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Designing and operating safe chemical reaction processes HSG143

Designing and operating safe chemical reaction processes HSG143

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Health <strong>and</strong> SafetyExecutive100 The results of the screening tests will give you a preliminary indication of:(a) the possibility of thermal decomposition;(b) the quantity <strong>and</strong> rate of heat release;(c) gas evolution;(d) induction time effects (autocatalysis) - ie the development of thermal instabilityafter prolonged storage; <strong>and</strong>(e) high-rate decompositions (showing that a substance could deflagrate).101 Often the initial deviation in the temperature trace is quoted as the initialexotherm temperature or the onset temperature (see Glossary). You must take carein interpreting these temperatures. A number of factors affect the temperature thatare unrelated to the inherent <strong>chemical</strong> stability of the test material. These include:(a) the sensitivity of the test device;(b) the sample size;(c) the experimental heating mode <strong>and</strong> heating rate (eg the onset temperatureincreases as the rate of heating of the sample increases);(d) heat losses from the sample container;(e) <strong>reaction</strong>s with the sample container; <strong>and</strong>(f) sample vaporisation prior to decomposition.An explosion occurred in a process vessel involving a thermally unstablematerial. Published values of the onset temperature for thermal decomposition inlaboratory tests were in the range 270-300 o C. However, following the incident,further investigation indicated that the material would decompose at around150 o C on the plant scale.102 What you have achieved at this point in the assessment process is a goodintroductory underst<strong>and</strong>ing of your chosen <strong>chemical</strong> process <strong>and</strong> the hazardsinvolved. You may now have sufficient information to define the <strong>safe</strong> <strong>operating</strong>envelope for full-scale plant, particularly if you are going to operate at temperatureswell below the onset temperature for runaway or decomposition when related tothe <strong>operating</strong> conditions.103 However, in a number of cases, you will need to carry out more detailed teststo determine the <strong>safe</strong> <strong>operating</strong> envelope.Reaction calorimetry104 It is possible for you to directly measure the instantaneous heat output of areacting system due to <strong>chemical</strong> or physical <strong>processes</strong> as a function of the processtime. This quantity shows directly whether <strong>and</strong> how quickly <strong>chemical</strong> conversionsoccur in the process phase under consideration. Such an approach can be useful,not only from a <strong>safe</strong>ty perspective but also for process design <strong>and</strong> optimisation.<strong>Designing</strong> <strong>and</strong> <strong>operating</strong> <strong>safe</strong> <strong>chemical</strong> <strong>reaction</strong> <strong>processes</strong> Page 22 of 64

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