Research Article

Speeds of Sound and Excess Molar Volume for Binary Mixture of 1,4-Dioxane with 1-Heptanol at Five Temperatures

Table 2

(a) Experimental values (, ) and excess thermodynamic parameters (, , , , and ) for 1,4-dioxane + 1-heptanol system at 298.15, 303.15, and 308.15 K. (b) Experimental values (, ) and excess thermodynamic parameters (, , , , and ) for 1,4-dioxane + 1-heptanol system at 313.15 and 318.15 K.
(a)


ms−1

kgm−3
*
m2N−1
*
m3 mol−1
*
m
*
kgm−2s−1

ms−1

298.15 K
0.00001327.9819.70.00000.00000.00000.00000.0000
0.16171318.1838.80.19060.02060.0805−0.0300−12.4113
0.29211313.3857.30.29190.03200.1247−0.0480−19.4349
0.40901311.7876.20.33980.03850.1469−0.0584−22.8951
0.52441312.4897.40.35100.04120.1538−0.0635−23.9247
0.63591315.8920.90.32910.03980.1463−0.0627−22.8495
0.70831318.3938.20.29660.03630.1331−0.0584−21.0012
0.79471323.6961.10.23690.02920.1077−0.0485−17.3789
0.86871329.3982.70.16660.02040.0767−0.0353−12.7616
0.93881336.61005.90.08370.01010.0390−0.0183−6.7714
1.00001344.31026.80.00000.00000.00000.00000.0000

303.15 K
0.00001310.9816.20.00000.00000.00000.00000.0000
0.16171301.6835.00.18610.02060.0781−0.0284−11.1370
0.29211296.6853.40.28850.03210.1223−0.0455−17.7549
0.40901294.3872.10.34000.03860.1457−0.0558−21.2511
0.52441294.3893.10.35490.04130.1539−0.0608−22.4960
0.63591296.8916.30.33490.03980.1472−0.0602−21.6492
0.70831298.9933.40.30240.03630.1341−0.0561−19.9310
0.79471303.6956.10.24150.02920.1085−0.0465−16.4669
0.86871308.7977.50.16940.02050.0770−0.0338−12.0406
0.93881315.41000.50.08480.01020.0390−0.0175−6.3496
1.00001322.31021.20.00000.00000.00000.00000.0000

308.15 K
0.00001294.1812.60.00000.00000.00000.00000.0000
0.16171284.4831.20.18940.02060.0787−0.0273−10.6121
0.29211279.1849.40.29490.03210.1237−0.0439−17.0206
0.40901276.2868.00.34770.03860.1473−0.0538−20.3393
0.52441275.9888.70.36290.04140.1555−0.0586−21.4749
0.63591277.8911.70.34240.03990.1486−0.0580−20.6255
0.70831279.5928.60.30900.03640.1354−0.0540−18.9585
0.79471283.6951.10.24630.02930.1093−0.0447−15.6073
0.86871288.1972.30.17230.02050.0773−0.0324−11.3437
0.93881294.4995.10.08570.01020.0390−0.0167−5.9248
1.00001300.51015.50.00000.00000.00000.00000.0000

(b)


ms−1

kgm−3
*
m2N−1
*
m3 mol−1
*
m
*
kgm−2s−1

ms−1

313.15 K
0.00001277.3809.00.00000.00000.00000.00000.0000
0.16171267.4827.40.19300.02060.0792−0.0263−10.1247
0.29211261.8845.40.29690.03220.1232−0.0420−15.8967
0.40901259.0863.80.34950.03870.1465−0.0513−18.9159
0.52441257.8884.30.36510.04140.1547−0.0559−19.9470
0.63591259.0907.10.34450.04000.1478−0.0553−19.1057
0.70831261.0923.80.31060.03650.1345−0.0514−17.5155
0.79471263.8946.10.24740.02930.1084−0.0425−14.3816
0.86871267.7967.10.17310.02050.0767−0.0307−10.4522
0.93881273.3989.60.08630.01010.0387−0.0158−5.4790
1.00001278.61009.80.00000.00000.00000.00000.0000

318.15 K
0.00001260.7805.40.00000.00000.00000.00000.0000
0.16171250.4823.60.19800.02070.0805−0.0254−9.7832
0.29211244.5841.40.30270.03230.1243−0.0404−15.1454
0.40901241.0859.60.35990.03880.1491−0.0497−18.3128
0.52441239.5879.90.37770.04150.1581−0.0542−19.4234
0.63591240.2902.40.35390.04010.1500−0.0533−18.3277
0.70831241.8919.00.31610.03660.1352−0.0493−16.5045
0.79471244.8941.00.24890.02940.1077−0.0405−13.2710
0.86871248.3961.80.17320.02060.0758−0.0292−9.5740
0.93881252.4984.20.08690.01020.0384−0.0151−5.0789
1.00001257.31004.10.00000.00000.00000.00000.0000