Variability of operating safety limits with catalyst within a fixed-bed catalytic reactor for vapour-phase nitrobenzene hydrogenation

Author:

Maria Gheorghe,Stefan Dragos-Nicolae

Publisher

Elsevier BV

Subject

Industrial and Manufacturing Engineering,Management Science and Operations Research,Energy Engineering and Power Technology,Safety, Risk, Reliability and Quality,General Chemical Engineering,Food Science,Control and Systems Engineering

Reference57 articles.

1. Guidelines for chemical process quantitative risk analysis;AIChE,2000

2. Kinetic investigations of the deactivation by coking of a noble metal catalyst in the catalytic hydrogenation of nitrobenzene using a catalytic wall reactor;Amon;Chemical Engineering and Processing,1999

3. Explicit runaway criterion for catalytic reactors with transport limitations;Balakotaiah;AIChE Journal,2004

4. Analysis of non-isothermal kinetic data. III. Application of Wilson method to the calculation of constants of a kinetic equation for hydrogenation of nitrobenzene, acetone and benzene;Cerny;Chemicky Prumysl,1968

5. Consideration of sensitivity and parameter uncertainty in optimal process design;Chen;Industrial & Engineering Chemistry Process Design and Development,1970

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