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Q4. A fluidized bed is used in the production of aniline by the hydrogenation of nitrobenzene. Single-stage cyclones, followed by candle filters, are used to remove fines from the gases leaving the fluidized bed. The reactor operates at a temperature 270°C and a pressure of 2.5 bara. The reactor diameter is 10 m. Hydrogen is used in large excess in the reaction, and for the purposes of this exercise, the properties of the gas may be taken as those of hydrogen at the reactor conditions. The density of the catalyst particles is 1800 kg/m'. The estimated particle size distribution of the fines is: Particle size, um Percentage by weight less than 50 30 20 20 5 5 40 10 100 70 40 10 A 70% recovery of the solids is required in the cyclones. For a gas flow rate of 100,000m/h, at the reactor conditions, determine how many cyclones operating in parallel are needed and design a suitable cyclone? Estimate the size distribution of the particles entering the filters? 22

Q4. A fluidized bed is used in the production of aniline by the hydrogenation of nitrobenzene. Single-stage cyclones, followed by candle filters, are used to remove fines from the gases leaving the fluidized bed. The reactor operates at a temperature 270°C and a pressure of 2.5 bara. The reactor diameter is 10 m. Hydrogen is used in large excess in the reaction, and for the purposes of this exercise, the properties of the gas may be taken as those of hydrogen at the reactor conditions. The density of the catalyst particles is 1800 kg/m'. The estimated particle size distribution of the fines is: Particle size, um Percentage by weight less than 50 30 20 20 5 5 40 10 100 70 40 10 A 70% recovery of the solids is required in the cyclones. For a gas flow rate of 100,000m/h, at the reactor conditions, determine how many cyclones operating in parallel are needed and design a suitable cyclone? Estimate the size distribution of the particles entering the filters? 22

Introduction to Chemical Engineering Thermodynamics
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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Q4. A fluidized bed is used in the production of aniline by the hydrogenation of nitrobenzene. Single-stage cyclones, followed by candle filters, are used to remove fines from the gases leaving the fluidized bed. The reactor operates at a temperature 270°C and a pressure of 2.5 bara. The reactor diameter is 10 m. Hydrogen is used in large excess in the reaction, and for the purposes of this exercise, the properties of the gas may be taken as those of hydrogen at the reactor conditions. The density of the catalyst particles is 1800 kg/m. The estimated particle size distribution of the fines is: Particle size, um 50 40 30 20 10 5 Percentage by weight less than 100 70 40 20 10 5 A 70% recovery of the solids is required in the cyclones. For a gas flow rate of 100,000m/h, at the reactor conditions, determine how many cyclones operating in parallel are needed and design a suitable cyclone? Estimate the size distribution of the particles entering the filters?
Transcribed Image Text:Q4. A fluidized bed is used in the production of aniline by the hydrogenation of nitrobenzene. Single-stage cyclones, followed by candle filters, are used to remove fines from the gases leaving the fluidized bed. The reactor operates at a temperature 270°C and a pressure of 2.5 bara. The reactor diameter is 10 m. Hydrogen is used in large excess in the reaction, and for the purposes of this exercise, the properties of the gas may be taken as those of hydrogen at the reactor conditions. The density of the catalyst particles is 1800 kg/m. The estimated particle size distribution of the fines is: Particle size, um 50 40 30 20 10 5 Percentage by weight less than 100 70 40 20 10 5 A 70% recovery of the solids is required in the cyclones. For a gas flow rate of 100,000m/h, at the reactor conditions, determine how many cyclones operating in parallel are needed and design a suitable cyclone? Estimate the size distribution of the particles entering the filters?
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