refs #294: Corrected/unified abbreviation "w.r.t"/"wrt" --> "w.r.t."

Modelica/Fluid/Dissipation.mo

@@ -2992,7 +2992,7 @@ This record is used as <strong>input record</strong> for the heat transfer funct
         SI.ReynoldsNumber Re=max(Re_min, 4*abs(m_flow)/(PI*IN_con.d_hyd*IN_var.eta))
           "Reynolds number";
 
-        //mass flow rate boundaries for w.r.t flow regimes
+        //mass flow rate boundaries for w.r.t. flow regimes
         SI.MassFlowRate m_flow_smooth=Re_min*PI*IN_con.d_hyd*IN_var.eta/4;
 
         //SOURCE_1: p.357, diag. 6-1, sec. 2 / p.336, sec. 15 (turbulent regime + hydraulically rough):
@@ -3130,7 +3130,7 @@ This record is used as <strong>input record</strong> for the heat transfer funct
         TYP.LocalResistanceCoefficient zeta_LOC_sharp_turb=max(MIN, A1*B1*C1)
           "Local resistance coefficient for turbulent regime (Re > Re_turb_max)";
 
-        //SOURCE_1: p.357, diag. 6-1: pressure loss boundaries for w.r.t flow regimes
+        //SOURCE_1: p.357, diag. 6-1: pressure loss boundaries for w.r.t. flow regimes
         //IN_con.R_0/d_hyd <=3
         SI.AbsolutePressure dp_lam_max=(zeta_LOC_sharp_turb + A2/Re_lam_leave)*IN_var.rho
             /2*(Re_lam_leave*IN_var.eta/(IN_var.rho*d_hyd))^2
@@ -3175,7 +3175,7 @@ This record is used as <strong>input record</strong> for the heat transfer funct
             zeta_LOC_sharp_turb)))
           "Mean velocity in turbulent regime with independence on pressure loss coefficient (Re > Re_turb_max)";
 
-        //mean velocity under smooth conditions w.r.t flow regime
+        //mean velocity under smooth conditions w.r.t. flow regime
         SI.Velocity v_smooth=if dp < dp_lam_max then v_lam else if dp < dp_turb_min then
                   SMOOTH(
             dp_lam_max,
@@ -3332,7 +3332,7 @@ and <a href=\"modelica://Modelica.Fluid.Dissipation.PressureLoss.Bend.dp_curvedO
         TYP.LocalResistanceCoefficient zeta_LOC=max(MIN, 0.95*sin(PI/180*delta/2)^2
              + 2.05*sin(PI/180*delta/2)^4) "Local resistance coefficient";
 
-        //SOURCE_1: p.365: Correction w.r.t effect of Reynolds number in laminar regime
+        //SOURCE_1: p.365: Correction w.r.t. effect of Reynolds number in laminar regime
         Real B=24.8
           "Coefficient considering effect of Reynolds number on zeta_TOT";
         Real exp=0.263
@@ -3357,7 +3357,7 @@ and <a href=\"modelica://Modelica.Fluid.Dissipation.PressureLoss.Bend.dp_curvedO
             lambda_FRI_smooth))) + SMOOTH(Re_lam_min, Re_lam_leave, Re)
           "Correction factor for surface roughness";
 
-        //SOURCE_2: p.208, diag. 9.3: Correction w.r.t effect of Reynolds number
+        //SOURCE_2: p.208, diag. 9.3: Correction w.r.t. effect of Reynolds number
         Real CF_Re=SMOOTH(
             Re_turb_min,
             Re_turb_max,
@@ -3459,7 +3459,7 @@ Generally this function is numerically best used for the <strong>incompressible
         TYP.LocalResistanceCoefficient zeta_LOC=max(MIN, 0.95*sin(PI/180*delta/2)^2
              + 2.05*sin(PI/180*delta/2)^4) "Local resistance coefficient";
 
