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5 changed files with 211 additions and 148 deletions

View File

@@ -102,6 +102,19 @@
} else {
$(".PFR").show();
}
const updateDx = () => {
const length = parseFloat($("#node-input-length").val()) || 0;
const resolution = parseFloat($("#node-input-resolution_L").val()) || 1;
const dx = resolution > 0 ? (length / resolution).toFixed(6) : "N/A";
$("#dx-output").text(dx + " m");
};
// Set up event listeners for real-time updates
$("#node-input-length, #node-input-resolution_L").on("change keyup", updateDx);
// Initial calculation
updateDx();
},
oneditsave: function() {
// save logger fields
@@ -144,6 +157,10 @@
<label for="node-input-resolution_L"><i class="fa fa-tag"></i> Resolution</label>
<input type="text" id="node-input-resolution_L" placeholder="#">
</div>
<div class="form-row PFR">
<label for="node-input-dx"><i class="fa fa-tag"></i> dx (length / resolution) [m]</label>
<span id="dx-output" style="display: inline-block; padding: 8px; font-weight: bold; color: #333;">--</span>
</div>
<h3> Internal mass transfer calculation (optional) </h3>
<div class="form-row">
<label for="node-input-kla"><i class="fa fa-tag"></i> kLa [d-1]</label>

View File

@@ -34,7 +34,6 @@ class nodeClass {
switch (msg.topic) {
case "clock":
this.source.updateState(msg.timestamp);
send([msg, null, null]);
break;
case "Fluent":
this.source.setInfluent = msg;
@@ -42,9 +41,6 @@ class nodeClass {
case "OTR":
this.source.setOTR = msg;
break;
case "Temperature":
this.source.setTemperature = msg;
break;
case "Dispersion":
this.source.setDispersion = msg;
break;

View File

@@ -7,17 +7,7 @@ const ASM_CONSTANTS = {
NUM_SPECIES: 13
};
/**
* ASM3 class for the Activated Sludge Model No. 3 (ASM3). Using Koch et al. 2000 parameters.
*/
class ASM3 {
constructor() {
/**
* Kinetic parameters for ASM3 at 20 C. Using Koch et al. 2000 parameters.
* @property {Object} kin_params - Kinetic parameters
*/
this.kin_params = {
const KINETIC_CONSTANTS = {
// Hydrolysis
k_H: 9., // hydrolysis rate constant [g X_S g-1 X_H d-1]
K_X: 1., // hydrolysis saturation constant [g X_S g-1 X_H]
@@ -42,13 +32,9 @@ class ASM3 {
K_A_HCO: 0.5, // saturation constant S_HCO [mole HCO3 m-3]
b_A_O: 0.20, // aerobic respiration rate [d-1]
b_A_NO: 0.10 // anoxic respiration rate [d-1]
};
};
/**
* Stoichiometric and composition parameters for ASM3. Using Koch et al. 2000 parameters.
* @property {Object} stoi_params - Stoichiometric parameters
*/
this.stoi_params = {
const STOICHIOMETRIC_CONSTANTS = {
// Fractions
f_SI: 0., // fraction S_I from hydrolysis [g S_I g-1 X_S]
f_XI: 0.2, // fraction X_I from decomp X_H [g X_I g-1 X_H]
@@ -75,7 +61,25 @@ class ASM3 {
// Composition (charge)
i_cNH: 1/14, // charge per S_NH [mole H+ g-1 NH3-N]
i_cNO: -1/14 // charge per S_NO [mole H+ g-1 NO3-N]
};
};
/**
* ASM3 class for the Activated Sludge Model No. 3 (ASM3). Using Koch et al. 2000 parameters.
*/
class ASM3 {
constructor() {
/**
* Kinetic parameters for ASM3 at 20 C. Using Koch et al. 2000 parameters.
* @property {Object} kin_params - Kinetic parameters
*/
this.kin_params = KINETIC_CONSTANTS;
/**
* Stoichiometric and composition parameters for ASM3. Using Koch et al. 2000 parameters.
* @property {Object} stoi_params - Stoichiometric parameters
*/
this.stoi_params = STOICHIOMETRIC_CONSTANTS;
/**
* Temperature theta parameters for ASM3. Using Koch et al. 2000 parameters.
@@ -215,4 +219,4 @@ class ASM3 {
}
}
module.exports = { ASM3, ASM_CONSTANTS };
module.exports = { ASM3, ASM_CONSTANTS, KINETIC_CONSTANTS, STOICHIOMETRIC_CONSTANTS };

