150
308.15 0.2944 0.4960
308.15 0.3013 0.5050
308.15 0.2935 0.4960
308.15 0.3952 0.5970
308.15 0.3846 0.5890
308.15 0.3829 0.5910
308.15 0.4720 0.6850
308.15 0.4830 0.6920
308.15 0.4941 0.7060
308.15 0.6132 0.8240
308.15 0.6043 0.8160
308.15 0.6086 0.8190
308.15 0.6966 0.8880
308.15 0.7051 0.8980
308.15 0.7167 0.8940
308.15 0.7946 0.9460
308.15 0.7962 0.9480
308.15 0.7983 0.9490
308.15 0.8529 0.9770
308.15 0.8891 0.9800
308.15 0.8935 0.9840
318.15 0.0947 0.3730
318.15 0.0978 0.3790
318.15 0.0812 0.3690
318.15 0.1923 0.4380
318.15 0.1939 0.4360
318.15 0.1907 0.4330
318.15 0.2930 0.5020
318.15 0.2922 0.5080
318.15 0.2914 0.5130
318.15 0.3767 0.5870
318.15 0.3905 0.6000
318.15 0.3843 0.5960
318.15 0.4863 0.7010
318.15 0.4939 0.7140
318.15 0.4939 0.7110
318.15 0.5980 0.8020
318.15 0.5895 0.7820
318.15 0.6001 0.8080
318.15 0.6888 0.8730
318.15 0.7050 0.8840
318.15 0.7028 0.8810
318.15 0.7979 0.9350
318.15 0.8003 0.9420
318.15 0.7919 0.9300
318.15 0.8938 0.9800
318.15 0.8907 0.9700
318.15 0.9005 0.9750

Sources