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THESE_EL HAMMAMI.pdf - Toubkal

THESE_EL HAMMAMI.pdf - Toubkal

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5.2 Cas du mélange binaire 90W * sr1,00,80,60,40,2T=30KT=10KT=15KT=30K Re 0=1000W 0=0,8 Hr=100%R134aH 2O0,01,0 1,2 1,4 1,6 1,8 2,0FIG. 5.5 – Variation de la fraction massique adimensionnelle à la sortie du tubem H O 2( 10 -4 )I302520151050Re 0=2000Re 0=1500Re 0=1000R134aH 2OT=30KHr=100%W 0=0,8T=30K15,012,510,07,55,02,510 100 200z *m R134a ( 10 -4 )IFIG. 5.6 – Variation de la densité massique condensé pour la vapeur d’eau et R134a

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