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Constitutive Relations

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Constitutive relations are essential in chemical engineering, linking conserved extensive quantities to intensive variables. They define the behavior of physico-chemical properties such as enthalpies, densities, and viscosities, and play a crucial role in transfer rates of mass and energy. These relations stem from conservation equations for mass, energy, and momentum, and involve both convective and molecular flow terms. By establishing transaction relations, reaction rates, and thermodynamic relations, constitutive relations help model complex systems, such as Continuous Stirred-Tank Reactors (CSTR), while considering factors like control systems, sensors, and valves.

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Constitutive Relations

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  1. Constitutive Relations

  2. What are constitutive relations? • Relate conserved extensive quantities to intensive variables • Help define physico-chemical quantities (e.g. enthalpies, densities, viscosities ,…) • Define transfer rates (mass, energy, …) • Other relations to “constitute” the model

  3. How do constitutive relations arise ? • Related to the terms in the conservation equations for mass, energy and momentum • Convective flow terms (process streams) • Molecular flow streams (fluxes) • Internal processes • Defining intensive variables in terms of extensive quantities and other physico-chemical properties • Constraints on the system (control relations)

  4. Balance volumes, flows and system processes

  5. CSTR Example A  B Constant V

  6. Transfer relations Reaction rates Constitutive Property definitions Equations Balance volume relations Equipment and control constraints Classes of Relations

  7. 1. Transfer Relations • General form • Particular forms • mass transfer • heat transfer

  8. CSTR Example - Qloss Qloss = UA(T-Tamb) A  B Qloss

  9. 2. Reaction rates • Reaction rate (batch reactor only) • General reaction expression

  10. CSTR Example A  B

  11. 3. Thermodynamic relations • Property relations (density, viscosity, …) • Equilibrium relations • Raoult’s law • Relative volatility, K-value • Activity coefficient

  12. CSTR Example A  B

  13. Thermodynamic properties • Enthalpy • linear • nonlinear

  14. CSTR Example A  B

  15. Thermodynamic properties • Equations of state • ideal gas • cubic EoS • Soave Redlich Kwong • Peng Robinson • NRTL

  16. 4. Balance volume relations • Relations between phases VG VL

  17. 5. Control systems

  18. 5a. Sensors • Sensors

  19. 5b. Transmitters • Transmitters (4-20mA, 20-100kPa)

  20. 5c. Controllers • Traditional (P, PI, PID)

  21. 5d. Actuators

  22. 5e. Valves • Static valves • Control valves • characteristics

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