Cantera  3.0.0
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IdealMolalSoln.cpp
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1/**
2 * @file IdealMolalSoln.cpp
3 * ThermoPhase object for the ideal molal equation of
4 * state (see @ref thermoprops
5 * and class @link Cantera::IdealMolalSoln IdealMolalSoln@endlink).
6 *
7 * Definition file for a derived class of ThermoPhase that handles variable
8 * pressure standard state methods for calculating thermodynamic properties that
9 * are further based upon activities on the molality scale. The Ideal molal
10 * solution assumes that all molality-based activity coefficients are equal to
11 * one. This turns out, actually, to be highly nonlinear when the solvent
12 * densities get low.
13 */
14
15// This file is part of Cantera. See License.txt in the top-level directory or
16// at https://cantera.org/license.txt for license and copyright information.
17
20#include "cantera/thermo/PDSS.h"
22
23#include <iostream>
24
25namespace {
26double X_o_cutoff_default = 0.20;
27double gamma_o_min_default = 0.00001;
28double gamma_k_min_default = 10.0;
29double slopefCut_default = 0.6;
30double slopegCut_default = 0.0;
31double cCut_default = .05;
32}
33
34namespace Cantera
35{
36
37IdealMolalSoln::IdealMolalSoln(const string& inputFile, const string& id_) :
38 IMS_X_o_cutoff_(X_o_cutoff_default),
39 IMS_gamma_o_min_(gamma_o_min_default),
40 IMS_gamma_k_min_(gamma_k_min_default),
41 IMS_slopefCut_(slopefCut_default),
42 IMS_slopegCut_(slopegCut_default),
43 IMS_cCut_(cCut_default)
44{
45 initThermoFile(inputFile, id_);
46}
47
49{
51 return mean_X(m_tmpV);
52}
53
55{
57 return mean_X(m_tmpV);
58}
59
61{
63 return mean_X(m_tmpV);
64}
65
67{
69 return mean_X(m_tmpV);
70}
71
73{
75 return mean_X(m_tmpV);
76}
77
78// ------- Mechanical Equation of State Properties ------------------------
79
81{
83 double dd = meanMolecularWeight() / mean_X(m_tmpV);
85}
86
88{
89 return 0.0;
90}
91
93{
94 return 0.0;
95}
96
97// ------- Activities and Activity Concentrations
98
100{
101 if (m_formGC == 0) {
102 return Units(1.0); // dimensionless
103 } else {
104 // kmol/m^3 for bulk phases
105 return Units(1.0, 0, -static_cast<double>(nDim()), 0, 0, 0, 1);
106 }
107}
108
110{
111 if (m_formGC != 1) {
112 double c_solvent = standardConcentration();
113 getActivities(c);
114 for (size_t k = 0; k < m_kk; k++) {
115 c[k] *= c_solvent;
116 }
117 } else {
118 getActivities(c);
119 for (size_t k = 0; k < m_kk; k++) {
120 double c0 = standardConcentration(k);
121 c[k] *= c0;
122 }
123 }
124}
125
127{
128 switch (m_formGC) {
129 case 0:
130 return 1.0;
131 case 1:
132 return 1.0 / m_speciesMolarVolume[k];
133 case 2:
134 return 1.0 / m_speciesMolarVolume[0];
135 default:
136 throw CanteraError("IdealMolalSoln::standardConcentration",
137 "m_formGC is set to an incorrect value. \
138 Allowed values are 0, 1, and 2");
139 }
140}
141
142void IdealMolalSoln::getActivities(double* ac) const
143{
145
146 // Update the molality array, m_molalities(). This requires an update due to
147 // mole fractions
148 if (IMS_typeCutoff_ == 0) {
150 for (size_t k = 0; k < m_kk; k++) {
151 ac[k] = m_molalities[k];
152 }
153 double xmolSolvent = moleFraction(0);
154 // Limit the activity coefficient to be finite as the solvent mole
155 // fraction goes to zero.
156 xmolSolvent = std::max(m_xmolSolventMIN, xmolSolvent);
157 ac[0] = exp((xmolSolvent - 1.0)/xmolSolvent);
158 } else {
159
161
162 // Now calculate the array of activities.
