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HAZARDS OF CATALYSTS

Hazards of Catalysts Discusses the special hazards of catalysts, where you might encounter these, and how you can safely handle these materials in the laboratory. [Pg.218]

Minimize exposure to the hazards of catalysts by carefully planning experiments and taking steps to ensure you are protected from exposures and their consequences, such as fires, explosions, and allergic reactions. [Pg.349]

Basic process chemistry using less hazardous materials and chemical reactions offers the greatest potential for improving inherent safety in the chemical industry. Alternate chemistry may use less hazardous raw material or intermediates, reduced inventories of hazardous materials, or less severe processing conditions. Identification of catalysts to enhance reaction selectivity or to allow desired reactions to be carried out at a lower temperature or pressure is often a key to development of inherently safer chemical synthesis routes. Some specific examples of innovations in process chemistry which result in inherently safer processes include ... [Pg.36]

The primary need for gas-solid separation processes is for gas cleaning the removal of dispersed finely divided solids (dust) and liquid mists from gas streams. Process gas streams must often be cleaned up to prevent contamination of catalysts or products, and to avoid damage to equipment, such as compressors. Also, effluent gas streams must be cleaned to comply with air-pollution regulations and for reasons of hygiene, to remove toxic and other hazardous materials see IChemE (1992). [Pg.448]

Dining chlorination of hydrocarbons with Lewis acid catalysis, the catalyst must be premixed with the hydrocarbon before admission of chlorine. Addition of catalyst to the chlorine-hydrocarbon mixture is very hazardous, causing instantaneous release of large volumes of hydrogen chloride. [Pg.1407]

Direct routes from hazardous elements Routes at increased concentration or even solvent-free Routes at elevated temperature and/or pressure Routes mixing the reactants all at once Routes using unstable intermediates Routes in the explosive or thermal runaway regime Process simplification - e.g., routes omitting the need of catalysts or (complex) separation... [Pg.217]

A measure is preventive if it prevents the occurrence of a runaway, a decomposition, or a hazardous secondary reaction. The system conditions remain close to operating conditions. Excessive increases in temperatures and/or pressures are avoided. Preventive measures include feed rate control systems, interlocks to prevent the reaction from starting unless sufficient diluent is present or the cooling system is working, and tests for the presence of catalysts or unwanted impurities. Preventive measures are always to be preferred over protective or mitigating (defensive) measures. [Pg.99]

Asphyxiation and Toxicity Hazards An asphyxiant is a chemical (either a gas or a vapor) that can cause death or unconsciousness by suffocation (BP, Hazards of Nitrogen and Catalyst Handling, 2003). A simple asphyxiant is a chemical, such as N2, He, or Ar, whose effects are caused by the displacement of 02 in air, reducing the 02 concentration below its normal value of approximately 21 vol %. The physiological effects of oxygen concentration reduction by simple asphyxiants are illustrated in Table 23-18 (BP, Hazards of Nitrogen and Catalyst Handling, 2003). [Pg.36]

Injuries and fatalities from asphyxiation are often associated with personnel entry into inerted equipment or enclosures. Guidance on safe procedures for confined space access are provided by OSHA (OSHA, 29 CFR 1910.146, Confined Space Entry Standard, 2000), the American National Standards Institute (ANSI, Z117.1, Safety Requirements for Confined Spaces, 2003), Hodson (Hodson, Safe Entry into Confined Spaces, Handbook of Chemical Health and Safety, American Chemical Society, 2001), and BP (BP, Hazards of Nitrogen and Catalyst Handling, 2003). OSHA has established 19.5 vol % as the minimum safe oxygen concentration for confined space entry without supplemental oxygen supply (see Table 23-18). Note that OSHA imposes a safe upper limit on 02 concentration of 23.5 vol % to protect against the enhanced flammability hazards associated with 02-enriched atmospheres. [Pg.37]

The later sections of the book deal with the actual laboratory use of catalysts for asymmetric reduction and oxidation reactions. Most of the protocols describe non-natural catalysts principally because many of the corresponding biological procedures were featured in the sister volume Preparative Biotransformations. As in this earlier book, we have spelt out the procedures in great detail, giving where necessary, helpful tips and, where appropriate, clear warnings of toxicity, fire hazards, etc. [Pg.239]


See other pages where HAZARDS OF CATALYSTS is mentioned: [Pg.347]    [Pg.349]    [Pg.348]    [Pg.349]    [Pg.351]    [Pg.797]    [Pg.347]    [Pg.349]    [Pg.348]    [Pg.349]    [Pg.351]    [Pg.797]    [Pg.475]    [Pg.131]    [Pg.392]    [Pg.211]    [Pg.18]    [Pg.632]    [Pg.187]    [Pg.148]    [Pg.156]    [Pg.174]    [Pg.252]    [Pg.182]    [Pg.327]    [Pg.47]    [Pg.44]    [Pg.197]    [Pg.198]    [Pg.509]    [Pg.375]    [Pg.178]    [Pg.179]    [Pg.6]    [Pg.2]    [Pg.18]    [Pg.392]    [Pg.381]    [Pg.381]    [Pg.182]   


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