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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> SafetyExecutive52 To additionally illustrate the effect of scale up on the heat balance consider anexothermic <strong>reaction</strong> where the heat of <strong>reaction</strong> is -416 kJ kg -1 of reactant mass;the specific heat of the <strong>reaction</strong> mass is 1.26 kJ kg -1 K -1 ; <strong>and</strong> the <strong>reaction</strong> is carriedout over one hour with a jacket-to-contents temperature differential of 80 o C. Thedifferences between laboratory scale <strong>and</strong> plant scale are:Laboratory scalePlant scale(100 ml) (4500 litres)Heat loss (W kg -1 K -1 ) 2.3 0.04Cooling rate (K hr -1 ) 520 9Adiabatic temperature rise (K) 330 330(See paragraph 79)Result No exotherm seen Possible runawayAn explosion occurred during the manufacture of a phenolic resin by a phenolformaldehyde<strong>reaction</strong> catalysed by caustic soda in a 5.9 m 3 <strong>reaction</strong> vessel. Theexplosion ruptured the vessel <strong>and</strong> caused considerable damage to the building.The incident occurred because of insufficient cooling capacity on scaling up theprocess. The <strong>reaction</strong> process was scaled up from 2.3 m 3 to 5.9 m 3 withouttaking due account of the reduction in vessel cooling capacity. This resulted inan increased <strong>reaction</strong> temperature that caused a runaway exothermic <strong>reaction</strong>.The <strong>safe</strong> <strong>operating</strong> envelope53 What the designer is trying to achieve is a controlled <strong>chemical</strong> <strong>reaction</strong> processthat avoids a hazardous situation from occurring. The <strong>safe</strong> <strong>operating</strong> envelopedefines the boundaries that contain the controlled <strong>reaction</strong>.54 It is inherently <strong>safe</strong>r if you develop <strong>processes</strong> with wide <strong>safe</strong> <strong>operating</strong>envelopes. These are less sensitive to variations in critical <strong>operating</strong> parameters.For example, controlling your process within a very small temperature b<strong>and</strong> toavoid hazardous conditions means that the process has a narrow <strong>safe</strong> <strong>operating</strong>envelope. A process with a larger temperature b<strong>and</strong> will have a wider <strong>safe</strong><strong>operating</strong> envelope.55 Discussion about the determination of the <strong>safe</strong> <strong>operating</strong> envelope occurs inparagraphs 123-125.<strong>Designing</strong> <strong>and</strong> <strong>operating</strong> <strong>safe</strong> <strong>chemical</strong> <strong>reaction</strong> <strong>processes</strong> Page 14 of 64

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