163 for (size_t k = 1; k < m_kk; k++) {
164 ac[k] = m_molalities[k] * exp(IMS_lnActCoeffMolal_[k]);
165 }
166 double xmolSolvent = moleFraction(0);
167 ac[0] = exp(IMS_lnActCoeffMolal_[0]) * xmolSolvent;
168 }
169}
170
172{
173 if (IMS_typeCutoff_ == 0) {
174 for (size_t k = 0; k < m_kk; k++) {
175 acMolality[k] = 1.0;
176 }
177 double xmolSolvent = moleFraction(0);
178 // Limit the activity coefficient to be finite as the solvent mole
179 // fraction goes to zero.
180 xmolSolvent = std::max(m_xmolSolventMIN, xmolSolvent);
181 acMolality[0] = exp((xmolSolvent - 1.0)/xmolSolvent) / xmolSolvent;
182 } else {
184 std::copy(IMS_lnActCoeffMolal_.begin(), IMS_lnActCoeffMolal_.end(), acMolality);
185 for (size_t k = 0; k < m_kk; k++) {
186 acMolality[k] = exp(acMolality[k]);
187 }
188 }
189}
190
191// ------ Partial Molar Properties of the Solution -----------------
192
194{
195 // First get the standard chemical potentials. This requires updates of
196 // standard state as a function of T and P These are defined at unit
197 // molality.
199
200 // Update the molality array, m_molalities(). This requires an update due to
201 // mole fractions
203
204 // get the solvent mole fraction
205 double xmolSolvent = moleFraction(0);
206
207 if (IMS_typeCutoff_ == 0 || xmolSolvent > 3.* IMS_X_o_cutoff_/2.0) {
208 for (size_t k = 1; k < m_kk; k++) {
209 double xx = std::max(m_molalities[k], SmallNumber);
210 mu[k] += RT() * log(xx);
211 }
212
213 // Do the solvent
214 // -> see my notes
215 double xx = std::max(xmolSolvent, SmallNumber);
216 mu[0] += (RT() * (xmolSolvent - 1.0) / xx);
217 } else {
218 // Update the activity coefficients. This also updates the internal
219 // molality array.
221
222 for (size_t k = 1; k < m_kk; k++) {
223 double xx = std::max(m_molalities[k], SmallNumber);
224 mu[k] += RT() * (log(xx) + IMS_lnActCoeffMolal_[k]);
225 }
226 double xx = std::max(xmolSolvent, SmallNumber);
227 mu[0] += RT() * (log(xx) + IMS_lnActCoeffMolal_[0]);
228 }
229}
230
232{
233 getEnthalpy_RT(hbar);
234 for (size_t k = 0; k < m_kk; k++) {
235 hbar[k] *= RT();
236 }
237}
238
240{
241 getIntEnergy_RT(ubar);
242 for (size_t k = 0; k < m_kk; k++) {
243 ubar[k] *= RT();
244 }
245}
246
248{
249 getEntropy_R(sbar);
251 if (IMS_typeCutoff_ == 0) {
252 for (size_t k = 1; k < m_kk; k++) {
253 double mm = std::max(SmallNumber, m_molalities[k]);
254 sbar[k] -= GasConstant * log(mm);
255 }
256 double xmolSolvent = moleFraction(0);
257 sbar[0] -= (GasConstant * (xmolSolvent - 1.0) / xmolSolvent);
258 } else {
259 // Update the activity coefficients, This also update the internally
260 // stored molalities.
262
263 // First we will add in the obvious dependence on the T term out front
264 // of the log activity term
265 double mm;
266 for (size_t k = 1; k < m_kk; k++) {
267 mm = std::max(SmallNumber, m_molalities[k]);
268 sbar[k] -= GasConstant * (log(mm) + IMS_lnActCoeffMolal_[k]);
269 }
270 double xmolSolvent = moleFraction(0);
271 mm = std::max(SmallNumber, xmolSolvent);
272 sbar[0] -= GasConstant *(log(mm) + IMS_lnActCoeffMolal_[0]);
273 }
274}
275
277{
278 getStandardVolumes(vbar);
279}
280
281void IdealMolalSoln::getPartialMolarCp(double* cpbar) const
282{
283 // Get the nondimensional Gibbs standard state of the species at the T and P
284 // of the solution.
