Kinetics of Catalytic Oxidation of Benzene, n-Hexane, and Emission Gas from a Refinery Oil/Water Separator over a Chromium Oxide Catalyst

• Published in: Journal of the Air & Waste Management Association 2000-02, Vol.50 (2), p.227-233
• Main Authors: Wang, Jenshi B., Chou, Ming-Shean
• Format: Article
• Language: English
• Subjects: Air Pollutants, Occupational - analysis; Applied sciences; Atmospheric pollution; benzene; Benzene - analysis; Carcinogens - analysis; Catalysis; Catalytic reactions; Chemistry; Chromium Compounds - chemistry; Exact sciences and technology; General and physical chemistry; hexane; Hexanes - analysis; Industry - instrumentation; Kinetics; Other pollution sources in industry; Oxidation-Reduction; Petroleum; Pollution; Prevention and purification methods; Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry
• ISSN: 1096-2247; 1047-3289; 2162-2906
• DOI: 10.1080/10473289.2000.10464003

With the advances made in the past decade, catalytic incineration of volatile organic compounds (VOCs) has become the technology of choice in a wide range of pollution abatement strategies. In this study, a test was undertaken for the catalytic incineration, over a chromium oxide (Cr 2 O 3 ) catalyst, of n-hexane, benzene, and an emission air/vapor mixture collected from an oil/water separator of a refinery. Reactions were carried out by controlling the feed stream to constant VOC concentrations and temperatures, in the ranges of 1300-14,700 mg/m 3 and 240-400 ° C, respectively. The destruction efficiency for each of the three VOCs as a function of influent gas temperature and empty bed gas residence time was obtained. Results indicate that n-hexane and the oil vapor with a composition of straight- and branch-chain aliphatic hydrocarbons exhibited similar catalytic incineration effects, while benzene required a higher incineration temperature or longer gas retention time to achieve comparable results. In the range of the VOC concentrations studied, at a given gas residence time, increasing the operating temperature of the catalyst bed increased the destruction efficiency. However, the much higher temperatures required for a destruction efficiency of over 99% may be not cost-effective and are not suggested. A first-order kinetics with respect to VOC concentration and an Arrhenius temperature dependence of the kinetic constant appeared to be an adequate representation for the catalytic oxidation of these volatile organics. Activation energy and kinetic constants were estimated for each of the VOCs. Low-temperature destruction of the target volatile organics could be achieved by using the Cr 2 O 3 catalyst.