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September 29, 1999 Department of Chemical Engineering University of South Florida Tampa, USA Population Balance Techniques in Chemical Engineering by Richard.

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Presentation on theme: "September 29, 1999 Department of Chemical Engineering University of South Florida Tampa, USA Population Balance Techniques in Chemical Engineering by Richard."— Presentation transcript:

1 September 29, 1999 Department of Chemical Engineering University of South Florida Tampa, USA Population Balance Techniques in Chemical Engineering by Richard Gilbert & Nihat M. Gürmen

2 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 Part I -- Overview

3 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 What is the Population Balance Technique (PBT)? PBT is a mathematical framework for an accounting procedure for particles of certain types you are interested in. The technique is very useful where identity of individual particles is modified or destroyed by coalescence or breakage.

4 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 (Dis)advantage of PBT Advantage Analysis of complex dispersed phase system Disadvantage Difficult integro-partial differential equations

5 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 Application Areas colloidal systems crystallization fluidization microbial growths demographic analysis

6 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 Origins of population balances: Demographic Analysis Time = t Age =  Tampa n( ,t) N i ( ,t)N o ( ,t) EmigrationImmigration Birth Rate Death Rate

7 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 A Mixed Suspension, Mixed Product Removal (MSMPR) Crystallizer Q i, C i, n i Q o, C o, n Particle Size Distribution (PSD)

8 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 Information diagram showing feedback interaction Mass Balance Growth Kinetics Nucleation Kinetics Crystal Area Population Balance Growth Rate Nucleation Rate PSD Feed Growth Rate Supersaturation (from Theory of Particulate Processes, Randolp and Larson, p. 3, 1988)

9 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 Part II -- Mathematical Background

10 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 Two common density distributions by particle number Size, L Population Density, n(L) Normal Distribution Population Density, n(L) Size, L Exponential Distribution

11 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 Exponential density distribution by particle number Size, L Cumulative Population, N(L) Size, L Population Density, n(L) N1N1 N1N1 N 1 is the number of particles less than size L 1 n 1 is the number of particles per size L 1 L1L1 L1L1 n1n1

12 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 Normal density distribution by particle number Size, L Cumulative Population, N(L) N total = Total number of particles L max Size, L Population Density, n(L) N total L max

13 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 Normalization of a distribution normalized One way to normalize n(L) Size, L Normalized Population Density, f(L) L max 1 0 Area under the curve

14 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 Average properties of a distribution The two important parameters of a particle size distribution are * How large are the particles? mean size, * How much variation do they have with respect to the mean size? coefficient of variation, c.v. where  2 (variance) is

15 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 Moments of a distribution j-th moment, m j, of a distribution f(L) about L 1 Mean,= the first moment about zero Variance,  2 = the second moment about the mean

16 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 Further average properties: Skewness and Kurtosis j-th moment,  j, of a distribution f(L) about mean Skewness,  1 = measure of the symmetry about the mean (zero for symmetric distributions) Kurtosis,  2 = measure of the shape of tails of a distribution

17 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 Part III -- Formulation of Population Balance Technique

18 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 Basic Assumptions of PBT (Population Balance Technique) Particles are numerous enough to approximate a continuum Each particle has identical trajectory in particle phase space S spanned by the chosen independent variables Systems can be micro- or macrodistributed Check these Assumptions

19 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 Basic Definitions Number density function n(S,t) is defined in an (m+3)-dimensional space S consisted of 3 external (spatial) coordinates m internal coordinates (size, age, etc.) Total number of particles is given by Space S

20 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 The particle number continuity equation R1R1 S a subregion R 1 from the Lagrangian viewpoint

21 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 where is the set of internal and external coordinates spanning the phase space R 1 Convenient variable and operator definitions

22 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 Applying the product rule of differentiation to the LHS

23 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 Substituting all the terms derived earlier As the region R 1 is arbitrary

24 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 In terms of m+3 coordinates Averaging the equation in the external coordinates Micro-distributed Population Balance Equation Macro-distributed Population Balance Equation

25 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 B - D terms represent the rate of coalescence conventionally collision integrals are used for B and D the rate at which a bubble of volume u coalesces with a bubble of volume v-u to make a new bubble of volume v is a death function consistent with the above birth function would be

26 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 C(x,y) : the rate at which bubbles of volumes x and y collide and coalesce. in the modeling of aerosols two of the functions used for C(x,y) are where K a is the coalescence rate constant 1) Brownian motion 2) Shear flow Coagulation kernel, C(x,y)

27 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 Simplifications for a Solvable System dynamic system => t spatially distributed => x, y, z single internal variable, size => L Growth rate G is at most linearly dependent with particle size =>

28 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 Moment Transformation Defining the j th moment of the number density function as Averaging PB in in the L dimension

29 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 j = 0,1,2,...  Microdistributed form of moment transformation Macrodistributed form of moment transformation j = 0,1,2,... 

30 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 If Assumptions Do Not Allow Moment Transformations You have to use other methods of solving PDEs like method of lines finite element methods difficult if both of your variables go to infinity

31 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 Part IV -- Examples

32 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 Example 1 : Demographic Analysis Tampa n( ,t) N i ( ,t)N o ( ,t) neglect spatial variations of population one internal coordinate, age  EmigrationImmigration Set up the general population balance equation?

33 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 Example 2: Steady-state MSMPR Crystallizer Q i, C i, n i Q o, C o, n The system is at steady-state Volume of the tank : V Outflow equals the inflow Feed stream is free of particles Growth rate of particles is independent of size There are no particles formed by agglomeration or coalescnce Derive the model equations for the system.

34 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 References BOOK Randolph A. D. and M. A. Larson, Theory of Particulate Processes, 2 nd edition, 1988, Academic Press PAPERS Hounslow M. J., R. L. Ryall, and V. R. Marhsall, A discretized population balance for nucleation, growth, and aggregation, AIChE Journal, 34:11, p. 1821-1832, 1988 Hulburt H. M. and T. Akiyama, Liouville equations for agglomeration and dispersion processes, I&EC Fundamentals, 8:2, p. 319-324, 1969 Ramkrishna D., The prospects of population balances, Chemical Engineering Education, p. 14-17,43, 1978

35 R. Gilbert & N. Gürmen, v.1.0, Tampa 1999 THE END


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