285 getCp_R(cpbar);
286 for (size_t k = 0; k < m_kk; k++) {
287 cpbar[k] *= GasConstant;
288 }
289}
290
291// -------------- Utilities -------------------------------
292
293bool IdealMolalSoln::addSpecies(shared_ptr<Species> spec)
294{
295 bool added = MolalityVPSSTP::addSpecies(spec);
296 if (added) {
297 m_speciesMolarVolume.push_back(0.0);
298 m_tmpV.push_back(0.0);
299 IMS_lnActCoeffMolal_.push_back(0.0);
300 }
301 return added;
302}
303
305{
307
308 if (m_input.hasKey("standard-concentration-basis")) {
309 setStandardConcentrationModel(m_input["standard-concentration-basis"].asString());
310 }
311 if (m_input.hasKey("cutoff")) {
312 auto& cutoff = m_input["cutoff"].as<AnyMap>();
313 setCutoffModel(cutoff.getString("model", "none"));
314 IMS_gamma_o_min_ = cutoff.getDouble("gamma_o", gamma_o_min_default);
315 IMS_gamma_k_min_ = cutoff.getDouble("gamma_k", gamma_k_min_default);
316 IMS_X_o_cutoff_ = cutoff.getDouble("X_o", X_o_cutoff_default);
317 IMS_cCut_ = cutoff.getDouble("c_0", cCut_default);
318 IMS_slopefCut_ = cutoff.getDouble("slope_f", slopefCut_default);
319 IMS_slopegCut_ = cutoff.getDouble("slope_g", slopegCut_default);
320 }
321
322 for (size_t k = 0; k < nSpecies(); k++) {
323 m_speciesMolarVolume[k] = providePDSS(k)->molarVolume();
324 }
325 if (IMS_typeCutoff_ == 2) {
327 }
328 setMoleFSolventMin(1.0E-5);
329}
330
332{
334
335 // "solvent-molar-volume" (m_formGC == 2) is the default, and can be omitted
336 if (m_formGC == 0) {
337 phaseNode["standard-concentration-basis"] = "unity";
338 } else if (m_formGC == 1) {
339 phaseNode["standard-concentration-basis"] = "species-molar-volume";
340 }
341
342 AnyMap cutoff;
343 if (IMS_typeCutoff_ == 1) {
344 cutoff["model"] = "poly";
345 } else if (IMS_typeCutoff_ == 2) {
346 cutoff["model"] = "polyexp";
347 }
348
349 if (IMS_gamma_o_min_ != gamma_o_min_default) {
350 cutoff["gamma_o"] = IMS_gamma_o_min_;
351 }
352 if (IMS_gamma_k_min_ != gamma_k_min_default) {
353 cutoff["gamma_k"] = IMS_gamma_k_min_;
354 }
355 if (IMS_X_o_cutoff_ != X_o_cutoff_default) {
356 cutoff["X_o"] = IMS_X_o_cutoff_;
357 }
358 if (IMS_cCut_ != cCut_default) {
359 cutoff["c_0"] = IMS_cCut_;
360 }
361 if (IMS_slopefCut_ != slopefCut_default) {
362 cutoff["slope_f"] = IMS_slopefCut_;
363 }
364 if (IMS_slopegCut_ != slopegCut_default) {
365 cutoff["slope_g"] = IMS_slopegCut_;
366 }
367
368 if (cutoff.size()) {
369 phaseNode["cutoff"] = std::move(cutoff);
370 }
371}
372
374{
375 if (caseInsensitiveEquals(model, "unity")) {
376 m_formGC = 0;
377 } else if (caseInsensitiveEquals(model, "species-molar-volume")
378 || caseInsensitiveEquals(model, "molar_volume")) {
379 m_formGC = 1;
380 } else if (caseInsensitiveEquals(model, "solvent-molar-volume")
381 || caseInsensitiveEquals(model, "solvent_volume")) {
382 m_formGC = 2;
383 } else {
384 throw CanteraError("IdealMolalSoln::setStandardConcentrationModel",
385 "Unknown standard concentration model '{}'", model);
386 }
387}
388
389void IdealMolalSoln::setCutoffModel(const string& model)
390{
391 if (caseInsensitiveEquals(model, "none")) {
392 IMS_typeCutoff_ = 0;
393 } else if (caseInsensitiveEquals(model, "poly")) {
394 IMS_typeCutoff_ = 1;
395 } else if (caseInsensitiveEquals(model, "polyexp")) {
396 IMS_typeCutoff_ = 2;
397 } else {
398 throw CanteraError("IdealMolalSoln::setCutoffModel",
399 "Unknown cutoff model '{}'", model);
400 }
401}
402
403// ------------ Private and Restricted Functions ------------------
404
406{
407 // Calculate the molalities. Currently, the molalities may not be current
408 // with respect to the contents of the State objects' data.