-        //SOURCE_1: p.365: Correction w.r.t effect of Reynolds number
+        //SOURCE_1: p.365: Correction w.r.t. effect of Reynolds number
         Real B=24.8
           "Coefficient considering effect of Reynolds number on zeta_TOT";
         Real exp=0.263 "Exponent for Reynolds number correction";
@@ -3532,7 +3532,7 @@ Generally this function is numerically best used for the <strong>incompressible
             dp_min,
             1/pow) "Mean velocity under laminar conditions";
 
-        //mean velocity under smooth conditions w.r.t flow regime
+        //mean velocity under smooth conditions w.r.t. flow regime
         SI.Velocity v_smooth=if abs(dp) > dp_turb_max then v_turb
             else if abs(dp) < dp_turb_min then v_lam
             else SMOOTH(
@@ -8126,7 +8126,7 @@ Note that the Darcy friction factor for a smooth surface <strong> lambda_FRI_smo
 </p>
 
 <p>
-The correction for surface roughness through <strong> CF_Fri </strong> is used only in the turbulent regime, where the fluid flow is influenced by surface asperities not covered by a laminar boundary layer. Here the correction according to friction starts at <strong> Re &ge; Re_lam_leave </strong> according to <em>[Idelchik 2006, p. 336, sec. 15]</em>. Here the end of the laminar regime is restricted to a Reynolds number smaller than 2e3 w.r.t <em>[VDI, p. Lac 6, fig. 16]</em>.
+The correction for surface roughness through <strong> CF_Fri </strong> is used only in the turbulent regime, where the fluid flow is influenced by surface asperities not covered by a laminar boundary layer. Here the correction according to friction starts at <strong> Re &ge; Re_lam_leave </strong> according to <em>[Idelchik 2006, p. 336, sec. 15]</em>. Here the end of the laminar regime is restricted to a Reynolds number smaller than 2e3 w.r.t. <em>[VDI, p. Lac 6, fig. 16]</em>.
 </p>
 
 <p>

Modelica/Media/R134a.mo

@@ -22,9 +22,9 @@ package R134a "R134a: Medium model for R134a"
         "Isobaric expansion coefficient";
       Modelica.SIunits.IsentropicExponent gamma "Isentropic exponent";
       Modelica.SIunits.DerPressureByTemperature pt
-        "Derivative of pressure wrt temperature";
+        "Derivative of pressure w.r.t. temperature";
       Modelica.SIunits.DerPressureByDensity pd
-        "Derivative of pressure wrt density";
+        "Derivative of pressure w.r.t. density";
 
     end PhaseBoundaryProperties;
 
@@ -39,8 +39,8 @@ package R134a "R134a: Medium model for R134a"
       Modelica.SIunits.SpecificEnthalpy h "Specific enthalpy";
       Modelica.SIunits.SpecificHeatCapacity cv
         "Specific heat capacity at constant volume";
-      Real pt "Derivative of pressure wrt temperature";
-      Real pd "Derivative of pressure wrt density";
+      Real pt "Derivative of pressure w.r.t. temperature";
+      Real pd "Derivative of pressure w.r.t. density";
       Real dpT "dp/dT derivative of saturation curve";
 
     end InverseDerivatives_rhoT;
@@ -750,7 +750,7 @@ the fundamental equation of state of Tillner-Roth and Baehr (1994) and the Maxwe
     end saturationTemperature_der_p;
 
     redeclare function extends bubbleDensity
-      "Density of liquid phase w.r.t saturation pressure | use setSat_p function for input"
+      "Density of liquid phase w.r.t. saturation pressure | use setSat_p function for input"
 
     protected
       constant Real dl_coef[:, :]=R134aData.dlcoef
@@ -781,7 +781,7 @@ the fundamental equation of state of Tillner-Roth and Baehr (1994) and the Maxwe
     end bubbleDensity;
 
