Add support for multiple reactor types (CSTR and PFR) with corresponding properties (Dichelet BC for now)
This commit is contained in:
@@ -4,7 +4,10 @@
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color: "#c4cce0",
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color: "#c4cce0",
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defaults: {
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defaults: {
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name: { value: "" },
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name: { value: "" },
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volume: { value: 0., required: true},
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reactor_type: { value: "CSTR", required: true },
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volume: { value: 0., required: true },
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length: { value: 0.},
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resolution_L: { value: 0.},
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n_inlets: { value: 1, required: true},
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n_inlets: { value: 1, required: true},
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kla: { value: null },
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kla: { value: null },
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S_O_init: { value: 0., required: true },
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S_O_init: { value: 0., required: true },
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@@ -45,6 +48,32 @@
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type:"num",
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type:"num",
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types:["num"]
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types:["num"]
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});
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});
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$("#node-input-reactor_type").typedInput({
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types: [
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{
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value: "CSTR",
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options: [
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{ value: "CSTR", label: "CSTR"},
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{ value: "PFR", label: "PFR"}
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]
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}
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]
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})
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$("#node-input-reactor_type").on("change", function() {
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const type = $("#node-input-reactor_type").typedInput("value");
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if (type === "CSTR") {
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$(".PFR").hide();
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} else {
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$(".PFR").show();
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}
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});
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// Set initial visibility on dialog open
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const initialType = $("#node-input-reactor_type").typedInput("value");
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if (initialType === "CSTR") {
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$(".PFR").hide();
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} else {
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$(".PFR").show();
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}
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},
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},
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oneditsave: function() {
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oneditsave: function() {
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let volume = parseFloat($("#node-input-volume").typedInput("value"));
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let volume = parseFloat($("#node-input-volume").typedInput("value"));
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@@ -65,10 +94,22 @@
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<input type="text" id="node-input-name" placeholder="Name">
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<input type="text" id="node-input-name" placeholder="Name">
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</div>
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</div>
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<h2> Reactor properties </h2>
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<h2> Reactor properties </h2>
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<div class="form-row">
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<label for="node-input-reactor_type"><i class="fa fa-tag"></i> Reactor type</label>
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<input type="text" id="node-input-reactor_type">
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</div>
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<div class="form-row">
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<div class="form-row">
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<label for="node-input-volume"><i class="fa fa-tag"></i> Fluid volume [m3]</label>
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<label for="node-input-volume"><i class="fa fa-tag"></i> Fluid volume [m3]</label>
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<input type="text" id="node-input-volume" placeholder="m3">
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<input type="text" id="node-input-volume" placeholder="m3">
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</div>
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</div>
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<div class="form-row PFR">
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<label for="node-input-length"><i class="fa fa-tag"></i> Reactor length [m]</label>
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<input type="text" id="node-input-length" placeholder="m">
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</div>
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<div class="form-row PFR">
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<label for="node-input-resolution_L"><i class="fa fa-tag"></i> Resolution</label>
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<input type="text" id="node-input-resolution_L" placeholder="#">
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</div>
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<div class="form-row">
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<div class="form-row">
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<label for="node-input-n_inlets"><i class="fa fa-tag"></i> Number of inlets</label>
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<label for="node-input-n_inlets"><i class="fa fa-tag"></i> Number of inlets</label>
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<input type="text" id="node-input-n_inlets" placeholder="#">
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<input type="text" id="node-input-n_inlets" placeholder="#">
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@@ -7,26 +7,60 @@ module.exports = function(RED) {
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const Reactor = require('./dependencies/reactor_class');
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const Reactor = require('./dependencies/reactor_class');
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const reactor = new Reactor(
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let new_reactor;
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parseFloat(config.volume),
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parseInt(config.n_inlets),
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switch (config.reactor_type) {