410
411 double xmolSolvent = moleFraction(0);
412 double xx = std::max(m_xmolSolventMIN, xmolSolvent);
413
414 if (IMS_typeCutoff_ == 0) {
415 for (size_t k = 1; k < m_kk; k++) {
416 IMS_lnActCoeffMolal_[k]= 0.0;
417 }
418 IMS_lnActCoeffMolal_[0] = - log(xx) + (xx - 1.0)/xx;
419 return;
420 } else if (IMS_typeCutoff_ == 1) {
421 if (xmolSolvent > 3.0 * IMS_X_o_cutoff_/2.0) {
422 for (size_t k = 1; k < m_kk; k++) {
423 IMS_lnActCoeffMolal_[k]= 0.0;
424 }
425 IMS_lnActCoeffMolal_[0] = - log(xx) + (xx - 1.0)/xx;
426 return;
427 } else if (xmolSolvent < IMS_X_o_cutoff_/2.0) {
428 double tmp = log(xx * IMS_gamma_k_min_);
429 for (size_t k = 1; k < m_kk; k++) {
430 IMS_lnActCoeffMolal_[k]= tmp;
431 }
433 return;
434 } else {
435 // If we are in the middle region, calculate the connecting polynomials
436 double xminus = xmolSolvent - IMS_X_o_cutoff_/2.0;
437 double xminus2 = xminus * xminus;
438 double xminus3 = xminus2 * xminus;
439 double x_o_cut2 = IMS_X_o_cutoff_ * IMS_X_o_cutoff_;
440 double x_o_cut3 = x_o_cut2 * IMS_X_o_cutoff_;
441
442 double h2 = 3.5 * xminus2 / IMS_X_o_cutoff_ - 2.0 * xminus3 / x_o_cut2;
443 double h2_prime = 7.0 * xminus / IMS_X_o_cutoff_ - 6.0 * xminus2 / x_o_cut2;
444
445 double h1 = (1.0 - 3.0 * xminus2 / x_o_cut2 + 2.0 * xminus3/ x_o_cut3);
446 double h1_prime = (- 6.0 * xminus / x_o_cut2 + 6.0 * xminus2/ x_o_cut3);
447
448 double h1_g = h1 / IMS_gamma_o_min_;
449 double h1_g_prime = h1_prime / IMS_gamma_o_min_;
450
451 double alpha = 1.0 / (exp(1.0) * IMS_gamma_k_min_);
452 double h1_f = h1 * alpha;
453 double h1_f_prime = h1_prime * alpha;
454
455 double f = h2 + h1_f;
456 double f_prime = h2_prime + h1_f_prime;
457
458 double g = h2 + h1_g;
459 double g_prime = h2_prime + h1_g_prime;
460
461 double tmp = (xmolSolvent/ g * g_prime + (1.0-xmolSolvent) / f * f_prime);
462 double lngammak = -1.0 - log(f) + tmp * xmolSolvent;
463 double lngammao =-log(g) - tmp * (1.0-xmolSolvent);
464
465 tmp = log(xmolSolvent) + lngammak;
466 for (size_t k = 1; k < m_kk; k++) {
467 IMS_lnActCoeffMolal_[k]= tmp;
468 }
469 IMS_lnActCoeffMolal_[0] = lngammao;
470 }
471 } else if (IMS_typeCutoff_ == 2) {
472 // Exponentials - trial 2
473 if (xmolSolvent > IMS_X_o_cutoff_) {
474 for (size_t k = 1; k < m_kk; k++) {
475 IMS_lnActCoeffMolal_[k]= 0.0;
476 }
477 IMS_lnActCoeffMolal_[0] = - log(xx) + (xx - 1.0)/xx;
478 return;
479 } else {
480 double xoverc = xmolSolvent/IMS_cCut_;
481 double eterm = std::exp(-xoverc);
482
483 double fptmp = IMS_bfCut_ - IMS_afCut_ / IMS_cCut_ - IMS_bfCut_*xoverc
484 + 2.0*IMS_dfCut_*xmolSolvent - IMS_dfCut_*xmolSolvent*xoverc;
485 double f_prime = 1.0 + eterm*fptmp;
