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10 Commits
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9c3a32c2cb
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| 9c3a32c2cb | |||
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| dd70b8c890 | |||
| 3d93f2a7b9 | |||
| cc89833530 | |||
| f3bbf63602 | |||
| 70af0885e3 | |||
| dbfc4a81b2 | |||
| f14e2c8d8e | |||
| 7e34b9aa71 |
17
reactor.html
17
reactor.html
@@ -102,6 +102,19 @@
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} else {
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} else {
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$(".PFR").show();
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$(".PFR").show();
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}
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}
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const updateDx = () => {
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const length = parseFloat($("#node-input-length").val()) || 0;
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const resolution = parseFloat($("#node-input-resolution_L").val()) || 1;
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const dx = resolution > 0 ? (length / resolution).toFixed(6) : "N/A";
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$("#dx-output").text(dx + " m");
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};
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// Set up event listeners for real-time updates
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$("#node-input-length, #node-input-resolution_L").on("change keyup", updateDx);
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// Initial calculation
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updateDx();
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},
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},
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oneditsave: function() {
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oneditsave: function() {
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// save logger fields
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// save logger fields
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@@ -144,6 +157,10 @@
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<label for="node-input-resolution_L"><i class="fa fa-tag"></i> Resolution</label>
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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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<input type="text" id="node-input-resolution_L" placeholder="#">
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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-dx"><i class="fa fa-tag"></i> dx (length / resolution) [m]</label>
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<span id="dx-output" style="display: inline-block; padding: 8px; font-weight: bold; color: #333;">--</span>
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</div>
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<h3> Internal mass transfer calculation (optional) </h3>
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<h3> Internal mass transfer calculation (optional) </h3>
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<div class="form-row">
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<div class="form-row">
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<label for="node-input-kla"><i class="fa fa-tag"></i> kLa [d-1]</label>
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<label for="node-input-kla"><i class="fa fa-tag"></i> kLa [d-1]</label>
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@@ -34,7 +34,6 @@ class nodeClass {
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switch (msg.topic) {
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switch (msg.topic) {
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case "clock":
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case "clock":
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this.source.updateState(msg.timestamp);
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this.source.updateState(msg.timestamp);
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send([msg, null, null]);
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break;
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break;
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case "Fluent":
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case "Fluent":
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this.source.setInfluent = msg;
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this.source.setInfluent = msg;
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@@ -42,9 +41,6 @@ class nodeClass {
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case "OTR":
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case "OTR":
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this.source.setOTR = msg;
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this.source.setOTR = msg;
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break;
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break;
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case "Temperature":
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this.source.setTemperature = msg;
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break;
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case "Dispersion":
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case "Dispersion":
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this.source.setDispersion = msg;
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this.source.setDispersion = msg;
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break;
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break;
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@@ -7,17 +7,7 @@ const ASM_CONSTANTS = {
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NUM_SPECIES: 13
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NUM_SPECIES: 13
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};
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};
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/**
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const KINETIC_CONSTANTS = {
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* ASM3 class for the Activated Sludge Model No. 3 (ASM3). Using Koch et al. 2000 parameters.
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*/
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class ASM3 {
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constructor() {
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/**
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* Kinetic parameters for ASM3 at 20 C. Using Koch et al. 2000 parameters.
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* @property {Object} kin_params - Kinetic parameters
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*/
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this.kin_params = {
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// Hydrolysis
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// Hydrolysis
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k_H: 9., // hydrolysis rate constant [g X_S g-1 X_H d-1]
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k_H: 9., // hydrolysis rate constant [g X_S g-1 X_H d-1]
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K_X: 1., // hydrolysis saturation constant [g X_S g-1 X_H]
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K_X: 1., // hydrolysis saturation constant [g X_S g-1 X_H]
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@@ -42,13 +32,9 @@ class ASM3 {
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K_A_HCO: 0.5, // saturation constant S_HCO [mole HCO3 m-3]
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K_A_HCO: 0.5, // saturation constant S_HCO [mole HCO3 m-3]
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b_A_O: 0.20, // aerobic respiration rate [d-1]
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b_A_O: 0.20, // aerobic respiration rate [d-1]
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b_A_NO: 0.10 // anoxic respiration rate [d-1]
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b_A_NO: 0.10 // anoxic respiration rate [d-1]
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};
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};
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/**
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const STOICHIOMETRIC_CONSTANTS = {
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* Stoichiometric and composition parameters for ASM3. Using Koch et al. 2000 parameters.
