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IAPWS_IF97.m
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IAPWS_IF97.m
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function out = IAPWS_IF97(fun,in1,in2)
% IAPWS_IF97(FUN,IN1,IN2)
% 27 basic water functions of water properties, based on the International
% Association on Properties of Water and Steam Industrial Formulation 1997
% (IAPWS-IF97), IAPWS-IF97-S01, IAPWS-IF97-S03rev, IAPWS-IF97-S04,
% IAPWS-IF97-S05, Revised Advisory Note No. 3 Thermodynamic Derivatives from
% IAPWS Formulations 2008, Release on the IAPWS Formulation 2008 for the
% Viscosity of Ordinary Water Substance, 2008 Revised Release on the IAPWS
% Formulation 1985 for the Thermal Conductivity of Ordinary Water Substance.
%
% FUN is the desired function that may take 1 input, IN1, or 2 inputs, IN1
% and IN2. IN1 and IN2 can be scalar, column vector or matrix, and IN1 and
% IN2 should be the same size. If a row vector is entered, it is transposed.
% If a scalar is entered for one input and the other input is a vector or
% matrix, then the scalar is repeated to form a vector or matrix of the same
% size as the other input.
%
% FUN is a string that is formed by the property symbol, an underscore
% and the property symbols the function depends on. EG: 'k_pT' is thermal
% conductivity, 'k', as a function of pressure, 'p', and temperature,
% 'T'. Derivatives are formed by prefixing 'd' to the property symbol and
% suffixing 'd' + the property symbol to which the derivative is with
% respect. EG: 'dTdp_ph' is the derivative of temperature with respect to
% pressure as a function of pressure and enthalpy, 'h' at constant
% enthalpy. The exception to this rule is 'cp_ph' which is equivalent to
% 'dhdT_ph' or the derivative of temperature with respect to pressure as a
% function of pressure and enthalpy at constant pressure. All derivatives
% are with respect to pressure at constant enthalpy or v.v.
%
% Saturation is indicated by suffixing 'sat', saturated liquid 'L' and
% saturated vapor 'V'.
%
% FUN = [d]<property-symbol>[sat|L|V][d<property-symbol>]_<property-symbol>...
%
% Property Symbols:
% p - [MPa] pressure
% T - [K] temperature
% h - [kJ/kg] enthalpy
% v - [m^3/kg] specific volume the reciprocal of density, IE: v = 1/rho
% x - quality, mass fraction of liquid water in mixture
% k - [W/m/K] thermal conductivity
% mu - [Pa*s] viscosity
% cp - [kJ/kg/K] specific heat at constant pressure
%
% Basic funcitons:
% h_pT, v_pT, vL_p, vV_p, hL_p, hV_p, T_ph, v_ph, k_pT, k_ph, mu_pT, mu_ph,
% dhLdp_p, dhVdp_p, dvdp_ph, dvdh_ph, dTdp_ph, cp_ph, dmudh_ph, dmudp_ph,
% psat_T, Tsat_p, dTsatdpsat_p, x_ph, x_hT, x_pv, x_vT
%
% Example:
% >> press_rng = logspace(-2,2,300); % [MPa] pressure (p) range
% >> temp_rng = 273.15+linspace(1,800,300); % [K] temperature (T) range
% >> [p,T] = meshgrid(press_rng,temp_rng); % [MPa,K] mesh p & T
% >> h = IAPWS_IF97('h_pT',p,T); % [kJ/kg] enthalpy = f(p,T)
% >> psat = IAPWS_IF97('psat_T',temp_rng); % [MPa] saturation pressure
% >> psat = psat(~isnan(psat)); % trim out of range temperatures
% >> hLsat = IAPWS_IF97('hL_p',psat); % [kJ/kg] saturated liquid enthalpy
% >> hVsat = IAPWS_IF97('hV_p',psat); % [kJ/kg] saturated vapor enthalpy
% >> pcrit = 22.064; % [MPa] critical pressure
% >> hLcrit = IAPWS_IF97('hL_p',pcrit);hVcrit = IAPWS_IF97('hV_p',pcrit);
% >> Tcrit = IAPWS_IF97('Tsat_p',pcrit); hcrit = IAPWS_IF97('h_pT',pcrit,Tcrit);
% >> hVL = hVsat - hLsat; % [kJ/kg] heat of vaporization
% >> hX = hLsat*ones(1,9) + hVL*(0.1:0.1:0.9); % [kJ/kg] mixture enthalpy
%
% Reference: <a href="http://www.iapws.org/relguide/IF97-Rev.pdf">Revised IAPWS Industrial Formulation 1997</a>
%
% Copyright (c) 2013 Mark Mifofski
%% check inputs
seeHelp = 'See <a href="matlab: help IAPWS_IF97">help</a>.';
assert(nargin>1, 'IAPWS_IF97:noInput', ...
['Not enough inputs. ',seeHelp])
assert(any(strcmpi(fun,{'x_ph','x_hT','x_pv','x_vT', ... (4)
'k_pT','k_ph','mu_pT','mu_ph', ... (4)
'dmudh_ph','dmudp_ph','dhLdp_p','dhVdp_p','dvLdp_p','dvVdp_p', ... (6)
'dvdp_ph','dvdh_ph','dTdp_ph','cp_ph', ... (4)
'h_pT','v_pT','vL_p','vV_p','hL_p','hV_p','T_ph','v_ph', ... (8)
'psat_T','Tsat_p','dTsatdpsat_p', ... (3)
'h1_pT','h2_pT','h3_rhoT','v1_pT','v2_pT', ... (5)
'cp1_pT','cp2_pT','cp3_rhoT','cv3_rhoT', ... (4)
'alphav1_pT','alphav2_pT','alphap3_rhoT', ... (3)
'betap3_rhoT','kappaT1_pT','kappaT2_pT',... (3)
'dgammadtau1_pT','dgammadpi1_pT','dgammadtautau1_pT','dgammadpipi1_pT','dgammadpitau1_pT', ... (5)
'dgammadtau2_pT','dgammadpi2_pT','dgammadtautau2_pT','dgammadpipi2_pT','dgammadpitau2_pT', ... (5)
'dphidtau3_rhoT','dphiddelta3_rhoT','dphidtautau3_rhoT','dphiddeltatau3_rhoT','dphiddeltadelta3_rhoT', ... (5)
'T1_ph','T2a_ph','T2b_ph','T2c_ph','T3a_ph','T3b_ph','v3a_ph','v3b_ph', ... (8)
'h2bc_p','h3ab_p','TB23_p','pB23_T','p3sat_h','v3a_pT','v3b_pT','v3c_pT', ... (8)
'v3d_pT','v3e_pT','v3f_pT','v3g_pT','v3h_pT','v3i_pT','v3j_pT','v3k_pT', ... (8)
'v3l_pT','v3m_pT','v3n_pT','v3o_pT','v3p_pT','v3q_pT','v3r_pT','v3s_pT', ... (8)
'v3t_pT','v3u_pT','v3v_pT','v3w_pT','v3x_pT','v3y_pT','v3z_pT','T3ab_p', ... (8)
'T3cd_p','T3ef_p','T3gh_p','T3ij_p','T3jk_p','T3mn_p','T3op_p','T3qu_p','T3rx_p','T3uv_p','T3wx_p', ... (11)
'd2gammadtau2_pT','d2gammadpi2_pT','d2gammadtautau2_pT','d2gammadpipi2_pT','d2gammadpitau2_pT',...
'w1_pT','w2_pT','u1_pT','u2_pT','cv1_pT','cv2_pT',...
'gamma1_pT','gamma2_pT','s1_pT','s2_pT','phi3_rhoT'})),...
'IAPWS_IF97:noInput', ['Sorry, %s is not a valid IAPWS_IF97 function. ',seeHelp],fun)
% assert(any(strcmpi(fun,{'x_ph','x_hT','x_pv','x_vT', ... (4)
% 'k_pT','k_ph','mu_pT','mu_ph', ... (4)
% 'dmudh_ph','dmudp_ph','dhLdp_p','dhVdp_p','dvLdp_p','dvVdp_p', ... (6)
% 'dvdp_ph','dvdh_ph','dTdp_ph','cp_ph', ... (4)
% 'h_pT','v_pT','vL_p','vV_p','hL_p','hV_p','T_ph','v_ph', ... (8)
% 'psat_T','Tsat_p','dTsatdpsat_p', ... (3)
% 'h1_pT','h2_pT','h3_rhoT','v1_pT','v2_pT', ... (5)
% 'cp1_pT','cp2_pT','cp3_rhoT','cv3_rhoT', ... (4)
% 'alphav1_pT','alphav2_pT','alphap3_rhoT', ... (3)
% 'betap3_rhoT','kappaT1_pT','kappaT2_pT',... (3)
% 'dgammadtau1_pT','dgammadpi1_pT','dgammadtautau1_pT','dgammadpipi1_pT','dgammadpitau1_pT', ... (5)
% 'dgammadtau2_pT','dgammadpi2_pT','dgammadtautau2_pT','dgammadpipi2_pT','dgammadpitau2_pT', ... (5)
% 'dphidtau3_rhoT','dphiddelta3_rhoT','dphidtautau3_rhoT','dphiddeltatau3_rhoT','dphiddeltadelta3_rhoT', ... (5)
% 'T1_ph','T2a_ph','T2b_ph','T2c_ph','T3a_ph','T3b_ph','v3a_ph','v3b_ph', ... (8)
% 'h2bc_p','h3ab_p','TB23_p','pB23_T','p3sat_h','v3a_pT','v3b_pT','v3c_pT', ... (8)
% 'v3d_pT','v3e_pT','v3f_pT','v3g_pT','v3h_pT','v3i_pT','v3j_pT','v3k_pT', ... (8)
% 'v3l_pT','v3m_pT','v3n_pT','v3o_pT','v3p_pT','v3q_pT','v3r_pT','v3s_pT', ... (8)
% 'v3t_pT','v3u_pT','v3v_pT','v3w_pT','v3x_pT','v3y_pT','v3z_pT','T3ab_p', ... (8)
% 'T3cd_p','T3ef_p','T3gh_p','T3ij_p','T3jk_p','T3mn_p','T3op_p','T3qu_p','T3rx_p','T3uv_p','T3wx_p'})), ... (11)
% 'IAPWS_IF97:noInput', ['Sorry, %s is not a valid IAPWS_IF97 function. ',seeHelp],fun)
if nargin==2
dim = size(in1);
if length(dim)>2,out = NaN;return,end
if dim(1)==1 && dim(2)>1,in1 = in1';end
out = feval(fun,in1);
end
if nargin==3
