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2.5.12 Sulphonation<br />

Chapter 2<br />

[6, Ullmann, 2001, 15, Köppke, 2000, 16, Winnacker and Kuechler, 1982, 46, Ministerio <strong>de</strong><br />

Medio Ambiente, 2003]<br />

For environmental issues and treatment of waste streams, see Section 4.3.2.8.<br />

The direct introduction of the sulphonic acid group to an aromatic system is one of the most<br />

important reactions in industrial organic chemistry. It gives high yields un<strong>de</strong>r relatively mild<br />

conditions and usually results in well <strong>de</strong>fined <strong>de</strong>rivatives. Arylsulphonic acids are used chiefly<br />

as intermediates in the manufacture of dyes, insectici<strong>de</strong>s, pharmaceuticals, plasticisers, optical<br />

brighteners, etc. Among the typical raw materials are also halogenated compounds, thus<br />

contributing to the AOX load of waste water streams.<br />

Chemical reaction<br />

Sulphonation is usually carried out with concentrated sulphuric acid in excess of<br />

about 50 to 100 % or using oleum. Due to the fundamental rules of electrophilic aromatic<br />

substitution, the product is a mixture of the target molecule and isomers. The reaction is<br />

reversible, with the yield and isomer distribution <strong>de</strong>pending on the reaction conditions (e.g.<br />

temperature, removal of reaction water by azeotrope distillation or addition of thionyl chlori<strong>de</strong>).<br />

R<br />

H<br />

H 2SO 4<br />

- H 2O<br />

(Oleum)<br />

Figure 2.25: Sulphonation of an aromatic system<br />

SO 3H<br />

Increased temperature and reaction water removal also favour the formation of sulphones as byproducts.<br />

Depending on the reactants (aromatic, H2SO4, oleum) and temperature, the oxidative<br />

effects of sulphuric acid or sulphur trioxi<strong>de</strong> can lead to unwanted oxidation reactions.<br />

Operations<br />

Figure 2.26 shows a typical sequence of operations for sulphonation, possible input materials<br />

and associated waste streams. The reaction is carried out at temperatures of about 60 to 90 ºC in<br />

cast steel or enamelled steel vessels. The sulphonating agent is fed into the vessel, the aromatic<br />

compound is then ad<strong>de</strong>d, and the reaction is controlled by means of temperature profiles or<br />

metering.<br />

On completion of the reaction, the batch is transferred into water, which causes unconverted<br />

aromatic compounds to be released. The dilute sulphonation mass is cooled, and the free acid is<br />

separated by filtration. For further purification, recrystallisation may be necessary.<br />

If the free acid is too soluble and isolation is not possible in this way, other techniques are<br />

carried out, such as:<br />

• salting out with sodium sulphate or sodium chlori<strong>de</strong><br />

• temperature controlled crystallisation, or<br />

• reactive extraction.<br />

OFC_BREF Dezember 2005 59<br />

R

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