Phase Equilibria

Go to Vapor-Liquid Equilibria
drop.gif (1033 Byte) Azeotropic Data
drop.gif (1033 Byte) Activity Coefficients at Infinite Dilution
drop.gif (1033 Byte) Liquid-Liquid Equilibria
drop.gif (1033 Byte) Solid-Liquid Equilibria
drop.gif (1033 Byte) Gas Solubilities
drop.gif (1033 Byte) Henry Coefficients
drop.gif (1033 Byte) Critical Data
drop.gif (1033 Byte) Vapor-Liquid-Liquid Equilibria
drop.gif (1033 Byte) Solubilities of High Boiling Substances in Supercritical Fluids

To measure these properties different experimental devices are available to meet the requirements of different applications. By choosing one of the suggested properties you will get more information.

 


Vapor-Liquid Equilibria

Distillation is still the most used separation process in the chemical and petrochemical industry. Simulation programs provide a larger variety of possibilities for process synthesis, design and optimization. However, the quality of the results obtained with these programs depends on the quality of the models and  model parameters used. In some cases the results based on calculations using group contribution methods might be sufficient. In other cases the exact knowledge of the phase equilibrium of the involved components is indispensable. In these cases exact experimental data and a good description of them with the used thermodynamic models ought to be aspired.

The LTP GmbH (in cooperation with the University of Oldenburg) deploys several apparatuses to measure the VLE data. Each experimental setup has its special advantages, preferences, and its own range of applicability. In the following numeration the different methods are suggested and explained in detail.

Go to Static Apparatus, High Pressure, Phase Analysis; Pressure range: < 400 bar
Go to Static Apparatus, High Pressure, Phase Analysis; Pressure range: < 250 bar
Go to Static Apparatus, High Pressure
Go to Static Apparatus, High Pressure; Pressure range: < 250 bar
Go to Computer Driven Static Apparatus; Pressure range: < 3 bar  

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Go to Computer Driven Static Apparatus; Pressure range: < 30 bar
Go to Computer Driven Dynamic Apparatus
Go to Flow Apparatus, Determination of Critical Points
Go to Flow Apparatus, Spinning Coil
Go to Headspace Chromatograph
Go to Dynamic Still (NORMAG)
Go to Swietoslawski Ebulliometer
Go to Scott Ebulliometer

 

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Azeotropic Data

Azeotropic informations are most important for the synthesis of distillation processes.

Go to Spinning Band

 

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Activity Coefficients at Infinite Dilution

Activity coefficients at infinite dilution (g¥) are important for:

Several methods were developed for the measurement of g¥. The most important methods are: gas-liquid chromatography (GLC), non-steady-state gas-liquid chromatography, differential ebulliometry, static methods and the dilutor method. Chromatographic methods allow the determination of g¥ of volatile solutes in high (classical GLC) and low boiling (non-steady-state GLC) solvents. The dilutor method permits the determination of g¥ in solvent mixtures. The addition of water to selective solvents (e.g. NMP + water) often increases the selectivity of the solvents used.

Go to Gas-Liquid Chromatograph
Go to Dilutor

 

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Liquid - Liquid Equilibria

Go to Analytical Method
Go to Liquid - Liquid Countercurrent Chromatography
Go to Static Apparatus, High Pressure

 

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Solid - Liquid Equilibria

Go to Synthetic Method (Visual)

 

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