2006
DOI: 10.1080/13873950500068823
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Bond graph modelling for chemical reactors

Abstract: In this paper we present a bond graph model of a continuous stirred tank reactor which represents the reaction kinetics as well as the heat and mass transport phenomena in the reactor. The consequences of reticulation of the phenomena and of the systematic use of the power conjugated variables on the formulation of the thermodynamic properties, the reaction kinetics and the energy and mass transport are shown. A classical example of chemical reaction is chosen to illustrate this approach: the equilibrated reac… Show more

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Cited by 80 publications
(52 citation statements)
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“…c i , where T 0 and c i are constants [14]. The state space of the heat exchanger is then defined as the following submanifold L U of the Thermodynamic Phase Space where Gibbs' equation is satisfied…”
Section: The Example Of the Heat Exchangermentioning
confidence: 99%
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“…c i , where T 0 and c i are constants [14]. The state space of the heat exchanger is then defined as the following submanifold L U of the Thermodynamic Phase Space where Gibbs' equation is satisfied…”
Section: The Example Of the Heat Exchangermentioning
confidence: 99%
“…Let us now express the matching equation (13) with θ d defined by (14) in terms of a matching equation in the function F and the feedback α. The Lie derivatives in (13) may be developed as…”
Section: Proposition 41 the 1-form (14) Is A Contact Formmentioning
confidence: 99%
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“…where the state variable x = (x 1 , x 2 ) ⊤ ∈ R 2 is the vector of the entropies x 1 and x 2 of subsystem 1 and 2, U (x 1 , x 2 ) = U 1 (x 1 ) + U 2 (x 2 ) is the internal energy of the overall system composed of the addition of the internal energies of each subsystem, the gradient of the total internal energy ∂U ∂xi = T i (x i ) being the temperatures of each compartment with T (x i ) = T 0 exp xi ci , where T 0 and c i are constants (Couenne et al, 2006), λ, λ e > 0 denote Fourier's heat conduction coefficients of the internal and external walls respectively and the controlled input u(t) is the temperature of the external heat source. The Thermodynamic Phase Space is R 5 ∋ (x 0 , x 1 , x 2 , p 1 , p 2 ) ⊤ and its elements correspond respectively to the total internal energy, the entropies and the temperatures.…”
Section: Example: the Heat Exchangermentioning
confidence: 99%
“…where is the number of vertices of the graph, and ℓ is equal to the number of components 3 of the complex graph 4 , the linkage classes in the terminology of [11], [7], [8].…”
Section: The Linkage Classes Of the Complex Graphmentioning
confidence: 99%