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parseFloat(config.kla),
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case "CSTR":
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[
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new_reactor = new Reactor(
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parseFloat(config.S_O_init),
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parseFloat(config.volume),
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parseFloat(config.S_I_init),
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parseInt(config.n_inlets),
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parseFloat(config.S_S_init),
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parseFloat(config.kla),
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parseFloat(config.S_NH_init),
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[
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parseFloat(config.S_N2_init),
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parseFloat(config.S_O_init),
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parseFloat(config.S_NO_init),
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parseFloat(config.S_I_init),
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parseFloat(config.S_HCO_init),
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parseFloat(config.S_S_init),
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parseFloat(config.X_I_init),
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parseFloat(config.S_NH_init),
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parseFloat(config.X_S_init),
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parseFloat(config.S_N2_init),
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parseFloat(config.X_H_init),
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parseFloat(config.S_NO_init),
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parseFloat(config.X_STO_init),
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parseFloat(config.S_HCO_init),
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parseFloat(config.X_A_init),
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parseFloat(config.X_I_init),
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parseFloat(config.X_TS_init)
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parseFloat(config.X_S_init),
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]
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parseFloat(config.X_H_init),
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);
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parseFloat(config.X_STO_init),
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parseFloat(config.X_A_init),
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parseFloat(config.X_TS_init)
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]
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);
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break;
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case "PFR":
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new_reactor = new Reactor(
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parseFloat(config.volume),
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parseFloat(config.L),
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parseInt(config.resolution_L),
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parseInt(config.n_inlets),
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parseFloat(config.kla),
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[
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parseFloat(config.S_O_init),
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parseFloat(config.S_I_init),
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parseFloat(config.S_S_init),
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parseFloat(config.S_NH_init),
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parseFloat(config.S_N2_init),
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parseFloat(config.S_NO_init),
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parseFloat(config.S_HCO_init),
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parseFloat(config.X_I_init),
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parseFloat(config.X_S_init),
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parseFloat(config.X_H_init),
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parseFloat(config.X_STO_init),
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parseFloat(config.X_A_init),
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parseFloat(config.X_TS_init)
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]
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);
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break;
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default:
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console.warn("Unknown reactor type: " + config.reactor_type);
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}
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const reactor = new_reactor; // protect from reassignment
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node.on('input', function(msg, send, done) {
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node.on('input', function(msg, send, done) {
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let toggleUpdate = false;
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let toggleUpdate = false;
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110
dependencies/reactor_class.js
vendored
110
dependencies/reactor_class.js
vendored
@@ -5,7 +5,6 @@ class Reactor_CSTR {
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constructor(volume, n_inlets, kla, initial_state) {
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constructor(volume, n_inlets, kla, initial_state) {
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this.state = initial_state;
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this.state = initial_state;
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console.log(this.state);
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this.asm = new ASM3();
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this.asm = new ASM3();
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this.Vl = volume; // fluid volume reactor [m3]
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this.Vl = volume; // fluid volume reactor [m3]
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@@ -17,7 +16,7 @@ class Reactor_CSTR {
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this.currentTime = Date.now(); // milliseconds since epoch [ms]
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this.currentTime = Date.now(); // milliseconds since epoch [ms]
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this.timeStep = 1/(24*60*15); // time step [d]
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this.timeStep = 1/(24*60*15); // time step [d]
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this.speedUpFactor = 30;
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this.speedUpFactor = 1;
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}
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}
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set setInfluent(input) { // setter for C_in (WIP)
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set setInfluent(input) { // setter for C_in (WIP)
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@@ -69,6 +68,113 @@ class Reactor_CSTR {
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}
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}
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}
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}
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class Reactor_PFR {
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constructor(volume, length, resolution_L, n_inlets, kla, initial_state) {
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this.asm = new ASM3();
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this.Vl = volume; // fluid volume reactor [m3]