View File

@@ -7,17 +7,7 @@ const ASM_CONSTANTS = {
NUM_SPECIES: 13
};
/**
* ASM3 class for the Activated Sludge Model No. 3 (ASM3).
*/
class ASM3 {
constructor() {
/**
* Kinetic parameters for ASM3 at 20 C.
* @property {Object} kin_params - Kinetic parameters
*/
this.kin_params = {
const KINETIC_CONSTANTS = {
// Hydrolysis
k_H: 3., // hydrolysis rate constant [g X_S g-1 X_H d-1]
K_X: 1., // hydrolysis saturation constant [g X_S g-1 X_H]
@@ -42,13 +32,9 @@ class ASM3 {
K_A_HCO: 0.5, // saturation constant S_HCO [mole HCO3 m-3]
b_A_O: 0.15, // aerobic respiration rate [d-1]
b_A_NO: 0.05 // anoxic respiration rate [d-1]
};
};
/**
* Stoichiometric and composition parameters for ASM3.
* @property {Object} stoi_params - Stoichiometric parameters
*/
this.stoi_params = {
const STOICHIOMETRIC_CONSTANTS = {
// Fractions
f_SI: 0., // fraction S_I from hydrolysis [g S_I g-1 X_S]
f_XI: 0.2, // fraction X_I from decomp X_H [g X_I g-1 X_H]
@@ -75,7 +61,25 @@ class ASM3 {
// Composition (charge)
i_cNH: 1/14, // charge per S_NH [mole H+ g-1 NH3-N]
i_cNO: -1/14 // charge per S_NO [mole H+ g-1 NO3-N]
};
};
/**
* ASM3 class for the Activated Sludge Model No. 3 (ASM3).
*/
class ASM3 {
constructor() {
/**
* Kinetic parameters for ASM3 at 20 C.
* @property {Object} kin_params - Kinetic parameters
*/
this.kin_params = KINETIC_CONSTANTS;
/**
* Stoichiometric and composition parameters for ASM3.
* @property {Object} stoi_params - Stoichiometric parameters
*/
this.stoi_params = STOICHIOMETRIC_CONSTANTS;
/**
* Temperature theta parameters for ASM3.
@@ -215,4 +219,4 @@ class ASM3 {
}
}
module.exports = { ASM3, ASM_CONSTANTS };
module.exports = { ASM3, ASM_CONSTANTS, KINETIC_CONSTANTS, STOICHIOMETRIC_CONSTANTS };

