Boiling Point-Composition Diagram For The System 1,4-Dioxane-n-Butyl Alcohol

1956 ◽  
Vol 60 (6) ◽  
pp. 826-826 ◽  
Author(s):  
James B. McCormack ◽  
John H. Walkup ◽  
R. I. Rush
Keyword(s):  
Boiling Point ◽  
Butyl Alcohol ◽  
Composition Diagram ◽  
Point Composition

The boiling point-composition diagram of immiscible and partially miscible liquid systems

1940 ◽  
Vol 17 (11) ◽  
pp. 536
Author(s):  
Merle Randall ◽  
William Avila
Keyword(s):  
Boiling Point ◽  
Composition Diagram ◽  
Partially Miscible ◽  
Liquid Systems ◽  
Point Composition

Two safety improvements for a standard experiment on the boiling point-composition diagram of a binary system

1982 ◽  
Vol 59 (2) ◽  
pp. 157
Author(s):  
Bro. Leo P. Michiels ◽  
Raymond C. Barile ◽  
German F. de la Fuente
Keyword(s):  
Binary System ◽  
Boiling Point ◽  
Composition Diagram ◽  
Point Composition

scholarly journals Boiling-point-composition diagram for dilute aqueous solutions of deuterium oxide

1936 ◽  
Vol 17 (6) ◽  
pp. 841
Author(s):  
Edgar R. Smith ◽  
Mieczyslaw Wojciechowski
Keyword(s):  
Aqueous Solutions ◽  
Boiling Point ◽  
Deuterium Oxide ◽  
Composition Diagram ◽  
Dilute Aqueous Solutions ◽  
Point Composition

Isothermal and isobaric vapour-liquid equilibrium data in the tetrachloromethane-sec-butyl alcohol system

1983 ◽  
Vol 48 (9) ◽  
pp. 2446-2453 ◽  
Author(s):  
Jan Linek
Keyword(s):  
Experimental Data ◽  
Boiling Point ◽  
Butyl Alcohol ◽  
Correlation Equations ◽  
Wilson Equation ◽  
Liquid Equilibrium ◽  
Raoult’S Law ◽  
System A ◽  
Equilibrium Data ◽  
Alcohol System

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.

scholarly journals Boiling-point-composition digram of the system dioxane-water

1937 ◽  
Vol 18 (4) ◽  
pp. 461 ◽  
Author(s):  
E.R. Smith ◽  
M. Wojceichowski
Keyword(s):  
Boiling Point ◽  
Point Composition

Vapor-Liquid Equilibria and Boiling-Point Composition Relations for Systems n-Butanol–Water and Isobutanol–Water1,2

1931 ◽  
Vol 23 (12) ◽  
pp. 1438-1440 ◽  
Author(s):  
J. S. Stockhardt ◽  
C. M. Hull
Keyword(s):  
Boiling Point ◽  
Point Composition ◽  
Vapor Liquid Equilibria ◽  
Vapor Liquid

Vapour-liquid equilibrium. The effect of temperature on the equilibrium vapour phase composition and on the azeotropic point composition

1991 ◽  
Vol 56 (4) ◽  
pp. 745-749 ◽  
Author(s):  
Josef P. Novák ◽  
Jaroslav Matouš ◽  
Petr Voňka
Keyword(s):  
Phase Composition ◽  
Vapour Phase ◽  
Butyl Alcohol ◽  
Effect Of Temperature ◽  
Calorimetric Data ◽  
Liquid Equilibrium ◽  
Azeotropic Point ◽  
Tert Butyl Alcohol ◽  
Point Composition ◽  
Heats Of Vaporization

On the basis of analysis of calorimetric data, it is shown that the tert-butyl alcohol(1)-water(2) system exhibits the non-monotonous dependence of the equilibrium vapour phase composition on temperature which is reflected in the non-monotonous dependence of azeotropic composition on temperature. This behaviour is conditioned primarily by the fact that the molar heats of vaporization of both the substances have the same value at the temperature of 57°C. From the values of heats of vaporization of C3 and C4 alcohols and water it is evident that the analogous behaviour occurs also in aqueous systems of these alcohols at common temperatures.

Isothermal and isobaric vapour-liquid equilibrium data in the tetrachloromethane-n-butyl alcohol system

1983 ◽  
Vol 48 (10) ◽  
pp. 2879-2887 ◽  
Author(s):  
Jan Linek
Keyword(s):  
Experimental Data ◽  
Boiling Point ◽  
Butyl Alcohol ◽  
Correlation Equations ◽  
Wilson Equation ◽  
Liquid Equilibrium ◽  
System A ◽  
Equilibrium Data ◽  
Alcohol System ◽  
Kister Equation

Isothermal vapour-liquid equilibrium data at 65, 73 and 80 °C and isobaric ones at 101.3 kPa were measured in the tetrachloromethane-n-butyl alcohol system. A modified circulation still of the Gilespie type was used for the measurements. Under the conditions of measurements, 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 best correlation was reached with the Wilson equation but the regression failed in some cases. Therefore the results for the 5th order Redlich-Kister equation are presented.

Apparatus for determination of boiling point-composition curves of miscible liquid pairs

1933 ◽  
Vol 10 (12) ◽  
pp. 749
Author(s):  
E. M. Collins ◽  
J. O. Morrison ◽  
J. R. Stone
Keyword(s):  
Boiling Point ◽  
Point Composition
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