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* @property {Object} stoi_params - Stoichiometric parameters
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*/
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this.stoi_params = {
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// Fractions
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// Fractions
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f_SI: 0., // fraction S_I from hydrolysis [g S_I g-1 X_S]
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f_SI: 0., // fraction S_I from hydrolysis [g S_I g-1 X_S]
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f_XI: 0.2, // fraction X_I from decomp X_H [g X_I g-1 X_H]
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f_XI: 0.2, // fraction X_I from decomp X_H [g X_I g-1 X_H]
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@@ -75,7 +61,25 @@ class ASM3 {
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// Composition (charge)
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// Composition (charge)
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i_cNH: 1/14, // charge per S_NH [mole H+ g-1 NH3-N]
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i_cNH: 1/14, // charge per S_NH [mole H+ g-1 NH3-N]
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i_cNO: -1/14 // charge per S_NO [mole H+ g-1 NO3-N]
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i_cNO: -1/14 // charge per S_NO [mole H+ g-1 NO3-N]
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};
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};
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/**
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* ASM3 class for the Activated Sludge Model No. 3 (ASM3). Using Koch et al. 2000 parameters.
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*/
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class ASM3 {
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constructor() {
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/**
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* Kinetic parameters for ASM3 at 20 C. Using Koch et al. 2000 parameters.
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* @property {Object} kin_params - Kinetic parameters
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*/
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this.kin_params = KINETIC_CONSTANTS;
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/**
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* Stoichiometric and composition parameters for ASM3. Using Koch et al. 2000 parameters.
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* @property {Object} stoi_params - Stoichiometric parameters
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*/
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this.stoi_params = STOICHIOMETRIC_CONSTANTS;
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/**
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/**
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* Temperature theta parameters for ASM3. Using Koch et al. 2000 parameters.
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* Temperature theta parameters for ASM3. Using Koch et al. 2000 parameters.
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@@ -215,4 +219,4 @@ class ASM3 {
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}
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}
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}
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}
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module.exports = { ASM3, ASM_CONSTANTS };
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module.exports = { ASM3, ASM_CONSTANTS, KINETIC_CONSTANTS, STOICHIOMETRIC_CONSTANTS };
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@@ -7,17 +7,7 @@ const ASM_CONSTANTS = {
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NUM_SPECIES: 13
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NUM_SPECIES: 13
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};
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};
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/**
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const KINETIC_CONSTANTS = {
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* ASM3 class for the Activated Sludge Model No. 3 (ASM3).
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*/
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class ASM3 {
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constructor() {
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/**
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* Kinetic parameters for ASM3 at 20 C.
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* @property {Object} kin_params - Kinetic parameters
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*/
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this.kin_params = {
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// Hydrolysis
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// Hydrolysis
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k_H: 3., // hydrolysis rate constant [g X_S g-1 X_H d-1]
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k_H: 3., // hydrolysis rate constant [g X_S g-1 X_H d-1]
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K_X: 1., // hydrolysis saturation constant [g X_S g-1 X_H]
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K_X: 1., // hydrolysis saturation constant [g X_S g-1 X_H]
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@@ -42,13 +32,9 @@ class ASM3 {
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K_A_HCO: 0.5, // saturation constant S_HCO [mole HCO3 m-3]
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K_A_HCO: 0.5, // saturation constant S_HCO [mole HCO3 m-3]
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b_A_O: 0.15, // aerobic respiration rate [d-1]
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b_A_O: 0.15, // aerobic respiration rate [d-1]
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b_A_NO: 0.05 // anoxic respiration rate [d-1]
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b_A_NO: 0.05 // anoxic respiration rate [d-1]
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};
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};
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/**
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const STOICHIOMETRIC_CONSTANTS = {
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* Stoichiometric and composition parameters for ASM3.
