Q1// The elementary liquid-phase reaction A+B C, r=k CA CB is carried out in a batchreactor with a cooling coil to keep the reactor isothermal at 27 °C. The reactor is initially chargedwith equal concentrations of A and B and no C, CAO = CB0 = 2.0 mol/L. How long does it taketo reach 95% conversion? Rate constant 0.01725 L/mol.min=

:A + B -> CThe rate law for this reaction is given as:r = k * CA * CBwhere:r is the reaction rate…

Answered: Q1// The elementary liquid-phase…

Introduction to Chemical Engineering Thermodynamics

8th Edition

ISBN:9781259696527

Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart

Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart

Chapter1: Introduction

Section: Chapter Questions

Problem 1.1P

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A reaction with an activation energy of 94.8 kJ/mol is carried out at 281. K and 376. K. The reaction rate at 376. K is a) should be the same as at the other temperature b) approximately 1.338 times faster than at 281. K c) approximately 2.821e+4 times faster than at 281. K d) approximately 6.496e+4 times faster than at 281. K
In the experiment, a gas-phase, elementary reaction A → B + 2C is carried out in an isothermal flow reactor without pressure change. In the operation, pure A enters the reactor at 1010.2 kPa and 400 K with a molar flow rate of 2.5 mol/min. From literature, it was found that the specific reaction rate at 323 K is 0.0001 min-1 and the activation energy is 85 kJ/mol. Calculate yA0, δ, ε and then the volume to achieve 80% conversion in 1. a plug-flow reactor and 2. a continuous-stirred tank reactor. Gas constant: R = 8.314 J/(K∙mol) = 8.314 kPa • dm3/mol/k. Equation for integration use: (see photo)
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4.53 We wish to produce B in the reaction A → B in a continuous reactor at = 5 liter/min with CAo = 4 moles/liter. However, we find that there is a second reaction B → C that can also occur. We find that both reactions are first order and irreversible with k₁ = 1.0 min-¹ and k₂= 0.1 min-¹. Find T, V, CB.SB, and YB for 95% conversion of A in a PFTR and in a CSTR.
Chemical A reacts to form R (k1 = 6 hr-1) and R reacts away to form S (k2 = 3 hr-1). In addition R slowly decomposes to form T (k3 = 1 hr-1). If a solution containing 1.0 mol/L of A is introduced into a batch reactor, how long would it take to reach CR,max, and what would be CR,max?
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avoid typing the answers and kindly answer the question

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