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this.length = length; // reactor length [m]
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this.n_x = resolution_L; // number of slices
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this.d_x = length / resolution_L;
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this.A = volume / length; // crosssectional area [m2]
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this.state = Array.from(Array(this.n_x), () => initial_state.slice())
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this.Fs = Array(n_inlets).fill(0.0); // fluid debits per inlet [m3 d-1]
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this.Cs_in = Array.from(Array(n_inlets), () => new Array(13).fill(0.0)); // composition influents
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this.OTR = 0.0; // oxygen transfer rate [g O2 d-1]
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this.D = 0.0; // axial dispersion [m2 d-1]
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this.kla = kla; // if NaN, use external OTR [d-1]
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this.currentTime = Date.now(); // milliseconds since epoch [ms]
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this.timeStep = 1/(24*60*15); // time step [d]
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this.speedUpFactor = 1;
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this.D_op = makeDoperator();
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this.D2_op = makeD2operator();
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}
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set setInfluent(input) { // setter for C_in (WIP)
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let index_in = input.payload.inlet;
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this.Fs[index_in] = input.payload.F;
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this.Cs_in[index_in] = input.payload.C;
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}
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set setOTR(input) { // setter for OTR (WIP) [g O2 d-1]
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this.OTR = input.payload;
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}
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set setDispersion(input) { // setter for Axial dispersion [m2 d-1]
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this.D = input.payload;
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}
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get getEffluent() { // getter for Effluent, defaults to inlet 0
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return {topic: "Fluent", payload: {inlet: 0, F: math.sum(this.Fs), C:this.state}, timestamp: this.currentTime};
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}
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calcOTR(S_O, T=20.0) { // caculate the OTR using basic correlation, default to temperature: 20 C
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let S_O_sat = 14.652 - 4.1022e-1*T + 7.9910e-3*T*T + 7.7774e-5*T*T*T;
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return this.kla * (S_O_sat - S_O);
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}
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// expect update with timestamp
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updateState(newTime) {
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const day2ms = 1000 * 60 * 60 * 24;
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let n_iter = Math.floor(this.speedUpFactor*(newTime - this.currentTime) / (this.timeStep * day2ms));
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if (n_iter) {
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let n = 0;
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while (n < n_iter) {
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this.tick_fe(this.timeStep);
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n += 1;
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}
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this.currentTime += n_iter * this.timeStep * day2ms / this.speedUpFactor;
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}
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}
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tick_fe(time_step) { // tick reactor state using forward Euler method
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if (math.sum(this.Fs) > 0) {
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this.state[0] = math.multiply(math.divide([this.Fs], this.A), this.Cs_in)[0] // Dichelet boundary condition
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}
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const dispersion = math.multiply(this.D / (this.d_x*this.d_x), this.D2_op, this.state);
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const advection = math.multiply(math.sum(this.Fs)/(this.A*this.d_x), this.D_op, this.state);
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const reaction = this.state.map(this.asm.compute_dC);
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const transfer = Array.from(Array(this.n_x), () => new Array(13).fill(0.0))
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if (isNaN(this.kla)) { // calculate OTR if kla is not NaN, otherwise use externally calculated OTR
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transfer.forEach((x) => { x[0] = this.OTR; });
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} else {
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transfer.forEach((x, i) => { x[0] = this.calcOTR(this.state[i][0]); });
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}
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const dC_total = math.multiply(math.add(dispersion, advection, reaction, transfer), time_step);
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this.state = math.abs(math.add(this.state, dC_total)); // make sure that concentrations do not go negative
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return this.state;
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}
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makeDoperator() { // create the upwind scheme gradient operator
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const I = math.identity(this.n_x);
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const A = math.diag(Array(this.n_x).fill(-1), 1).resize([this.n_x, this.n_x]);
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I[this.n_x-1, this.n_x-1] = 0; // Neumann boundary condition at x=L
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return math.add(I, A);
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}
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makeD2operator() { // create the upwind scheme second derivative operator
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const I = math.diag(Array(this.n_x).fill(2), 0);
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const A = math.diag(Array(this.n_x).fill(-1), 1).resize([this.n_x, this.n_x]);
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const B = math.diag(Array(this.n_x).fill(-1), -1).resize([this.n_x, this.n_x]);
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I[0, 0] = 1;
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return math.add(I, A, B);
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}
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}
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// testing stuff
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// testing stuff
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// state: S_O, S_I, S_S, S_NH, S_N2, S_NO, S_HCO, X_I, X_S, X_H, X_STO, X_A, X_TS
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// state: S_O, S_I, S_S, S_NH, S_N2, S_NO, S_HCO, X_I, X_S, X_H, X_STO, X_A, X_TS
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// let initial_state = [0.1, 0.1, 0.1, 0.1, 0.1, 0.1, 0.1, 0.1, 0.1, 0.1, 0.1, 0.1, 0.1];
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// let initial_state = [0.1, 0.1, 0.1, 0.1, 0.1, 0.1, 0.1, 0.1, 0.1, 0.1, 0.1, 0.1, 0.1];
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Block a user