dim1 = size(in1);dim2 = size(in2);
if length(dim1)>2 || length(dim2)>2,out = NaN;return,end
if any(dim1~=dim2);
if dim1==ones(1,2),in1 = in1*ones(dim2);dim1=dim2;
elseif dim2==ones(1,2),in2 = in2*ones(dim1);
elseif dim1==fliplr(dim2),in1 = in1';dim1=dim2;
else out = NaN;return
end
end
if dim1(1)==1 && dim1(2)>1,in1 = in1';in2 = in2';end
out = feval(fun,in1,in2);
end
end
%% suppress definition not used for this entire file
%#ok<*DEFNU>
%% quality
function x = x_ph(p,h)
x = (h - hL_p(p))./(hV_p(p) - hL_p(p));
end
function x = x_hT(h,T)
x = (h - hL_p(psat_T(T)))./(hV_p(psat_T(T)) - hL_p(psat_T(T)));
end
function x = x_pv(p,v)
x = (v - vL_p(p))./(vV_p(p) - vL_p(p));
end
function x = x_vT(v,T)
x = (v - vL_p(psat_T(T)))./(vV_p(psat_T(T)) - vL_p(psat_T(T)));
end
%% stand alone functions
function k = k_pT(p,T)
% k = k_pT(p,T)
% thermal conductivity, k [W/m/K], as a function of pressure, p [MPa], and temperature, T [K]
% based on Revised Release on the IAPWS Formulation 1985 for the Thermal Conductivity of Ordinary Water Substance, 2008
% Reference: http://www.iapws.org/
% June 23, 2009
% Mark Mikofski
%% size of inputs
dim = size(p);
initnan = NaN(dim);
k = initnan;
%% constants and calculated
Tstar = 647.26; % [K]
rhostar = 317.7; % [K]
kstar = 1; % [W/m/K]
a = [0.0102811, 0.0299621, 0.0156146, -0.00422464];
b = [-0.397070, 0.400302, 1.060000];
B = [-0.171587, 2.392190];
d = [0.0701309, 0.0118520, 0.00169937, -1.0200];
C = [0.642857, -4.11717, -6.17937, 0.00308976, 0.0822994, 10.0932];
Tmin = 273.16; % [K] minimum temperature is triple point
TB13 = 623.15; % [K] temperature at boundary between region 1 and 3
TB23 = 863.15; % [K] temperature of boundary between region 2 and 3
Tmax = 1073.15; % [K] maximum valid temperature
pmin = psat_T(Tmin); % [MPa] minimum pressure is 611.657 Pa
pmax = 100; % [MPa] maximum valid pressure
psat = psat_T(T); % [MPa] saturation pressures
pB23 = initnan; valid = T>=TB13 & T<=TB23;
pB23(valid) = pB23_T(T(valid)); % [MPa] pressure on boundary between region 2 and region 3
%% valid ranges
valid1 = p>=psat & p<=pmax & T>=Tmin & T<=TB13; % valid range for region 1, include B13 in region 1
valid2 = p>=pmin & ((T>=Tmin & T<=TB13 & p<=psat) | (T>TB13 & T<=TB23 & p<=pB23) | (T>TB23 & T<=Tmax & p<=pmax)); % valid range for region 2, include B23 in region 2
valid3 = p>pB23 & p<=pmax & T>TB13 & T<TB23;
% [valid1 valid2 valid3]
if any(any(valid1))
T1 = T(valid1);rho1bar = 1./v1_pT(p(valid1),T1)/rhostar;T1bar = T1/Tstar;
k0 = sqrt(T1bar).*(a(1) + (a(2) + (a(3) + a(4).*T1bar).*T1bar).*T1bar);
k1 = b(1) + b(2)*rho1bar + b(3)*exp(B(1)*(rho1bar + B(2)).^2);
deltaTbar = abs(T1bar-1)+C(4);Q = 2 + C(5)./deltaTbar.^0.6;S = (1./deltaTbar).*(T1bar>=1) + (C(6)./deltaTbar.^0.6).*(T1bar<1);
k2 = (d(1)./T1bar.^10 + d(2)).*rho1bar.^1.8.*exp(C(1)*(1-rho1bar.^2.8)) + d(3)*S.*rho1bar.^Q.*exp(Q./(1+Q).*(1-rho1bar.^(1+Q))) + d(4)*exp(C(2)*T1bar.^1.5 + C(3)./rho1bar.^5);
k(valid1) = (k0+k1+k2)*kstar;
end
if any(any(valid2))
T2 = T(valid2);rho2bar = 1./v2_pT(p(valid2),T2)/rhostar;T2bar = T2/Tstar;
k0 = sqrt(T2bar).*(a(1) + (a(2) + (a(3) + a(4).*T2bar).*T2bar).*T2bar);
k1 = b(1) + b(2)*rho2bar + b(3)*exp(B(1)*(rho2bar + B(2)).^2);
deltaTbar = abs(T2bar-1)+C(4);Q = 2 + C(5)./deltaTbar.^0.6;S = (1./deltaTbar).*(T2bar>=1) + (C(6)./deltaTbar.^0.6).*(T2bar<1);
k2 = (d(1)./T2bar.^10 + d(2)).*rho2bar.^1.8.*exp(C(1)*(1-rho2bar.^2.8)) + d(3)*S.*rho2bar.^Q.*exp(Q./(1+Q).*(1-rho2bar.^(1+Q))) + d(4)*exp(C(2)*T2bar.^1.5 + C(3)./rho2bar.^5);
k(valid2) = (k0+k1+k2)*kstar;
end
if any(any(valid3))
T3 = T(valid3);rho3bar = 1./v_pT(p(valid3),T3)/rhostar;T3bar = T3/Tstar;
k0 = sqrt(T3bar).*(a(1) + (a(2) + (a(3) + a(4).*T3bar).*T3bar).*T3bar);
k1 = b(1) + b(2)*rho3bar + b(3)*exp(B(1)*(rho3bar + B(2)).^2);
deltaTbar = abs(T3bar-1)+C(4);Q = 2 + C(5)./deltaTbar.^0.6;S = (1./deltaTbar).*(T3bar>=1) + (C(6)./deltaTbar.^0.6).*(T3bar<1);
k2 = (d(1)./T3bar.^10 + d(2)).*rho3bar.^1.8.*exp(C(1)*(1-rho3bar.^2.8)) + d(3)*S.*rho3bar.^Q.*exp(Q./(1+Q).*(1-rho3bar.^(1+Q))) + d(4)*exp(C(2)*T3bar.^1.5 + C(3)./rho3bar.^5);
k(valid3) = (k0+k1+k2)*kstar;
end
end
function k = k_ph(p,h)
% k = k_ph(p,h)
% thermal conductivity, k [W/m/K], as a function of pressure, p [MPa], and enthalpy, h [kJ/kg]
% based on Revised Release on the IAPWS Formulation 1985 for the Thermal Conductivity of Ordinary Water Substance, 2008
% Reference: http://www.iapws.org/
% June 23, 2009
% Mark Mikofski
%% size of inputs
dim = size(p);
initnan = NaN(dim);
k = initnan;
%% constants and calculated
Tstar = 647.26; % [K]
rhostar = 317.7; % [K]
kstar = 1; % [W/m/K]
a = [0.0102811, 0.0299621, 0.0156146, -0.00422464];
b = [-0.397070, 0.400302, 1.060000];
B = [-0.171587, 2.392190];
d = [0.0701309, 0.0118520, 0.00169937, -1.0200];
C = [0.642857, -4.11717, -6.17937, 0.00308976, 0.0822994, 10.0932];
Tmin = 273.16; % [K] minimum temperature is triple point
T2bcsat = 554.485; % [K] saturation temperature at 5.85 kJ/kg/K isentropic line between region 2b and 2c
TB13 = 623.15; % [K] temperature at boundary between region 1 and 3
Tmax = 1073.15; % [K] maximum temperature
pmin = psat_T(Tmin); % [MPa] minimum pressure is 611.657 Pa
p2ab = 4; % [MPa] pressure along boundary between region 2a and 2b
p2bcsat = psat_T(T2bcsat); % [MPa] saturation pressure at 5.85 kJ/kg/K isentropic line between region 2b and 2c
pB13sat = psat_T(TB13); % [MPa] saturation pressure at boundary between region 1 and 3, 16.5291643 MPa
pmax = 100; % [MPa] maximum pressure
h1B13L = h1_pT(pB13sat,TB13); % [kJ/kg] saturated liquid enthalpy at boundary between region 1, region 3 and region 4
h2B13V = h2_pT(pB13sat,TB13); % [kJ/kg] saturated vapor enthalpy at boundary between region 2, region 3 and region 4
%% calculated matrices
Tsat = Tsat_p(p); % [K] saturation temperatures
h1min = initnan;h2max = initnan;valid = p>=pmin & p<=pmax;pvalid = p(valid); % initialize matricies with NaN and set valid range of parameters
if any(any(valid))
Tmin = Tmin*ones(dim);Tmax = Tmax*ones(dim); % copy to matrix of size dim
h1min(valid) = h1_pT(pvalid,Tmin(valid)); % [kJ/kg] minimum enthalpies
h2max(valid) = h2_pT(pvalid,Tmax(valid)); % [kJ/kg] maximum enthalpies in region 2
end
h1L = initnan;h2V = initnan;valid = p>=pmin & p<=pB13sat;pvalid = p(valid); % initialize matricies with NaN and set valid range of parameters
if any(any(valid))
h1L(valid) = h1_pT(pvalid,Tsat(valid)); % [kJ/kg] saturated liquid enthalpies in region 1
h2V(valid) = h2_pT(pvalid,Tsat(valid)); % [kJ/kg] saturated vapor enthalpies in region 2
end
h1B13 = initnan;h3ab = initnan;h2B23 = initnan;valid = p>=pB13sat & p<=pmax;pvalid = p(valid); % initialize matricies with NaN and set valid range of parameters
if any(any(valid))
TB13 = TB13*ones(dim); % copy to matrix of size dim
h1B13(valid) = h1_pT(pvalid,TB13(valid)); % [kJ/kg] enthalpies on boundary between region 1 and region 3
h3ab(valid) = h3ab_p(pvalid); % [kJ/kg] enthalpies on critical entropy isentropic line between regions 3a and region 3b
h2B23(valid) = h2_pT(pvalid,TB23_p(pvalid)); % [kJ/kg] enthalpies on boundary between region 2 and region 3
end
h2bc = initnan;valid = p>=p2bcsat & p<=pmax; % initialize matricies with NaN and set valid range of parameters
