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9781856174190

Solid/ Liquid Separation

by ;
  • ISBN13:

    9781856174190

  • ISBN10:

    1856174190

  • Format: Hardcover
  • Copyright: 2005-11-04
  • Publisher: Elsevier Science
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Summary

The separation of solids from liquids in an industrial setting is a complex process involving specialised equipment and expertise: some would say that there is still an element of 'black art' about it. A clear understanding of the principles involved is essential if perfection in separation is to be achieved. This volume, written by two acknowledged experts in the field, provides that understanding. It takes a sequential and logical route through the major factors affecting industrial separation: the properties of liquids and particles; the fluid dynamic background to the filtration process; the use of gravity in the processes plus the formation, deliquoring and washing of filter cake. The whole is fully illustrated and supported by references to the literature.

Table of Contents

Preface ix
Introduction
1(18)
The separation process
1(12)
Solid/liquid separation in the process flowsheet
4(2)
Filter media
6(4)
Cake and depth filtration
10(1)
``Laws'' of filtration
10(3)
Particle and liquid properties in filtration
13(5)
Particle shape
13(1)
Particle size
14(1)
The solution environment
15(3)
The nature of the fluid
18(1)
Conclusions -- Perfection in separation!
18(1)
Fluid dynamic background to filtration processes
19(53)
Motion of particles in a fluid
19(7)
Gravity settling at low concentrations
22(2)
Settling in a centrifugal field
24(1)
Suspensions with high concentrations of solid - hindered settling
25(1)
Darcy's Law
26(2)
Darcy's Law in filtration
28(1)
Permeability and specific resistance
28(10)
The Kozeny-Carman equation
29(4)
Permeabilities calculated from cell models
33(1)
Properties of porous media
34(2)
The friction factor for particulate beds
36(2)
Depth filtration (clarification)
38(6)
Capture mechanisms
38(4)
Modelling the capture process
42(1)
Deposition and scour
43(1)
Flow through fibrous and woven media
44(7)
Flow through nonwoven, random fibre media
44(1)
Monofilament woven media
45(5)
Multifilament woven media
50(1)
Cake deliquoring -- multiphase flow in porous media
51(9)
Capillary pressure and threshold pressure
52(1)
Relative permeability and capillary pressure
53(4)
Application to cake deliquoring
57(1)
Other deliquoring models
58(2)
Cake washing -- Hydrodynamic dispersion
60(8)
The equations of hydrodynamic dispersion
62(3)
Washing deliquored filter cakes
65(2)
Other models for cake washing
67(1)
Expression -- deliquoring by compression
68(3)
Conclusions
71(1)
Gravity clarification and thickening
72(24)
Basics of gravity settling
72(4)
Batch sedimentation
73(1)
Types of sedimentation
74(2)
Clarification
76(3)
Thickening
79(16)
Relating batch test data to thickeners
80(5)
Thickener area
85(3)
Thickener depth
88(4)
Zone sedimentation models
92(1)
Compression subsidence models
92(1)
Zone settling vs. compression subsidence models
93(2)
Conclusions
95(1)
Filtration: cake formation
96(66)
Relationships between process variables
100(4)
Compressible cake filtration
104(14)
Pressure conditions in a compressible filter cake
105(2)
Working relationships for compressible filtration
107(1)
Effects of pressure on filter cake properties
108(1)
Other factors affecting filter cake properties
109(7)
Expressions for the solids mass deposited
116(1)
Expressions for suspension concentration
116(1)
Relationships between cake thickness and filtrate volume
117(1)
Basis for filtration calculations
118(11)
Constant pressure operation
119(7)
Constant rate operation
126(2)
Variable pressure-variable rate operation
128(1)
Filtration tests to determine cake formation data
129(4)
Filtration onto cylindrical elements
133(4)
Constant pressure filtration
134(1)
Constant rate filtration
135(2)
Filtration in centrifuges
137(6)
Centrifugation rate and filtrate flow rate
138(4)
Cake thickness dynamics
142(1)
Filtration from suspensions of Non-Newtonian liquids
143(1)
Process calculations
144(12)
Optimisation of cycle times
152(4)
Advanced models of cake filtration
156(5)
Constitutive properties
158(2)
Models incorporating interparticle interactions
160(1)
Conclusions
161(1)
Cake deliquoring
162(34)
Threshold pressure and irreducible saturation
163(5)
Irreducible saturation of vacuum or pressure deliquored cakes
166(1)
Irreducible saturation of centrifuge cakes
166(2)
Design charts for deliquoring
168(9)
Vacuum and pressure deliquoring
171(1)
Centrifugal deliquoring
172(1)
Gravitational drainage
173(1)
Experimental validation of the design charts
173(4)
Example calculations for deliquoring
177(15)
Summary of deliquoring calculations for vacuum and pressure filters
179(8)
Effects of particle size, cake thickness and pressure difference
187(1)
Summary of deliquoring calculations for centrifugal filters
187(5)
Cake cracking
192(3)
Stresses in partially saturated filter cakes
192(3)
Conclusions
195(1)
Cake washing
196(51)
The wash liquid and washing curves
198(7)
Measurement of washing curves
199(3)
Representation of washing data
202(1)
``Washing efficiency''
203(2)
Cake washing models for design
205(7)
Continuous washing processes
212(10)
Correction factors for full scale filters
215(5)
Washing deliquored filter cakes
220(1)
Cake washability
221(1)
Reslurry washing
222(6)
Multiple reslurry systems
223(3)
Countercurrent multiple reslurry systems
226(2)
Multiple washing filter installations
228(17)
Rotary vacuum filter flow sheets
229(7)
Countercurrent washing on belt filters
236(9)
Conclusions
245(2)
Expression (compression deliquoring)
247(19)
Experimental evaluation of expression
249(3)
General treatment of experimental expression data
250(2)
Interpretation of expression data
252(9)
Analysis of the first stage -- cake formation
252(2)
Analysis of the second stage -- cake consolidation
254(7)
Expression on curved (2-dimensional) filter media
261(1)
Factors affecting expression characteristics
261(4)
Expression rate increase by inserted strings
263(1)
``Torsional'' expression
264(1)
Conclusions
265(1)
Membrane filtration
266(30)
Membrane filtration processes
268(12)
Crossflow filtration vs. normal (cake) filtration
270(1)
How much permeate could be produced?
270(1)
Membrane fouling and concentration polarisation
271(3)
Fouling by proteins and other biological materials
274(2)
Fouling by inorganic particulates - effects on MF performance
276(4)
Ultrafiltration
280(7)
Rejection
280(1)
Mass transfer analysis
280(2)
Determining the mass transfer coefficient
282(1)
The diffusion coefficient
283(3)
Limiting flux
286(1)
Limiting concentration
287(1)
Microfiltration
287(4)
Filtration rate equations
287(1)
Deadend filtration
288(2)
Crossflow filtration
290(1)
Critical flux operation
291(3)
Deposit characteristics
292(2)
Conclusions
294(2)
List of notation 296(11)
Bibliography and additional bibliography 307(21)
Index 328

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