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* @property {Object} stoi_params - Stoichiometric parameters
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*/
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this.stoi_params = {
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// Fractions
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// Fractions
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f_SI: 0., // fraction S_I from hydrolysis [g S_I g-1 X_S]
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f_SI: 0., // fraction S_I from hydrolysis [g S_I g-1 X_S]
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f_XI: 0.2, // fraction X_I from decomp X_H [g X_I g-1 X_H]
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f_XI: 0.2, // fraction X_I from decomp X_H [g X_I g-1 X_H]
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@@ -75,7 +61,25 @@ class ASM3 {
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// Composition (charge)
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// Composition (charge)
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i_cNH: 1/14, // charge per S_NH [mole H+ g-1 NH3-N]
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i_cNH: 1/14, // charge per S_NH [mole H+ g-1 NH3-N]
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i_cNO: -1/14 // charge per S_NO [mole H+ g-1 NO3-N]
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i_cNO: -1/14 // charge per S_NO [mole H+ g-1 NO3-N]
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};
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};
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/**
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* ASM3 class for the Activated Sludge Model No. 3 (ASM3).
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*/
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class ASM3 {
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constructor() {
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/**
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* Kinetic parameters for ASM3 at 20 C.
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* @property {Object} kin_params - Kinetic parameters
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*/
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this.kin_params = KINETIC_CONSTANTS;
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/**
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* Stoichiometric and composition parameters for ASM3.
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* @property {Object} stoi_params - Stoichiometric parameters
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*/
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this.stoi_params = STOICHIOMETRIC_CONSTANTS;
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/**
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/**
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* Temperature theta parameters for ASM3.
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* Temperature theta parameters for ASM3.
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@@ -215,4 +219,4 @@ class ASM3 {
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}
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}
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}
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}
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module.exports = { ASM3, ASM_CONSTANTS };
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module.exports = { ASM3, ASM_CONSTANTS, KINETIC_CONSTANTS, STOICHIOMETRIC_CONSTANTS };
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@@ -10,9 +10,9 @@ const mathConfig = {
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const math = create(all, mathConfig);
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const math = create(all, mathConfig);
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const BC_PADDING = 2;
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const BC_PADDING = 2; // Boundary Condition padding for open boundaries in extendedState variable
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const DEBUG = false;
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const DEBUG = false;
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const DAY2MS = 1000 * 60 * 60 * 24;
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const DAY2MS = 1000 * 60 * 60 * 24; // convert between days and milliseconds
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class Reactor {
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class Reactor {
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/**
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/**
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@@ -25,13 +25,14 @@ class Reactor {
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this.logger = new logger(this.config.general.logging.enabled, this.config.general.logging.logLevel, config.general.name);
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this.logger = new logger(this.config.general.logging.enabled, this.config.general.logging.logLevel, config.general.name);
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this.emitter = new EventEmitter();
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this.emitter = new EventEmitter();
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this.measurements = new MeasurementContainer();
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this.measurements = new MeasurementContainer();
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this.childRegistrationUtils = new childRegistrationUtils(this); // Child registration utility
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this.childRegistrationUtils = new childRegistrationUtils(this); // child registration utility
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// placeholder variables for children and parents
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this.upstreamReactor = null;
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this.upstreamReactor = null;
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this.downstreamReactor = null;
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this.downstreamReactor = null;
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this.returnPump = null;
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this.returnPump = null;
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|
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this.asm = new ASM3();
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this.asm = new ASM3(); // Reaction model
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|
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this.volume = config.volume; // fluid volume reactor [m3]
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this.volume = config.volume; // fluid volume reactor [m3]
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@@ -42,9 +43,9 @@ class Reactor {
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|
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this.kla = config.kla; // if NaN, use externaly provided OTR [d-1]
|
this.kla = config.kla; // if NaN, use externaly provided OTR [d-1]
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|
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this.currentTime = Date.now(); // milliseconds since epoch [ms]
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this.currentTime = null; // milliseconds since epoch [ms]
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this.timeStep = 1 / (24*60*60) * this.config.timeStep; // time step in seconds, converted to days.
