de - Beste verfügbare Techniken (BVT) - Umweltbundesamt
de - Beste verfügbare Techniken (BVT) - Umweltbundesamt de - Beste verfügbare Techniken (BVT) - Umweltbundesamt
Chapter 2 2.1.1 Intermediates [6, Ullmann, 2001, 16, Winnacker and Kuechler, 1982, 19, Booth, 1988] The number of intermediates actually or potentially available is very large and the technology of their manufacture is an important part of industrial organic chemistry. Starting raw materials are aromatic hydrocarbons, such as benzene, toluene, naphthalene, anthracene, pyrene, phenol, pyridine and carbazol, as well as a wide range of aliphatic compounds like, e.g. alcohols, carbonic acids, heterocyclic compounds. Aromatic hydrocarbons undergo four electrophilic substitution reactions – the Friedel-Crafts reaction, halogenation, nitration and sulphonation – as well as oxidation and reduction. The reactions lead to substituted hydrocarbons (primary intermediates). Most manufacturing processes for primary intermediates are run continuously and with dedicated equipment, because of the large production volume. Subsequent modification steps are usually carried out in batches. Table 2.2 gives some examples. “One pot” synthesis indicates that several reaction steps are carried out without work-up of the intermediates. Compound Unit process Mode of operation Use Primary Nitrobenzene Nitration Continuous intermediate Chlorobenzene Chlorination Continuous p-toluene sulphonic acid Sulphonation Continuous o-nitroaniline Exchange Continuous Intermediates 4-chloro-3-nitrobenzene sulphonic acid Sulphonation Batch Dyes 2,3,4-trichloro-6nitrophenol Exchange Sulphonation Batch, semi-batch Pesticides Bromamine acid Amination Sulphonation Bromination Batch, “one pot” Dyes Pyrazolone Diazotisation Condensation Batch, “one pot” Pharmaceuticals Dyes Table 2.2: Examples for primary intermediates and intermediates 20 Dezember 2005 OFC_BREF
2.1.2 Isomers and by-products Chapter 2 The stepwise introduction of substituents and their subsequent modification (see Figure 2.1), in combination with the unavoidable drastic reaction conditions (e.g. reactivity of halogens, oxidative effects of concentrated sulphuric/nitric acids, higher reaction temperatures for deactivated aromatics), can lead to an increasing number of side reactions and unwanted byproducts, e.g: • position isomers • higher and lower substituted compounds • modification of substituents • oxidation products • by-products derived from the by-products if work-up is omitted (“one pot synthesis”). Cl Cl OFC_BREF Dezember 2005 21 NO 2 Chlorination Nitration Exchange OCH 3 OCH3 OCH3 OCH3 OCH3 NH NH Reductive coupling Rearrangement Figure 2.1: Illustrative example of a synthesis using several unit processes Often recovery and re-use of isomers or by-products is technically possible (e.g. as starting material in other plants or sectors). But in many cases a recovery appears difficult due to economical, ecological or legal reqirements. If a recovery is not possible, unwanted isomers/by-products have to be separated from the product and contribute to waste or waste water streams. The nitration of toluene given in Table 2.3 can be used as an illustrative example. In this case, the isomers are separated and purified by distillation. Starting material Process Isomers By-products Nitrophenols Toluene Nitration with HNO3 o-Nitrotoluene (59.5 %) m-Nitrotoluene (4 %) p-Nitrotoluene (36 %) Nitrocresols Nitrohydroxy benzoic acids Phenylnitromethane Tetranitromethane Table 2.3: Example for the formation of isomers and by-products NH 2 NO 2 NH 2
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Chapter 2<br />
2.1.1 Intermediates<br />
[6, Ullmann, 2001, 16, Winnacker and Kuechler, 1982, 19, Booth, 1988]<br />
The number of intermediates actually or potentially available is very large and the technology of<br />
their manufacture is an important part of industrial organic chemistry.<br />
Starting raw materials are aromatic hydrocarbons, such as benzene, toluene, naphthalene,<br />
anthracene, pyrene, phenol, pyridine and carbazol, as well as a wi<strong>de</strong> range of aliphatic<br />
compounds like, e.g. alcohols, carbonic acids, heterocyclic compounds.<br />
Aromatic hydrocarbons un<strong>de</strong>rgo four electrophilic substitution reactions – the Frie<strong>de</strong>l-Crafts<br />
reaction, halogenation, nitration and sulphonation – as well as oxidation and reduction. The<br />
reactions lead to substituted hydrocarbons (primary intermediates).<br />
Most manufacturing processes for primary intermediates are run continuously and with<br />
<strong>de</strong>dicated equipment, because of the large production volume. Subsequent modification steps<br />
are usually carried out in batches. Table 2.2 gives some examples. “One pot” synthesis indicates<br />
that several reaction steps are carried out without work-up of the intermediates.<br />
Compound Unit process<br />
Mo<strong>de</strong> of<br />
operation<br />
Use<br />
Primary Nitrobenzene Nitration Continuous<br />
intermediate Chlorobenzene Chlorination Continuous<br />
p-toluene sulphonic acid Sulphonation Continuous<br />
o-nitroaniline Exchange Continuous<br />
Intermediates 4-chloro-3-nitrobenzene<br />
sulphonic acid<br />
Sulphonation Batch Dyes<br />
2,3,4-trichloro-6nitrophenol<br />
Exchange<br />
Sulphonation<br />
Batch, semi-batch Pestici<strong>de</strong>s<br />
Bromamine acid<br />
Amination<br />
Sulphonation<br />
Bromination<br />
Batch, “one pot” Dyes<br />
Pyrazolone<br />
Diazotisation<br />
Con<strong>de</strong>nsation<br />
Batch, “one pot”<br />
Pharmaceuticals<br />
Dyes<br />
Table 2.2: Examples for primary intermediates and intermediates<br />
20 Dezember 2005 OFC_BREF