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
Chapter2: Loads On Structures
Section: Chapter Questions
Problem 1P
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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](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2Fd23b70c8-e78e-4b7d-97a3-dcd2d001b881%2F6b814441-b4d5-4646-a34c-20c8cc6b5d11%2Fx0f4qt3_processed.jpeg&w=3840&q=75)
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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