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PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Modelling Lumped Parameter Systems C5A.

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Presentation on theme: "PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Modelling Lumped Parameter Systems C5A."— Presentation transcript:

1 PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Modelling Lumped Parameter Systems C5A

2 PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences General 3D conservation space Governing equation

3 PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences General 3D conservation space Governing equation General differential form where  can vary in space and time Governing equation Lumped form where  does not vary in space but varies in time

4 PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences The lumped conservation balance General conservation balance Assuming homogeneity in the conserved quantity Lumped conservation balance

5 PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Model Characteristics

6 PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences The mass balance volume

7 PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences A Process Example

8 PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Overall mass balance

9 PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Component mass balances

10 PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Molar Balance Mass balances that involve reactions are most conveniently expressed as molar balances. i.e., where g i is the rate of generation or consumption of species i through reaction. i.e., ~

11 PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Tank mass balance z P 1 P 2 P 3 P 0 F 1 F 2 Balance volumes  tank holdup  valves Conservation Constitutive A1: Well mixed in x,y,z directions A2: no mass holdup in valves A3: no physical losses from system A4: no mass losses from evaporation A5: Isothermal operation z x y Assumptions

12 PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences The energy balance volume

13 PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Energy balance Components of the balance  Convective energy flows  Conductive/radiative flows  Work terms

14 PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Energy Balance Terms   Convective flows   Heat flows   Work terms   shaft work   expansion work   flow work

15 PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Total energy balance

16 PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Reduced energy balances  Neglect P E, K E  PV constant or small  Output specific enthalpies equivalent to bulk phase

17 PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Reduced energy balances (cont.)  all enthalpies evaluated at system temperature  explicit appearance of reaction terms and temperature

18 PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Tank energy balance Balance volumes tank holdup jacket holdup A5: Fixed mass holdup in jacket A6: well mixed jacket contents A7: negligible KE terms A8: negligible PE terms A9: negligible PV terms A10: jacket temperature is averaged A11: fixed heat capacities Assumptions

19 PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Tank energy balances Conservation Constitutive Tank Conservation Constitutive Jacket System

20 PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Momentum balance

21 PROCESS MODELLING AND MODEL ANALYSIS © CAPE Centre, The University of Queensland Hungarian Academy of Sciences Example momentum balance


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