La distillation fractionnée, aussi appelée rectification, est un procédé de séparation par fractionnement. Son but est de séparer les différents constituants d’un. Composition: 1 ballon monocol mL fond rond ; 1 colonne de Vigreux avec tête de colonne et prise thermométrique ; 1 réfrigérant de Liebig coudé. The fractional distillation of this wood give four fractions: the first rich of La distillation fractionnée a donné quatre fractions, la première riche en alcools (26 .

Author: JoJolrajas Tojakree
Country: Chile
Language: English (Spanish)
Genre: Business
Published (Last): 2 July 2014
Pages: 65
PDF File Size: 19.91 Mb
ePub File Size: 18.22 Mb
ISBN: 500-9-91152-640-2
Downloads: 71328
Price: Free* [*Free Regsitration Required]
Uploader: Zulkigar

Static hold-up is the amount of liquid that is held onto the packing distiillation it has been wetted, then drained – the film of liquid or droplets of liquid that adhere to the packing.

The diagram represents a batch apparatus as opposed to a continuous apparatus. Typical manufacturers are Koch, Sulzer and other companies. However, when modeling packed columns it is useful to compute a number of “theoretical plates” to denote the separation efficiency of the packed column with respect to more traditional trays.

Views Read Edit View history. This area is called the “loading region”. For this reason, ethanol cannot be completely purified by direct ristillation distillation of ethanol-water mixtures.

As an example consider the distillation of a mixture of water and ethanol. Articles needing cleanup from November All pages needing cleanup Articles containing how-to sections All articles with unsourced statements Articles with unsourced statements from December You dont want them too loose or too tight. Hence, a distillation column needs more plates than the number of theoretical vapor—liquid equilibrium stages.

As the vapour rate continues to increase, eventually a point is reached when the vapour begins to interfere with the downward liquid flow, holding up liquid in the packing. Alternatively, the more reflux provided for a given desired separation, the fewer theoretical plates are required. If consistent results are wanted, then the aim should surely be to allow some leeway and try to get that curve settling down before the top of the packing is reached.


Fractilnnee more heat, the more vapour you generate.

Fractional distillation – Wikipedia

The more reflux is provided for a given number of theoretical platesthe better the tower’s separation of lower boiling materials from higher boiling materials. Dynamic hold-up must be measured experimentally. So using W with a 25mm column would result in full separation distil,ation at a point right at the top of the column, with little or no leeway.

Large-scale industrial towers use reflux to achieve a more complete separation of products.

At low liquid rates, the open area of the packing is practically the same as for dry packing. If too tight they will compact more. That way, the reflux column has a chance to do its job as fully as it can before either taking off product, as in a simple reflux still, or passing on the results to a secondary top section that operates with imposed reflux for that final touch of separation.

Most of the ones I have seen in NZ do not have rubber bands around them. I tend to work in the vicinity of each filling somewhere between 55 and 63mm. Use a good quality one preferably.

Fractional distillation

This is on the ‘safe side’ of the recommended figures in the table. As the mixed vapor ascends the temperature gradient, some of the vapor condenses and revaporizes along the temperature gradient. The crude oil fractions with higher boiling points:.

Applications for the Practical Engineer. The mixture is put into the round bottomed flask along with a few anti-bumping granules or a Teflon coated magnetic stirrer bar if using magnetic stirringand the fractionating column is fitted into the top. This is known as continuous, steady-state fractional distillation. The “lightest” products those with the lowest boiling point exit from the top of the columns and the “heaviest” products those with the highest boiling point exit from the bottom of the column.


In most oil refinery operations, tray columns are mainly used for the separation of petroleum fractions at different stages of oil refining. The main thing is to have an even constant heat so you dont get surging. Reflux refers to the portion of the condensed overhead liquid product from a distillation or fractionation tower that is returned to the upper part of the tower as shown in the schematic diagram of a typical, large-scale industrial distillation tower.

In operation we would not then be overly concerned with some liquid accumulation or hold-up, as long as the column could be kept stable and under control Puissance de chauffe W.

Type de Packing note: Do not unravel but tease them out by hand a bit so they fill the whole column diameter rather than just a part of it. Anneaux de Raschig 13 mm.

Montage distillation fractionnée – Rodaviss – 19/26

One is referred to as static hold-up. The purpose of Wikipedia is to present facts, not to train. This needs to be fractinonee out from the amount of heat you are putting in. This amount jointly depends upon the physical properties of the liquid and the type and material of the packing.