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Passive Safety Aspects of Tubular Reactors

A reaction A—— P is to be performed in a PFR. The reaction follows first-order kinetics, and at 50 °C in the batch mode, the conversion reaches 99% in 60 seconds. Pure plug flow behavior is assumed. The flow velocity should be 1 m s 1 and the overall heat transfer coefficient 1000Wm 2 K 1. (Why is it higher than in stirred tank reactors ). The maximum temperature difference with the cooling system is 50 K. [Pg.194]

Reactor design calculate the required tube length and diameters required to achieve the same performance as the 5 m3 semi-batch reactor with time-cycle of 2 hours and a conversion of 99%. [Pg.194]

Isothermal reaction under which conditions is this strategy possible  [Pg.194]

Slow reaction what happens with a 100 times slower reaction  [Pg.194]

Cooling failure what happens in case of cooling failure  [Pg.194]


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