h2bc(valid) = h2bc_p(p(valid)); % [kJ/kg] enthalpies on boundary between region 2b and 2c
p3sat = pB13sat*ones(dim);valid = h>=h1B13L & h<=h2B13V; % % do NOT use NaN to initialize p3sat, b/c for h<h1B13L or h>h2B13V p>NaN = 0, instead use pB13sat
if any(any(valid))
p3sat(valid) = p3sat_h(h(valid)); % [MPa] saturation pressure on boundary between region 3 and 4
end
%% valid ranges
valid1 = (p>=pmin & p<=pB13sat & h>=h1min & h<=h1L) | (p>pB13sat & p<=pmax & h>=h1min & h<=h1B13); % valid range for region 1
valid2a = p>=pmin & p<=p2ab & h>h2V & h<=h2max; % valid range for region 2a
valid2b = (p>p2ab & p<=p2bcsat & h>h2V & h<=h2max) | (p>p2bcsat & p<=pmax & h>h2bc & h<=h2max); % valid range for region 2b
valid2c = (p>p2bcsat & p<=pB13sat & h>h2V & h<=h2bc) | (p>pB13sat & p<=pmax & h>h2B23 & h<=h2bc); % valid range for region 2c
valid3a = p>p3sat & p<=pmax & h>h1B13 & h<=h3ab; % valid range for region 3a
valid3b = p>p3sat & p<=pmax & h>h3ab & h<=h2B23; % valid range for region 3b
valid4a = p>=pmin & p<=pB13sat & h>h1L & h<=h2V; % valid range for region 4a
valid4b = p>pB13sat & p<=p3sat & h>h1B13L & h<=h2B13V; % valid range for region 4b
if any(any(valid1))
p1 = p(valid1);T1 = T1_ph(p1,h(valid1));rho1bar = 1./v1_pT(p1,T1)/rhostar;T1bar = T1/Tstar;
k0 = sqrt(T1bar).*(a(1) + (a(2) + (a(3) + a(4).*T1bar).*T1bar).*T1bar);
k1 = b(1) + b(2)*rho1bar + b(3)*exp(B(1)*(rho1bar + B(2)).^2);
deltaTbar = abs(T1bar-1)+C(4);Q = 2 + C(5)./deltaTbar.^0.6;S = (1./deltaTbar).*(T1bar>=1) + (C(6)./deltaTbar.^0.6).*(T1bar<1);
k2 = (d(1)./T1bar.^10 + d(2)).*rho1bar.^1.8.*exp(C(1)*(1-rho1bar.^2.8)) + d(3)*S.*rho1bar.^Q.*exp(Q./(1+Q).*(1-rho1bar.^(1+Q))) + d(4)*exp(C(2)*T1bar.^1.5 + C(3)./rho1bar.^5);
k(valid1) = (k0+k1+k2)*kstar;
end
if any(any(valid2a))
p2a = p(valid2a);T2a = T2a_ph(p2a,h(valid2a));rho2abar = 1./v2_pT(p2a,T2a)/rhostar;T2abar = T2a/Tstar;
k0 = sqrt(T2abar).*(a(1) + (a(2) + (a(3) + a(4).*T2abar).*T2abar).*T2abar);
k1 = b(1) + b(2)*rho2abar + b(3)*exp(B(1)*(rho2abar + B(2)).^2);
deltaTbar = abs(T2abar-1)+C(4);Q = 2 + C(5)./deltaTbar.^0.6;S = (1./deltaTbar).*(T2abar>=1) + (C(6)./deltaTbar.^0.6).*(T2abar<1);
k2 = (d(1)./T2abar.^10 + d(2)).*rho2abar.^1.8.*exp(C(1)*(1-rho2abar.^2.8)) + d(3)*S.*rho2abar.^Q.*exp(Q./(1+Q).*(1-rho2abar.^(1+Q))) + d(4)*exp(C(2)*T2abar.^1.5 + C(3)./rho2abar.^5);
k(valid2a) = (k0+k1+k2)*kstar;
end
if any(any(valid2b))
p2b = p(valid2b);T2b = T2b_ph(p2b,h(valid2b));rho2bbar = 1./v2_pT(p2b,T2b)/rhostar;T2bbar = T2b/Tstar;
k0 = sqrt(T2bbar).*(a(1) + (a(2) + (a(3) + a(4).*T2bbar).*T2bbar).*T2bbar);
k1 = b(1) + b(2)*rho2bbar + b(3)*exp(B(1)*(rho2bbar + B(2)).^2);
deltaTbar = abs(T2bbar-1)+C(4);Q = 2 + C(5)./deltaTbar.^0.6;S = (1./deltaTbar).*(T2bbar>=1) + (C(6)./deltaTbar.^0.6).*(T2bbar<1);
k2 = (d(1)./T2bbar.^10 + d(2)).*rho2bbar.^1.8.*exp(C(1)*(1-rho2bbar.^2.8)) + d(3)*S.*rho2bbar.^Q.*exp(Q./(1+Q).*(1-rho2bbar.^(1+Q))) + d(4)*exp(C(2)*T2bbar.^1.5 + C(3)./rho2bbar.^5);
k(valid2b) = (k0+k1+k2)*kstar;
end
if any(any(valid2c))
p2c = p(valid2c);T2c = T2c_ph(p2c,h(valid2c));rho2cbar = 1./v2_pT(p2c,T2c)/rhostar;T2cbar = T2c/Tstar;
k0 = sqrt(T2cbar).*(a(1) + (a(2) + (a(3) + a(4).*T2cbar).*T2cbar).*T2cbar);
k1 = b(1) + b(2)*rho2cbar + b(3)*exp(B(1)*(rho2cbar + B(2)).^2);
deltaTbar = abs(T2cbar-1)+C(4);Q = 2 + C(5)./deltaTbar.^0.6;S = (1./deltaTbar).*(T2cbar>=1) + (C(6)./deltaTbar.^0.6).*(T2cbar<1);
k2 = (d(1)./T2cbar.^10 + d(2)).*rho2cbar.^1.8.*exp(C(1)*(1-rho2cbar.^2.8)) + d(3)*S.*rho2cbar.^Q.*exp(Q./(1+Q).*(1-rho2cbar.^(1+Q))) + d(4)*exp(C(2)*T2cbar.^1.5 + C(3)./rho2cbar.^5);
k(valid2c) = (k0+k1+k2)*kstar;
end
if any(any(valid3a))
p3a = p(valid3a);h3a = h(valid3a);T3abar = T3a_ph(p3a,h3a)/Tstar;rho3abar = 1./v3a_ph(p3a,h3a)/rhostar;
k0 = sqrt(T3abar).*(a(1) + (a(2) + (a(3) + a(4).*T3abar).*T3abar).*T3abar);
k1 = b(1) + b(2)*rho3abar + b(3)*exp(B(1)*(rho3abar + B(2)).^2);
deltaTbar = abs(T3abar-1)+C(4);Q = 2 + C(5)./deltaTbar.^0.6;S = (1./deltaTbar).*(T3abar>=1) + (C(6)./deltaTbar.^0.6).*(T3abar<1);
k2 = (d(1)./T3abar.^10 + d(2)).*rho3abar.^1.8.*exp(C(1)*(1-rho3abar.^2.8)) + d(3)*S.*rho3abar.^Q.*exp(Q./(1+Q).*(1-rho3abar.^(1+Q))) + d(4)*exp(C(2)*T3abar.^1.5 + C(3)./rho3abar.^5);
k(valid3a) = (k0+k1+k2)*kstar;
end
if any(any(valid3b))
p3b = p(valid3b);h3b = h(valid3b);T3bbar = T3b_ph(p3b,h3b)/Tstar;rho3bbar = 1./v3b_ph(p3b,h3b)/rhostar;
k0 = sqrt(T3bbar).*(a(1) + (a(2) + (a(3) + a(4).*T3bbar).*T3bbar).*T3bbar);
k1 = b(1) + b(2)*rho3bbar + b(3)*exp(B(1)*(rho3bbar + B(2)).^2);
deltaTbar = abs(T3bbar-1)+C(4);Q = 2 + C(5)./deltaTbar.^0.6;S = (1./deltaTbar).*(T3bbar>=1) + (C(6)./deltaTbar.^0.6).*(T3bbar<1);
k2 = (d(1)./T3bbar.^10 + d(2)).*rho3bbar.^1.8.*exp(C(1)*(1-rho3bbar.^2.8)) + d(3)*S.*rho3bbar.^Q.*exp(Q./(1+Q).*(1-rho3bbar.^(1+Q))) + d(4)*exp(C(2)*T3bbar.^1.5 + C(3)./rho3bbar.^5);
k(valid3b) = (k0+k1+k2)*kstar;
end
if any(any(valid4a))
p4a = p(valid4a);Tsat4a = Tsat(valid4a);h1L4a = h1L(valid4a);
x = (h(valid4a)-h1L4a)./(h2V(valid4a)-h1L4a); % quality
v1L = v1_pT(p4a,Tsat4a); % [m^3/kg] saturated liquid specific volumes
v2V = v2_pT(p4a,Tsat4a); % [m^3/kg] saturated vapor specific volumes
T4abar = Tsat4a/Tstar;rho4abar = 1./(v1L + x.*(v2V - v1L))/rhostar;
k0 = sqrt(T4abar).*(a(1) + (a(2) + (a(3) + a(4).*T4abar).*T4abar).*T4abar);
k1 = b(1) + b(2)*rho4abar + b(3)*exp(B(1)*(rho4abar + B(2)).^2);
deltaTbar = abs(T4abar-1)+C(4);Q = 2 + C(5)./deltaTbar.^0.6;S = (1./deltaTbar).*(T4abar>=1) + (C(6)./deltaTbar.^0.6).*(T4abar<1);
k2 = (d(1)./T4abar.^10 + d(2)).*rho4abar.^1.8.*exp(C(1)*(1-rho4abar.^2.8)) + d(3)*S.*rho4abar.^Q.*exp(Q./(1+Q).*(1-rho4abar.^(1+Q))) + d(4)*exp(C(2)*T4abar.^1.5 + C(3)./rho4abar.^5);
k(valid4a) = (k0+k1+k2)*kstar;
end
if any(any(valid4b))
p4b = p(valid4b); Tsat4b = Tsat(valid4b);
v3L = vL_p(p4b); v3V = vV_p(p4b);
h3L = h3_rhoT(1./v3L,Tsat4b);
h3V = h3_rhoT(1./v3V,Tsat4b);
x = (h(valid4b)-h3L)./(h3V-h3L); % quality
T4bbar = Tsat4b/Tstar;rho4bbar = 1./(v3L + x.*(v3V - v3L))/rhostar;
k0 = sqrt(T4bbar).*(a(1) + (a(2) + (a(3) + a(4).*T4bbar).*T4bbar).*T4bbar);
k1 = b(1) + b(2)*rho4bbar + b(3)*exp(B(1)*(rho4bbar + B(2)).^2);
deltaTbar = abs(T4bbar-1)+C(4);Q = 2 + C(5)./deltaTbar.^0.6;S = (1./deltaTbar).*(T4bbar>=1) + (C(6)./deltaTbar.^0.6).*(T4bbar<1);
k2 = (d(1)./T4bbar.^10 + d(2)).*rho4bbar.^1.8.*exp(C(1)*(1-rho4bbar.^2.8)) + d(3)*S.*rho4bbar.^Q.*exp(Q./(1+Q).*(1-rho4bbar.^(1+Q))) + d(4)*exp(C(2)*T4bbar.^1.5 + C(3)./rho4bbar.^5);
k(valid4b) = (k0+k1+k2)*kstar;
end
end
function mu = mu_ph(p,h)
% mu = mu_ph(p,h)
% Viscosity, mu [Pa*s], as a function of pressure, p [MPa], and enthalpy, h [kJ/kg]
% based on IAPWS95 Release on the IAPWS Formulation 2008 for the Viscosity of Ordinary Water Substance
% Reference: http://www.iapws.org/
% June 23, 2009
% Mark Mikofski
%% size of inputs
dim = size(p);
initnan = NaN(dim);
mu = initnan;
%% constants and calculated
Tc = 647.096; % [K]
rhoc = 322.0; % [kg/m^3]
mustar = 1.00e-6; % [Pa*s]
Hi = [1.67752 2.20462 0.6366564 -0.241605];
Hij = [0,1,2,3,0,1,2,3,5,0,1,2,3,4,0,1,0,3,4,3,5;0,0,0,0,1,1,1,1,1,2,2,2,2,2,3,3,4,4,5,6,6; ...
0.520094,0.0850895,-1.08374,-0.289555,0.222531,0.999115,1.88797,1.26613,0.120573,-0.281378,-0.906851,-0.772479, ...
