In chemistry, fractional crystallization is a stage-wise separation technique that relies on the liquid-solid phase change. fractional crystallisation. This is an old
established method which is nevertheless capable of
excellent results and a description is available in "The practical Methods of organic Chemistry" by Ludwig Gattermann in 1898 and a translation was available in English by WILLIAM B. SHOBER who was a Lehigh University, USA.
This technique fractionates via differences in crystallization temperature and enables the purification of multi-component mixtures, as long as none of the constituents can act as solvents to the others. Due to the high selectivity of the solid – liquid equilibrium, very high purities can be achieved for the selected component.
The crystallization process starts with the partial freezing of the initial liquid mixture by slowly decreasing its temperature. The frozen solid phase subsequently has a different composition than the remaining liquid. This is the fundamental physical principle behind the melt fractionating process and quite comparable to distillation, which operates between a liquid and the gas phase.
The crystals will grow on a cooled surface or alternatively as a suspension in the liquid. The heat released by the solidification process is withdrawn through a cooling surface or via the liquid. In theory, 100% of the product could be solidified and recovered. In practice, various strategies such as partial melting of the solid fraction (sweating) need to be applied in order to reach high purity levels.
Fractional crystallization has various advantages over other separation technologies. First of all, it makes the purification of close boilers possible. This allows for very high purities even for challenging components. Furthermore, because of the lower operating temperature, the thermal stress applied to the product is very low. This is in particular relevant for products that would otherwise oligomerize or degrade. Next, fractional crystallization is usually an inherently safe technology, because it operates at low pressures and low temperatures. Also, it does not use any solvents and is emission-free. Finally, since the latent heat of solidification is 3–6x lower than the heat of evaporation, the energy consumption is – in comparison to distillation – much lower.
Fractional crystallization involves several key steps:
There are three differenct fractional crystallization technologies available:
In the falling-film crystallizer, crystals grow from a melt that forms a thin film along the inside of cooled tubes. A concurrent cooling medium flows on the outside of these tubes. This arrangement allows for reproducible and high transfer rates of heat, facilitating the growth of crystals from the falling film of melt. The solid–liquid separation of the resulting slurry can be accomplished using a wash column or a centrifuge. This technology is more complex than others but offers the advantage of high separation efficiency and very high purities. A typical feed has concentrations between 90–99%, which is purified up to 99.99 wt.-% or greater. For example, glacial acrylic acid, optical grade bisphenol-A and battery grade ethylene carbonate can be purified to their highest grade using a falling-film crystallizer.
The static crystallizer allows crystals to grow from a stagnant melt, making it a versatile and robust technology. It can purify highly challenging products, including those with most challenging properties, such as high viscosities and high or low melting points. Examples of applications include isopulegol, phosphoric acid, wax and paraffins, anthracene / carbazole and even satellite-grade hydrazine.
In suspension crystallization, crystals are generated on a cooling surface and then scraped off to continue growing in size within a stirred vessel in suspension or slurry. The solid–liquid separation is performed either through a wash-column or a centrifuge. This method is more complex to operate, but offers the advantage of a high separation efficiency, which translates to considerable engery savings. Examples of applications include paraxylene, halogenated aromatics, and also aqueous feeds.
C. A. Soch, Fractional Crystallization, The Journal of Physical Chemistry 1898 2 (1), 43-50; DOI: 10.1021/j150001a002