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ege/Basra 04: A continuous rotary filter is required for an industrial process for the filtration of a suspension to produce 0.002 m³/s of filtrate. A sample was tested on a small laboratory filter of area 0.023 m² to which it was fed by means of a slurry pump to give filtrate at a constant rate of 0.0125 m³/s. The pressure difference across the test filter increased from 14 kN/m² after 300 s filtration to 28 kN/m² after 900 s, at which time the cake thickness had reached 38 mm. What are suitable dimensions and operating conditions for the rotary filter, assuming that the resistance of the cloth used is one-half that on the test filter, and that the vacuum system is capable of maintaining a constant pressure difference of 70 kN/m² across the filter? phy

ege/Basra 04: A continuous rotary filter is required for an industrial process for the filtration of a suspension to produce 0.002 m³/s of filtrate. A sample was tested on a small laboratory filter of area 0.023 m² to which it was fed by means of a slurry pump to give filtrate at a constant rate of 0.0125 m³/s. The pressure difference across the test filter increased from 14 kN/m² after 300 s filtration to 28 kN/m² after 900 s, at which time the cake thickness had reached 38 mm. What are suitable dimensions and operating conditions for the rotary filter, assuming that the resistance of the cloth used is one-half that on the test filter, and that the vacuum system is capable of maintaining a constant pressure difference of 70 kN/m² across the filter? phy

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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ege/Basra 04: A continuous rotary filter is required for an industrial process for the filtration of a suspension to produce 0.002 m³/s of filtrate. A sample was tested on a small laboratory filter of area 0.023 m² to which it was fed by means of a slurry pump to give filtrate at a constant rate of 0.0125 m³/s. The pressure difference across the test filter increased from 14 kN/m² after 300 s filtration to 28 kN/m² after 900 s, at which time the cake thickness had reached 38 mm. What are suitable dimensions and operating conditions for the rotary filter, assuming that the resistance of the cloth used is one-half that on the test filter, and that the vacuum system is capable of maintaining a constant pressure difference of 70 kN/m² across the filter? phy
Transcribed Image Text:ege/Basra 04: A continuous rotary filter is required for an industrial process for the filtration of a suspension to produce 0.002 m³/s of filtrate. A sample was tested on a small laboratory filter of area 0.023 m² to which it was fed by means of a slurry pump to give filtrate at a constant rate of 0.0125 m³/s. The pressure difference across the test filter increased from 14 kN/m² after 300 s filtration to 28 kN/m² after 900 s, at which time the cake thickness had reached 38 mm. What are suitable dimensions and operating conditions for the rotary filter, assuming that the resistance of the cloth used is one-half that on the test filter, and that the vacuum system is capable of maintaining a constant pressure difference of 70 kN/m² across the filter? phy
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