Consider a bimolecular irreversible reaction, A + B = C + D To be carried out in a liquid phase plug flow reactor. Given the reaction is second order and the mass flow of A and B are respectively 95kg/hr and 117kg/hr. The reactor has a volume of 0.02m² and is operated isothermally at 112°C giving a conversion of 55%. Can you conduct the following sub tasks: (a) From first principles show that the design equation for a plug flow reactor is: Xa dXA (-ra) FAO Where, V, = Volume of reactor, m² FAo = Initial flow of A, XA = Conversion of A (-Ta) = Reaction rate, kmol/hr (b) Calculate the molar feed rates of A and B and the magnitude of the term kCAo?. The relative molecular masses of A and B are 139 and 172. (c) If a continuous stirred tank reactor of the same content volume is installed in series upstream of the plug flow reactor, what is the new overall conversion? All other parameters being unchanged.

For the toolbar, press ALT+F10 (PC) or ALT+FN+F10 (Mac).   Paragraph   Arial   14px                                                         P 0 WORDSPOWERED BY TINY   25 points    QUESTION 4 The tank in figure below is filled through point 1 with velocity equal to 5 m/s and point 3 with volumetric flow rate equal to 0.012m3/s. If the level of the water h is constant, determine the exit velocity V2. If the water level h varies and V2 =8 m/s, find the rate change (dh/dt). Assume d=1m.

U0zden GEÇir Görünüm Aa- E-= - EE T Aralık Yok T Konu Ba. T Liste Par.. T Normal Paragraf Stiller Derive the transfer function of the process from the block diagram shown in the figure. G,(s) X(s)} G (s) Y(s) G (s) G(s) G(5). SONY REDMI NOTE 8 AI QUAD CAMERA

7.1. A step change of magnitude 4 is introduced into a system having the transfer function Y(s) 10 X(s) s² + 1.65 +4 Determine (a) Percent overshoot (b) Rise time (c) Maximum value of Y(t) (d) Ultimate value of Y(t) (e) Period of oscillation