486 double f = xmolSolvent + IMS_efCut_ + eterm * (IMS_afCut_ + xmolSolvent * (IMS_bfCut_ + IMS_dfCut_*xmolSolvent));
487
488 double gptmp = IMS_bgCut_ - IMS_agCut_ / IMS_cCut_ - IMS_bgCut_*xoverc
489 + 2.0*IMS_dgCut_*xmolSolvent - IMS_dgCut_*xmolSolvent*xoverc;
490 double g_prime = 1.0 + eterm*gptmp;
491 double g = xmolSolvent + IMS_egCut_ + eterm * (IMS_agCut_ + xmolSolvent * (IMS_bgCut_ + IMS_dgCut_*xmolSolvent));
492
493 double tmp = (xmolSolvent / g * g_prime + (1.0 - xmolSolvent) / f * f_prime);
494 double lngammak = -1.0 - log(f) + tmp * xmolSolvent;
495 double lngammao =-log(g) - tmp * (1.0-xmolSolvent);
496
497 tmp = log(xx) + lngammak;
498 for (size_t k = 1; k < m_kk; k++) {
499 IMS_lnActCoeffMolal_[k]= tmp;
500 }
501 IMS_lnActCoeffMolal_[0] = lngammao;
502 }
503 }
504}
505
507{
508 IMS_afCut_ = 1.0 / (std::exp(1.0) * IMS_gamma_k_min_);
509 IMS_efCut_ = 0.0;
510 bool converged = false;
511 for (int its = 0; its < 100 && !converged; its++) {
512 double oldV = IMS_efCut_;
513 IMS_afCut_ = 1.0 / (std::exp(1.0) * IMS_gamma_k_min_) - IMS_efCut_;
514 IMS_bfCut_ = IMS_afCut_ / IMS_cCut_ + IMS_slopefCut_ - 1.0;
515 IMS_dfCut_ = ((- IMS_afCut_/IMS_cCut_ + IMS_bfCut_ - IMS_bfCut_*IMS_X_o_cutoff_/IMS_cCut_)
516 /
518 double tmp = IMS_afCut_ + IMS_X_o_cutoff_*(IMS_bfCut_ + IMS_dfCut_ * IMS_X_o_cutoff_);
519 double eterm = std::exp(-IMS_X_o_cutoff_/IMS_cCut_);
520 IMS_efCut_ = - eterm * (tmp);
521 if (fabs(IMS_efCut_ - oldV) < 1.0E-14) {
522 converged = true;
523 }
524 }
525 if (!converged) {
526 throw CanteraError("IdealMolalSoln::calcCutoffParams_",
527 "failed to converge on the f polynomial");
528 }
529 converged = false;
530 double f_0 = IMS_afCut_ + IMS_efCut_;
531 double f_prime_0 = 1.0 - IMS_afCut_ / IMS_cCut_ + IMS_bfCut_;
532 IMS_egCut_ = 0.0;
533 for (int its = 0; its < 100 && !converged; its++) {
534 double oldV = IMS_egCut_;
535 double lng_0 = -log(IMS_gamma_o_min_) - f_prime_0 / f_0;
536 IMS_agCut_ = exp(lng_0) - IMS_egCut_;
537 IMS_bgCut_ = IMS_agCut_ / IMS_cCut_ + IMS_slopegCut_ - 1.0;
538 IMS_dgCut_ = ((- IMS_agCut_/IMS_cCut_ + IMS_bgCut_ - IMS_bgCut_*IMS_X_o_cutoff_/IMS_cCut_)
539 /
541 double tmp = IMS_agCut_ + IMS_X_o_cutoff_*(IMS_bgCut_ + IMS_dgCut_ *IMS_X_o_cutoff_);
542 double eterm = std::exp(-IMS_X_o_cutoff_/IMS_cCut_);
543 IMS_egCut_ = - eterm * (tmp);
544 if (fabs(IMS_egCut_ - oldV) < 1.0E-14) {
545 converged = true;
546 }
547 }
548 if (!converged) {
549 throw CanteraError("IdealMolalSoln::calcCutoffParams_",
550 "failed to converge on the g polynomial");
551 }
552}
553
554}
ThermoPhase object for the ideal molal equation of state (see Thermodynamic Properties and class Idea...
