Participants
| Role | Name | HCID | Charge |
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| Reactant | Nitrobenzene | HCID 7416 | — |
| Solvent | Water | HCID 962 | — |
| Product | Nitrobenzene | HCID 7416 | — |
| Product | Nitrosobenzene | HCID 11473 | — |
Reaction Steps
A mixture of nitrobenzene and nitrogen, preheated to 396° C., was continuously conducted through a glass pipe with an inside diameter of 1 cm and a length of about 50 cm, which contained 16 cc of a freshly prepared Pb/Mn catalyst (catalyst preparation 1) in the form of 1 mm spherules. The throughput was 27 g/hour (0.22 mol) of nitrobenzene and 45 Nlit/hour of nitrogen. After leaving the reaction pipe, which, by means of electrical heating, was kept practically isothermally at 396° C., the reaction mixture was indirectly cooled with water to 25° C. and the constituents of low volatility were separated. The small quantities of compounds with low volatility still present in the exhaust gas were subsequently absorbed by a washer filled with dioxane. A nitrobenzene conversion of 17% was obtained under these conditions, whereby nitrosobenzene had been formed with a selectivity of 89%. The remainder of the solution was composed of azobenzene, azoxybenzene and aniline. The reactor was operated continuously for a total of 10 hours, during which it was not possible to determine any decline in the activity of the catalyst. A gas-chromatographic investigation of the exhaust gas showed only carbon dioxide and water in addition to nitrogen, as well as traces of nitrosobenzene and nitrobenzene. The following Table I shows the yields and selectivities in dependence upon the duration of operation.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US04317947 |
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| Source dataset | uspto-grants-1982_03 |
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| ORD ID | ord-771e11ede5144cb286381d8149025a41 |
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| Source note | uspto-grants-1982_03 |
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