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this.timeStep = 1 / (24*60*60) * this.config.timeStep; // time step in seconds, converted to days.
|
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this.speedUpFactor = 100; // speed up factor for simulation, 60 means 1 minute per simulated second
|
this.speedUpFactor = 1; // speed up factor for simulation, 60 means 1 minute per simulated second
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}
|
}
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|
|
||||||
/**
|
/**
|
||||||
@@ -113,6 +114,11 @@ class Reactor {
|
|||||||
}
|
}
|
||||||
}
|
}
|
||||||
|
|
||||||
|
/**
|
||||||
|
* Register child function required for child registration.
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|
* @param {object} child
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||||||
|
* @param {string} softwareType
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||||||
|
*/
|
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registerChild(child, softwareType) {
|
registerChild(child, softwareType) {
|
||||||
if(!child) {
|
if(!child) {
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||||||
this.logger.error(`Invalid ${softwareType} child provided.`);
|
this.logger.error(`Invalid ${softwareType} child provided.`);
|
||||||
@@ -161,18 +167,14 @@ class Reactor {
|
|||||||
|
|
||||||
_connectReactor(reactorChild) {
|
_connectReactor(reactorChild) {
|
||||||
if (reactorChild.config.functionality.positionVsParent != "upstream") {
|
if (reactorChild.config.functionality.positionVsParent != "upstream") {
|
||||||
this.logger.warn("Reactor children of reactors should always be upstream.");
|
this.logger.warn("Reactor children of other reactors should always be upstream!");
|
||||||
}
|
|
||||||
|
|
||||||
if (math.abs(reactorChild.d_x - this.d_x) / this.d_x < 0.025) {
|
|
||||||
this.logger.warn("Significant grid sizing discrepancies between adjacent reactors! Change resolutions to match reactors grid step, or implement boundary value interpolation.");
|
|
||||||
}
|
}
|
||||||
|
|
||||||
// set upstream and downstream reactor variable in current and child nodes respectively for easy access
|
// set upstream and downstream reactor variable in current and child nodes respectively for easy access
|
||||||
this.upstreamReactor = reactorChild;
|
this.upstreamReactor = reactorChild;
|
||||||
reactorChild.downstreamReactor = this;
|
reactorChild.downstreamReactor = this;
|
||||||
|
|
||||||
reactorChild.emitter.on("stateChange", (eventData) => {
|
reactorChild.emitter.on("stateChange", (eventData) => { // Triggers state update in downstream reactor.
|
||||||
this.logger.debug(`State change of upstream reactor detected.`);
|
this.logger.debug(`State change of upstream reactor detected.`);
|
||||||
this.updateState(eventData);
|
this.updateState(eventData);
|
||||||
});
|
});
|
||||||
@@ -203,20 +205,32 @@ class Reactor {
|
|||||||
* Update the reactor state based on the new time.
|
* Update the reactor state based on the new time.
|
||||||
* @param {number} newTime - New time to update reactor state to, in milliseconds since epoch.
|
* @param {number} newTime - New time to update reactor state to, in milliseconds since epoch.
