User:Milton Beychok/Sandbox: Difference between revisions

From Citizendium
Jump to navigation Jump to search
imported>Milton Beychok
imported>Milton Beychok
Line 26: Line 26:
As shown in the diagram, the reaction flask is placed inside an oil bath. A thermally stable bath of [[silicone oil]] is generally used  rather than water which evaporates too readily to be useful for lengthy reactions. Using an oil bath also allows higher temperatures to be achieved than could be done with a water bath. If even higher temperatures are required, the oil bath can be replaced with a [[sand bath]].
As shown in the diagram, the reaction flask is placed inside an oil bath. A thermally stable bath of [[silicone oil]] is generally used  rather than water which evaporates too readily to be useful for lengthy reactions. Using an oil bath also allows higher temperatures to be achieved than could be done with a water bath. If even higher temperatures are required, the oil bath can be replaced with a [[sand bath]].


== Reflux in beverage distillation ==


By controlling the temperature of the condenser, a '''reflux still''' may be used to ensure that higher boiling point components  (which are also of higher [[molecular weight]]) are returned to the flask while lighter elements are passed out to a secondary condenser. This is useful in producing high quality [[alcohol|alcoholic]] beverages, while ensuring that less desirable components (such as [[fusel alcohol]]s) are returned to the primary flask. This is particularly effective in the production of alcoholic beverages in which it is appropriate to retain the flavors and aromas of the source fruit - such as [[Applejack (beverage)|applejack]]. For high quality neutral spirits (such as [[vodka]]), or post distillation flavored spirits, a process of multiple distillations or charcoal filtering may be applied to obtain a product lacking in any suggestion of its original source material for [[fermentation (food)|fermentation]].


==See also==
==See also==

Revision as of 00:33, 17 November 2008

Reflux is a distillation technique involving the condensation of the distilled product vapors and the return of a portion of the condensate to the distillation system from which it originated.

Reflux is widely used in large-scale, industrial continuous distillation columns as well as in laboratory distillation apparatus setups. It is also used in laboratories to supply energy to reactions over a long period of time.

Reflux in industrial distillation

(PD) Image: Milton Beychok
Figure 1: Industrial distillation column with typical overhead reflux system.

The use of reflux[1][2] is widely practiced in industries that utilize large-scale distillation columns such as petroleum refineries, petrochemical and chemical plants, and natural gas processing plants.

As shown in the schematic diagram of a typical industrial distillation column (Figure 1), reflux is the portion of the overhead liquid product from a distillation column that is returned to the upper part of the column.

Inside the column, the downflowing reflux liquid provides cooling and condensation of the upflowing vapors thereby increasing the efficacy of the distillation column. The more reflux is provided for a given number of distillation plates, the better is the column's separation of lower boiling materials from higher boiling materials. Conversely, for a given desired separation, the more reflux is provided, the fewer distillation plates are required.

Reflux in laboratory distillation

(PD) Image: Milton Beychok
Figure 2: Laboratory distillation apparatus setup.

The apparatus shown in the Figure 2 represents a batch distillation as opposed to a continuous distillation. The liquid feed mixture to be distilled is placed into the round-bottomed flask along with a few anti-bumping granules, and the fractionating column is fitted into the top. As the mixture is heated and boils, vapor rises up the column. The vapor condenses on the glass platforms (known as plates or trays) inside the column and runs back down into the liquid below, thereby refluxing the upflowing distillate vapor. The hottest tray is at the bottom of the column and the coolest tray is at the top. At steady state conditions, the vapor and liquid on each tray is at equilibrium. Only the most volatile of the vapors stays in gaseous form all the way to the top. The vapor at the top of the column then passes into the condenser, where it cools until it condenses into a liquid. The separation can be enhanced with the addition of more trays (to a practical limitation of heat, flow, etc.). The process continues until all the most volatile components in the liquid feed boil out of the mixture. This point can be recognized by the rise in temperature shown on the thermometer. For continuous distillation, the feed mixture enters in the middle of the column.

Reflux to supply heat to chemical reactions

(PD) Image: Milton Beychok
Laboratory distillation setup for total reflux.

Figure 3 is depicts a laboratory apparatus setup for supplying heat to a chemical reaction. A liquid reaction mixture is placed in a flask connected to a Liebig condenser, such that any vapors given off are condensed to a liquid, and drop back into the reaction vessel. The flask is heated for the entire course of the reaction. The purpose is to thermally accelerate the reaction by conducting it at an elevated temperature.

The advantage of this technique is that it can be left for a long period of time without fear of the reaction vessel boiling dry since any evolved vapor is condensed and returned to the reaction flask. The constant boiling action also serves to continuously mix the liquid reactant mixture, although a magnetic stirring rod mechanism is often used to achieve a uniform solution.

As shown in the diagram, the reaction flask is placed inside an oil bath. A thermally stable bath of silicone oil is generally used rather than water which evaporates too readily to be useful for lengthy reactions. Using an oil bath also allows higher temperatures to be achieved than could be done with a water bath. If even higher temperatures are required, the oil bath can be replaced with a sand bath.


See also


References

  1. Kister, Henry Z. (1992). Distillation Design, 1st Edition. McGraw-Hill. 0070349096. 
  2. Perry, Robert H. and Green, Don W. (1984). Perry's Chemical Engineers' Handbook, 6th Edition. McGraw-Hill. 0070494797. 

External links