2.10 Irreversible consecutive reactions A B C occur in a jacketed, stirred-tank reactor as shown in Fig. E2.10. Derive a dynamic model based on the following assumptions: (i) The contents of the tank and cooling jacket are well mixed. The volumes of material in the jacket and in the tank do not vary with time. (ii) The reaction rates are given by r₁ = k₁e -E√/RTC CA [=] mol A/h L 12=k2e ERT CB [=] mol B/h L (iii) The thermal capacitances of the tank contents and the jacket contents are significant relative to the thermal capaci- tances of the jacket and tank walls, which can be neglected. (iv) Constant physical properties and heat transfer coeffi- cients can be assumed. Note: All flow rates are volumetric flow rates in L/h. The concentra- tions have units of mol/L. The heats of reaction are AH₁ and AH2. Feed CAi CBi qi T H V Coolant out 9e Te Coolant in qci. Tei Jacketed reactor Product CA. CB. CC. T. q Figure E2.10 " t