Changeset 757 for branches/gui/eml/mixers_splitters/splitter.mso
- Timestamp:
- Jun 3, 2009, 5:07:22 PM (14 years ago)
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branches/gui/eml/mixers_splitters/splitter.mso
r739 r757 219 219 220 220 end 221 222 Model splitter_column 223 ATTRIBUTES 224 Pallete = true; 225 Icon = "icon/splitter_column"; 226 Brief = "Splitter with 2 outlet streams to be used with column section model"; 227 Info = 228 "== Assumptions == 229 *Thermodynamics equilibrium 230 *Adiabatic 231 232 == Specify == 233 * The inlet stream 234 * One FlowRatios of split of the outlet streams: 235 236 FlowRatios(i) = (Mole Flow of the outlet stream i / 237 Mole Flow of the inlet stream) 238 where i = 1, 2 239 "; 240 241 VARIABLES 242 in Inlet as stream (Brief = "Inlet stream", PosX=0.5, PosY=0, Symbol="_{in}"); 243 out Reflux as stream (Brief = "Reflux stream", PosX=0.25, PosY=1, Symbol="_{reflux}"); 244 out Distillate as stream (Brief = "Distillate stream", PosX=0.75, PosY=1, Symbol="_{distillate}"); 245 FlowRatios(2) as fraction (Brief = "Distribution of Outlets", Default=0.33, Symbol="\phi"); 246 247 EQUATIONS 248 249 "Normalize Flow Ratios" 250 sum(FlowRatios) = 1; 251 252 "Flow" 253 Reflux.F = Inlet.F * FlowRatios(1); 254 Inlet.F = Reflux.F + Distillate.F; 255 256 "Composition" 257 Reflux.z = Inlet.z; 258 Distillate.z = Inlet.z; 259 260 "Pressure" 261 Reflux.P = Inlet.P; 262 Distillate.P = Inlet.P; 263 264 "Enthalpy" 265 Reflux.h = Inlet.h; 266 Distillate.h = Inlet.h; 267 268 "Temperature" 269 Reflux.T = Inlet.T; 270 Distillate.T = Inlet.T; 271 272 "Vapourisation Fraction" 273 Reflux.v = Inlet.v; 274 Distillate.v = Inlet.v; 275 276 end
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