-0.489837,-0.257040,0.161913,0.257399,-0.0325372,0.0698452,0.00872102,-0.00435673,-0.000593264];
Nterms = 21;
Tmin = 273.16; % [K] minimum temperature is triple point
T2bcsat = 554.485; % [K] saturation temperature at 5.85 kJ/kg/K isentropic line between region 2b and 2c
TB13 = 623.15; % [K] temperature at boundary between region 1 and 3
Tmax = 1073.15; % [K] maximum temperature
pmin = psat_T(Tmin); % [MPa] minimum pressure is 611.657 Pa
p2ab = 4; % [MPa] pressure along boundary between region 2a and 2b
p2bcsat = psat_T(T2bcsat); % [MPa] saturation pressure at 5.85 kJ/kg/K isentropic line between region 2b and 2c
pB13sat = psat_T(TB13); % [MPa] saturation pressure at boundary between region 1 and 3, 16.5291643 MPa
pmax = 100; % [MPa] maximum pressure
h1B13L = h1_pT(pB13sat,TB13); % [kJ/kg] saturated liquid enthalpy at boundary between region 1, region 3 and region 4
h2B13V = h2_pT(pB13sat,TB13); % [kJ/kg] saturated vapor enthalpy at boundary between region 2, region 3 and region 4
%% calculated matrices
Tsat = Tsat_p(p); % [K] saturation temperatures
h1min = initnan;h2max = initnan;valid = p>=pmin & p<=pmax;pvalid = p(valid); % initialize matricies with NaN and set valid range of parameters
if any(any(valid))
Tmin = Tmin*ones(dim);Tmax = Tmax*ones(dim); % copy to matrix of size dim
h1min(valid) = h1_pT(pvalid,Tmin(valid)); % [kJ/kg] minimum enthalpies
h2max(valid) = h2_pT(pvalid,Tmax(valid)); % [kJ/kg] maximum enthalpies in region 2
end
h1L = initnan;h2V = initnan;valid = p>=pmin & p<=pB13sat;pvalid = p(valid); % initialize matricies with NaN and set valid range of parameters
if any(any(valid))
h1L(valid) = h1_pT(pvalid,Tsat(valid)); % [kJ/kg] saturated liquid enthalpies in region 1
h2V(valid) = h2_pT(pvalid,Tsat(valid)); % [kJ/kg] saturated vapor enthalpies in region 2
end
h1B13 = initnan;h3ab = initnan;h2B23 = initnan;valid = p>=pB13sat & p<=pmax;pvalid = p(valid); % initialize matricies with NaN and set valid range of parameters
if any(any(valid))
TB13 = TB13*ones(dim); % copy to matrix of size dim
h1B13(valid) = h1_pT(pvalid,TB13(valid)); % [kJ/kg] enthalpies on boundary between region 1 and region 3
h3ab(valid) = h3ab_p(pvalid); % [kJ/kg] enthalpies on critical entropy isentropic line between regions 3a and region 3b
h2B23(valid) = h2_pT(pvalid,TB23_p(pvalid)); % [kJ/kg] enthalpies on boundary between region 2 and region 3
end
h2bc = initnan;valid = p>=p2bcsat & p<=pmax; % initialize matricies with NaN and set valid range of parameters
h2bc(valid) = h2bc_p(p(valid)); % [kJ/kg] enthalpies on boundary between region 2b and 2c
p3sat = pB13sat*ones(dim);valid = h>=h1B13L & h<=h2B13V; % % do NOT use NaN to initialize p3sat, b/c for h<h1B13L or h>h2B13V p>NaN = 0, instead use pB13sat
if any(any(valid))
p3sat(valid) = p3sat_h(h(valid)); % [MPa] saturation pressure on boundary between region 3 and 4
end
%% valid ranges
valid1 = (p>=pmin & p<=pB13sat & h>=h1min & h<=h1L) | (p>pB13sat & p<=pmax & h>=h1min & h<=h1B13); % valid range for region 1
valid2a = p>=pmin & p<=p2ab & h>h2V & h<=h2max; % valid range for region 2a
valid2b = (p>p2ab & p<=p2bcsat & h>h2V & h<=h2max) | (p>p2bcsat & p<=pmax & h>h2bc & h<=h2max); % valid range for region 2b
valid2c = (p>p2bcsat & p<=pB13sat & h>h2V & h<=h2bc) | (p>pB13sat & p<=pmax & h>h2B23 & h<=h2bc); % valid range for region 2c
valid3a = p>p3sat & p<=pmax & h>h1B13 & h<=h3ab; % valid range for region 3a
valid3b = p>p3sat & p<=pmax & h>h3ab & h<=h2B23; % valid range for region 3b
valid4a = p>=pmin & p<=pB13sat & h>h1L & h<=h2V; % valid range for region 4a
valid4b = p>pB13sat & p<=p3sat & h>h1B13L & h<=h2B13V; % valid range for region 4b
if any(any(valid1))
p1 = p(valid1);T1 = T1_ph(p1,h(valid1));rho1bar = 1./v1_pT(p1,T1)/rhoc;T1bar = T1/Tc;
mu0 = 100*sqrt(T1bar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T1bar)./T1bar)./T1bar);
L = length(p1);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T1bar = T1bar*ones(1,Nterms);rho1bar = rho1bar*ones(1,Nterms);
mu1 = exp(sum(rho1bar.*(1./T1bar-1).^I.*HIJ.*(rho1bar-1).^J,2));
mu(valid1) = mu0.*mu1*mustar;
end
if any(any(valid2a))
p2a = p(valid2a);T2a = T2a_ph(p2a,h(valid2a));rho2abar = 1./v2_pT(p2a,T2a)/rhoc;T2abar = T2a/Tc;
mu0 = 100*sqrt(T2abar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T2abar)./T2abar)./T2abar);
L = length(p2a);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T2abar = T2abar*ones(1,Nterms);rho2abar = rho2abar*ones(1,Nterms);
mu1 = exp(sum(rho2abar.*(1./T2abar-1).^I.*HIJ.*(rho2abar-1).^J,2));
mu(valid2a) = mu0.*mu1*mustar;
end
if any(any(valid2b))
p2b = p(valid2b);T2b = T2b_ph(p2b,h(valid2b));rho2bbar = 1./v2_pT(p2b,T2b)/rhoc;T2bbar = T2b/Tc;
mu0 = 100*sqrt(T2bbar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T2bbar)./T2bbar)./T2bbar);
L = length(p2b);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T2bbar = T2bbar*ones(1,Nterms);rho2bbar = rho2bbar*ones(1,Nterms);
mu1 = exp(sum(rho2bbar.*(1./T2bbar-1).^I.*HIJ.*(rho2bbar-1).^J,2));
mu(valid2b) = mu0.*mu1*mustar;
end
if any(any(valid2c))
p2c = p(valid2c);T2c = T2c_ph(p2c,h(valid2c));rho2cbar = 1./v2_pT(p2c,T2c)/rhoc;T2cbar = T2c/Tc;
mu0 = 100*sqrt(T2cbar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T2cbar)./T2cbar)./T2cbar);
L = length(p2c);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T2cbar = T2cbar*ones(1,Nterms);rho2cbar = rho2cbar*ones(1,Nterms);
mu1 = exp(sum(rho2cbar.*(1./T2cbar-1).^I.*HIJ.*(rho2cbar-1).^J,2));
mu(valid2c) = mu0.*mu1*mustar;
end
if any(any(valid3a))
p3a = p(valid3a);h3a = h(valid3a);T3abar = T3a_ph(p3a,h3a)/Tc;rho3abar = 1./v3a_ph(p3a,h3a)/rhoc;
mu0 = 100*sqrt(T3abar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T3abar)./T3abar)./T3abar);
L = length(p3a);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T3abar = T3abar*ones(1,Nterms);rho3abar = rho3abar*ones(1,Nterms);
mu1 = exp(sum(rho3abar.*(1./T3abar-1).^I.*HIJ.*(rho3abar-1).^J,2));
mu(valid3a) = mu0.*mu1*mustar;
end
if any(any(valid3b))
p3b = p(valid3b);h3b = h(valid3b);T3bbar = T3b_ph(p3b,h3b)/Tc;rho3bbar = 1./v3b_ph(p3b,h3b)/rhoc;
mu0 = 100*sqrt(T3bbar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T3bbar)./T3bbar)./T3bbar);
L = length(p3b);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T3bbar = T3bbar*ones(1,Nterms);rho3bbar = rho3bbar*ones(1,Nterms);
mu1 = exp(sum(rho3bbar.*(1./T3bbar-1).^I.*HIJ.*(rho3bbar-1).^J,2));
mu(valid3b) = mu0.*mu1*mustar;
end
if any(any(valid4a))
p4a = p(valid4a);Tsat4a = Tsat(valid4a);h1L4a = h1L(valid4a);
x = (h(valid4a)-h1L4a)./(h2V(valid4a)-h1L4a); % quality
v1L = v1_pT(p4a,Tsat4a); % [m^3/kg] saturated liquid specific volumes
v2V = v2_pT(p4a,Tsat4a); % [m^3/kg] saturated vapor specific volumes
T4abar = Tsat4a/Tc;rho4abar = 1./(v1L + x.*(v2V - v1L))/rhoc;
mu0 = 100*sqrt(T4abar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T4abar)./T4abar)./T4abar);
L = length(p4a);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T4abar = T4abar*ones(1,Nterms);rho4abar = rho4abar*ones(1,Nterms);
mu1 = exp(sum(rho4abar.*(1./T4abar-1).^I.*HIJ.*(rho4abar-1).^J,2));
mu(valid4a) = mu0.*mu1*mustar;
end
if any(any(valid4b))
p4b = p(valid4b); Tsat4b = Tsat(valid4b);
v3L = vL_p(p4b); v3V = vV_p(p4b);
h3L = h3_rhoT(1./v3L,Tsat4b);
h3V = h3_rhoT(1./v3V,Tsat4b);
x = (h(valid4b)-h3L)./(h3V-h3L); % quality
T4bbar = Tsat4b/Tc;rho4bbar = 1./(v3L + x.*(v3V - v3L))/rhoc;
mu0 = 100*sqrt(T4bbar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T4bbar)./T4bbar)./T4bbar);
L = length(p4b);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T4bbar = T4bbar*ones(1,Nterms);rho4bbar = rho4bbar*ones(1,Nterms);
mu1 = exp(sum(rho4bbar.*(1./T4bbar-1).^I.*HIJ.*(rho4bbar-1).^J,2));
mu(valid4b) = mu0.*mu1*mustar;
end
end
function mu = mu_pT(p,T)
% mu = mu_pT(p,T)
% Viscosity, mu [Pa*s], as a function of pressure, p [MPa], and temperature, T [K]
% based on IAPWS95 Release on the IAPWS Formulation 2008 for the Viscosity of Ordinary Water Substance
% Reference: http://www.iapws.org/
% June 23, 2009
% Mark Mikofski
%% size of inputs
dim = size(p);
initnan = NaN(dim);
mu = initnan;
%% constants and calculated
Tc = 647.096; % [K]
rhoc = 322.0; % [kg/m^3]
mustar = 1.00e-6; % [Pa*s]
Hi = [1.67752 2.20462 0.6366564 -0.241605];
Hij = [0,1,2,3,0,1,2,3,5,0,1,2,3,4,0,1,0,3,4,3,5;0,0,0,0,1,1,1,1,1,2,2,2,2,2,3,3,4,4,5,6,6; ...
0.520094,0.0850895,-1.08374,-0.289555,0.222531,0.999115,1.88797,1.26613,0.120573,-0.281378,-0.906851,-0.772479, ...
