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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> SafetyExecutiveHazard assessment of<strong>chemical</strong> <strong>reaction</strong>s56 The primary aim of this publication is to give you an underst<strong>and</strong>ing of thephilosophies <strong>and</strong> stages you should go through when designing a <strong>safe</strong> <strong>chemical</strong><strong>reaction</strong> process. It does not cover all aspects of this process but concentrates onthe hazards that may be generated during the <strong>chemical</strong> <strong>reaction</strong>.57 The three major <strong>chemical</strong> <strong>reaction</strong> hazards you need to consider are:(a) the thermal instability of reactants, reactant mixtures <strong>and</strong> products (includingany intermediates, potential contaminants <strong>and</strong> by-products);(b) exothermic <strong>reaction</strong>s which raise the temperature to produce decomposition<strong>reaction</strong>s or violent boiling; <strong>and</strong>(c) gas evolution.58 The approach taken relies upon the life cycle concept 15 discussed earlier(paragraph 27) <strong>and</strong> the risk assessment you must carry out to comply with health<strong>and</strong> <strong>safe</strong>ty regulations.59 A typical <strong>safe</strong>ty assessment procedure will include:(a) defining the chemistry, the process <strong>operating</strong> conditions <strong>and</strong> the process plant;(b) identifying the hazards;(c) assessing the consequences, in terms of their severity <strong>and</strong> likelihood;(d) selecting <strong>and</strong> specifying a basis of <strong>safe</strong>ty; <strong>and</strong>(e) implementing <strong>and</strong> maintaining the <strong>safe</strong>ty measures.60 For new <strong>processes</strong> <strong>and</strong> plant, beginning this assessment procedure at theearliest stages of research <strong>and</strong> development allows you to achieve the highestlevel of inherent <strong>safe</strong>ty. At this stage you can also minimise the costs of <strong>safe</strong>typrecautions. For existing plant <strong>and</strong> <strong>processes</strong>, you should consider your riskassessment to ensure you have taken all necessary steps to reduce risks to as lowas is reasonably practicable.61 Chemical <strong>reaction</strong> hazards need assessing by technically qualified peoplewho have some experience of hazard evaluation <strong>and</strong> a good knowledge ofprocess chemistry. Ideally they should be part of an independent team to avoidconflicts of interest between production <strong>and</strong> <strong>safe</strong>ty. However, they do needgood communications with plant staff in order to minimise the chance of anymisunderst<strong>and</strong>ings.62 The depth of the hazard assessment depends on the nature <strong>and</strong> magnitudeof the hazards <strong>and</strong> on the scale of operation <strong>and</strong> its complexity. For example, itmay be easy to show for some <strong>processes</strong> that they are unable to runaway fromknowledge of the process chemistry combined with small scale screening tests.For others, you will need to do more detailed <strong>and</strong> accurate tests. There may belittle justification for accurately measuring the rate of temperature rise of a runaway<strong>reaction</strong> if the process is only being operated at the gram scale in the laboratory.<strong>Designing</strong> <strong>and</strong> <strong>operating</strong> <strong>safe</strong> <strong>chemical</strong> <strong>reaction</strong> <strong>processes</strong> Page 15 of 64

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