Aniline

Thomas Kahl

Thomas Kahl

BASF AG, Ludwigshafen, Germany

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Kai-Wilfrid Schröder

Kai-Wilfrid Schröder

BASF AG, Ludwigshafen, Germany

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F. R. Lawrence

F. R. Lawrence

E. I. du Pont de Nemours & Co., Deepwater, New Jersey, United States, 08023

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W. J. Marshall

W. J. Marshall

E. I. du Pont de Nemours & Co., Deepwater, New Jersey, United States, 08023

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Hartmut Höke

Hartmut Höke

Weinheim, Germany

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Rudolf Jäckh

Rudolf Jäckh

BASF AG, Ludwigshafen, Germany

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First published: 15 October 2011
Citations: 31

Abstract

The article contains sections titled:

1.

Introduction

2.

Physical and Chemical Properties

3.

Production

3.1.

Raw Materials

3.2.

Processes

3.2.1.

Catalytic Hydrogenation of Nitrobenzene

3.2.1.1.

Catalytic Vapor-Phase Hydrogenation

3.2.1.2.

Catalytic Liquid-Phase Hydrogenation

3.2.2.

Reduction of Nitrobenzene with Iron and Iron Salts

3.2.3.

Amination of Phenol

4.

Quality Specifications

5.

Handling, Storage and Transportation

6.

Uses

6.1.

Methylene Diphenylene Isocyanate (MDI)

6.2.

Rubber Processing Chemicals

6.3.

Dyes and Pigments

6.4.

Agricultural Chemicals

6.5.

Pharmaceuticals

6.6.

Cyclohexylamine/Dicyclohexylamine

6.7.

Miscellaneous

7.

Economic Aspects

8.

Derivatives

9.

Toxicology

9.1.

Toxicokinetic Properties and Metabolism

9.2.

Toxicological Properties

10.

Occupational Health

The full text of this article hosted at iucr.org is unavailable due to technical difficulties.