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The article contains sections titled: 1. Nitric Acid 1.1. Introduction 1.2. Properties 1.3. Industrial Production 1.3.1. Oxidation of Ammonia 1.3.2. Oxidation and Absorption of Nitrogen Oxides 1.3.3. Equipment 1.3.3.1. Filters and Mixers 1.3.3.2. Burners and Waste‐Heat Boilers 1.3.3.3. Compressors and Turbines 1.3.3.4. Heat Exchangers and Columns 1.3.3.5. Construction Materials 1.3.4. Processes 1.3.4.1. Weak Acid Processes 1.3.4.2. Concentrated Acid Processes 1.4. Environmental Protection 1.4.1. Wastewater 1.4.2. Stack Gas 1.4.2.1. Emission Limits 1.4.2.2. Analysis 1.4.2.3. Control of NO x Emissions 1.5. Storage and Transportation 1.6. Uses and Economic Aspects 2. Nitrous Acid 3. Nitrogen Oxides 3.1. Dinitrogen Monoxide 3.2. Nitrogen Monoxide 3.3. Nitrogen Dioxide and Dinitrogen Tetroxide 3.4. Dinitrogen Trioxide 3.5. Dinitrogen Pentoxide 4. Toxicology and Occupational Health
The article contains sections titled: 1. Nitric Acid 1.1. Introduction 1.2. Properties 1.3. Industrial Production 1.3.1. Oxidation of Ammonia 1.3.2. Oxidation and Absorption of Nitrogen Oxides 1.3.3. Equipment 1.3.3.1. Filters and Mixers 1.3.3.2. Burners and Waste‐Heat Boilers 1.3.3.3. Compressors and Turbines 1.3.3.4. Heat Exchangers and Columns 1.3.3.5. Construction Materials 1.3.4. Processes 1.3.4.1. Weak Acid Processes 1.3.4.2. Concentrated Acid Processes 1.4. Environmental Protection 1.4.1. Wastewater 1.4.2. Stack Gas 1.4.2.1. Emission Limits 1.4.2.2. Analysis 1.4.2.3. Control of NO x Emissions 1.5. Storage and Transportation 1.6. Uses and Economic Aspects 2. Nitrous Acid 3. Nitrogen Oxides 3.1. Dinitrogen Monoxide 3.2. Nitrogen Monoxide 3.3. Nitrogen Dioxide and Dinitrogen Tetroxide 3.4. Dinitrogen Trioxide 3.5. Dinitrogen Pentoxide 4. Toxicology and Occupational Health
ChemInform Abstract In the course of investigations concerning the corrosion resistance of aluminum materials in highly concentrated nitric acid the thermal decomposition of this acid is observed at atmospheric pressure between 0 and 60 rc C for up to 273 d. The reversible decomposition reaction, which is shown in the scheme, is second order with respect of HNO3. The rate and equilibrium constants are determinedby evaluation the kinetic runs. The activation energy is found to be -134 kJ/mol.
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