Mixture of Propane, 2,2-dimethoxy- + Benzene, 1,2,4-trimethyl-

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Propane, 2,2-dimethoxy-

Name
Propane, 2,2-dimethoxy-
InChI
InChI=1S/C5H12O2/c1-5(2,6-3)7-4/h1-4H3
InChI Key
HEWZVZIVELJPQZ-UHFFFAOYSA-N
Formula
C5H12O2
SMILES
COC(C)(C)OC
Mol. Weight (g/mol)
104.15
CAS
77-76-9

Benzene, 1,2,4-trimethyl-

Name
Benzene, 1,2,4-trimethyl-
InChI
InChI=1S/C9H12/c1-7-4-5-8(2)9(3)6-7/h4-6H,1-3H3
InChI Key
GWHJZXXIDMPWGX-UHFFFAOYSA-N
Formula
C9H12
SMILES
Cc1ccc(C)c(C)c1
Mol. Weight (g/mol)
120.19
CAS
95-63-6
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Datasets

  1. γ - Surface tension liquid-gas, N/m (2)
  2. Excess molar volume, m3/mol (2)

Surface tension liquid-gas, N/m [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 2,2-dimethoxy- (1) - Liquid Surface tension liquid-gas, N/m - Liquid
298.15 0.0000 0.0293
298.15 0.0523 0.0287
298.15 0.0998 0.0282
298.15 0.1497 0.0276
298.15 0.1996 0.0271
298.15 0.2517 0.0266
298.15 0.3009 0.0261
298.15 0.3494 0.0257
298.15 0.3987 0.0252
298.15 0.4502 0.0248
298.15 0.4994 0.0244
298.15 0.5498 0.0239
298.15 0.5996 0.0236
298.15 0.6508 0.0232
298.15 0.6997 0.0228
298.15 0.7498 0.0225
298.15 0.7992 0.0222
298.15 0.8508 0.0220
298.15 0.8997 0.0218
298.15 0.9489 0.0216
298.15 1.0000 0.0215
308.15 0.0000 0.0282
308.15 0.0515 0.0276
308.15 0.0998 0.0270
308.15 0.1499 0.0265
308.15 0.2001 0.0260
308.15 0.2475 0.0255
308.15 0.3020 0.0250
308.15 0.3512 0.0245
308.15 0.3995 0.0241
308.15 0.4485 0.0237
308.15 0.4989 0.0232
308.15 0.5542 0.0228
308.15 0.5998 0.0224
308.15 0.6518 0.0220
308.15 0.6987 0.0217
308.15 0.7455 0.0214
308.15 0.7962 0.0211
308.15 0.8510 0.0209
308.15 0.8973 0.0207
308.15 0.9456 0.0205
308.15 1.0000 0.0204
313.15 0.0000 0.0277
313.15 0.0506 0.0270
313.15 0.0996 0.0264
313.15 0.1509 0.0259
313.15 0.1994 0.0254
313.15 0.2511 0.0249
313.15 0.3032 0.0244
313.15 0.3475 0.0239
313.15 0.3981 0.0235
313.15 0.4501 0.0231
313.15 0.5000 0.0227
313.15 0.5487 0.0222
313.15 0.5993 0.0218
313.15 0.6504 0.0215
313.15 0.6993 0.0211
313.15 0.7486 0.0208
313.15 0.7987 0.0205
313.15 0.8417 0.0203
313.15 0.8929 0.0201
313.15 0.9487 0.0200
313.15 1.0000 0.0199

Surface tension liquid-gas, N/m [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 2,2-dimethoxy- (1) - Liquid Surface tension liquid-gas, N/m - Liquid
298.15 0.0000 0.0293
298.15 0.0523 0.0287
298.15 0.0998 0.0282
298.15 0.1497 0.0276
298.15 0.1996 0.0271
298.15 0.2517 0.0266
298.15 0.3009 0.0261
298.15 0.3494 0.0257
298.15 0.3987 0.0252
298.15 0.4502 0.0248
298.15 0.4994 0.0244
298.15 0.5498 0.0239
298.15 0.5996 0.0236
298.15 0.6508 0.0232
298.15 0.6997 0.0228
298.15 0.7498 0.0225
298.15 0.7992 0.0222
298.15 0.8508 0.0220
298.15 0.8997 0.0218
298.15 0.9489 0.0216
298.15 1.0000 0.0215
308.15 0.0000 0.0282
308.15 0.0515 0.0276
308.15 0.0998 0.0270
308.15 0.1499 0.0265
308.15 0.2001 0.0260
308.15 0.2475 0.0255
308.15 0.3020 0.0250
308.15 0.3512 0.0245
308.15 0.3995 0.0241
308.15 0.4485 0.0237
308.15 0.4989 0.0232
308.15 0.5542 0.0228
308.15 0.5998 0.0224
308.15 0.6518 0.0220
308.15 0.6987 0.0217
308.15 0.7455 0.0214
308.15 0.7962 0.0211
308.15 0.8510 0.0209
308.15 0.8973 0.0207
308.15 0.9456 0.0205
308.15 1.0000 0.0204
313.15 0.0000 0.0277
313.15 0.0506 0.0270
313.15 0.0996 0.0264
313.15 0.1509 0.0259
313.15 0.1994 0.0254
313.15 0.2511 0.0249
313.15 0.3032 0.0244
313.15 0.3475 0.0239
313.15 0.3981 0.0235
313.15 0.4501 0.0231
313.15 0.5000 0.0227
313.15 0.5487 0.0222
313.15 0.5993 0.0218
313.15 0.6504 0.0215
313.15 0.6993 0.0211
313.15 0.7486 0.0208
313.15 0.7987 0.0205
313.15 0.8417 0.0203
313.15 0.8929 0.0201
313.15 0.9487 0.0200
313.15 1.0000 0.0199

