run clang-format

Author: PENGYAN777

SU2_CFD/src/fluid/CCoolProp.cpp

@@ -1,39 +1,39 @@
 /*!
-* \file CCoolProp.cpp
-* \brief Source of the fluid model from CoolProp.
-* \author P. Yan, G. Gori, A. Guardone
-* \version 7.4.0 "Blackbird"
-*
-* SU2 Project Website: https://su2code.github.io
-*
-* The SU2 Project is maintained by the SU2 Foundation
-* (http://su2foundation.org)
-*
-* Copyright 2012-2022, SU2 Contributors (cf. AUTHORS.md)
-*
-* SU2 is free software; you can redistribute it and/or
-* modify it under the terms of the GNU Lesser General Public
-* License as published by the Free Software Foundation; either
-* version 2.1 of the License, or (at your option) any later version.
-*
-* SU2 is distributed in the hope that it will be useful,
-* but WITHOUT ANY WARRANTY; without even the implied warranty of
-* MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE. See the GNU
-* Lesser General Public License for more details.
-*
-* You should have received a copy of the GNU Lesser General Public
-* License along with SU2. If not, see <http://www.gnu.org/licenses/>.
-*/
+ * \file CCoolProp.cpp
+ * \brief Source of the fluid model from CoolProp.
+ * \author P. Yan, G. Gori, A. Guardone
+ * \version 7.5.1 "Blackbird"
+ *
+ * SU2 Project Website: https://su2code.github.io
+ *
+ * The SU2 Project is maintained by the SU2 Foundation
+ * (http://su2foundation.org)
+ *
+ * Copyright 2012-2023, SU2 Contributors (cf. AUTHORS.md)
+ *
+ * SU2 is free software; you can redistribute it and/or
+ * modify it under the terms of the GNU Lesser General Public
+ * License as published by the Free Software Foundation; either
+ * version 2.1 of the License, or (at your option) any later version.
+ *
+ * SU2 is distributed in the hope that it will be useful,
+ * but WITHOUT ANY WARRANTY; without even the implied warranty of
+ * MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE. See the GNU
+ * Lesser General Public License for more details.
+ *
+ * You should have received a copy of the GNU Lesser General Public
+ * License along with SU2. If not, see <http://www.gnu.org/licenses/>.
+ */
 
 #include "../../include/fluid/CCoolProp.hpp"
 
 #ifdef USE_COOLPROP
-#include "CoolProp.h"
 #include "AbstractState.h"
+#include "CoolProp.h"
 
 CCoolProp::CCoolProp(string fluidname) : CFluidModel() {
-  fluid_entity = std::unique_ptr<CoolProp::AbstractState>(CoolProp::AbstractState::factory("HEOS",fluidname));
-  Gas_Constant = fluid_entity->gas_constant()/fluid_entity->molar_mass();
+  fluid_entity = std::unique_ptr<CoolProp::AbstractState>(CoolProp::AbstractState::factory("HEOS", fluidname));
+  Gas_Constant = fluid_entity->gas_constant() / fluid_entity->molar_mass();
   Pressure_Critical = fluid_entity->p_critical();
   Temperature_Critical = fluid_entity->T_critical();
   acentric_factor = fluid_entity->acentric_factor();
@@ -58,28 +58,28 @@ void CCoolProp::SetTDState_rhoe(su2double rho, su2double e) {
   if (fluid_entity->phase() == 6) {
     // assume it is pure gas
     fluid_entity->specify_phase(CoolProp::iphase_gas);
-    if(abs(Pressure/Pressure_Critical-1)<0.01){
+    if (abs(Pressure / Pressure_Critical - 1) < 0.01) {
       // if P is very cloase to Pc, the CoolProp has issue
-      Pressure = Pressure_Critical*0.99;
+      Pressure = Pressure_Critical * 0.99;
     }
     fluid_entity->update(CoolProp::PT_INPUTS, Pressure, Temperature);
-    if(abs(fluid_entity->rhomass()/Density-1)*100 < 1){
+    if (abs(fluid_entity->rhomass() / Density - 1) * 100 < 1) {
       // origial phase is near saturation gas, then just compute sound speed
       SoundSpeed2 = pow(fluid_entity->speed_sound(), 2);
     }
-    else{
+    else {
       // original phase is not near saturation gas, then specify the phase as gas phase
       fluid_entity->specify_phase(CoolProp::iphase_gas);
-      SetTDState_PT(Pressure,Temperature);
+      SetTDState_PT(Pressure, Temperature);
     }
   }
-  else{
+  else {
     SoundSpeed2 = pow(fluid_entity->speed_sound(), 2);
   }
 }
 