-0.489837,-0.257040,0.161913,0.257399,-0.0325372,0.0698452,0.00872102,-0.00435673,-0.000593264];
Nterms = 21;
Tmin = 273.16; % [K] minimum temperature is triple point
TB13 = 623.15; % [K] temperature at boundary between region 1 and 3
TB23 = 863.15; % [K] temperature of boundary between region 2 and 3
Tmax = 1073.15; % [K] maximum valid temperature
pmin = psat_T(Tmin); % [MPa] minimum pressure is 611.657 Pa
pmax = 100; % [MPa] maximum valid pressure
psat = psat_T(T); % [MPa] saturation pressures
pB23 = initnan; valid = T>=TB13 & T<=TB23;
pB23(valid) = pB23_T(T(valid)); % [MPa] pressure on boundary between region 2 and region 3
%% valid ranges
valid1 = p>=psat & p<=pmax & T>=Tmin & T<=TB13; % valid range for region 1, include B13 in region 1
valid2 = p>=pmin & ((T>=Tmin & T<=TB13 & p<=psat) | (T>TB13 & T<=TB23 & p<=pB23) | (T>TB23 & T<=Tmax & p<=pmax)); % valid range for region 2, include B23 in region 2
valid3 = p>pB23 & p<=pmax & T>TB13 & T<TB23;
if any(any(valid1))
T1 = T(valid1);rho1bar = 1./v1_pT(p(valid1),T1)/rhoc;T1bar = T1/Tc;
mu0 = 100*sqrt(T1bar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T1bar)./T1bar)./T1bar);
L = length(T1);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T1bar = T1bar*ones(1,Nterms);rho1bar = rho1bar*ones(1,Nterms);
mu1 = exp(sum(rho1bar.*(1./T1bar-1).^I.*HIJ.*(rho1bar-1).^J,2));
mu(valid1) = mu0.*mu1*mustar;
end
if any(any(valid2))
T2 = T(valid2);rho2bar = 1./v2_pT(p(valid2),T2)/rhoc;T2bar = T2/Tc;
mu0 = 100*sqrt(T2bar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T2bar)./T2bar)./T2bar);
L = length(T2);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T2bar = T2bar*ones(1,Nterms);rho2bar = rho2bar*ones(1,Nterms);
mu1 = exp(sum(rho2bar.*(1./T2bar-1).^I.*HIJ.*(rho2bar-1).^J,2));
mu(valid2) = mu0.*mu1*mustar;
end
if any(any(valid3))
T3 = T(valid3);rho3bar = 1./v_pT(p(valid3),T3)/rhoc;T3bar = T3/Tc;
mu0 = 100*sqrt(T3bar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T3bar)./T3bar)./T3bar);
L = length(T3);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T3bar = T3bar*ones(1,Nterms);rho3bar = rho3bar*ones(1,Nterms);
mu1 = exp(sum(rho3bar.*(1./T3bar-1).^I.*HIJ.*(rho3bar-1).^J,2));
mu(valid3) = mu0.*mu1*mustar;
end
end
function dmudh = dmudh_ph(p,h)
% dmudh = dmudh_ph(p,h)
% Derivative of viscosity, dmudh [(Pa*s)/(kJ/kg)], with respect to enthalpy, h [kJ/kg] at constant pressure as a function of
% pressure, p [MPa], and enthalpy, h [kJ/kg]
% based on IAPWS95 Release on the IAPWS Formulation 2008 for the Viscosity of Ordinary Water Substance
% Reference: http://www.iapws.org/
% June 23, 2009
% Mark Mikofski
%% size of inputs
dim = size(p);
initnan = NaN(dim);
dmudh = initnan;
%% constants and calculated
Tc = 647.096; % [K]
rhoc = 322.0; % [kg/m^3]
mustar = 1.00e-6; % [Pa*s]
Hi = [1.67752 2.20462 0.6366564 -0.241605];
Hij = [0,1,2,3,0,1,2,3,5,0,1,2,3,4,0,1,0,3,4,3,5;0,0,0,0,1,1,1,1,1,2,2,2,2,2,3,3,4,4,5,6,6; ...
0.520094,0.0850895,-1.08374,-0.289555,0.222531,0.999115,1.88797,1.26613,0.120573,-0.281378,-0.906851,-0.772479, ...
-0.489837,-0.257040,0.161913,0.257399,-0.0325372,0.0698452,0.00872102,-0.00435673,-0.000593264];
Nterms = 21;
Tmin = 273.16; % [K] minimum temperature is triple point
T2bcsat = 554.485; % [K] saturation temperature at 5.85 kJ/kg/K isentropic line between region 2b and 2c
TB13 = 623.15; % [K] temperature at boundary between region 1 and 3
Tmax = 1073.15; % [K] maximum temperature
pmin = psat_T(Tmin); % [MPa] minimum pressure is 611.657 Pa
p2ab = 4; % [MPa] pressure along boundary between region 2a and 2b
p2bcsat = psat_T(T2bcsat); % [MPa] saturation pressure at 5.85 kJ/kg/K isentropic line between region 2b and 2c
pB13sat = psat_T(TB13); % [MPa] saturation pressure at boundary between region 1 and 3, 16.5291643 MPa
pmax = 100; % [MPa] maximum pressure
h1B13L = h1_pT(pB13sat,TB13); % [kJ/kg] saturated liquid enthalpy at boundary between region 1, region 3 and region 4
h2B13V = h2_pT(pB13sat,TB13); % [kJ/kg] saturated vapor enthalpy at boundary between region 2, region 3 and region 4
%% calculated matrices
Tsat = Tsat_p(p); % [K] saturation temperatures
h1min = initnan;h2max = initnan;valid = p>=pmin & p<=pmax;pvalid = p(valid); % initialize matricies with NaN and set valid range of parameters
if any(any(valid))
Tmin = Tmin*ones(dim);Tmax = Tmax*ones(dim); % copy to matrix of size dim
h1min(valid) = h1_pT(pvalid,Tmin(valid)); % [kJ/kg] minimum enthalpies
h2max(valid) = h2_pT(pvalid,Tmax(valid)); % [kJ/kg] maximum enthalpies in region 2
end
h1L = initnan;h2V = initnan;valid = p>=pmin & p<=pB13sat;pvalid = p(valid); % initialize matricies with NaN and set valid range of parameters
if any(any(valid))
h1L(valid) = h1_pT(pvalid,Tsat(valid)); % [kJ/kg] saturated liquid enthalpies in region 1
h2V(valid) = h2_pT(pvalid,Tsat(valid)); % [kJ/kg] saturated vapor enthalpies in region 2
end
h1B13 = initnan;h3ab = initnan;h2B23 = initnan;valid = p>=pB13sat & p<=pmax;pvalid = p(valid); % initialize matricies with NaN and set valid range of parameters
if any(any(valid))
TB13 = TB13*ones(dim); % copy to matrix of size dim
h1B13(valid) = h1_pT(pvalid,TB13(valid)); % [kJ/kg] enthalpies on boundary between region 1 and region 3
h3ab(valid) = h3ab_p(pvalid); % [kJ/kg] enthalpies on critical entropy isentropic line between regions 3a and region 3b
h2B23(valid) = h2_pT(pvalid,TB23_p(pvalid)); % [kJ/kg] enthalpies on boundary between region 2 and region 3
end
h2bc = initnan;valid = p>=p2bcsat & p<=pmax; % initialize matricies with NaN and set valid range of parameters
h2bc(valid) = h2bc_p(p(valid)); % [kJ/kg] enthalpies on boundary between region 2b and 2c
p3sat = pB13sat*ones(dim);valid = h>=h1B13L & h<=h2B13V; % % do NOT use NaN to initialize p3sat, b/c for h<h1B13L or h>h2B13V p>NaN = 0, instead use pB13sat
if any(any(valid))
p3sat(valid) = p3sat_h(h(valid)); % [MPa] saturation pressure on boundary between region 3 and 4
end
%% valid ranges
valid1 = (p>=pmin & p<=pB13sat & h>=h1min & h<=h1L) | (p>pB13sat & p<=pmax & h>=h1min & h<=h1B13); % valid range for region 1
valid2a = p>=pmin & p<=p2ab & h>h2V & h<=h2max; % valid range for region 2a
valid2b = (p>p2ab & p<=p2bcsat & h>h2V & h<=h2max) | (p>p2bcsat & p<=pmax & h>h2bc & h<=h2max); % valid range for region 2b
valid2c = (p>p2bcsat & p<=pB13sat & h>h2V & h<=h2bc) | (p>pB13sat & p<=pmax & h>h2B23 & h<=h2bc); % valid range for region 2c
valid3a = p>p3sat & p<=pmax & h>h1B13 & h<=h3ab; % valid range for region 3a
valid3b = p>p3sat & p<=pmax & h>h3ab & h<=h2B23; % valid range for region 3b
valid4a = p>=pmin & p<=pB13sat & h>h1L & h<=h2V; % valid range for region 4a
valid4b = p>pB13sat & p<=p3sat & h>h1B13L & h<=h2B13V; % valid range for region 4b
if any(any(valid1))
p1 = p(valid1);h1 = h(valid1);T1 = T1_ph(p1,h1);v1 = v1_pT(p1,T1);rho1bar = 1./v1/rhoc;T1bar = T1/Tc;
mu0 = 100*sqrt(T1bar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T1bar)./T1bar)./T1bar);
dmu0dT = mu0/2./T1bar.*(Hi(1) + (3*Hi(2) + (5*Hi(3) + 7*Hi(4)./T1bar)./T1bar)./T1bar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T1bar)./T1bar)./T1bar);
L = length(p1);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T1bar = T1bar*ones(1,Nterms);rho1bar = rho1bar*ones(1,Nterms);
mu1 = exp(sum(rho1bar.*(1./T1bar-1).^I.*HIJ.*(rho1bar-1).^J,2));
dmu1dT = mu1.*(sum(rho1bar.*I.*(1./T1bar-1).^(I-1).*(-1./T1bar.^2).*HIJ.*(rho1bar-1).^J,2));
dmudT = (dmu0dT.*mu1 + mu0.*dmu1dT)*mustar/Tc;
dmu1drho = mu1.*(sum((1./T1bar-1).^I.*HIJ.*(rho1bar-1).^J,2) + sum(rho1bar.*(1./T1bar-1).^I.*J.*HIJ.*(rho1bar-1).^(J-1),2));
dmudrho = mu0.*dmu1drho*mustar/rhoc;
dmudh(valid1) = -dmudrho./v1.^2.*dvdh_ph(p1,h1) + dmudT./cp_ph(p1,h1);
end
if any(any(valid2a))
p2a = p(valid2a);h2 = h(valid2a);T2a = T2a_ph(p2a,h2);v2 = v2_pT(p2a,T2a);rho2abar = 1./v2/rhoc;T2abar = T2a/Tc;
mu0 = 100*sqrt(T2abar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T2abar)./T2abar)./T2abar);
