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Journal ArticleDOI

Crystallization of potassium sulfate by cooling and salting-out using 1-propanol in a calorimetric reactor

TLDR
In this article, a study was made on a isothermal process for the crystallization of potassium sulfate as an alternative to the cooling process, which employed addition of 1-propanol to aqueous salt solutions to achieve the salting-out of the K 2 SO 4.
Abstract
A study was made on a isothermal process for the crystallization of potassium sulfate as an alternative to the cooling process. The process employs addition of 1-propanol to aqueous salt solutions to achieve the salting-out of the K 2 SO 4 . This work was carried out using an automated Mettler Toledo model RC1 reactor-crystallizer with 800 ml capacity, and controlled isothermally at 25°C to test the crystallization of K 2 SO 4 by addition of the alcohol, and from 50 to 10°C for the cooling crystallization. In both systems, the line of nucleation points was shown to be approximately parallel to the saturation curve, with an average width of 13°C or 3 % mass for crystallization by cooling, compared with 0.2 to 1 % by salting-out. In experiments on crystallization by cooling, the K 2 SO 4 crystals were 0.27 mm in mean size, showed 7 % agglomeration, and contained 8.5 % moisture. Crystals obtained by salting-out had a mean size of 0.79 mm, 28 % agglomeration, and 9-10 % moisture content. A crystal shape factor of approximately of 0.7 was obtained in both systems, apart from the agglomeration.

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Citations
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Journal ArticleDOI

Novel Approach to Analyze Metastable Zone Width Determined by the Polythermal Method: Physical Interpretation of Various Parameters

TL;DR: In this article, a semi-empirical approach based on the classical theory of three-dimensional nucleation combined with the formation of n-sized embryos from monomers according to the law of mass action is proposed.
Journal ArticleDOI

Nucleation behavior of eszopiclone-butyl acetate solutions from metastable zone widths

TL;DR: In this article, a modified model based on the Sangwal's theory in which the nucleation parameters are not dependent on saturation temperature T 0 and nucleation temperature T 1 was proposed.
Journal ArticleDOI

Liquid–liquid equilibrium of aqueous two-phase systems containing poly(ethylene glycol) of different molecular weights and several ammonium salts at 298.15 K

TL;DR: In this article, the effect of poly(ethylene glycol) molecular weight on binodal curves was investigated, and it was found that the biphasic region expanded with an increase in PEG molecular weight.
Journal ArticleDOI

Organic solvent‐assisted crystallization of inorganic salts from acidic media

TL;DR: In this paper, 2-propanol was selected as an effective salting out agent to precipitate crystalline metal sulfates of practical interest; differences in crystallization behaviour among the various salts were linked to the hydration energy of the cation.
Journal ArticleDOI

On the interpretation of metastable zone width in anti‐solvent crystallization

TL;DR: O'Grady et al. as mentioned in this paper proposed a modified Nývlt-like equation based on traditional power-law relation between nucleation rate and developing supersaturation and a new equation to explain the dependence of anti-solvent addition rate on metastable zone width.
References
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Book

Chemical Engineers' Handbook

TL;DR: The Chemical Engineers handbook as mentioned in this paper, Chemical engineers handbook, Chemical engineer handbook, Chemical engineers Handbook, Chemical Engineering handbook and Chemical Engineers Handbook, 2007.2.1.
Book

The> kinetics of industrial crystallization

TL;DR: The most comprehensive collection of data on the kinetics of crystallization from solution can be found in this article, which provides a link between crystallization mechanisms and crystallization kinetics, and provides cohesion between published results from different sources.
Journal ArticleDOI

Crystallization kinetics of potassium-sulfate in an msmpr agitated vessel

TL;DR: In this paper, the growth rate of potassium sulfate is strongly size-dependent, second order with respect to supersaturation, with a high overall activation energy, and a marked deviation is detected in growth rates at small sizes at which very strong curvature is exhibited in population density distributions.
Journal ArticleDOI

Dissolution mass transfer in a turbine agitated baffled vessel

TL;DR: In this paper, mass transfer coefficients were measured for the dissolution of crystalline electrolytes suspended in a baffled vessel by means of disc turbines and the effect of impeller speed, size and clearance from the base was studied.
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