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[null,null,null,null,null,null,null,null,"2) Saisie des données d'entrée",null,null,null,null,"3) Options",null,null,"4) Création du transitoire"]
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[null,null,null,null,null,null,null,null,null,"VolL",35,"m3",null,"AN","Oui",null,"Nœud","Temps","Volume phase liquide"]
[null,null,null,null,null,null,null,null,null,"AE",155,null,null,"AO","Oui",null,"n°","s","m3"]
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[null,null,null,null,null,null,null,null,null,"U",99.7791,null,null,null,null,null,2,30,35]
[null,null,null,null,null,null,null,null,null,"V",1580.41,null,null,null,null,null,3,60,32]
[null,null,null,null,null,null,null,null,null,"T",607.45600000000002]
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[null,null,"1) Remise à zéro des données et du tableau                                                             (à effectuer à chaque ouverture du classeur !)  "]
[]
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{"sheet":"Poly_Vapeur","index":2,"n_rows":149,"n_cols":3402,"rows_kept":69,"cut":true,"hidden":false,"merged":[[10,14,13,14],[10,15,10,19],[11,15,12,15],[11,16,12,16],[11,17,12,17],[11,18,12,18],[11,19,12,19],[6,14,9,14],[6,15,6,19],[7,15,8,15],[7,16,8,16],[7,17,8,17],[7,18,8,18],[7,19,8,19],[2,14,5,14],[1,1,1,5],[1,8,1,12],[1,14,1,19],[2,15,2,19],[3,15,4,15],[3,16,4,16],[3,17,4,17],[3,18,4,18],[3,19,4,19]],"bounds":{"rows_first":31,"rows_last":7,"rows_between":31,"halvings":6}}
[]
["T = f(uV)","T = a.uV^4 + b.uV^3 + c.uV^2 + d.uV + e",null,null,null,null,null,"ρV = f(uV)","ρV = a.uV^4 + b.uV^3 + c.uV^2 + d.uV + e",null,null,null,null,null,"Saturation"]
["P (bars)","coeff1","coeff2","coeff3","coeff4","coeff5",null,"P (bars)","coeff6","coeff7","coeff8","coeff9","coeff10",null,"uVsat = f(P)","uVsat = a.P^4 + b.P^3 + c.P^2 + d.P + e"]
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{"sheet":"Poly_Liquide","index":3,"n_rows":74,"n_cols":21,"rows_kept":74,"cut":false,"hidden":false,"merged":[[6,15,9,15],[6,16,6,20],[7,16,8,16],[7,17,8,17],[7,18,8,18],[7,19,8,19],[7,20,8,20],[1,1,1,5],[2,15,5,15],[1,8,1,12],[1,15,1,20],[2,16,2,20],[3,16,4,16],[3,17,4,17],[3,18,4,18],[3,19,4,19],[3,20,4,20]]}
[]
["T = f(uL)","T = a.uL^4 + b.uL^3 + c.uL^2 + d.uL + e",null,null,null,null,null,"ρL = f(uL)","ρL = a.uL^4 + b.uL^3 + c.uL^2 + d.uL + e",null,null,null,null,null,null,"Saturation"]
["P (bars)","coeff1","coeff2","coeff3","coeff4","coeff5",null,"P (bars)","a","b","c","d","e",null,null,"uLsat = f(P)","uLsat = a.P^4 + b.P^3 + c.P^2 + d.P + e"]
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[]
[]
["Saturation"]
["P","uV","T","ρV"]
["(bar)","(kJ/kg)","(°C)","(kg/m3)"]
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[]
[]
["Saturation"]
["P","uL","T","ρL"]
["(bar)","(kJ/kg)","(°C)","(kg/m3)"]
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