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| 1 | +%% Property functions of dry air at ambient pressure |
| 2 | +%GNU General Public License v3.0 |
| 3 | +%By Stefan Thanheiser: https://orcid.org/0000-0003-2765-1156 |
| 4 | +% |
| 5 | +%Modified from: |
| 6 | +%Stefan Thanheiser, "sthanhe/HeatTransfer: Round 3 Release”. Zenodo, Jan. |
| 7 | +%22, 2022. doi: 10.5281/zenodo.5911319. |
| 8 | +% |
| 9 | +% |
| 10 | +%Part of the paper: |
| 11 | +% |
| 12 | +%Thanheiser, S.; Haider, M. |
| 13 | +%Particle Mass Diffusion Model for Level Control of Bubbling Fluidized Beds |
| 14 | +%with Horizontal Particle Flow |
| 15 | +%Powder Technology 2023 |
| 16 | +% |
| 17 | +%All required files for this class can be found in the software |
| 18 | +%repository: |
| 19 | +%https://doi.org/10.5281/zenodo.xxxxxxx |
| 20 | +% |
| 21 | +% |
| 22 | +% |
| 23 | +%This class describes the thermo-physical properties of dry air as an ideal |
| 24 | +%gas according to: |
| 25 | +% |
| 26 | +%Span, R. Properties of Dry Air. In VDI Heat Atlas, 2nd ed.; Stephan, P., |
| 27 | +%Kabelac, S., et al., Eds.; Springer: Berlin Heidelberg, Germany, 2010; |
| 28 | +%pp. 172–191. https://doi.org/10.1007/978-3-540-77877-6_11 |
| 29 | +% |
| 30 | +% |
| 31 | +%Requires all files packaged in the class folder and on the MATLAB path |
| 32 | +% |
| 33 | +%Required products: |
| 34 | +% - MATLAB, version 9.14 |
| 35 | +%Data files: |
| 36 | +% - dryAir.xls |
| 37 | +% - dryAirTable.mat |
| 38 | + |
| 39 | + |
| 40 | +classdef DryAir |
| 41 | + %All parameters and results in SI base units |
| 42 | + |
| 43 | + %% Constants |
| 44 | + properties(Constant) |
| 45 | + M=28.9583e-3; %molar mass |
| 46 | + R=287.12; %specific gas constant |
| 47 | + end |
| 48 | + |
| 49 | + |
| 50 | + %% prop(T) functions |
| 51 | + methods(Static) |
| 52 | + function rho=rho(p,T) |
| 53 | + %Density |
| 54 | + rho=p./(DryAir.R.*T); |
| 55 | + end |
| 56 | + |
| 57 | + |
| 58 | + function h=h(T) |
| 59 | + %Specific enthalpy |
| 60 | + persistent tab |
| 61 | + if isempty(tab) |
| 62 | + tabStruct=coder.load('@DryAir\dryAirTable.mat','tab'); |
| 63 | + tab=tabStruct.tab; |
| 64 | + end |
| 65 | + |
| 66 | + h=interp1(tab.T,tab.h,T); |
| 67 | + end |
| 68 | + |
| 69 | + |
| 70 | + function s=s(T) |
| 71 | + %Specific entropy. Does not account for pressure variations! |
| 72 | + persistent tab |
| 73 | + if isempty(tab) |
| 74 | + tabStruct=coder.load('@DryAir\dryAirTable.mat','tab'); |
| 75 | + tab=tabStruct.tab; |
| 76 | + end |
| 77 | + |
| 78 | + s=interp1(tab.T,tab.s,T); |
| 79 | + end |
| 80 | + |
| 81 | + |
| 82 | + function c_p=c_p(T) |
| 83 | + %Specific isobaric heat capacity |
| 84 | + persistent tab |
| 85 | + if isempty(tab) |
| 86 | + tabStruct=coder.load('@DryAir\dryAirTable.mat','tab'); |
| 87 | + tab=tabStruct.tab; |
| 88 | + end |
| 89 | + |
| 90 | + c_p=interp1(tab.T,tab.c_p,T); |
| 91 | + end |
| 92 | + |
| 93 | + |
| 94 | + function c_v=c_v(T) |
| 95 | + %Specific isochoric heat capacity |
| 96 | + persistent tab |
| 97 | + if isempty(tab) |
| 98 | + tabStruct=coder.load('@DryAir\dryAirTable.mat','tab'); |
| 99 | + tab=tabStruct.tab; |
| 100 | + end |
| 101 | + |
| 102 | + c_v=interp1(tab.T,tab.c_v,T); |
| 103 | + end |
| 104 | + |
| 105 | + |
| 106 | + function kappa=kappa(T) |
| 107 | + %Isentropic exponent |
| 108 | + kappa=DryAir.c_p(T)./DryAir.c_v(T); |
| 109 | + end |
| 110 | + |
| 111 | + |
| 112 | + function beta=beta(T) |
| 113 | + %Coefficient of thermal expansion |