Declarations for the virtual base class PDSS (pressure dependent standard state) which handles calcul...
Headers for the factory class that can create known ThermoPhase objects (see Thermodynamic Properties...
A map of string keys to values whose type can vary at runtime.
Definition AnyMap.h:427
size_t size() const
Returns the number of elements in this map.
Definition AnyMap.h:622
bool hasKey(const string &key) const
Returns true if the map contains an item named key.
Definition AnyMap.cpp:1423
Base class for exceptions thrown by Cantera classes.
void calcIMSCutoffParams_()
Calculate parameters for cutoff treatments of activity coefficients.
double enthalpy_mole() const override
Molar enthalpy of the solution. Units: J/kmol.
double thermalExpansionCoeff() const override
The thermal expansion coefficient. Units: 1/K.
void getPartialMolarEnthalpies(double *hbar) const override
Returns an array of partial molar enthalpies for the species in the mixture.
void getChemPotentials(double *mu) const override
Get the species chemical potentials: Units: J/kmol.
double IMS_slopegCut_
Parameter in the polyExp cutoff treatment.
double IMS_gamma_o_min_
gamma_o value for the cutoff process at the zero solvent point
int IMS_typeCutoff_
Cutoff type.
IdealMolalSoln(const string &inputFile="", const string &id="")
Constructor for phase initialization.
void getParameters(AnyMap &phaseNode) const override
Store the parameters of a ThermoPhase object such that an identical one could be reconstructed using ...
void initThermo() override
Initialize the ThermoPhase object after all species have been set up.
vector< double > m_tmpV
vector of size m_kk, used as a temporary holding area.
void getActivityConcentrations(double *c) const override
This method returns an array of generalized concentrations.
void getPartialMolarVolumes(double *vbar) const override
vector< double > IMS_lnActCoeffMolal_
Logarithm of the molal activity coefficients.
void setStandardConcentrationModel(const string &model)
Set the standard concentration model.
double IMS_slopefCut_
Parameter in the polyExp cutoff treatment.
double isothermalCompressibility() const override
The isothermal compressibility. Units: 1/Pa.
double intEnergy_mole() const override
Molar internal energy of the solution: Units: J/kmol.
double entropy_mole() const override
Molar entropy of the solution. Units: J/kmol/K.
void calcDensity() override
Calculate the density of the mixture using the partial molar volumes and mole fractions as input.
void setCutoffModel(const string &model)
Set cutoff model. Must be one of 'none', 'poly', or 'polyExp'.
double IMS_gamma_k_min_
gamma_k minimum for the cutoff process at the zero solvent point
int m_formGC
The standard concentrations can have one of three different forms: 0 = 'unity', 1 = 'species-molar-vo...
vector< double > m_speciesMolarVolume
Species molar volume .
double cp_mole() const override
Molar heat capacity of the solution at constant pressure. Units: J/kmol/K.
void getActivities(double *ac) const override
Get the array of non-dimensional activities at the current solution temperature, pressure,...
