Abstract
This chapter deals with dilute suspensions, that is, where the behaviour of the suspension as a fluid is not affected by the presence of the particles. For example, the suspension is assumed to have the same Newtonian characteristics as the liquid in which the particles are suspended.
Access this chapter
Tax calculation will be finalised at checkout
Purchases are for personal use only
Preview
Unable to display preview. Download preview PDF.
Abbreviations
- a:
-
centrifugal acceleration
m s-2
- A:
-
area normal to flow direction
m2
- AP :
-
area of paddle blade normal to motion
m2
- Cd :
-
drag coefficient of a paddle blade
−
- d:
-
diameter of Poiseuille flow tube
m
- d1 :
-
diameter of a primary particle
m
- df :
-
diameter of a filter grain
m
- di :
-
diameter of an i-fold particle
m
- F:
-
voltage gradient
V m-1
- g:
-
gravitational acceleration 9.81
m s-2
- G:
-
velocity gradient
s-1
- H:
-
head loss, liquid gauge
m
- i:
-
number of primary particles in an aggregate
−
- k:
-
friction coefficient for turbulent flow
m-1
- L:
-
distance in direction of flow
m
- m:
-
index in Richardson-Zaki equation
−
- p:
-
pressure drop
N m-2
- P:
-
power dissipated in fluid motion
W
- Q:
-
volumetric flow rate
m3 s-1
- R1 :
-
radius of inner cylinder (Couette apparatus)
m
- R2 :
-
radius of outer cylinder (Couette apparatus)
m
- t:
-
time
s
- Tq :
-
torque on paddle shaft
N m
- u:
-
electrophoretic mobility (v /F)
m2 s-1 V-1
- v:
-
velocity of liquid suspension
m s-1
- ve :
-
velocity of particle in electrophoresis cell
m s-1
- vp :
-
velocity (mean) of paddle blade
m s-1
- vt :
-
terminal settling velocity of a particle
m s-1
- V:
-
volume of suspension
m3
- ∈:
-
porosity of filter media
−
- ∈:
-
static permittivity of water 80 x 8.85 x 10-12
C2 N-1 m-2
- ζ:
-
electrokinetic potential of particles
V
- μ:
-
dynamic viscosity
kg m-1 s-1
- ν:
-
kinematic viscosity
m2 s-1
- p:
-
density of liquid
kg m-3
- ps :
-
density of particle
kg m-3
- φ:
-
volume of particles per unit liquid volume
−
- ψδ :
-
potential at the inner boundary of the diffuse ion layer round a particle
V
- ω:
-
angular velocity
rad s-1
- ω2 :
-
angular velocity of outer cylinder rad (Couette apparatus)
s-1
References
Gregory, J., and Sheiham, I., Kinetic aspects of flocculation by cationic polymers, Br. Polym. J., 6, 47, 1974.
Bhole, A.G., Hydrodynamics of Flocculation in Water Treatment, Ph.D. Thesis, University of London, 1970.
Van Duuren, F.A., Defined velocity gradient model flocculator, J. San. Eng. Div., Proc. Am. Soc. Civ. Engrs., 94, SA4, 671, 1968.
Ives, K.J., and Bhole, A.G., Study of flowthrough Couette flocculators-I. Design for uniform and tapered flocculation, Wat. Res., 9, 1085, 1975.
Hubley, C.E., Robertson, A., and Mason, S.G., Flocculation in suspensions of large particles, Can. J. Res., 28B, 770, 1950.
Swift, D.L., and Friedlander, S.K., The coagulation of hydrosols by Brownian motion and laminar shear flow, J. Coll. Sci., 19, 621, 1964.
Ives, K.J., Theory of operation of sludge blanket clarifiers, Proc. Inst. Civ. Engrs., 39, 245, 1968.
Camp, T.R., Discussion on Agglomerate size changes in coagulation, J. San. Eng. Div., Proc. Am, Soc. Civ. Engrs., 95, (SA6), 1210, 1969.
Smith, A.L., Electrokinetic phenomena-associated with the solid-liquid interface, in Dispersion of Powders in Liquids, Parfitt, G.D., Ed., Elsevier, Amsterdam, 1973.
Author information
Authors and Affiliations
Editor information
Editors and Affiliations
Rights and permissions
Copyright information
© 1978 Sijthoff & Noordhoff International Publishers B.V.
About this chapter
Cite this chapter
Ives, K.J. (1978). Experimental Methods (2). In: Ives, K.J. (eds) The Scientific Basis of Flocculation. NATO Advanced Study Institutes Series, vol 27. Springer, Dordrecht. https://doi.org/10.1007/978-94-009-9938-1_8
Download citation
DOI: https://doi.org/10.1007/978-94-009-9938-1_8
Publisher Name: Springer, Dordrecht
Print ISBN: 978-94-009-9940-4
Online ISBN: 978-94-009-9938-1
eBook Packages: Springer Book Archive