dmu0dT = mu0/2./T2abar.*(Hi(1) + (3*Hi(2) + (5*Hi(3) + 7*Hi(4)./T2abar)./T2abar)./T2abar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T2abar)./T2abar)./T2abar);
L = length(p2a);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T2abar = T2abar*ones(1,Nterms);rho2abar = rho2abar*ones(1,Nterms);
mu1 = exp(sum(rho2abar.*(1./T2abar-1).^I.*HIJ.*(rho2abar-1).^J,2));
dmu1dT = mu1.*(sum(rho2abar.*I.*(1./T2abar-1).^(I-1).*(-1./T2abar.^2).*HIJ.*(rho2abar-1).^J,2));
dmudT = (dmu0dT.*mu1 + mu0.*dmu1dT)*mustar/Tc;
dmu1drho = mu1.*(sum((1./T2abar-1).^I.*HIJ.*(rho2abar-1).^J,2) + sum(rho2abar.*(1./T2abar-1).^I.*J.*HIJ.*(rho2abar-1).^(J-1),2));
dmudrho = mu0.*dmu1drho*mustar/rhoc;
dmudh(valid2a) = -dmudrho./v2.^2.*dvdh_ph(p2a,h2) + dmudT./cp_ph(p2a,h2);
end
if any(any(valid2b))
p2b = p(valid2b);h2 = h(valid2b);T2b = T2b_ph(p2b,h2);v2 = v2_pT(p2b,T2b);rho2bbar = 1./v2/rhoc;T2bbar = T2b/Tc;
mu0 = 100*sqrt(T2bbar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T2bbar)./T2bbar)./T2bbar);
dmu0dT = mu0/2./T2bbar.*(Hi(1) + (3*Hi(2) + (5*Hi(3) + 7*Hi(4)./T2bbar)./T2bbar)./T2bbar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T2bbar)./T2bbar)./T2bbar);
L = length(p2b);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T2bbar = T2bbar*ones(1,Nterms);rho2bbar = rho2bbar*ones(1,Nterms);
mu1 = exp(sum(rho2bbar.*(1./T2bbar-1).^I.*HIJ.*(rho2bbar-1).^J,2));
dmu1dT = mu1.*(sum(rho2bbar.*I.*(1./T2bbar-1).^(I-1).*(-1./T2bbar.^2).*HIJ.*(rho2bbar-1).^J,2));
dmudT = (dmu0dT.*mu1 + mu0.*dmu1dT)*mustar/Tc;
dmu1drho = mu1.*(sum((1./T2bbar-1).^I.*HIJ.*(rho2bbar-1).^J,2) + sum(rho2bbar.*(1./T2bbar-1).^I.*J.*HIJ.*(rho2bbar-1).^(J-1),2));
dmudrho = mu0.*dmu1drho*mustar/rhoc;
dmudh(valid2b) = -dmudrho./v2.^2.*dvdh_ph(p2b,h2) + dmudT./cp_ph(p2b,h2);
end
if any(any(valid2c))
p2c = p(valid2c);h2 = h(valid2c);T2c = T2c_ph(p2c,h2);v2 = v2_pT(p2c,T2c);rho2cbar = 1./v2/rhoc;T2cbar = T2c/Tc;
mu0 = 100*sqrt(T2cbar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T2cbar)./T2cbar)./T2cbar);
dmu0dT = mu0/2./T2cbar.*(Hi(1) + (3*Hi(2) + (5*Hi(3) + 7*Hi(4)./T2cbar)./T2cbar)./T2cbar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T2cbar)./T2cbar)./T2cbar);
L = length(p2c);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T2cbar = T2cbar*ones(1,Nterms);rho2cbar = rho2cbar*ones(1,Nterms);
mu1 = exp(sum(rho2cbar.*(1./T2cbar-1).^I.*HIJ.*(rho2cbar-1).^J,2));
dmu1dT = mu1.*(sum(rho2cbar.*I.*(1./T2cbar-1).^(I-1).*(-1./T2cbar.^2).*HIJ.*(rho2cbar-1).^J,2));
dmudT = (dmu0dT.*mu1 + mu0.*dmu1dT)*mustar/Tc;
dmu1drho = mu1.*(sum((1./T2cbar-1).^I.*HIJ.*(rho2cbar-1).^J,2) + sum(rho2cbar.*(1./T2cbar-1).^I.*J.*HIJ.*(rho2cbar-1).^(J-1),2));
dmudrho = mu0.*dmu1drho*mustar/rhoc;
dmudh(valid2c) = -dmudrho./v2.^2.*dvdh_ph(p2c,h2) + dmudT./cp_ph(p2c,h2);
end
if any(any(valid3a))
p3a = p(valid3a);h3a = h(valid3a);T3 = T3a_ph(p3a,h3a);T3abar = T3/Tc;v3 = v3a_ph(p3a,h3a);rho3abar = 1./v3/rhoc;
mu0 = 100*sqrt(T3abar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T3abar)./T3abar)./T3abar);
dmu0dT = mu0/2./T3abar.*(Hi(1) + (3*Hi(2) + (5*Hi(3) + 7*Hi(4)./T3abar)./T3abar)./T3abar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T3abar)./T3abar)./T3abar);
L = length(p3a);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T3abar = T3abar*ones(1,Nterms);rho3abar = rho3abar*ones(1,Nterms);
mu1 = exp(sum(rho3abar.*(1./T3abar-1).^I.*HIJ.*(rho3abar-1).^J,2));
dmu1dT = mu1.*(sum(rho3abar.*I.*(1./T3abar-1).^(I-1).*(-1./T3abar.^2).*HIJ.*(rho3abar-1).^J,2));
dmudT = (dmu0dT.*mu1 + mu0.*dmu1dT)*mustar/Tc;
dmu1drho = mu1.*(sum((1./T3abar-1).^I.*HIJ.*(rho3abar-1).^J,2) + sum(rho3abar.*(1./T3abar-1).^I.*J.*HIJ.*(rho3abar-1).^(J-1),2));
dmudrho = mu0.*dmu1drho*mustar/rhoc;
dmudh(valid3a) = -dmudrho./v3.^2.*dvdh_ph(p3a,h3a) + dmudT./cp_ph(p3a,h3a);
end
if any(any(valid3b))
p3b = p(valid3b);h3b = h(valid3b);T3 = T3b_ph(p3b,h3b);T3bbar = T3/Tc;v3 = v3b_ph(p3b,h3b);rho3bbar = 1./v3/rhoc;
mu0 = 100*sqrt(T3bbar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T3bbar)./T3bbar)./T3bbar);
dmu0dT = mu0/2./T3bbar.*(Hi(1) + (3*Hi(2) + (5*Hi(3) + 7*Hi(4)./T3bbar)./T3bbar)./T3bbar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T3bbar)./T3bbar)./T3bbar);
L = length(p3b);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T3bbar = T3bbar*ones(1,Nterms);rho3bbar = rho3bbar*ones(1,Nterms);
mu1 = exp(sum(rho3bbar.*(1./T3bbar-1).^I.*HIJ.*(rho3bbar-1).^J,2));
dmu1dT = mu1.*(sum(rho3bbar.*I.*(1./T3bbar-1).^(I-1).*(-1./T3bbar.^2).*HIJ.*(rho3bbar-1).^J,2));
dmudT = (dmu0dT.*mu1 + mu0.*dmu1dT)*mustar/Tc;
dmu1drho = mu1.*(sum((1./T3bbar-1).^I.*HIJ.*(rho3bbar-1).^J,2) + sum(rho3bbar.*(1./T3bbar-1).^I.*J.*HIJ.*(rho3bbar-1).^(J-1),2));
dmudrho = mu0.*dmu1drho*mustar/rhoc;
dmudh(valid3b) = -dmudrho./v3.^2.*dvdh_ph(p3b,h3b) + dmudT./cp_ph(p3b,h3b);
end
if any(any(valid4a))
p4a = p(valid4a);Tsat4a = Tsat(valid4a);h1L4a = h1L(valid4a);
h4 = h(valid4a);x = (h4-h1L4a)./(h2V(valid4a)-h1L4a); % quality
v1L = v1_pT(p4a,Tsat4a); % [m^3/kg] saturated liquid specific volumes
v2V = v2_pT(p4a,Tsat4a); % [m^3/kg] saturated vapor specific volumes
T4abar = Tsat4a/Tc;v4 = v1L + x.*(v2V - v1L);rho4abar = 1./v4/rhoc;
mu0 = 100*sqrt(T4abar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T4abar)./T4abar)./T4abar);
dmu0dT = mu0/2./T4abar.*(Hi(1) + (3*Hi(2) + (5*Hi(3) + 7*Hi(4)./T4abar)./T4abar)./T4abar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T4abar)./T4abar)./T4abar);
L = length(p4a);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T4abar = T4abar*ones(1,Nterms);rho4abar = rho4abar*ones(1,Nterms);
mu1 = exp(sum(rho4abar.*(1./T4abar-1).^I.*HIJ.*(rho4abar-1).^J,2));
dmu1dT = mu1.*(sum(rho4abar.*I.*(1./T4abar-1).^(I-1).*(-1./T4abar.^2).*HIJ.*(rho4abar-1).^J,2));
dmudT = (dmu0dT.*mu1 + mu0.*dmu1dT)*mustar/Tc;
dmu1drho = mu1.*(sum((1./T4abar-1).^I.*HIJ.*(rho4abar-1).^J,2) + sum(rho4abar.*(1./T4abar-1).^I.*J.*HIJ.*(rho4abar-1).^(J-1),2));
dmudrho = mu0.*dmu1drho*mustar/rhoc;
dmudh(valid4a) = -dmudrho./v4.^2.*dvdh_ph(p4a,h4) + dmudT./cp_ph(p4a,h4);
end
if any(any(valid4b))
p4b = p(valid4b); Tsat4b = Tsat(valid4b);
v3L = vL_p(p4b); v3V = vV_p(p4b);
h3L = h3_rhoT(1./v3L,Tsat4b);
h3V = h3_rhoT(1./v3V,Tsat4b);
h4 = h(valid4b);x = (h4-h3L)./(h3V-h3L); % quality
T4bbar = Tsat4b/Tc;v4 = v3L + x.*(v3V - v3L);rho4bbar = 1./v4/rhoc;
mu0 = 100*sqrt(T4bbar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T4bbar)./T4bbar)./T4bbar);
dmu0dT = mu0/2./T4bbar.*(Hi(1) + (3*Hi(2) + (5*Hi(3) + 7*Hi(4)./T4bbar)./T4bbar)./T4bbar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T4bbar)./T4bbar)./T4bbar);
L = length(p4b);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T4bbar = T4bbar*ones(1,Nterms);rho4bbar = rho4bbar*ones(1,Nterms);
mu1 = exp(sum(rho4bbar.*(1./T4bbar-1).^I.*HIJ.*(rho4bbar-1).^J,2));
dmu1dT = mu1.*(sum(rho4bbar.*I.*(1./T4bbar-1).^(I-1).*(-1./T4bbar.^2).*HIJ.*(rho4bbar-1).^J,2));
dmudT = (dmu0dT.*mu1 + mu0.*dmu1dT)*mustar/Tc;
dmu1drho = mu1.*(sum((1./T4bbar-1).^I.*HIJ.*(rho4bbar-1).^J,2) + sum(rho4bbar.*(1./T4bbar-1).^I.*J.*HIJ.*(rho4bbar-1).^(J-1),2));
dmudrho = mu0.*dmu1drho*mustar/rhoc;
dmudh(valid4b) = -dmudrho./v4.^2.*dvdh_ph(p4b,h4) + dmudT./cp_ph(p4b,h4);
end
end
function dmudp = dmudp_ph(p,h)
% dmudp = dmudp_ph(p,h)
% Derivative of viscosity, dmudp [(Pa*s)/MPa], with respect to pressure, p [MPa] at constant enthalpy as a function of
% pressure, p [MPa], and enthalpy, h [kJ/kg]
% based on IAPWS95 Release on the IAPWS Formulation 2008 for the Viscosity of Ordinary Water Substance
% Reference: http://www.iapws.org/
% June 23, 2009
% Mark Mikofski
%% size of inputs
dim = size(p);
initnan = NaN(dim);
dmudp = initnan;
%% constants and calculated
Tc = 647.096; % [K]
rhoc = 322.0; % [kg/m^3]
mustar = 1.00e-6; % [Pa*s]
Hi = [1.67752 2.20462 0.6366564 -0.241605];
Hij = [0,1,2,3,0,1,2,3,5,0,1,2,3,4,0,1,0,3,4,3,5;0,0,0,0,1,1,1,1,1,2,2,2,2,2,3,3,4,4,5,6,6; ...
0.520094,0.0850895,-1.08374,-0.289555,0.222531,0.999115,1.88797,1.26613,0.120573,-0.281378,-0.906851,-0.772479, ...
