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PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Conservation Principles.

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Presentation on theme: "PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Conservation Principles."— Presentation transcript:

1 PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Conservation Principles

2 PROCESS MODELLING AND MODEL ANALYSIS 2 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Overview of Chapter   Thermodynamic system principles   Balance volumes in process systems   Extensive and intensive variables   Principle of conservation   Conservation equations   Induced algebraic equations

3 PROCESS MODELLING AND MODEL ANALYSIS 3 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Thermodynamic system principles Spaces and their characteristics open systems closed systems isolated systems Mass Energy

4 PROCESS MODELLING AND MODEL ANALYSIS 4 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Scalar field P(x,y,z,t) examples? Vector field v(x,y,z,t) examples? Scalar and Vector Fields

5 PROCESS MODELLING AND MODEL ANALYSIS 5 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Scalar field P(x,y,z)  P = grad P = (  P/  x,  P/  y,  P/  z) (vector field)  2 P = div grad P =  2 P/  x 2 +  2 P/  y 2 +  2 P/  z 2 (scalar field) Vector field v(x,y,z)  v = div v =  v x /  x +  v y /  y +  v z /  z (scalar field) Operations on Scalar and Vector Fields

6 PROCESS MODELLING AND MODEL ANALYSIS 6 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Balance or “Control” Volumes V F  F n  J General principle Particular application ? Copper converter Gas compressor

7 PROCESS MODELLING AND MODEL ANALYSIS 7 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Balance Volumes  Defined by physical equipment  Defined by distinct phases  Dictated by the modelling goal  Need for a co-ordinate system  rectangular  cylindrical  spherical

8 PROCESS MODELLING AND MODEL ANALYSIS 8 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Principal Co-ordinate Systems

9 PROCESS MODELLING AND MODEL ANALYSIS 9 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Relation Between Balance Volumes  Mass balance volume set: primary set  Energy balance volume set can span or encapsulate mass balance sets  Balance volume manipulations  coalescence  division

10 PROCESS MODELLING AND MODEL ANALYSIS 10 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Balance Volumes for a Heated CSTR

11 PROCESS MODELLING AND MODEL ANALYSIS 11 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Relationship Between Balance Volumes

12 PROCESS MODELLING AND MODEL ANALYSIS 12 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Balance Volumes for a Vaporizer

13 PROCESS MODELLING AND MODEL ANALYSIS 13 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Balance Volumes for Copper Converter

14 PROCESS MODELLING AND MODEL ANALYSIS 14 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Extensive and Intensive Properties  Extensive Properties  depend on the extent of the system  Intensive Properties  do not depend on extent

15 PROCESS MODELLING AND MODEL ANALYSIS 15 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Extensive Properties Canonical set – overall mass – component masses (n-1 independent) – energy or enthalpy E = M f(I j, I i ) Extensive properties are conserved

16 PROCESS MODELLING AND MODEL ANALYSIS 16 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Intensive Properties Intensive – P, T, compositions – mass specific properties – key variables for constitutive relations Potentials – driving forces for diffusive flow of their extensive counterpart

17 PROCESS MODELLING AND MODEL ANALYSIS 17 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Principal Variables for Process Models Canonical set: intensive properties and total mass for every balance volume  pressure (P)  temperature (T)  compositions (x 1, x 2, …, x n-1 )  total mass (M)

18 PROCESS MODELLING AND MODEL ANALYSIS 18 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Balance or “Control” Volume V F  F n  J Conservation for the general balance volume

19 PROCESS MODELLING AND MODEL ANALYSIS 19 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Principle of Conservation  Word form  Integral equation form

20 PROCESS MODELLING AND MODEL ANALYSIS 20 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Differential Form of Conservation (V to 0) J C = convective flows J D = diffusive flows Source/Sink terms – chemical reaction – rate processes – external sources

21 PROCESS MODELLING AND MODEL ANALYSIS 21 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Differential Form of Conservation (expanded) Flow terms expanded  convective flows: J C =  v  diffusive flows: J D = -D grad  (assuming D=constant and no interaction effects) (co-ordinate system independent form)

22 PROCESS MODELLING AND MODEL ANALYSIS 22 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Conservation in Rectangular Co-ordinates Expand the differential operators in rectangular co-ordinate system Co-ordinate independent form

23 PROCESS MODELLING AND MODEL ANALYSIS 23 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Conservation Equation in Rectangular Co-ordinates Parabolic type partial differential equation+ Induced algebraic equations - extensive-intensive relations - rate equations (transfer and reaction)

24 PROCESS MODELLING AND MODEL ANALYSIS 24 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Example: Spherical Catalyst Pellet  Spherical geometry assumed  Coupled equation system via reaction term  Parabolic partial differential equations

25 PROCESS MODELLING AND MODEL ANALYSIS 25 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences For Discussion (1)  Double pipe heat exchanger

26 PROCESS MODELLING AND MODEL ANALYSIS 26 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences For Discussion (2) Closed tank system

27 PROCESS MODELLING AND MODEL ANALYSIS 27 © CAPE Centre, The University of Queensland Hungarian Academy of Sciences For Discussion (3)


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