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 2,2-dimethoxy- (1) - Liquid Excess molar volume, m3/mol - Liquid
298.15 0.0523 -1.0000e-08
298.15 0.0998 -1.6000e-08
298.15 0.1497 -2.3000e-08
298.15 0.1996 -3.0000e-08
298.15 0.2517 -3.8000e-08
298.15 0.3009 -4.3000e-08
298.15 0.3494 -4.7000e-08
298.15 0.3987 -5.1000e-08
298.15 0.4502 -5.3000e-08
298.15 0.4994 -5.6000e-08
298.15 0.5498 -5.6000e-08
298.15 0.5996 -5.8000e-08
298.15 0.6508 -5.8000e-08
298.15 0.6997 -5.4000e-08
298.15 0.7498 -5.1000e-08
298.15 0.7992 -4.4000e-08
298.15 0.8508 -3.7000e-08
298.15 0.8997 -2.9000e-08
298.15 0.9489 -1.7000e-08
308.15 0.0515 -1.1000e-08
308.15 0.0998 -2.0000e-08
308.15 0.1499 -3.1000e-08
308.15 0.2001 -4.0000e-08
308.15 0.2475 -4.9000e-08
308.15 0.3020 -5.9000e-08
308.15 0.3512 -6.4000e-08
308.15 0.3955 -6.9000e-08
308.15 0.4485 -7.6000e-08
308.15 0.4989 -7.9000e-08
308.15 0.5542 -8.1000e-08
308.15 0.5998 -8.2000e-08
308.15 0.6518 -8.0000e-08
308.15 0.6987 -7.7000e-08
308.15 0.7455 -7.2000e-08
308.15 0.7962 -6.2000e-08
308.15 0.8510 -5.1000e-08
308.15 0.8973 -3.9000e-08
308.15 0.9456 -2.3000e-08
313.15 0.0506 -1.3000e-08
313.15 0.0996 -2.5000e-08
313.15 0.1509 -3.7000e-08
313.15 0.1994 -4.9000e-08
313.15 0.2511 -6.1000e-08
313.15 0.3032 -7.1000e-08
313.15 0.3475 -7.9000e-08
313.15 0.3981 -8.7000e-08
313.15 0.4501 -9.2000e-08
313.15 0.5000 -9.5000e-08
313.15 0.5487 -9.9000e-08
313.15 0.5993 -1.0000e-07
313.15 0.6504 -9.6000e-08
313.15 0.6993 -9.3000e-08
313.15 0.7486 -8.4000e-08
313.15 0.7987 -7.5000e-08
313.15 0.8417 -6.5000e-08
313.15 0.8929 -4.8000e-08
313.15 0.9487 -2.9000e-08

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 2,2-dimethoxy- (1) - Liquid Excess molar volume, m3/mol - Liquid
298.15 0.0523 -1.0000e-08
298.15 0.0998 -1.6000e-08
298.15 0.1497 -2.3000e-08
298.15 0.1996 -3.0000e-08
298.15 0.2517 -3.8000e-08
298.15 0.3009 -4.3000e-08
298.15 0.3494 -4.7000e-08
298.15 0.3987 -5.1000e-08
298.15 0.4502 -5.3000e-08
298.15 0.4994 -5.6000e-08
298.15 0.5498 -5.6000e-08
298.15 0.5996 -5.8000e-08
298.15 0.6508 -5.8000e-08
298.15 0.6997 -5.4000e-08
298.15 0.7498 -5.1000e-08
298.15 0.7992 -4.4000e-08
298.15 0.8508 -3.7000e-08
298.15 0.8997 -2.9000e-08
298.15 0.9489 -1.7000e-08
308.15 0.0515 -1.1000e-08
308.15 0.0998 -2.0000e-08
308.15 0.1499 -3.1000e-08
308.15 0.2001 -4.0000e-08
308.15 0.2475 -4.9000e-08
308.15 0.3020 -5.9000e-08
308.15 0.3512 -6.4000e-08
308.15 0.3955 -6.9000e-08
308.15 0.4485 -7.6000e-08
308.15 0.4989 -7.9000e-08
308.15 0.5542 -8.1000e-08
308.15 0.5998 -8.2000e-08
308.15 0.6518 -8.0000e-08
308.15 0.6987 -7.7000e-08
308.15 0.7455 -7.2000e-08
308.15 0.7962 -6.2000e-08
308.15 0.8510 -5.1000e-08
308.15 0.8973 -3.9000e-08
308.15 0.9456 -2.3000e-08
313.15 0.0506 -1.3000e-08
313.15 0.0996 -2.5000e-08
313.15 0.1509 -3.7000e-08
313.15 0.1994 -4.9000e-08
313.15 0.2511 -6.1000e-08
313.15 0.3032 -7.1000e-08
313.15 0.3475 -7.9000e-08
313.15 0.3981 -8.7000e-08
313.15 0.4501 -9.2000e-08
313.15 0.5000 -9.5000e-08
313.15 0.5487 -9.9000e-08
313.15 0.5993 -1.0000e-07
313.15 0.6504 -9.6000e-08
313.15 0.6993 -9.3000e-08
313.15 0.7486 -8.4000e-08
313.15 0.7987 -7.5000e-08
313.15 0.8417 -6.5000e-08
313.15 0.8929 -4.8000e-08
313.15 0.9487 -2.9000e-08

Sources