     redeclare function extends dBubbleDensity_dPressure
-      "Derivative of liquid density in two-phase region w.r.t pressure"
+      "Derivative of liquid density in two-phase region w.r.t. pressure"
 
     protected
       constant Real dl_coef[:, :]=R134aData.dlcoef
@@ -809,14 +809,14 @@ the fundamental equation of state of Tillner-Roth and Baehr (1994) and the Maxwe
     end dBubbleDensity_dPressure;
 
     function dBubbleDensity_dPressure_der_sat
-      "Time derivative of liquid density in two-phase region w.r.t pressure"
+      "Time derivative of liquid density in two-phase region w.r.t. pressure"
       extends Modelica.Icons.Function;
 
       input SaturationProperties sat
         "Saturation properties | pressure is used for interpolation";
       input SaturationProperties der_sat "Derivative of saturation properties";
       output Real der_ddldp
-        "Time derivative of liquid density in two-phase region w.r.t pressure";
+        "Time derivative of liquid density in two-phase region w.r.t. pressure";
     protected
       constant Real dl_coef[:, :]=R134aData.dlcoef
         "Coefficients of cubic spline for d_liq(p)";
@@ -843,7 +843,7 @@ the fundamental equation of state of Tillner-Roth and Baehr (1994) and the Maxwe
     end dBubbleDensity_dPressure_der_sat;
 
     redeclare function extends dewDensity
-      "Density of vapor phase w.r.t saturation pressure | use setSat_p function for input"
+      "Density of vapor phase w.r.t. saturation pressure | use setSat_p function for input"
 
     protected
       constant Real dv_coef[:, :]=R134aData.dvcoef
@@ -873,7 +873,7 @@ the fundamental equation of state of Tillner-Roth and Baehr (1994) and the Maxwe
     end dewDensity;
 
     redeclare function extends dDewDensity_dPressure
-      "Derivative of vapor density in two-phase region w.r.t pressure"
+      "Derivative of vapor density in two-phase region w.r.t. pressure"
 
     protected
       constant Real dv_coef[:, :]=R134aData.dvcoef
@@ -901,14 +901,14 @@ the fundamental equation of state of Tillner-Roth and Baehr (1994) and the Maxwe
     end dDewDensity_dPressure;
 
     function dDewDensity_dPressure_der_sat
-      "Time derivative of vapor density in two-phase region w.r.t pressure"
+      "Time derivative of vapor density in two-phase region w.r.t. pressure"
       extends Modelica.Icons.Function;
 
       input SaturationProperties sat
         "Saturation properties | pressure is used for interpolation";
       input SaturationProperties der_sat "Derivative of saturation properties";
       output Real der_ddvdp
-        "Time derivative of vapor density in two-phase region w.r.t pressure";
+        "Time derivative of vapor density in two-phase region w.r.t. pressure";
     protected
       constant Real dv_coef[:, :]=R134aData.dvcoef
         "Coefficients of cubic spline for d_vap(p)";
@@ -935,7 +935,7 @@ the fundamental equation of state of Tillner-Roth and Baehr (1994) and the Maxwe
     end dDewDensity_dPressure_der_sat;
 
     redeclare function extends bubbleEnthalpy
-      "Specific enthalpy of liquid phase w.r.t saturation pressure | use setSat_p function for input"
+      "Specific enthalpy of liquid phase w.r.t. saturation pressure | use setSat_p function for input"
 
     protected
       constant Real hl_coef[:, :]=R134aData.hlcoef
@@ -966,7 +966,7 @@ the fundamental equation of state of Tillner-Roth and Baehr (1994) and the Maxwe
     end bubbleEnthalpy;
 
     redeclare function extends dBubbleEnthalpy_dPressure
-      "Derivative of liquid specific enthalpy in two-phase region w.r.t pressure"
+      "Derivative of liquid specific enthalpy in two-phase region w.r.t. pressure"
 
