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B-A thickener is designed to separate suspension containing 15 Kg of water/Kg of solid is to be thickened to a sludge containing 4.5 Kg of water/Kg of solid in a continuous operation. Calculate the minimum area of a thickener required to effect the separation of mass rate of feed of 103 Kg/s of solid? p H₂O = 1000 kg/m³ ps = 6000 kg/m³ De=0.002 m pu² 0.22

B-A thickener is designed to separate suspension containing 15 Kg of water/Kg of solid is to be thickened to a sludge containing 4.5 Kg of water/Kg of solid in a continuous operation. Calculate the minimum area of a thickener required to effect the separation of mass rate of feed of 103 Kg/s of solid? p H₂O = 1000 kg/m³ ps = 6000 kg/m³ De=0.002 m pu² 0.22

Structural Analysis
Structural Analysis
6th Edition
ISBN:9781337630931
Author:KASSIMALI, Aslam.
Publisher:KASSIMALI, Aslam.
Chapter2: Loads On Structures
Section: Chapter Questions
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B- A thickener is designed to separate suspension containing 15 Kg of water/Kg of solid is to be thickened to a sludge containing 4.5 Kg of water/Kg of solid in a continuous operation. Calculate the minimum area of a thickener required to effect the separation of mass rate of feed of 103 Kg/s of solid? p H₂0 = 1000 kg/m³ ps = 6000 kg/m³ De=0.002 m R' pu 10% 10³ 10² 10 100% 101 10 2 10:3 Region a 10 2 10 1 TELEGRAM MOTION OF PARTICLES IN A FLUID 10° Region b 10 R puz Region c = 0.22 10² Re' R/pu² versus Re' for spherical particles 10³ 10⁰ 105 Region d 10 10
Transcribed Image Text:B- A thickener is designed to separate suspension containing 15 Kg of water/Kg of solid is to be thickened to a sludge containing 4.5 Kg of water/Kg of solid in a continuous operation. Calculate the minimum area of a thickener required to effect the separation of mass rate of feed of 103 Kg/s of solid? p H₂0 = 1000 kg/m³ ps = 6000 kg/m³ De=0.002 m R' pu 10% 10³ 10² 10 100% 101 10 2 10:3 Region a 10 2 10 1 TELEGRAM MOTION OF PARTICLES IN A FLUID 10° Region b 10 R puz Region c = 0.22 10² Re' R/pu² versus Re' for spherical particles 10³ 10⁰ 105 Region d 10 10
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