de - Beste verfügbare Techniken (BVT) - Umweltbundesamt
de - Beste verfügbare Techniken (BVT) - Umweltbundesamt de - Beste verfügbare Techniken (BVT) - Umweltbundesamt
Chapter 2 2.5.11 Reduction of aromatic nitro compounds [6, Ullmann, 2001, 16, Winnacker and Kuechler, 1982, 19, Booth, 1988] For environmental issues and treatment of waste streams, see Section 4.3.2.7. One of the most industrially important reduction processes in industrial use is the conversion of an aromatic nitro or dinitro compound into an arylamine or arylene diamine. Aromatic amines are widely used as dye intermediates, especially for azo dyes, pigments, and optical brighteners; as intermediates for photographic chemicals, pharmaceuticals, and agricultural chemicals; in polymers via isocyanates for polyurethanes; and as antioxidants. Among reduction methods, there are three of major relevance in organic fine chemistry: • catalytic hydrogenation, which is extremely important industrially because of its universal applicability; most processes can be carried out successfully by catalytic hydrogenation • Béchamp and Brinmeyr reduction with iron, which is the classical method • alkali sulphide reduction, which is the selective method in specific cases, such as in the manufacture of nitroamines from dinitro compounds, the reduction of nitrophenols, the reduction of nitroanthraquinones and the manufacture of aminoazo compounds from the corresponding nitroazo derivative. All three methods are also applied to halogenated nitro compounds, and can thus contribute to AOX loads in waste water streams. 2.5.11.1 Catalytic reduction with hydrogen Chemical reaction The catalytic reduction of the nitro compounds is very exothermic. To reduce these hazards, the concentration of nitro compound, the amount and partial pressure of the hydrogen, the temperature, and the activity of the catalyst, are controlled. R NO 2 + 3 H 2 Catalyst Figure 2.23: Catalytic reduction of aromatic nitro compounds Most aromatic nitro compounds are hydrogenated in the liquid phase. In this case, the pressure and temperature can be changed independently. The temperature is limited by the hydrogenation reaction of the aromatic ring which occurs above 170 – 200 °C. Normally, the reduction is carried out at 100 – 170 °C. Sensitive compounds are hydrogenated at lower temperatures (20 – 70 °C) or at lower pressures (1 – 50 bar). 1 – 50 bar are used normally. 56 Dezember 2005 OFC_BREF R NH 2
Chapter 2 Process hazards The catalytic reduction of nitro compounds is very exothermic. Unless this heat is dissipated properly, decomposition and even explosions can result, especially if the thermal decomposition of the nitro compound occurs or if condensation reactions are initiated as may be the case with chloro-nitro compounds. The industrial hydrogenation of aromatic polynitro compounds in the liquid phase without solvents especially requires precautions. To reduce these hazards, the concentration of the nitro compound, the amount and partial pressure of the hydrogen, the temperature, and the activity of the catalyst are controlled. The nitro compound is continuously added in small quantities, thus keeping its concentration below 2 %. De-ionised water is added to remove the heat of the reaction by continuous evaporation and to slow down the activity of the catalyst. The preferred solvents are methanol and 2-propanol; and also dioxane, tetrahydrofuran, and N-methylpyrrolidone are used. In the hydrogenation with a water immiscible solvent, such as toluene, the water must be removed, as in solvent-free hydrogenation, in order to maintain the activity of the catalyst. If the amine has a good water solubility, water is used as the solvent. Water also can be used in cases where the nitro compound forms water-soluble salts with alkalis, such as with nitrocarbonic or sulphonic acids. In practice, only Raney nickel, Raney nickel-iron, Raney cobalt, and Raney copper are used as pure metal catalysts because of their relatively low cost. Precious metal catalysts, such as Pt and Pd, are generally used at concentrations of 0.5 – 5 wt-% on support material with large surfaces, such as charcoal, silica, aluminium oxide, or alkaline-earth carbonates. Operations The vast majority of aromatic amines have small annual volumes (
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Chapter 2<br />
2.5.11 Reduction of aromatic nitro compounds<br />
[6, Ullmann, 2001, 16, Winnacker and Kuechler, 1982, 19, Booth, 1988]<br />
For environmental issues and treatment of waste streams, see Section 4.3.2.7.<br />
One of the most industrially important reduction processes in industrial use is the conversion of<br />
an aromatic nitro or dinitro compound into an arylamine or arylene diamine. Aromatic amines<br />
are wi<strong>de</strong>ly used as dye intermediates, especially for azo dyes, pigments, and optical brighteners;<br />
as intermediates for photographic chemicals, pharmaceuticals, and agricultural chemicals; in<br />
polymers via isocyanates for polyurethanes; and as antioxidants. Among reduction methods,<br />
there are three of major relevance in organic fine chemistry:<br />
• catalytic hydrogenation, which is extremely important industrially because of its universal<br />
applicability; most processes can be carried out successfully by catalytic hydrogenation<br />
• Béchamp and Brinmeyr reduction with iron, which is the classical method<br />
• alkali sulphi<strong>de</strong> reduction, which is the selective method in specific cases, such as in the<br />
manufacture of nitroamines from dinitro compounds, the reduction of nitrophenols, the<br />
reduction of nitroanthraquinones and the manufacture of aminoazo compounds from the<br />
corresponding nitroazo <strong>de</strong>rivative.<br />
All three methods are also applied to halogenated nitro compounds, and can thus contribute to<br />
AOX loads in waste water streams.<br />
2.5.11.1 Catalytic reduction with hydrogen<br />
Chemical reaction<br />
The catalytic reduction of the nitro compounds is very exothermic. To reduce these hazards, the<br />
concentration of nitro compound, the amount and partial pressure of the hydrogen, the<br />
temperature, and the activity of the catalyst, are controlled.<br />
R<br />
NO 2<br />
+ 3 H 2<br />
Catalyst<br />
Figure 2.23: Catalytic reduction of aromatic nitro compounds<br />
Most aromatic nitro compounds are hydrogenated in the liquid phase. In this case, the pressure<br />
and temperature can be changed in<strong>de</strong>pen<strong>de</strong>ntly. The temperature is limited by the hydrogenation<br />
reaction of the aromatic ring which occurs above 170 – 200 °C.<br />
Normally, the reduction is carried out at 100 – 170 °C. Sensitive compounds are hydrogenated<br />
at lower temperatures (20 – 70 °C) or at lower pressures (1 – 50 bar). 1 – 50 bar are used<br />
normally.<br />
56 Dezember 2005 OFC_BREF<br />
R<br />
NH 2