Equations sheet

6s

s w pD

A

σ 02=p (1−p) σ R

2=p(1−p )

n

G= π4ρ sdeff

2. 5 g0 . 5( 1−cos β2sin3 β )

0. 5

S2=∑i=1

N

( yi−μ )2

N

S2=∑i=1

N

( yi− y )2

N−1

IP=σσ R

Flow of particles through a fluid

Fluidization

MF PMF

P (1 )( )gL

0.55MFRe 33.7 1 3.59 10 Ar 1

0.934 0.934 1.8P p

oMF 0.87 0.066

g ( ) DV

1110

0.80.4 0.5b o oMF0.2

0.54D V V z 4Ng

Filtration

m p1 ns tu u

13

pp 2

gK D

s4

1 0.5 1

2p p

tg D

u18

CD

Re=4

3( ρp−ρ )μ

u t3 ρ2

mc

AT=( 2cΔp1− sgc fn

α0 μ )1/2

Centrifugal Separation:

x=ρs ( ρplp−1000 )ρplp( ρ s−1000 )