Q5) Calculate the individual reactor volume for two reactors plug flow reactor(PFR)reactor connected in series. The intermediate conversion is 50% and the final conversion is 70% and themolar flow rate is (0.75 mol/s). The reaction rate constant is( 0.5 S-1) and the initial concentration is (4mol/m³).

Part 2:Explanation:Step 1: Calculate the conversion in the first reactor using the formula for plug…

Answered: Q5) Calculate the individual reactor…

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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6. Using the data in the table below, calculate the reactor volumes V₁ and V₂ for the plug-flow sequence shown in the following Figure when the intermediate conversion is 40% and the final conversion is 80%. The entering molar flow rate is 0.4 mol/sec. FAD (m³) (-₁) 0 0.89 F0.4 mol/sec 0.1 1.08 V₁ = ? 0.2 1.33 0.4 2.05 X₁=0.4 0.6 3.54 V₂ = ? 0.7 5.06 X₂=0.8 0.8 8
I need help with questions e and f
A- 1-Classify the Chemical Reaction and its definitions 2-What are the Types of Reactors, and its definitions, advantages, and disadvantages? B- The isomerization of butane C,H10 -C,H1o was carried out in the liquid phase. The data for this reversible reaction are given in Table below. 0.0 0.2 0.4 0.6 0.65 A (kmol/m".h) This reaction has been done in three different reactors as shown below: 39 53 59 38 25 X= 0.1 X 0.5 X 0.6 Calculate the volume of cach of the reactors for an entering molar flow rate of n-butane of 52 kmol/hr.
question in the photo
Two unequal size MFRS are arranged in series so that the volume of the second one is 1.5 times the first. Initially, 10 moles/m³ enters the first reactor and 4 moles/m³ comes out after reaching the steady-state condition. The order of reaction is 1.5. Find the final outlet concentration from the second reactor.
Q1// The elementary liquid-phase reaction A+B C, r=k CA CB is carried out in a batch reactor with a cooling coil to keep the reactor isothermal at 27 °C. The reactor is initially charged with equal concentrations of A and B and no C, CAO = CB0 = 2.0 mol/L. How long does it take to reach 95% conversion? Rate constant 0.01725 L/mol.min =
A B Make a plot of equilibrium conversion as a function of temperature. i. ii. iii. Combine the rate law and stoichiometric table to write -гд as a function of k, CA, X and Xe. Determine the adiabatic equilibrium temperature and conversion when pure A is fed to the reactor at a temperature of 300 K. What is the CSTR volume to achieve 85% of the adiabatic equilibrium conversion for v₂ = dm³ ? 5 min Additional information: H°(298K)=-40 000 cal/mol H°(298K) = −60 000 cal/mol cal CpA = 50- mol. K CPB 50- cal mol. K 1 Kc 100 000 at 298 K, k = 10-3 exp - min with E = 10 000 cal/mol 298
PLEASE SOLVE WITH NUMERICAL INTEGRAL METHOD.
Plz solve!!
A + B > P +S is a liquid phase reaction that is used to produce the desired product P in a plant. The data of the reaction is tabulated below. The product P is produced by using a plug flow reactor (PFR) in the plant. The product concentration in the exit stream is 0.10 mol/L. According to the new target of the management the product concentration in the exit stream is required to be increased to 0.15 mol/L. According to this new target, the first design engineer (DE-1) suggested using BMR following the existing PFR. Second design engineer (DE- 2) suggested to use BMR before the PFR. Supposing that you are the third design engineer (DE-3) what would you suggest in order to increase the product concentration to the desired value. Data: FA0 = Fe0 = 32 mol/min Qo = 167 L/min Note: Show the calculations of all alternative design approaches clearly. CA ; (mol/L) 0.2 0.16 0.12 0.10 0.08 0.06 0.04 -ra x 103; (mol/L min) 7.0 4.5 2.5 1.83 1.16 0.67 0.32
note: do not use excel please. show all the necessary steps/solutions. thank youuu..... type the answer please.

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