[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

Chamorro et al., 2002 - Google Patents

Isothermal vle and excess molar Gibbs energy of binary and ternary mixtures containing diisopropyl ether, n-heptane and isopropanol at T= 313.15 K

Chamorro et al., 2002

Document ID
4872991826682337522
Author
Chamorro C
Segovia J
Martı́n M
Villamañán M
Publication year
Publication venue
The Journal of Chemical Thermodynamics

External Links

Snippet

(Vapour+ liquid) equilibrium of {diisopropyl ether (DIPE)+ n-heptane+ isopropanol},{ diisopropyl ether (DIPE)+ n-heptane},{diisopropyl ether (DIPE)+ isopropanol} and (n- heptane+ isopropanol) were measured at T= 313.15 K. Data reduction by Barker's method …
Continue reading at www.sciencedirect.com (other versions)

Similar Documents

Publication Publication Date Title
Kell Effects of isotopic composition, temperature, pressure, and dissolved gases on the density of liquid water
Myers et al. Measurement and correlation of vapor pressure data for high boiling hydrocarbons
Yoon et al. High-pressure phase equilibria for carbon dioxide-methanol-water system: experimental data and critical evaluation of mixing rules
Chamorro et al. Isothermal vle and excess molar Gibbs energy of binary and ternary mixtures containing diisopropyl ether, n-heptane and isopropanol at T= 313.15 K
Segovia et al. Excess thermodynamic properties of binary and ternary mixtures containing methyl 1, 1-dimethylethyl ether (MTBE), n-heptane, and methanol atT= 313.15 K
Chen et al. Dew-point loci for methane-n-pentane binary system
Wilsak et al. Vapor—liquid equilibrium measurements for the methanol—acetone system at 372.8, 397.7 and 422.6 K
Humphrey et al. Vapor-liquid equilibrium at 60. degree. for n-hexane-alkyl amines and 1-hexene-alkyl amines
Yang et al. Vapor-liquid equilibria at subatmospheric pressures-n-octane-ethylbenzene system
Dourson et al. Phase Behavior in the Methane-propane-n-pentane System
Apelblat et al. Excess molar volumes of formic acid+ water acetic acid+ water and propionic acid+ water systems at 288.15, 298.15 and 308.15 K
Maripuri et al. Isothermal vapour‐liquid equilibria in binary mixtures of ketones and alkanes
Wu et al. Isothermal vapor-liquid equilibrium of binary mixtures containing morpholine
Smith et al. BOILING POINTS OF BENZENE, ETHYLENE CHLORIDE, n. HEPTANE, AND 2, 2, 4. TRIMETHYLPENTANE OVER THE RANGE 660· TO 860· MM PRESSURE
Chun et al. Vapor-liquid equilibrium of triethylamine-water and methyldiethylamine-water
Reamer et al. Phase equilibria in hydrocarbon systems-Methane-n-butane-decane system
Brunner et al. Phase equilibrium in the systems n-heptane-nitrogen, methylcyclohexane-nitrogen and n-heptane-methylcyclohexane-nitrogen at high pressures
Pividal et al. Ebulliometric method for measuring activity coefficients at infinite dilution: systems with cyclic ethers
Hauschild et al. Vapor-liquid and liquid-liquid equilibria of water, 2-methoxyethanol and cyclohexanone: experiment and correlation
Bae et al. Isothermal vapor-liquid equilibriums for the ethylene-carbon dioxide system at high pressure
Chamorro et al. Experimental investigation of the vapor–liquid equilibrium at 313.15 K of the ternary system tert-amylmethyl ether (TAME)+ n-heptane+ methanol
Chamorro et al. Vapor–liquid equilibrium of octane-enhancing additives in gasolines: 1. Total pressure data and gE for binary and ternary mixtures containing di-isopropyl ether (DIPE), n-heptane and benzene at 313.15 K
Zabaloy et al. Isothermal vapor-liquid equilibrium data for the binaries propane-2-propanol and propylene-2-propanol
Mehra et al. Vapor-liquid equilibrium constants for the ethane-butane-n-heptane system at 300. deg. and 350. deg. F
Villamañán et al. Phase equilibrium properties of binary and ternary systems containing di-isopropyl ether+ 1-butanol+ benzene at 313.15 K