|
||||||
*/
|
*/
|
||||||
updateState(newTime) { // expect update with timestamp
|
updateState(newTime) {
|
||||||
if (this.upstreamReactor) {
|
if (!this.currentTime) { // initialise currentTime variable
|
||||||
this.setInfluent = this.upstreamReactor.getEffluent[0]; // grab main effluent upstream reactor
|
this.currentTime = newTime;
|
||||||
|
return;
|
||||||
|
}
|
||||||
|
|
||||||
|
if (this.upstreamReactor) { // grab main effluent upstream reactor
|
||||||
|
this.setInfluent = this.upstreamReactor.getEffluent[0];
|
||||||
}
|
}
|
||||||
|
|
||||||
const n_iter = Math.floor(this.speedUpFactor * (newTime-this.currentTime) / (this.timeStep*DAY2MS));
|
const n_iter = Math.floor(this.speedUpFactor * (newTime-this.currentTime) / (this.timeStep*DAY2MS));
|
||||||
if (n_iter) {
|
|
||||||
|
if (n_iter == 0) { // no update required, change in currentTime smaller than time step
|
||||||
|
return;
|
||||||
|
}
|
||||||
|
|
||||||
let n = 0;
|
let n = 0;
|
||||||
while (n < n_iter) {
|
while (n < n_iter) {
|
||||||
this.tick(this.timeStep);
|
this.tick(this.timeStep);
|
||||||
n += 1;
|
n += 1;
|
||||||
}
|
}
|
||||||
this.currentTime += n_iter * this.timeStep * DAY2MS / this.speedUpFactor;
|
this.currentTime += n_iter * this.timeStep * DAY2MS / this.speedUpFactor;
|
||||||
this.emitter.emit("stateChange", this.currentTime);
|
this.emitter.emit("stateChange", this.currentTime); // update downstream reactors
|
||||||
|
|
||||||
|
if (this.returnPump) { // update recirculation pump state
|
||||||
|
this.returnPump.updateSourceSink();
|
||||||
}
|
}
|
||||||
}
|
}
|
||||||
}
|
}
|
||||||
@@ -231,6 +245,23 @@ class Reactor_CSTR extends Reactor {
|
|||||||
this.state = config.initialState;
|
this.state = config.initialState;
|
||||||
}
|
}
|
||||||
|
|
||||||
|
_updateMeasurement(measurementType, value, position, context) {
|
||||||
|
|
||||||
|
switch(measurementType) {
|
||||||
|
case "quantity (oxygen)":
|
||||||
|
this.state[ASM_CONSTANTS.S_O_INDEX] = value;
|
||||||
|
break;
|
||||||
|
case "quantity (ammonium)":
|
||||||
|
this.state[ASM_CONSTANTS.S_NH_INDEX] = value;
|
||||||
|
break;
|
||||||
|
case "quantity (nox)":
|
||||||
|
this.state[ASM_CONSTANTS.S_NO_INDEX] = value;
|
||||||
|
break;
|
||||||
|
default:
|
||||||
|
super._updateMeasurement(measurementType, value, position, context);
|
||||||
|
}
|
||||||
|
}
|
||||||
|
|
||||||
/**
|
/**
|
||||||
* Tick the reactor state using the forward Euler method.
|
* Tick the reactor state using the forward Euler method.
|
||||||
* @param {number} time_step - Time step for the simulation [d].
|
* @param {number} time_step - Time step for the simulation [d].
|
||||||
@@ -241,7 +272,7 @@ class Reactor_CSTR extends Reactor {
|
|||||||
const outflow = math.multiply(-1 * math.sum(this.Fs) / this.volume, this.state);
|
const outflow = math.multiply(-1 * math.sum(this.Fs) / this.volume, this.state);
|
||||||
const reaction = this.asm.compute_dC(this.state, this.temperature);
|
const reaction = this.asm.compute_dC(this.state, this.temperature);
|
||||||
const transfer = Array(ASM_CONSTANTS.NUM_SPECIES).fill(0.0);
|
const transfer = Array(ASM_CONSTANTS.NUM_SPECIES).fill(0.0);
|
||||||
transfer[ASM_CONSTANTS.S_O_INDEX] = isNaN(this.kla) ? this.OTR : this._calcOTR(this.state[S_O_INDEX], this.temperature); // calculate OTR if kla is not NaN, otherwise use externaly calculated OTR