     protected
       constant Real hl_coef[:, :]=R134aData.hlcoef
@@ -994,14 +994,14 @@ the fundamental equation of state of Tillner-Roth and Baehr (1994) and the Maxwe
     end dBubbleEnthalpy_dPressure;
 
     function dBubbleEnthalpy_dPressure_der_sat
-      "Time derivative of liquid specific enthalpy in two-phase region w.r.t pressure"
+      "Time derivative of liquid specific enthalpy in two-phase region w.r.t. pressure"
       extends Modelica.Icons.Function;
 
       input SaturationProperties sat
         "Saturation properties | pressure is used for interpolation";
       input SaturationProperties der_sat "Derivative of saturation properties";
       output Real der_dhldp
-        "Time derivative of liquid specific enthalpy in two-phase region w.r.t pressure";
+        "Time derivative of liquid specific enthalpy in two-phase region w.r.t. pressure";
     protected
       constant Real hl_coef[:, :]=R134aData.hlcoef
         "Coefficients of cubic spline for h_liq(p)";
@@ -1028,7 +1028,7 @@ the fundamental equation of state of Tillner-Roth and Baehr (1994) and the Maxwe
     end dBubbleEnthalpy_dPressure_der_sat;
 
     redeclare function extends dewEnthalpy
-      "Specific enthalpy of vapor phase w.r.t saturation pressure | use setSat_p function for input"
+      "Specific enthalpy of vapor phase w.r.t. saturation pressure | use setSat_p function for input"
 
     protected
       constant Real hv_coef[:, :]=R134aData.hvcoef
@@ -1059,7 +1059,7 @@ the fundamental equation of state of Tillner-Roth and Baehr (1994) and the Maxwe
     end dewEnthalpy;
 
     redeclare function extends dDewEnthalpy_dPressure
-      "Derivative of vapor specific enthalpy in two-phase region w.r.t pressure"
+      "Derivative of vapor specific enthalpy in two-phase region w.r.t. pressure"
 
     protected
       constant Real hv_coef[:, :]=R134aData.hvcoef
@@ -1087,14 +1087,14 @@ the fundamental equation of state of Tillner-Roth and Baehr (1994) and the Maxwe
     end dDewEnthalpy_dPressure;
 
     function dDewEnthalpy_dPressure_der_sat
-      "Time derivative of vapor specific enthalpy in two-phase region w.r.t pressure"
+      "Time derivative of vapor specific enthalpy in two-phase region w.r.t. pressure"
       extends Modelica.Icons.Function;
 
       input SaturationProperties sat
         "Saturation properties | pressure is used for interpolation";
       input SaturationProperties der_sat "Derivative of saturation properties";
       output Real der_dhvdp
-        "Derivative of vapor specific enthalpy in two-phase region w.r.t pressure";
+        "Derivative of vapor specific enthalpy in two-phase region w.r.t. pressure";
     protected
       constant Real hv_coef[:, :]=R134aData.hvcoef
         "Coefficients of cubic spline for h_vap(p)";
@@ -1121,7 +1121,7 @@ the fundamental equation of state of Tillner-Roth and Baehr (1994) and the Maxwe
     end dDewEnthalpy_dPressure_der_sat;
 
     redeclare function extends dewEntropy
-      "Specific entropy of vapor phase w.r.t saturation pressure | use setSat_p function for input"
+      "Specific entropy of vapor phase w.r.t. saturation pressure | use setSat_p function for input"
 
     protected
       constant Real sv_coef[:, :]=R134aData.svcoef
@@ -1151,13 +1151,13 @@ the fundamental equation of state of Tillner-Roth and Baehr (1994) and the Maxwe
     end dewEntropy;
 
     function dDewEntropy_dPressure
-      "Derivative of vapor specific entropy in two-phase region w.r.t pressure | use setState_phX function for input"
+      "Derivative of vapor specific entropy in two-phase region w.r.t. pressure | use setState_phX function for input"
       extends Modelica.Icons.Function;
 
