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/* autogenerated from "macros/Hydraulics/PerteDP.sci" */
function PerteDP() {
PerteDP.prototype.define = function PerteDP() {
model = scicos_model();
model.in1 = [1];
model.out = [1];
L = 10;
D = 0.2;
lambda = 0.03;
z1 = 0;
z2 = 0;
p_rho = 0;
model.rpar = [[L],[D],[lambda],[z1],[z2],[p_rho]];
model.sim = "PerteDP";
model.blocktype = "c";
model.dep_ut = [true,false];
mo = modelica();
mo.model = "PerteDP";
mo.inputs = "C1";
mo.outputs = "C2";
mo.parameters = list([["L"],["D"],["lambda"],["z1"],["z2"],["p_rho"]],[[L],[D],[lambda],[z1],[z2],[p_rho]]);
model.equations = mo;
model.in1 = ones(size(mo.inputs,"*"),1);
model.out = ones(size(mo.outputs,"*"),1);
exprs = [[string(L)],[string(D)],[string(lambda)],[string(z1)],[string(z2)],[string(p_rho)]];
gr_i = [];
this.x = standard_define([2,1],model,exprs,list(gr_i,0));
this.x.graphics.in_implicit = ["I"];
this.x.graphics.out_implicit = ["I"];
}
PerteDP.prototype.details = function PerteDP() {
return this.x;
}
PerteDP.prototype.get = function PerteDP() {
}
PerteDP.prototype.set = function PerteDP() {
this.x = arg1;
graphics = arg1.graphics;
exprs = graphics.exprs;
model = arg1.model;
while (true) {
[ok,L,D,lambda,z1,z2,p_rho,exprs] = scicos_getvalue("Parametres du tuyau",[["Longueur du tube : L (m)"],["Diamètre interne du tube : D (m)"],["Coefficient de perte de charge-frottement(S.U) : lambda"],["Altitude entrée tuyauterie : z1 (m)"],["Altitude sortie tuyauterie : z2 (m)"],["Si >0, masse volumique imposée fu fluide : p_rho (kg/m3)"]],list("vec",-1,"vec",-1,"vec",-1,"vec",-1,"vec",-1,"vec",-1),exprs);
if (!ok) {
break;
}
model.rpar = [[L],[D],[lambda],[z1],[z2],[p_rho]];
model.equations.parameters[2-1] = list(L,D,lambda,z1,z2,p_rho);
graphics.exprs = exprs;
this.x.graphics = graphics;
this.x.model = model;
break;
}
}
}
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