-0.489837,-0.257040,0.161913,0.257399,-0.0325372,0.0698452,0.00872102,-0.00435673,-0.000593264];
Nterms = 21;
Tmin = 273.16; % [K] minimum temperature is triple point
T2bcsat = 554.485; % [K] saturation temperature at 5.85 kJ/kg/K isentropic line between region 2b and 2c
TB13 = 623.15; % [K] temperature at boundary between region 1 and 3
Tmax = 1073.15; % [K] maximum temperature
pmin = psat_T(Tmin); % [MPa] minimum pressure is 611.657 Pa
p2ab = 4; % [MPa] pressure along boundary between region 2a and 2b
p2bcsat = psat_T(T2bcsat); % [MPa] saturation pressure at 5.85 kJ/kg/K isentropic line between region 2b and 2c
pB13sat = psat_T(TB13); % [MPa] saturation pressure at boundary between region 1 and 3, 16.5291643 MPa
pmax = 100; % [MPa] maximum pressure
h1B13L = h1_pT(pB13sat,TB13); % [kJ/kg] saturated liquid enthalpy at boundary between region 1, region 3 and region 4
h2B13V = h2_pT(pB13sat,TB13); % [kJ/kg] saturated vapor enthalpy at boundary between region 2, region 3 and region 4
%% calculated matrices
Tsat = Tsat_p(p); % [K] saturation temperatures
h1min = initnan;h2max = initnan;valid = p>=pmin & p<=pmax;pvalid = p(valid); % initialize matricies with NaN and set valid range of parameters
if any(any(valid))
Tmin = Tmin*ones(dim);Tmax = Tmax*ones(dim); % copy to matrix of size dim
h1min(valid) = h1_pT(pvalid,Tmin(valid)); % [kJ/kg] minimum enthalpies
h2max(valid) = h2_pT(pvalid,Tmax(valid)); % [kJ/kg] maximum enthalpies in region 2
end
h1L = initnan;h2V = initnan;valid = p>=pmin & p<=pB13sat;pvalid = p(valid); % initialize matricies with NaN and set valid range of parameters
if any(any(valid))
h1L(valid) = h1_pT(pvalid,Tsat(valid)); % [kJ/kg] saturated liquid enthalpies in region 1
h2V(valid) = h2_pT(pvalid,Tsat(valid)); % [kJ/kg] saturated vapor enthalpies in region 2
end
h1B13 = initnan;h3ab = initnan;h2B23 = initnan;valid = p>=pB13sat & p<=pmax;pvalid = p(valid); % initialize matricies with NaN and set valid range of parameters
if any(any(valid))
TB13 = TB13*ones(dim); % copy to matrix of size dim
h1B13(valid) = h1_pT(pvalid,TB13(valid)); % [kJ/kg] enthalpies on boundary between region 1 and region 3
h3ab(valid) = h3ab_p(pvalid); % [kJ/kg] enthalpies on critical entropy isentropic line between regions 3a and region 3b
h2B23(valid) = h2_pT(pvalid,TB23_p(pvalid)); % [kJ/kg] enthalpies on boundary between region 2 and region 3
end
h2bc = initnan;valid = p>=p2bcsat & p<=pmax; % initialize matricies with NaN and set valid range of parameters
h2bc(valid) = h2bc_p(p(valid)); % [kJ/kg] enthalpies on boundary between region 2b and 2c
p3sat = pB13sat*ones(dim);valid = h>=h1B13L & h<=h2B13V; % % do NOT use NaN to initialize p3sat, b/c for h<h1B13L or h>h2B13V p>NaN = 0, instead use pB13sat
if any(any(valid))
p3sat(valid) = p3sat_h(h(valid)); % [MPa] saturation pressure on boundary between region 3 and 4
end
%% valid ranges
valid1 = (p>=pmin & p<=pB13sat & h>=h1min & h<=h1L) | (p>pB13sat & p<=pmax & h>=h1min & h<=h1B13); % valid range for region 1
valid2a = p>=pmin & p<=p2ab & h>h2V & h<=h2max; % valid range for region 2a
valid2b = (p>p2ab & p<=p2bcsat & h>h2V & h<=h2max) | (p>p2bcsat & p<=pmax & h>h2bc & h<=h2max); % valid range for region 2b
valid2c = (p>p2bcsat & p<=pB13sat & h>h2V & h<=h2bc) | (p>pB13sat & p<=pmax & h>h2B23 & h<=h2bc); % valid range for region 2c
valid3a = p>p3sat & p<=pmax & h>h1B13 & h<=h3ab; % valid range for region 3a
valid3b = p>p3sat & p<=pmax & h>h3ab & h<=h2B23; % valid range for region 3b
valid4a = p>=pmin & p<=pB13sat & h>h1L & h<=h2V; % valid range for region 4a
valid4b = p>pB13sat & p<=p3sat & h>h1B13L & h<=h2B13V; % valid range for region 4b
if any(any(valid1))
p1 = p(valid1);h1 = h(valid1);T1 = T1_ph(p1,h1);v1 = v1_pT(p1,T1);rho1bar = 1./v1/rhoc;T1bar = T1/Tc;
mu0 = 100*sqrt(T1bar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T1bar)./T1bar)./T1bar);
dmu0dT = mu0/2./T1bar.*(Hi(1) + (3*Hi(2) + (5*Hi(3) + 7*Hi(4)./T1bar)./T1bar)./T1bar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T1bar)./T1bar)./T1bar);
L = length(p1);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T1bar = T1bar*ones(1,Nterms);rho1bar = rho1bar*ones(1,Nterms);
mu1 = exp(sum(rho1bar.*(1./T1bar-1).^I.*HIJ.*(rho1bar-1).^J,2));
dmu1dT = mu1.*(sum(rho1bar.*I.*(1./T1bar-1).^(I-1).*(-1./T1bar.^2).*HIJ.*(rho1bar-1).^J,2));
dmudT = (dmu0dT.*mu1 + mu0.*dmu1dT)*mustar/Tc;
dmu1drho = mu1.*(sum((1./T1bar-1).^I.*HIJ.*(rho1bar-1).^J,2) + sum(rho1bar.*(1./T1bar-1).^I.*J.*HIJ.*(rho1bar-1).^(J-1),2));
dmudrho = mu0.*dmu1drho*mustar/rhoc;
dmudp(valid1) = -dmudrho./v1.^2.*dvdp_ph(p1,h1) + dmudT.*dTdp_ph(p1,h1);
end
if any(any(valid2a))
p2a = p(valid2a);h2 = h(valid2a);T2a = T2a_ph(p2a,h2);v2 = v2_pT(p2a,T2a);rho2abar = 1./v2/rhoc;T2abar = T2a/Tc;
mu0 = 100*sqrt(T2abar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T2abar)./T2abar)./T2abar);
dmu0dT = mu0/2./T2abar.*(Hi(1) + (3*Hi(2) + (5*Hi(3) + 7*Hi(4)./T2abar)./T2abar)./T2abar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T2abar)./T2abar)./T2abar);
L = length(p2a);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T2abar = T2abar*ones(1,Nterms);rho2abar = rho2abar*ones(1,Nterms);
mu1 = exp(sum(rho2abar.*(1./T2abar-1).^I.*HIJ.*(rho2abar-1).^J,2));
dmu1dT = mu1.*(sum(rho2abar.*I.*(1./T2abar-1).^(I-1).*(-1./T2abar.^2).*HIJ.*(rho2abar-1).^J,2));
dmudT = (dmu0dT.*mu1 + mu0.*dmu1dT)*mustar/Tc;
dmu1drho = mu1.*(sum((1./T2abar-1).^I.*HIJ.*(rho2abar-1).^J,2) + sum(rho2abar.*(1./T2abar-1).^I.*J.*HIJ.*(rho2abar-1).^(J-1),2));
dmudrho = mu0.*dmu1drho*mustar/rhoc;
dmudp(valid2a) = -dmudrho./v2.^2.*dvdp_ph(p2a,h2) + dmudT.*dTdp_ph(p2a,h2);
end
if any(any(valid2b))
p2b = p(valid2b);h2 = h(valid2b);T2b = T2b_ph(p2b,h2);v2 = v2_pT(p2b,T2b);rho2bbar = 1./v2/rhoc;T2bbar = T2b/Tc;
mu0 = 100*sqrt(T2bbar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T2bbar)./T2bbar)./T2bbar);
dmu0dT = mu0/2./T2bbar.*(Hi(1) + (3*Hi(2) + (5*Hi(3) + 7*Hi(4)./T2bbar)./T2bbar)./T2bbar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T2bbar)./T2bbar)./T2bbar);
L = length(p2b);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T2bbar = T2bbar*ones(1,Nterms);rho2bbar = rho2bbar*ones(1,Nterms);
mu1 = exp(sum(rho2bbar.*(1./T2bbar-1).^I.*HIJ.*(rho2bbar-1).^J,2));
dmu1dT = mu1.*(sum(rho2bbar.*I.*(1./T2bbar-1).^(I-1).*(-1./T2bbar.^2).*HIJ.*(rho2bbar-1).^J,2));
dmudT = (dmu0dT.*mu1 + mu0.*dmu1dT)*mustar/Tc;
dmu1drho = mu1.*(sum((1./T2bbar-1).^I.*HIJ.*(rho2bbar-1).^J,2) + sum(rho2bbar.*(1./T2bbar-1).^I.*J.*HIJ.*(rho2bbar-1).^(J-1),2));
dmudrho = mu0.*dmu1drho*mustar/rhoc;
dmudp(valid2b) = -dmudrho./v2.^2.*dvdp_ph(p2b,h2) + dmudT.*dTdp_ph(p2b,h2);
end
if any(any(valid2c))
p2c = p(valid2c);h2 = h(valid2c);T2c = T2c_ph(p2c,h2);v2 = v2_pT(p2c,T2c);rho2cbar = 1./v2/rhoc;T2cbar = T2c/Tc;
mu0 = 100*sqrt(T2cbar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T2cbar)./T2cbar)./T2cbar);
dmu0dT = mu0/2./T2cbar.*(Hi(1) + (3*Hi(2) + (5*Hi(3) + 7*Hi(4)./T2cbar)./T2cbar)./T2cbar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T2cbar)./T2cbar)./T2cbar);
L = length(p2c);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T2cbar = T2cbar*ones(1,Nterms);rho2cbar = rho2cbar*ones(1,Nterms);
mu1 = exp(sum(rho2cbar.*(1./T2cbar-1).^I.*HIJ.*(rho2cbar-1).^J,2));
dmu1dT = mu1.*(sum(rho2cbar.*I.*(1./T2cbar-1).^(I-1).*(-1./T2cbar.^2).*HIJ.*(rho2cbar-1).^J,2));
dmudT = (dmu0dT.*mu1 + mu0.*dmu1dT)*mustar/Tc;
dmu1drho = mu1.*(sum((1./T2cbar-1).^I.*HIJ.*(rho2cbar-1).^J,2) + sum(rho2cbar.*(1./T2cbar-1).^I.*J.*HIJ.*(rho2cbar-1).^(J-1),2));
dmudrho = mu0.*dmu1drho*mustar/rhoc;
dmudp(valid2c) = -dmudrho./v2.^2.*dvdp_ph(p2c,h2) + dmudT.*dTdp_ph(p2c,h2);
end
if any(any(valid3a))
p3a = p(valid3a);h3a = h(valid3a);T3 = T3a_ph(p3a,h3a);T3abar = T3/Tc;v3 = v3a_ph(p3a,h3a);rho3abar = 1./v3/rhoc;
mu0 = 100*sqrt(T3abar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T3abar)./T3abar)./T3abar);
dmu0dT = mu0/2./T3abar.*(Hi(1) + (3*Hi(2) + (5*Hi(3) + 7*Hi(4)./T3abar)./T3abar)./T3abar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T3abar)./T3abar)./T3abar);
L = length(p3a);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T3abar = T3abar*ones(1,Nterms);rho3abar = rho3abar*ones(1,Nterms);
