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