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Designing and operating safe chemical reaction processes HSG143

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Health <strong>and</strong> SafetyExecutive(b) protective, ie they reduce the consequences of a hazardous situation.128 Whatever the basis of <strong>safe</strong>ty selected it is important that you consider:(a) all foreseeable hazards; <strong>and</strong>(b) that there are suitable <strong>and</strong> sufficient <strong>safe</strong>ty systems in place to reduce theoverall risk to a level that is as low as reasonably practicable.Preventive measures129 Preventive measures relate to your defined <strong>safe</strong> <strong>operating</strong> envelope. Theseare the means by which you control the desired <strong>chemical</strong> <strong>reaction</strong>. They includemeasures to control:(a) Temperature: the <strong>safe</strong>ty margin between the temperature at which anundesired exothermic <strong>reaction</strong> starts <strong>and</strong> the <strong>operating</strong> temperature.(b) Reactant addition: to prevent addition of the wrong reactant; or the correctreactant(s) too early, too late, too quickly, too slowly, in too much or too littlequantities, or in the wrong order.(c) Agitation: what happens when the agitator or circulation pump fails, is startedtoo late, is stopped or not turned on, or is <strong>operating</strong> at the wrong speed?(d) Other variables: used to control <strong>reaction</strong>s including varying pH, conductivity,concentration <strong>and</strong> pressure, etc.130 Other measures include aspects of the design of the process <strong>and</strong> plantalready discussed, particularly the inherently <strong>safe</strong>r options. But they also includethe engineering <strong>and</strong> procedural controls; the <strong>safe</strong>ty interlocks <strong>and</strong> emergencyshutdown systems. 15Controlling rates of <strong>reaction</strong>131 You can affect the heat balance by how you control the rate of <strong>reaction</strong>. Ifall the reactants are present in the reactor at the start of the process, <strong>and</strong> youthen start the <strong>reaction</strong> (eg by heating), then this is a batch <strong>reaction</strong>. The maindisadvantage of batch <strong>reaction</strong>s is that because all the reactants are present,if something goes wrong (eg failure of cooling) then nothing can be done tocontrol the <strong>reaction</strong>. You must then rely on protective measures to mitigate theconsequences.132 If you add one or more reactants gradually during the <strong>reaction</strong> then theprocess is a semi-batch <strong>reaction</strong>. The rate of <strong>reaction</strong> is controllable by a numberof factors, in particular addition rate <strong>and</strong> temperature.133 In most cases, stopping the addition will not completely stop the <strong>reaction</strong>.Some temperature rise can be developed in the <strong>reaction</strong> mass because some<strong>reaction</strong> of accumulated reactants continues. The effect of this accumulation <strong>and</strong>its extent depends on the balance between <strong>reaction</strong> kinetics <strong>and</strong> addition rate. Itmay be possible to control addition rates <strong>and</strong> temperatures so that there is only asmall accumulation of unreacted material in the reactor. In this case the <strong>reaction</strong>mixture cannot reach an un<strong>safe</strong> temperature. Isothermal calorimetry can be usefulin determining the optimum conditions for this.<strong>Designing</strong> <strong>and</strong> <strong>operating</strong> <strong>safe</strong> <strong>chemical</strong> <strong>reaction</strong> <strong>processes</strong> Page 27 of 64

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