double IMS_X_o_cutoff_
value of the solute mole fraction that centers the cutoff polynomials for the cutoff =1 process;
Units standardConcentrationUnits() const override
Returns the units of the "standard concentration" for this phase.
void getPartialMolarCp(double *cpbar) const override
Partial molar heat capacity of the solution:. UnitsL J/kmol/K.
double gibbs_mole() const override
Molar Gibbs function for the solution: Units J/kmol.
double standardConcentration(size_t k=0) const override
Return the standard concentration for the kth species.
bool addSpecies(shared_ptr< Species > spec) override
Add a Species to this Phase.
void getPartialMolarIntEnergies(double *hbar) const override
Returns an array of partial molar internal energies for the species in the mixture.
void s_updateIMS_lnMolalityActCoeff() const
This function will be called to update the internally stored natural logarithm of the molality activi...
void getMolalityActivityCoefficients(double *acMolality) const override
Get the array of non-dimensional molality-based activity coefficients at the current solution tempera...
void getPartialMolarEntropies(double *sbar) const override
Returns an array of partial molar entropies of the species in the solution.
void initThermo() override
Initialize the ThermoPhase object after all species have been set up.
double m_xmolSolventMIN
In any molality implementation, it makes sense to have a minimum solvent mole fraction requirement,...
vector< double > m_molalities
Current value of the molalities of the species in the phase.
void setMoleFSolventMin(double xmolSolventMIN)
Sets the minimum mole fraction in the molality formulation.
void calcMolalities() const
Calculates the molality of all species and stores the result internally.
bool addSpecies(shared_ptr< Species > spec) override
Add a Species to this Phase.
virtual double molarVolume() const
Return the molar volume at standard state.
Definition PDSS.cpp:63
void assignDensity(const double density_)
Set the internally stored constant density (kg/m^3) of the phase.
Definition Phase.cpp:718
size_t nSpecies() const
Returns the number of species in the phase.
Definition Phase.h:245
size_t m_kk
Number of species in the phase.
Definition Phase.h:947
size_t nDim() const
Returns the number of spatial dimensions (1, 2, or 3)
Definition Phase.h:646
double meanMolecularWeight() const
The mean molecular weight. Units: (kg/kmol)
Definition Phase.h:760
double moleFraction(size_t k) const
Return the mole fraction of a single species.
Definition Phase.cpp:545
double mean_X(const double *const Q) const
Evaluate the mole-fraction-weighted mean of an array Q.
Definition Phase.cpp:737
virtual void getParameters(AnyMap &phaseNode) const
Store the parameters of a ThermoPhase object such that an identical one could be reconstructed using ...
double RT() const
Return the Gas Constant multiplied by the current temperature.
void initThermoFile(const string &inputFile, const string &id)
Initialize a ThermoPhase object using an input file.
AnyMap m_input
Data supplied via setParameters.
A representation of the units associated with a dimensional quantity.
Definition Units.h:35
void getEntropy_R(double *sr) const override
Get the array of nondimensional Entropy functions for the standard state species at the current T and...
virtual void _updateStandardStateThermo() const
Updates the standard state thermodynamic functions at the current T and P of the solution.
void getStandardChemPotentials(double *mu) const override
Get the array of chemical potentials at unit activity for the species at their standard states at the...
void getCp_R(double *cpr) const override
Get the nondimensional Heat Capacities at constant pressure for the species standard states at the cu...
void getEnthalpy_RT(double *hrt) const override
Get the nondimensional Enthalpy functions for the species at their standard states at the current T a...
void getStandardVolumes(double *vol) const override
Get the molar volumes of the species standard states at the current T and P of the solution.
void getIntEnergy_RT(double *urt) const override
Returns the vector of nondimensional Internal Energies of the standard state species at the current T...
bool caseInsensitiveEquals(const string &input, const string &test)
Case insensitive equality predicate.
const double GasConstant
Universal Gas Constant [J/kmol/K].
Definition ct_defs.h:120
Namespace for the Cantera kernel.
Definition AnyMap.cpp:564
const double SmallNumber
smallest number to compare to zero.
Definition ct_defs.h:158
Contains declarations for string manipulation functions within Cantera.