| 114 | + persistent tab |
| 115 | + if isempty(tab) |
| 116 | + tabStruct=coder.load('@DryAir\dryAirTable.mat','tab'); |
| 117 | + tab=tabStruct.tab; |
| 118 | + end |
| 119 | + |
| 120 | + beta=interp1(tab.T,tab.beta,T); |
| 121 | + end |
| 122 | + |
| 123 | + |
| 124 | + function w_s=w_s(T) |
| 125 | + %Speed of sound |
| 126 | + persistent tab |
| 127 | + if isempty(tab) |
| 128 | + tabStruct=coder.load('@DryAir\dryAirTable.mat','tab'); |
| 129 | + tab=tabStruct.tab; |
| 130 | + end |
| 131 | + |
| 132 | + w_s=interp1(tab.T,tab.w_s,T); |
| 133 | + end |
| 134 | + |
| 135 | + |
| 136 | + function lambda=lambda(T) |
| 137 | + %Heat conductivity |
| 138 | + persistent tab |
| 139 | + if isempty(tab) |
| 140 | + tabStruct=coder.load('@DryAir\dryAirTable.mat','tab'); |
| 141 | + tab=tabStruct.tab; |
| 142 | + end |
| 143 | + |
| 144 | + lambda=interp1(tab.T,tab.lambda,T); |
| 145 | + end |
| 146 | + |
| 147 | + |
| 148 | + function eta=eta(T) %#codegen |
| 149 | + %Dynamic viscosity |
| 150 | + persistent tab |
| 151 | + if isempty(tab) |
| 152 | + tabStruct=coder.load('@DryAir\dryAirTable.mat','tab'); |
| 153 | + tab=tabStruct.tab; |
| 154 | + end |
| 155 | + |
| 156 | + eta=interp1(tab.T,tab.eta,T); |
| 157 | + end |
| 158 | + |
| 159 | + |
| 160 | + function ny=ny(p,T) |
| 161 | + %Kinematic viscosity |
| 162 | + persistent tab |
| 163 | + if isempty(tab) |
| 164 | + tabStruct=coder.load('@DryAir\dryAirTable.mat','tab'); |
| 165 | + tab=tabStruct.tab; |
| 166 | + end |
| 167 | + |
| 168 | + ny=DryAir.eta(T)./DryAir.rho(p,T); |
| 169 | + end |
| 170 | + |
| 171 | + |
| 172 | + function a=a(p,T) |
| 173 | + %Thermal diffusivity |
| 174 | + a=DryAir.ny(p,T)./DryAir.Pr(T); |
| 175 | + end |
| 176 | + |
| 177 | + |
| 178 | + function Pr=Pr(T) |
| 179 | + %Prandtl number |
| 180 | + persistent tab |
| 181 | + if isempty(tab) |
| 182 | + tabStruct=coder.load('@DryAir\dryAirTable.mat','tab'); |
| 183 | + tab=tabStruct.tab; |
| 184 | + end |
| 185 | + |
| 186 | + Pr=interp1(tab.T,tab.Pr,T); |
| 187 | + end |
| 188 | + end |
| 189 | + |
| 190 | + |
| 191 | + %% Other property functions |
| 192 | + methods(Static) |
| 193 | + function T=T_h(h) |
| 194 | + %Backwards-equation for temperature as function of specific |
| 195 | + %enthalpy |
| 196 | + persistent tab |
| 197 | + if isempty(tab) |
| 198 | + tabStruct=coder.load('@DryAir\dryAirTable.mat','tab'); |
| 199 | + tab=tabStruct.tab; |
| 200 | + end |
| 201 | + |
| 202 | + T=interp1(tab.h,tab.T,h); |
| 203 | + end |
| 204 | + end |
| 205 | + |
| 206 | + |
| 207 | + %% Auxilliary Functions |
| 208 | + methods(Static) |
| 209 | + function createConstants() |
| 210 | + %Creates the lookup-constants from the Excel-file |
| 211 | + clear('DryAir'); |
| 212 | + |
| 213 | + tab=readtable('@DryAir\dryAir.xls','Range','A1:M53'); |
| 214 | + |
| 215 | + tab{:,'T'}=tab{:,'T'}+273.15; |
| 216 | + tab{:,'h'}=tab{:,'h'}*1000; |
| 217 | + tab{:,'s'}=tab{:,'s'}*1000; |
| 218 | + tab{:,'c_p'}=tab{:,'c_p'}*1000; |
| 219 | + tab{:,'c_v'}=tab{:,'c_v'}*1000; |
| 220 | + tab{:,'beta'}=tab{:,'beta'}/1000; |
| 221 | + tab{:,'lambda'}=tab{:,'lambda'}/1000; |
| 222 | + tab{:,'eta'}=tab{:,'eta'}*10^-6; |
| 223 | + tab{:,'ny'}=tab{:,'ny'}*10^-7; |
| 224 | + tab{:,'a'}=tab{:,'a'}*10^-7; |
| 225 | + |
| 226 | + save('dryAirTable.mat','tab'); |
| 227 | + end |
| 228 | + end |
| 229 | +end |
| 230 | + |
| 231 | + |
| 232 | + |
| 233 | + |
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