Recommended Liquid–Liquid Equilibrium Data. Part 1. Binary Alkane–Water Systems

2004 ◽  
Vol 33 (2) ◽  
pp. 549-577 ◽  
Author(s):  
Andrzej Ma̧czyński ◽  
Barbara Wiśniewska-Gocłowska ◽  
Marian Góral
2020 ◽  
Vol 65 (4) ◽  
pp. 1369-1378
Author(s):  
Pedro P. A. Souza ◽  
Igor B. Julião ◽  
Marisa F. Mendes

2006 ◽  
Vol 35 (3) ◽  
pp. 1391-1414 ◽  
Author(s):  
Marian Góral ◽  
Barbara Wiśniewska-Gocłowska ◽  
Andrzej Mączyński

ChemInform ◽  
2004 ◽  
Vol 35 (43) ◽  
Author(s):  
Andrzej Maczynski ◽  
Barbara Wisniewska-Goclowska ◽  
Marian Goral

2004 ◽  
Vol 33 (4) ◽  
pp. 1159-1188 ◽  
Author(s):  
Marian Góral ◽  
Barbara Wiśniewska-Gocłowska ◽  
Andrzej Ma̧czyński

2007 ◽  
Vol 36 (4) ◽  
pp. 1399-1415 ◽  
Author(s):  
Marian Góral ◽  
Andrzej Mączyński ◽  
Paweł Oracz

ChemInform ◽  
2004 ◽  
Vol 35 (43) ◽  
Author(s):  
Marian Goral ◽  
Andrzej Maczynski ◽  
Barbara Wisniewska-Goclowska

2004 ◽  
Vol 33 (2) ◽  
pp. 579-591 ◽  
Author(s):  
Marian Góral ◽  
Andrzej Ma̧czyński ◽  
Barbara Wiśniewska-Gocłowska

ChemInform ◽  
2007 ◽  
Vol 38 (4) ◽  
Author(s):  
Marian Goral ◽  
Barbara Wisniewska-Goclowska ◽  
Andrzej Maczynski

1983 ◽  
Vol 48 (9) ◽  
pp. 2446-2453 ◽  
Author(s):  
Jan Linek

Isothermal vapour-liquid equilibrium data at 65, 73 and 80 °C and isobaric ones at 101.3 kPa were measured in the tetrachloromethane-sec-butyl alcohol system. A modified circulation still of the Gillespie type was used for the measurements. Under the conditions of measurement, the system exhibits positive deviations from Raoult's law and minimum boiling-point azeotropes. The experimental data were fitted to a number of correlation equations, the most suitable being the Wilson equation.


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