Experimental Determination of vapor-liquid equilibria of the system acetone-chloroform-methanol, AT 50oC. A project report

Experimental Determination of vapor-liquid equilibria of the system acetone-chloroform-methanol, AT 50oC. A project report PDF Author: J. K. Floess
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Category :
Languages : en
Pages : 128

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Experimental Determination of vapor-liquid equilibria of the system acetone-chloroform-methanol, AT 50oC. A project report

Experimental Determination of vapor-liquid equilibria of the system acetone-chloroform-methanol, AT 50oC. A project report PDF Author: J. K. Floess
Publisher:
ISBN:
Category :
Languages : en
Pages : 128

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Experimental Deterimation of Vapor-liquid Equilibria of the System Acetone-chloroform-methanol at 50 Degrees C.

Experimental Deterimation of Vapor-liquid Equilibria of the System Acetone-chloroform-methanol at 50 Degrees C. PDF Author: Joachim K. Floess
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ISBN:
Category :
Languages : en
Pages : 65

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The Vapor-liquid Equilibrium of the System Methanol-ethanol-acetone and Its Component Binaries

The Vapor-liquid Equilibrium of the System Methanol-ethanol-acetone and Its Component Binaries PDF Author: Hassanein Hamed Amer
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ISBN:
Category :
Languages : en
Pages : 320

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High Pressure Vapor-liquid Equilibria in the System Acetone-methanol-water

High Pressure Vapor-liquid Equilibria in the System Acetone-methanol-water PDF Author: Soon Yuck Wong
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Category : Chemical equilibrium
Languages : en
Pages : 0

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"In the field of synthetic liquid fuels and organic chemicals there is considerable industrial interest in Fischer-Tropsch-type processes for the production of liquid hydrocarbons and various organic chemicals as by-products. Processes developed primarily for the production of oxygenated organic chemicals by partial oxidation of paraffin hydrocarbons are also in commercial operation. For both processes, recovery and purification of the product constituents by fractional distillation constitute a major problem. Of primary importance to solutions of the problem are the availability of reliable vapor-liquid equilibrium data on the various systems encountered. The need for suitable data is increased by the fact that practically all existing vapor-liquid equilibrium data are for atmospheric pressure only, whereas actual distillation operations are most frequently conducted at pressure above one atmosphere because of favorable economics, design, operations, and control requirements. It is obvious that reliable data at pressure other than one atmosphere and in particular, superatmospheric data are needed. More fundamentally important however, is the need for complete and extended data to evaluate and test the applicability of proposed correlations of the vapor-liquid data. Such extension and correlation involve the change of vapor-liquid equilibria with temperature or pressure, the determination of these data with a minimum of experimental effort, and the extension of binary data into reliable ternary data. Of the numerous oxygenated components produced by the aforementioned processes, acetone, methanol, and water constitute the major portion of the crude products. Binary and ternary systems containing these components have been evaluated and the results reported herein"--Leaves iii-iv

Experimental Determination of Excess Enthalpy for the Ternary System Acetone-acetontrile-methyl Acetate and for the Binary Pairs of Acetone-chloroform-methanol at 50 (degrees C).

Experimental Determination of Excess Enthalpy for the Ternary System Acetone-acetontrile-methyl Acetate and for the Binary Pairs of Acetone-chloroform-methanol at 50 (degrees C). PDF Author: Patrick J. Mulvey
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Category :
Languages : en
Pages :

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Binary and multicomponent vapor-liquid equilibrium in the system 2,3-dimethyl-butane-methanol-acetone-chloroform

Binary and multicomponent vapor-liquid equilibrium in the system 2,3-dimethyl-butane-methanol-acetone-chloroform PDF Author: James Michael Willock
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ISBN:
Category : Vapor-liquid equilibrium
Languages : en
Pages : 210

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Vapor-liquid equilibria of acetone-methanol and acetone-methanol-water systems

Vapor-liquid equilibria of acetone-methanol and acetone-methanol-water systems PDF Author: Chester Bryan Buford
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ISBN:
Category : Equilibrium
Languages : en
Pages : 84

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Determination of Vapor-liquid Equilibrium for the System Methanol, Methyl-ethyl-ketone, and Water

Determination of Vapor-liquid Equilibrium for the System Methanol, Methyl-ethyl-ketone, and Water PDF Author: Thomas Marion Godbold
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ISBN:
Category : Vapor-liquid equilibrium
Languages : en
Pages : 118

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Vapor-liquid Equilibria System: Water-methanol-acetone

Vapor-liquid Equilibria System: Water-methanol-acetone PDF Author: Louis F. Kreek
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Category :
Languages : en
Pages : 58

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Determination of Vapor-Liquid Equilibrium Data for the Methanol-Water System

Determination of Vapor-Liquid Equilibrium Data for the Methanol-Water System PDF Author: Geraldine Anne Clifford
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ISBN:
Category : Chemistry
Languages : en
Pages : 0

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Methanol and water, at ordinary temperatures form a two-phase, two-component system, which according to the phase rule, can be completely described by two independent variables. For solutions of varying concentrations, either the boiling points at constant pressure, or the equilibrium-vapor pressures at constant temperature are useful for the study of the system. However, because the relationship of partial and total vapor pressure to composition at constant temperature can be checked theoretically by means of the equations discussed below, this is the criteria most often used for the study.