       input SaturationProperties sat
         "Saturation properties | pressure is used for interpolation";
       output Real dsvdp
-        "Derivative of vapor specific entropy in two-phase region w.r.t pressure";
+        "Derivative of vapor specific entropy in two-phase region w.r.t. pressure";
     protected
       constant Real sv_coef[:, :]=R134aData.svcoef
         "Coefficients of cubic spline for s_vap(p)";
@@ -1184,14 +1184,14 @@ the fundamental equation of state of Tillner-Roth and Baehr (1994) and the Maxwe
     end dDewEntropy_dPressure;
 
     function dDewEntropy_dPressure_der_sat
-      "Time derivative of vapor specific entropy in two-phase region w.r.t pressure | use setState_phX function for input"
+      "Time derivative of vapor specific entropy in two-phase region w.r.t. pressure | use setState_phX function for input"
       extends Modelica.Icons.Function;
 
       input SaturationProperties sat
         "Saturation properties | pressure is used for interpolation";
       input SaturationProperties der_sat "Derivative of saturation properties";
       output Real der_dsvdp
-        "Derivative of vapor specific entropy in two-phase region w.r.t pressure";
+        "Derivative of vapor specific entropy in two-phase region w.r.t. pressure";
     protected
       constant Real sv_coef[:, :]=R134aData.svcoef
         "Coefficients of cubic spline for s_liq(p)";
@@ -1218,7 +1218,7 @@ the fundamental equation of state of Tillner-Roth and Baehr (1994) and the Maxwe
     end dDewEntropy_dPressure_der_sat;
 
     redeclare function extends bubbleEntropy
-      "Specific entropy of liquid phase w.r.t saturation pressure | use setSat_p function for input"
+      "Specific entropy of liquid phase w.r.t. saturation pressure | use setSat_p function for input"
     protected
       constant Real sl_coef[:, :]=R134aData.slcoef
         "Coefficients of cubic spline for s_liq(p)";
@@ -1248,12 +1248,12 @@ the fundamental equation of state of Tillner-Roth and Baehr (1994) and the Maxwe
     end bubbleEntropy;
 
     function dBubbleEntropy_dPressure
-      "Derivative of liquid specific entropy in two-phase region w.r.t pressure | use setState_phX function for input"
+      "Derivative of liquid specific entropy in two-phase region w.r.t. pressure | use setState_phX function for input"
       extends Modelica.Icons.Function;
       input SaturationProperties sat
         "Saturation properties | pressure is used for interpolation";
       output Real dsldp
-        "Derivative of liquid specific entropy in two-phase region w.r.t pressure";
+        "Derivative of liquid specific entropy in two-phase region w.r.t. pressure";
     protected
       constant Real sl_coef[:, :]=R134aData.slcoef
         "Coefficients of cubic spline for s_liq(p)";
@@ -1280,13 +1280,13 @@ the fundamental equation of state of Tillner-Roth and Baehr (1994) and the Maxwe
     end dBubbleEntropy_dPressure;
 
     function dBubbleEntropy_dPressure_der_sat
-      "Time derivative of liquid specific entropy in two-phase region w.r.t pressure | use setState_phX function for input"
+      "Time derivative of liquid specific entropy in two-phase region w.r.t. pressure | use setState_phX function for input"
       extends Modelica.Icons.Function;
       input SaturationProperties sat
         "Saturation properties | pressure is used for interpolation";
       input SaturationProperties der_sat "Derivative of saturation properties";
       output Real der_dsldp
-        "Derivative of liquid specific entropy in two-phase region w.r.t pressure";
+        "Derivative of liquid specific entropy in two-phase region w.r.t. pressure";
     protected
       constant Real sl_coef[:, :]=R134aData.slcoef
         "Coefficients of cubic spline for s_liq(p)";