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. Kfs=conductivity and . Water, T=Tas-273,15;P=101,3) Rhof=Density(Water;T=Tu-273,15;P=101,3) {Masse volumique} Rhofs=Density(Water;T=Tas-273,15

A. {passage-du-fluide-du-distribueur-au-mini-canaux} and . N_c, Pertes de charges au niveau de la bifurcation entre le distributeur et les mini-canaux côté utile" PBn=((rhof*(A[a-1

. Vs, Vitesse dans les mini-canaux côté utile" Res[a]=rhofs*Dh*Vs

*. Qu2=mdot, *. , *. Cpf, and *. Deltat, Différence de température entrée-sortie dans l'échangeur côté sourceRésistance de convection totale de l'échangeur" Tbmax=(MAX(Tbase[1Températue de base maximal côté utileTempératue de base maximal côté source, Tbsmax=, vol.1, issue.1

. Rtot_ech=, Résistance totale de l'échangeur côté utile" Rtot_echs=(tas-tbsmax)/Qs1 "Résistance totale de l'échangeur côté source Annexes

B. Journal, J. David, and L. Ramousse, Luo Optimization of thermoelectric heat pumps: Heat exchanger design and operating conditions Energy Conversion and management

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A. B. Conférences-sans, J. David, and L. Ramousse, Luo Développement d'un générateur thermodynamique chaud-froid de nouvelle génération GDR Thermoélectricité, pp.7-8, 2009.

B. David, J. Ramousse, and L. , Luo Gestion et optimisation d'une pompe à chaleur thermoélectrique