View File

@@ -10,9 +10,9 @@ const mathConfig = {
const math = create(all, mathConfig);
const BC_PADDING = 2;
const BC_PADDING = 2; // Boundary Condition padding for open boundaries in extendedState variable
const DEBUG = false;
const DAY2MS = 1000 * 60 * 60 * 24;
const DAY2MS = 1000 * 60 * 60 * 24; // convert between days and milliseconds
class Reactor {
/**
@@ -25,13 +25,14 @@ class Reactor {
this.logger = new logger(this.config.general.logging.enabled, this.config.general.logging.logLevel, config.general.name);
this.emitter = new EventEmitter();
this.measurements = new MeasurementContainer();
this.childRegistrationUtils = new childRegistrationUtils(this); // Child registration utility
this.childRegistrationUtils = new childRegistrationUtils(this); // child registration utility
// placeholder variables for children and parents
this.upstreamReactor = null;
this.downstreamReactor = null;
this.returnPump = null;
this.asm = new ASM3();
this.asm = new ASM3(); // Reaction model
this.volume = config.volume; // fluid volume reactor [m3]
@@ -42,9 +43,9 @@ class Reactor {
this.kla = config.kla; // if NaN, use externaly provided OTR [d-1]
this.currentTime = Date.now(); // milliseconds since epoch [ms]
this.currentTime = null; // milliseconds since epoch [ms]
this.timeStep = 1 / (24*60*60) * this.config.timeStep; // time step in seconds, converted to days.
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
}
/**
@@ -113,6 +114,11 @@ class Reactor {
}
}
/**
* Register child function required for child registration.
* @param {object} child
* @param {string} softwareType
*/
registerChild(child, softwareType) {
if(!child) {
this.logger.error(`Invalid ${softwareType} child provided.`);
@@ -161,18 +167,14 @@ class Reactor {
_connectReactor(reactorChild) {
if (reactorChild.config.functionality.positionVsParent != "upstream") {
this.logger.warn("Reactor children of 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.");
this.logger.warn("Reactor children of other reactors should always be upstream!");
}
// set upstream and downstream reactor variable in current and child nodes respectively for easy access
this.upstreamReactor = reactorChild;
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.updateState(eventData);
});
@@ -203,20 +205,32 @@ class Reactor {
* Update the reactor state based on the new time.
* @param {number} newTime - New time to update reactor state to, in milliseconds since epoch.
*/
updateState(newTime) { // expect update with timestamp
if (this.upstreamReactor) {
this.setInfluent = this.upstreamReactor.getEffluent[0]; // grab main effluent upstream reactor
updateState(newTime) {
if (!this.currentTime) { // initialise currentTime variable
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));
if (n_iter) {
if (n_iter == 0) { // no update required, change in currentTime smaller than time step
return;
}
let n = 0;
while (n < n_iter) {
this.tick(this.timeStep);
n += 1;
}
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;
}
_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.
* @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 reaction = this.asm.compute_dC(this.state, this.temperature);
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)
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);
}
_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) {
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);
// (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.`);
if(DEBUG) {
@@ -375,8 +416,8 @@ class Reactor_PFR extends Reactor {
*/
_applyBoundaryConditions() {
// Upstream BC
if (this.upstreamReactor) {
// Open boundary
if (this.upstreamReactor && this.upstreamReactor.config.reactor_type == "PFR") {
// Open boundary, if upstream reactor is PFR
this.extendedState.splice(0, BC_PADDING, ...this.upstreamReactor.state.slice(-BC_PADDING));
} else {
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_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])));
// 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]);
} else {
// Neumann BC (no flux)
@@ -393,8 +434,8 @@ class Reactor_PFR extends Reactor {
}
// Downstream BC
if (this.downstreamReactor) {
// Open boundary
if (this.downstreamReactor && this.downstreamReactor.config.reactor_type == "PFR") {
// Open boundary, if downstream reactor is PFR
this.extendedState.splice(this.n_x+BC_PADDING, BC_PADDING, ...this.downstreamReactor.state.slice(0, BC_PADDING));
} else {
// Neumann BC (no flux)
@@ -404,7 +445,6 @@ class Reactor_PFR extends Reactor {
/**
* Create finite difference first derivative operator.
* @returns {Array} - First derivative operator matrix.
*/
_makeDoperator() { // create gradient operator
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.
* @returns {Array} - Second derivative operator matrix.
*/
_makeD2operator() { // create the central second derivative operator
const D_size = this.n_x+2*BC_PADDING;
@@ -433,6 +472,9 @@ class Reactor_PFR extends Reactor {
return D2;
}
/**
* Constrains dispersion so that local Péclet number stays below 2. Needed for stable central differencing method.
*/
_constrainDispersion(D) {
const Dmin = math.sum(this.Fs) * this.d_x / (1.999 * this.A);
if (D < Dmin) {