 void CCoolProp::SetTDState_PT(su2double P, su2double T) {
-  if(abs(P/Pressure_Critical-1)<0.01) {
+  if (abs(P / Pressure_Critical - 1) < 0.01) {
     P = Pressure_Critical * 0.99;
   }
   fluid_entity->update(CoolProp::PT_INPUTS, P, T);
@@ -89,17 +89,17 @@ void CCoolProp::SetTDState_PT(su2double P, su2double T) {
 }
 
 void CCoolProp::SetTDState_Prho(su2double P, su2double rho) {
-  if(abs(P/Pressure_Critical-1)<0.01){
-    P = Pressure_Critical*0.99;
+  if (abs(P / Pressure_Critical - 1) < 0.01) {
+    P = Pressure_Critical * 0.99;
   }
   fluid_entity->update(CoolProp::DmassP_INPUTS, rho, P);
   su2double e = fluid_entity->umass();
   SetTDState_rhoe(rho, e);
 }
 
-void CCoolProp::SetEnergy_Prho(su2double P, su2double rho){
-  if(abs(P/Pressure_Critical-1)<0.01){
-    P = Pressure_Critical*0.99;
+void CCoolProp::SetEnergy_Prho(su2double P, su2double rho) {
+  if (abs(P / Pressure_Critical - 1) < 0.01) {
+    P = Pressure_Critical * 0.99;
   }
   fluid_entity->update(CoolProp::DmassP_INPUTS, rho, P);
   StaticEnergy = fluid_entity->umass();
@@ -112,9 +112,9 @@ void CCoolProp::SetTDState_hs(su2double h, su2double s) {
   SetTDState_rhoe(rho, e);
 }
 
-void  CCoolProp::SetTDState_Ps(su2double P, su2double s) {
-  if(abs(P/Pressure_Critical-1)<0.01){
-    P = Pressure_Critical*0.99;
+void CCoolProp::SetTDState_Ps(su2double P, su2double s) {
+  if (abs(P / Pressure_Critical - 1) < 0.01) {
+    P = Pressure_Critical * 0.99;
   }
   fluid_entity->update(CoolProp::PSmass_INPUTS, P, s);
   su2double rho = fluid_entity->rhomass();
@@ -128,16 +128,19 @@ void CCoolProp::SetTDState_rhoT(su2double rho, su2double T) {
   SetTDState_rhoe(rho, e);
 }
 
-void  CCoolProp::ComputeDerivativeNRBC_Prho(su2double P, su2double rho) {
+void CCoolProp::ComputeDerivativeNRBC_Prho(su2double P, su2double rho) {
   SetTDState_Prho(P, rho);
-  dhdrho_P = fluid_entity->first_partial_deriv(CoolProp::iHmass,CoolProp::iDmass,CoolProp::iP);
-  dhdP_rho = fluid_entity->first_partial_deriv(CoolProp::iHmass,CoolProp::iP,CoolProp::iDmass);
-  dsdP_rho = fluid_entity->first_partial_deriv(CoolProp::iSmass,CoolProp::iP,CoolProp::iDmass);
-  dsdrho_P = fluid_entity->first_partial_deriv(CoolProp::iSmass,CoolProp::iDmass,CoolProp::iP);
+  dhdrho_P = fluid_entity->first_partial_deriv(CoolProp::iHmass, CoolProp::iDmass, CoolProp::iP);
+  dhdP_rho = fluid_entity->first_partial_deriv(CoolProp::iHmass, CoolProp::iP, CoolProp::iDmass);
+  dsdP_rho = fluid_entity->first_partial_deriv(CoolProp::iSmass, CoolProp::iP, CoolProp::iDmass);
+  dsdrho_P = fluid_entity->first_partial_deriv(CoolProp::iSmass, CoolProp::iDmass, CoolProp::iP);
 }
 
 #else
 CCoolProp::CCoolProp(string fluidname) {
-  SU2_MPI::Error("SU2 was not compiled with CoolProp (-Denable-coolprop=true). Note that CoolProp cannot be used with directdiff or autodiff", CURRENT_FUNCTION);
+  SU2_MPI::Error(
+      "SU2 was not compiled with CoolProp (-Denable-coolprop=true). Note that CoolProp cannot be used with directdiff "
+      "or autodiff",
+      CURRENT_FUNCTION);
 }
-#endif
+#endif