Heats of mixing for the partially miscible system ethanol-n-tetradecane

1969 ◽  
Vol 14 (1) ◽  
pp. 20-22 ◽  
Author(s):  
Rubens S. Ramalho ◽  
Maurice Ruel
Keyword(s):  
Heats Of Mixing ◽  
Partially Miscible

Heats of Mixing for Partially Miscible Systems: Methanoi-n-Hexane and Methanol-n-Heptane.

1965 ◽  
Vol 10 (2) ◽  
pp. 171-172 ◽  
Author(s):  
C. G. Savini ◽  
D. R. Winterhalter ◽  
H. C. Van Ness
Keyword(s):  
Heats Of Mixing ◽  
Partially Miscible

Heats of mixing in the system acetone – acetic anhydride – carbon disulfide, and the corresponding binary systems, at room temperature

1970 ◽  
Vol 48 (10) ◽  
pp. 1579-1584 ◽  
Author(s):  
A. N. Campbell ◽  
E. M. Kartzmark ◽  
S. C. Anand
Keyword(s):  
Acetic Anhydride ◽  
Carbon Disulfide ◽  
Room Temperature ◽  
Binary Systems ◽  
Thermodynamic Quantities ◽  
Molar Excess ◽  
Heats Of Mixing ◽  
Partially Miscible ◽  
Binary Section ◽  
Excess Thermodynamic Quantities

A simple calorimeter has been devised by means of which the heats of mixing (molar excess heats) of the following systems have been determined at 22 °C: acetone – acetic anhydride; acetone – carbon disulfide; acetic anhydride – carbon disulfide; and a pseudo-binary section of the ternary system acetone – acetic anhydride – carbon disulfide. From these data the partial molar excess heats have been obtained. All systems are very non-ideal except the system acetone – acetic anhydride, which is almost ideal.For the partially miscible system acetic anhydride – carbon disulfide, the excess thermodynamic quantities of mixing, GE, HE, and TSE, have been calculated,

Heat-of-mixing for the partially miscible system N2/C2H6

1988 ◽  
Vol 66 (4) ◽  
pp. 626-627 ◽  
Author(s):  
Jorge C. G. Calado ◽  
Prakash Gopal ◽  
John A. Zollweg ◽  
W. Reid Thompson
Keyword(s):  
Liquid System ◽  
Heat Of Mixing ◽  
Liquid Separation ◽  
Flow Calorimeter ◽  
Heats Of Mixing ◽  
Partially Miscible ◽  
Cryogenic Flow ◽  
Composition Curve

Heats-of-mixing for the liquid system nitrogen/ethane have been measured at 92.3 K and 0.6309 MPa using a cryogenic flow calorimeter. The heat-of-mixing versus composition curve shows that the system is only partially miscible; the compositions between which liquid–liquid separation occurs have been estimated.

Heats of mixing and dielectric constants of some partially miscible liquid pairs

1969 ◽  
Vol 47 (4) ◽  
pp. 619-623 ◽  
Author(s):  
A. N. Campbell ◽  
E. M. Kartzmark
Keyword(s):  
Experimental Data ◽  
Hydrogen Bonding ◽  
Acetic Anhydride ◽  
Carbon Disulfide ◽  
Dielectric Constants ◽  
Solution Temperature ◽  
Negative Deviation ◽  
Critical Solution Temperature ◽  
Heats Of Mixing ◽  
Partially Miscible

The physical properties mentioned in the title have been determined for the six systems: (a) aniline–hexane, (b) methanol–cyclohexane, (c) methanol–carbon disulfide, (d) acetic anhydride–carbon disulfide, (e) acetic anhydride–cyclohexane, and (f) triethylamine–water, over the complete range of composition. All six systems are partially miscible, above or below a critical solution temperature (c.s.t.).From the experimental data, the partial molal heats of mixing have been calculated, using the Redlich and Kister equations. The enthalpy of hydrogen bonding in the triethylamine–water compound appears to be about −1.33 kcal per hydrogen bond.The orientation polarization, according to the Syrkin formula, appears always to exhibit negative deviation from ideality, at least over part of the concentration range.

Heats of mixing of butanone and chloroform with alkanes: Ternary systems

1978 ◽  
Vol 43 (3) ◽  
pp. 837-847 ◽  
Author(s):  
Julius Pouchlý ◽  
Antonín Živný ◽  
Ján Biroš
Keyword(s):  
Ternary Systems ◽  
Heats Of Mixing
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