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Journal ArticleDOI

Melt Crystallization with Direct Contact Cooling Techniques

TLDR
In this paper, direct contact cooling was used for the separation of an n -decanol- n -dodecanol mixture. Butane was used as the main cooling agent and three coolants, air, water and butane, were employed.
Abstract
Melt crystallization using direct contact cooling techniques has been examined for the separation of an n -decanol- n -dodecanol mixture. Additionally, the heat transfer of melt crystallization by direct contact of coolants has been investigated. Three coolants, i.e. air (as a gas), water (as a liquid) and butane (as a liquefied gas) were employed. Volumetric heat transfer coefficients obtained by direct contact cooling in the melt crystallizer are in the range between 0.1 and 100kW/(m 3 K) and increased roughly with the 1.5 to 1.8 power of the linear superficial velocity of coolant. The volumetric production rate was found to be in the range between 0.01 and 0.2kg/(m 3 s) for the coolant air, 0.05 to 1.4kg/(m 3 s) for the coolant water and butane. The linear growth rate of crystals was proportional to the second power of subcooling. The quality of the crystals produced by this direct contact cooling technique was good, and the crystals are significantly larger than those obtained using scraped-surface crystallizers. A comparison between the effective distribution coefficient obtained before and after wiping has shown that the core of crystals is very pure and the impurity is concentrated in the outer layer of crystals. The described melt crystallization also shows the advantage of continuous operating, high thermal economy and no encrustation in spite of high mean temperature difference.

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Citations
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Journal ArticleDOI

Scraped surface heat exchangers.

TL;DR: Scraped surface heat exchangers (SSHEs) are commonly used in the food, chemical, and pharmaceutical industries for heat transfer, crystallization, and other continuous processes as mentioned in this paper.
Journal ArticleDOI

A study on crystallization kinetics of pentaerythritol in a batch cooling crystallizer

TL;DR: In this paper, the crystallization kinetics of pentaerythritol (PeE) in aqueous solution in the presence of impurity or not in a batch cooling crystallizer was explored.
Journal ArticleDOI

Separation of Acetic Acid from Acetic Acid-Water Mixture by Crystallization

TL;DR: In this article, the effect of the cooling rate, the amount of seeds, the seeding temperature, the sweating rate, and the sweating fraction on the distribution coefficient of acetic acid was investigated.
Journal ArticleDOI

Controllable Crystallization Behavior of Nylon-6/66 Copolymers Based on Regulating Sequence Distribution

TL;DR: In this article, the sequence distribution, crystal morphology, crystal forms, and melting and crystallization behavior of nylon-6/66 copolymers were systematically investigated by quantitative 13C NMR, polarized optical microscopy, wide-angle X-ray diffraction, and differential scanning calorimetry, respectively.
References
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BookDOI

Crystallization Technology Handbook

Alfons Mersmann
- 08 May 2001 - 
TL;DR: In this article, the authors discuss the interaction between balances, processes, and product quality design of Crystallizers and Crystallization Processes Control of the Crystallizer Reaction Crystallisation Additives and Impurities Crystallizing from the Melt Thermal Analysis and Economics of Processes Appendix 1: Physical Properties Appendix II: Examples of Large-Scale lndustrial Crystallisers
Journal ArticleDOI

The influence of internal crystal perfection on growth rate dispersion in a continuous suspension crystallizer

TL;DR: In this article, the influence of induced lattice strain on growth behavior of potassium alum crystals in a continuously operated mixed suspension mixed product removal (MSMPR) crystallizer was demonstrated and the mean growth rate of small particles in the sub-sieve size range is considerably smaller than the mean rate of product sized crystals at constant supersaturation.
Journal ArticleDOI

Initial-size-dependent growth rate dispersion of attrition fragments and secondary nuclei

TL;DR: In this paper, growth experiments have been carried out for attrition fragments of potassium nitrate in a growth cell with stagnant solution and the results show that the growth rate of any fragment-size class increases with increasing fragment size.
Journal ArticleDOI

Ice crystallization developments for the butane direct-contact process

TL;DR: In this paper, a study was conducted on a continuous crystallizer equipped with a slurry recycle loop which functioned as an isothermal holding zone, and it was shown that an increase in production rate from 1.44 to 3.6 kg/lit.hr had no effect on permeability or on crystal size.
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