|
transfer[ASM_CONSTANTS.S_O_INDEX] = isNaN(this.kla) ? this.OTR : this._calcOTR(this.state[ASM_CONSTANTS.S_O_INDEX], this.temperature); // calculate OTR if kla is not NaN, otherwise use externaly calculated OTR
|
||||||
|
|
||||||
const dC_total = math.multiply(math.add(inflow, outflow, reaction, transfer), time_step)
|
const dC_total = math.multiply(math.add(inflow, outflow, reaction, transfer), time_step)
|
||||||
this.state = this._arrayClip2Zero(math.add(this.state, dC_total)); // clip value element-wise to avoid negative concentrations
|
this.state = this._arrayClip2Zero(math.add(this.state, dC_total)); // clip value element-wise to avoid negative concentrations
|
||||||
@@ -290,13 +321,23 @@ class Reactor_PFR extends Reactor {
|
|||||||
this.D = this._constrainDispersion(input.payload);
|
this.D = this._constrainDispersion(input.payload);
|
||||||
}
|
}
|
||||||
|
|
||||||
|
_connectReactor(reactorChild) {
|
||||||
|
if (math.abs(reactorChild.d_x - this.d_x) / this.d_x < 0.025) {
|
||||||
|
this.logger.warn("Significant grid sizing discrepancies between adjacent reactors! Change resolutions to match reactors grid step, or implement boundary value interpolation.");
|
||||||
|
}
|
||||||
|
super._connectReactor(reactorChild);
|
||||||
|
}
|
||||||
|
|
||||||
|
/**
|
||||||
|
* Update the reactor state based on the new time. Performs checks specific to PFR.
|
||||||
|
* @param {number} newTime - New time to update reactor state to, in milliseconds since epoch.
|
||||||
|
*/
|
||||||
updateState(newTime) {
|
updateState(newTime) {
|
||||||
super.updateState(newTime);
|
super.updateState(newTime);
|
||||||
// let Pe_local = this.d_x*math.sum(this.Fs)/(this.D*this.A)
|
|
||||||
this.D = this._constrainDispersion(this.D);
|
this.D = this._constrainDispersion(this.D); // constrains D to minimum dispersion, so that local Péclet number is always above 2
|
||||||
const Co_D = this.D*this.timeStep/(this.d_x*this.d_x);
|
const Co_D = this.D*this.timeStep/(this.d_x*this.d_x);
|
||||||
|
|
||||||
// (Pe_local >= 2) && this.logger.warn(`Local Péclet number (${Pe_local}) is too high! Increase reactor resolution.`);
|
|
||||||
(Co_D >= 0.5) && this.logger.warn(`Courant number (${Co_D}) is too high! Reduce time step size.`);
|
(Co_D >= 0.5) && this.logger.warn(`Courant number (${Co_D}) is too high! Reduce time step size.`);
|
||||||
|
|
||||||
if(DEBUG) {
|
if(DEBUG) {
|
||||||
@@ -375,8 +416,8 @@ class Reactor_PFR extends Reactor {
|
|||||||
*/
|
*/
|
||||||
_applyBoundaryConditions() {
|
_applyBoundaryConditions() {
|
||||||
// Upstream BC
|
// Upstream BC
|
||||||
if (this.upstreamReactor) {
|
if (this.upstreamReactor && this.upstreamReactor.config.reactor_type == "PFR") {
|
||||||
// Open boundary
|
// Open boundary, if upstream reactor is PFR
|
||||||
this.extendedState.splice(0, BC_PADDING, ...this.upstreamReactor.state.slice(-BC_PADDING));
|
this.extendedState.splice(0, BC_PADDING, ...this.upstreamReactor.state.slice(-BC_PADDING));
|
||||||
} else {
|
} else {
|
||||||
if (math.sum(this.Fs) > 0) {
|
if (math.sum(this.Fs) > 0) {
|
||||||
@@ -384,7 +425,7 @@ class Reactor_PFR extends Reactor {
|
|||||||
const BC_C_in = math.multiply(1 / math.sum(this.Fs), [this.Fs], this.Cs_in)[0];
|
const BC_C_in = math.multiply(1 / math.sum(this.Fs), [this.Fs], this.Cs_in)[0];