mu1 = exp(sum(rho3abar.*(1./T3abar-1).^I.*HIJ.*(rho3abar-1).^J,2));
dmu1dT = mu1.*(sum(rho3abar.*I.*(1./T3abar-1).^(I-1).*(-1./T3abar.^2).*HIJ.*(rho3abar-1).^J,2));
dmudT = (dmu0dT.*mu1 + mu0.*dmu1dT)*mustar/Tc;
dmu1drho = mu1.*(sum((1./T3abar-1).^I.*HIJ.*(rho3abar-1).^J,2) + sum(rho3abar.*(1./T3abar-1).^I.*J.*HIJ.*(rho3abar-1).^(J-1),2));
dmudrho = mu0.*dmu1drho*mustar/rhoc;
dmudp(valid3a) = -dmudrho./v3.^2.*dvdp_ph(p3a,h3a) + dmudT.*dTdp_ph(p3a,h3a);
end
if any(any(valid3b))
p3b = p(valid3b);h3b = h(valid3b);T3 = T3b_ph(p3b,h3b);T3bbar = T3/Tc;v3 = v3b_ph(p3b,h3b);rho3bbar = 1./v3/rhoc;
mu0 = 100*sqrt(T3bbar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T3bbar)./T3bbar)./T3bbar);
dmu0dT = mu0/2./T3bbar.*(Hi(1) + (3*Hi(2) + (5*Hi(3) + 7*Hi(4)./T3bbar)./T3bbar)./T3bbar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T3bbar)./T3bbar)./T3bbar);
L = length(p3b);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T3bbar = T3bbar*ones(1,Nterms);rho3bbar = rho3bbar*ones(1,Nterms);
mu1 = exp(sum(rho3bbar.*(1./T3bbar-1).^I.*HIJ.*(rho3bbar-1).^J,2));
dmu1dT = mu1.*(sum(rho3bbar.*I.*(1./T3bbar-1).^(I-1).*(-1./T3bbar.^2).*HIJ.*(rho3bbar-1).^J,2));
dmudT = (dmu0dT.*mu1 + mu0.*dmu1dT)*mustar/Tc;
dmu1drho = mu1.*(sum((1./T3bbar-1).^I.*HIJ.*(rho3bbar-1).^J,2) + sum(rho3bbar.*(1./T3bbar-1).^I.*J.*HIJ.*(rho3bbar-1).^(J-1),2));
dmudrho = mu0.*dmu1drho*mustar/rhoc;
dmudp(valid3b) = -dmudrho./v3.^2.*dvdp_ph(p3b,h3b) + dmudT.*dTdp_ph(p3b,h3b);
end
if any(any(valid4a))
p4a = p(valid4a);Tsat4a = Tsat(valid4a);h1L4a = h1L(valid4a);
h4 = h(valid4a);x = (h4-h1L4a)./(h2V(valid4a)-h1L4a); % quality
v1L = v1_pT(p4a,Tsat4a); % [m^3/kg] saturated liquid specific volumes
v2V = v2_pT(p4a,Tsat4a); % [m^3/kg] saturated vapor specific volumes
T4abar = Tsat4a/Tc;v4 = v1L + x.*(v2V - v1L);rho4abar = 1./v4/rhoc;
mu0 = 100*sqrt(T4abar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T4abar)./T4abar)./T4abar);
dmu0dT = mu0/2./T4abar.*(Hi(1) + (3*Hi(2) + (5*Hi(3) + 7*Hi(4)./T4abar)./T4abar)./T4abar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T4abar)./T4abar)./T4abar);
L = length(p4a);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T4abar = T4abar*ones(1,Nterms);rho4abar = rho4abar*ones(1,Nterms);
mu1 = exp(sum(rho4abar.*(1./T4abar-1).^I.*HIJ.*(rho4abar-1).^J,2));
dmu1dT = mu1.*(sum(rho4abar.*I.*(1./T4abar-1).^(I-1).*(-1./T4abar.^2).*HIJ.*(rho4abar-1).^J,2));
dmudT = (dmu0dT.*mu1 + mu0.*dmu1dT)*mustar/Tc;
dmu1drho = mu1.*(sum((1./T4abar-1).^I.*HIJ.*(rho4abar-1).^J,2) + sum(rho4abar.*(1./T4abar-1).^I.*J.*HIJ.*(rho4abar-1).^(J-1),2));
dmudrho = mu0.*dmu1drho*mustar/rhoc;
dmudp(valid4a) = -dmudrho./v4.^2.*dvdp_ph(p4a,h4) + dmudT.*dTdp_ph(p4a,h4);
end
if any(any(valid4b))
p4b = p(valid4b); Tsat4b = Tsat(valid4b);
v3L = vL_p(p4b); v3V = vV_p(p4b);
h3L = h3_rhoT(1./v3L,Tsat4b);
h3V = h3_rhoT(1./v3V,Tsat4b);
h4 = h(valid4b);x = (h4-h3L)./(h3V-h3L); % quality
T4bbar = Tsat4b/Tc;v4 = v3L + x.*(v3V - v3L);rho4bbar = 1./v4/rhoc;
mu0 = 100*sqrt(T4bbar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T4bbar)./T4bbar)./T4bbar);
dmu0dT = mu0/2./T4bbar.*(Hi(1) + (3*Hi(2) + (5*Hi(3) + 7*Hi(4)./T4bbar)./T4bbar)./T4bbar)./(Hi(1) + (Hi(2) + (Hi(3) + Hi(4)./T4bbar)./T4bbar)./T4bbar);
L = length(p4b);I = ones(L,1)*Hij(1,:);J = ones(L,1)*Hij(2,:);HIJ = ones(L,1)*Hij(3,:);
T4bbar = T4bbar*ones(1,Nterms);rho4bbar = rho4bbar*ones(1,Nterms);
mu1 = exp(sum(rho4bbar.*(1./T4bbar-1).^I.*HIJ.*(rho4bbar-1).^J,2));
dmu1dT = mu1.*(sum(rho4bbar.*I.*(1./T4bbar-1).^(I-1).*(-1./T4bbar.^2).*HIJ.*(rho4bbar-1).^J,2));
dmudT = (dmu0dT.*mu1 + mu0.*dmu1dT)*mustar/Tc;
dmu1drho = mu1.*(sum((1./T4bbar-1).^I.*HIJ.*(rho4bbar-1).^J,2) + sum(rho4bbar.*(1./T4bbar-1).^I.*J.*HIJ.*(rho4bbar-1).^(J-1),2));
dmudrho = mu0.*dmu1drho*mustar/rhoc;
dmudp(valid4b) = -dmudrho./v4.^2.*dvdp_ph(p4b,h4) + dmudT.*dTdp_ph(p4b,h4);
end
end
function dhLdp = dhLdp_p(p)
% dhLdp = dhLdp_ph(p)
% Derivative of enthalpy wrt pressure of saturated liquid, dhLdp [(kJ/kg)/MPa], as a function of pressure, p [MPa]
% based on IAPWS-IF97
% Reference: http://www.iapws.org/
% June 16, 2009
% Mark Mikofski
%% size of inputs
dim = size(p);
dhLdp = NaN(dim);
%% constants and calculated
conversion_factor = 1e-3; % [MPa/(kJ/m^3)]
Tmin = 273.16; % [K] minimum temperature is triple point
TB13 = 623.15; % [K] temperature at boundary between region 1 and 3
pmin = psat_T(Tmin); % [MPa] minimum pressure is 611.657 Pa
pB13sat = psat_T(TB13); % [MPa] saturation pressure at boundary between region 1 and 3, 16.5291643 MPa
pc = 22.064; % [MPa] critical pressure
Tsat = Tsat_p(p); % [K] saturation temperatures
%% valid ranges
valid4a = p>=pmin & p<=pB13sat; % valid range for saturated liquid in region 4a
valid4b = p>pB13sat & p<=pc; % valid range for saturated liquid in region 4b
if any(any(valid4a))
p4a = p(valid4a);Tsat4a = Tsat(valid4a);
dhLdp(valid4a) = v1_pT(p4a,Tsat4a).*(1-Tsat4a.*alphav1_pT(p4a,Tsat4a))/conversion_factor + cp1_pT(p4a,Tsat4a).*dTsatdpsat_p(p4a); % [(kJ/kg)/MPa]
end
if any(any(valid4b))
p4b = p(valid4b); Tsat4b = Tsat(valid4b);v3L = vL_p(p4b);rho3L = 1./v3L;dTsatdpsat4b = dTsatdpsat_p(p4b);
betap3L = betap3_rhoT(rho3L,Tsat4b);alphap3L = alphap3_rhoT(rho3L,Tsat4b);cv3L = cv3_rhoT(rho3L,Tsat4b);
dhLdp(valid4b) = (v3L - Tsat4b.*alphap3L./betap3L.*(1 - p4b.*alphap3L.*dTsatdpsat4b))/conversion_factor + (cv3L + p4b.*v3L.*alphap3L).*dTsatdpsat4b;
end
end
function dhVdp = dhVdp_p(p)
% dhVdp = dhVdp_ph(p)
% Derivative of enthalpy wrt pressure of saturated vapor, dhVdp [(kJ/kg)/MPa], as a function of pressure, p [MPa]
% based on IAPWS-IF97
% Reference: http://www.iapws.org/
% June 16, 2009
% Mark Mikofski
%% size of inputs
dim = size(p);
dhVdp = NaN(dim);
%% constants and calculated
conversion_factor = 1e-3; % [MPa/(kJ/m^3)]
Tmin = 273.16; % [K] minimum temperature is triple point
TB13 = 623.15; % [K] temperature at boundary between region 1 and 3
pmin = psat_T(Tmin); % [MPa] minimum pressure is 611.657 Pa
pB13sat = psat_T(TB13); % [MPa] saturation pressure at boundary between region 1 and 3, 16.5291643 MPa
pc = 22.064; % [MPa] critical pressure
Tsat = Tsat_p(p); % [K] saturation temperatures
%% valid ranges
valid4a = p>=pmin & p<=pB13sat; % valid range for saturated liquid in region 4a
valid4b = p>pB13sat & p<=pc; % valid range for saturated liquid in region 4b
if any(any(valid4a))
p4a = p(valid4a);Tsat4a = Tsat(valid4a);
dhVdp(valid4a) = v2_pT(p4a,Tsat4a).*(1-Tsat4a.*alphav2_pT(p4a,Tsat4a))/conversion_factor + cp2_pT(p4a,Tsat4a).*dTsatdpsat_p(p4a); % [(kJ/kg)/MPa]
end
if any(any(valid4b))
p4b = p(valid4b); Tsat4b = Tsat(valid4b);v3V = vV_p(p4b);rho3V = 1./v3V;dTsatdpsat4b = dTsatdpsat_p(p4b);
betap3V = betap3_rhoT(rho3V,Tsat4b);alphap3V = alphap3_rhoT(rho3V,Tsat4b);cv3V = cv3_rhoT(rho3V,Tsat4b);
dhVdp(valid4b) = (v3V - Tsat4b.*alphap3V./betap3V.*(1 - p4b.*alphap3V.*dTsatdpsat4b))/conversion_factor + (cv3V + p4b.*v3V.*alphap3V).*dTsatdpsat4b;
end
end
function dvLdp = dvLdp_p(p)
% dvLdp = dvLdp_ph(p)
% Derivative of specific volument wrt pressure of saturated liquid, dvLdp [(m^3/kg)/MPa], as a function of pressure, p [MPa]
% based on IAPWS-IF97
% Reference: http://www.iapws.org/
% June 16, 2009
% Mark Mikofski
%% size of inputs
dim = size(p);
dvLdp = NaN(dim);
%% constants and calculated
Tmin = 273.16; % [K] minimum temperature is triple point
TB13 = 623.15; % [K] temperature at boundary between region 1 and 3
pmin = psat_T(Tmin); % [MPa] minimum pressure is 611.657 Pa
pB13sat = psat_T(TB13); % [MPa] saturation pressure at boundary between region 1 and 3, 16.5291643 MPa
pc = 22.064; % [MPa] critical pressure
Tsat = Tsat_p(p); % [K] saturation temperatures
%% valid ranges
valid4a = p>=pmin & p<=pB13sat; % valid range for saturated liquid in region 4a
valid4b = p>pB13sat & p<=pc; % valid range for saturated liquid in region 4b
if any(any(valid4a))
p4a = p(valid4a);Tsat4a = Tsat(valid4a);
vL4a = v1_pT(p4a,Tsat4a);dTsatdpsat4a = dTsatdpsat_p(p4a);
alphavL4a = alphav1_pT(p4a,Tsat4a);
dvLdp(valid4a) = vL4a.*(-kappaT1_pT(p4a,Tsat4a) + alphavL4a.*dTsatdpsat4a); % [(m^3/kg)/MPa]
end
if any(any(valid4b))
p4b = p(valid4b); Tsat4b = Tsat(valid4b);v3L = vL_p(p4b);rho3L = 1./v3L;dTsatdpsat4b = dTsatdpsat_p(p4b);