|
||||||
const BC_dispersion_term = this.D*this.A/(math.sum(this.Fs)*this.d_x);
|
const BC_dispersion_term = this.D*this.A/(math.sum(this.Fs)*this.d_x);
|
||||||
this.extendedState[BC_PADDING] = math.multiply(1/(1+BC_dispersion_term), math.add(BC_C_in, math.multiply(BC_dispersion_term, this.extendedState[BC_PADDING+1])));
|
this.extendedState[BC_PADDING] = math.multiply(1/(1+BC_dispersion_term), math.add(BC_C_in, math.multiply(BC_dispersion_term, this.extendedState[BC_PADDING+1])));
|
||||||
// Numerical boundary condition
|
// Numerical boundary condition (first-order accurate)
|
||||||
this.extendedState[BC_PADDING-1] = math.add(math.multiply(2, this.extendedState[BC_PADDING]), math.multiply(-2, this.extendedState[BC_PADDING+2]), this.extendedState[BC_PADDING+3]);
|
this.extendedState[BC_PADDING-1] = math.add(math.multiply(2, this.extendedState[BC_PADDING]), math.multiply(-2, this.extendedState[BC_PADDING+2]), this.extendedState[BC_PADDING+3]);
|
||||||
} else {
|
} else {
|
||||||
// Neumann BC (no flux)
|
// Neumann BC (no flux)
|
||||||
@@ -393,8 +434,8 @@ class Reactor_PFR extends Reactor {
|
|||||||
}
|
}
|
||||||
|
|
||||||
// Downstream BC
|
// Downstream BC
|
||||||
if (this.downstreamReactor) {
|
if (this.downstreamReactor && this.downstreamReactor.config.reactor_type == "PFR") {
|
||||||
// Open boundary
|
// Open boundary, if downstream reactor is PFR
|
||||||
this.extendedState.splice(this.n_x+BC_PADDING, BC_PADDING, ...this.downstreamReactor.state.slice(0, BC_PADDING));
|
this.extendedState.splice(this.n_x+BC_PADDING, BC_PADDING, ...this.downstreamReactor.state.slice(0, BC_PADDING));
|
||||||
} else {
|
} else {
|
||||||
// Neumann BC (no flux)
|
// Neumann BC (no flux)
|
||||||
@@ -404,7 +445,6 @@ class Reactor_PFR extends Reactor {
|
|||||||
|
|
||||||
/**
|
/**
|
||||||
* Create finite difference first derivative operator.
|
* Create finite difference first derivative operator.
|
||||||
* @returns {Array} - First derivative operator matrix.
|
|
||||||
*/
|
*/
|
||||||
_makeDoperator() { // create gradient operator
|
_makeDoperator() { // create gradient operator
|
||||||
const D_size = this.n_x+2*BC_PADDING;
|
const D_size = this.n_x+2*BC_PADDING;
|
||||||
@@ -420,7 +460,6 @@ class Reactor_PFR extends Reactor {
|
|||||||
|
|
||||||
/**
|
/**
|
||||||
* Create central finite difference second derivative operator.
|
* Create central finite difference second derivative operator.
|
||||||
* @returns {Array} - Second derivative operator matrix.
|
|
||||||
*/
|
*/
|
||||||
_makeD2operator() { // create the central second derivative operator
|
_makeD2operator() { // create the central second derivative operator
|
||||||
const D_size = this.n_x+2*BC_PADDING;
|
const D_size = this.n_x+2*BC_PADDING;
|
||||||
@@ -433,6 +472,9 @@ class Reactor_PFR extends Reactor {
|
|||||||
return D2;
|
return D2;
|
||||||
}
|
}
|
||||||
|
|
||||||
|
/**
|
||||||
|
* Constrains dispersion so that local Péclet number stays below 2. Needed for stable central differencing method.
|
||||||
|
*/
|
||||||
_constrainDispersion(D) {
|
_constrainDispersion(D) {
|
||||||
const Dmin = math.sum(this.Fs) * this.d_x / (1.999 * this.A);
|
const Dmin = math.sum(this.Fs) * this.d_x / (1.999 * this.A);
|
||||||
if (D < Dmin) {
|
if (D < Dmin) {
|
||||||
|
|||||||
Reference in New Issue
Block a user