- Timestamp:
- Aug 30, 2007, 2:39:11 AM (15 years ago)
- Location:
- trunk/eml
- Files:
-
- 16 edited
Legend:
- Unmodified
- Added
- Removed
-
trunk/eml/electrical/electrical.mso
r325 r352 43 43 44 44 VARIABLES 45 in inlet as wire (Brief = "Inlet", PosX=0.3831, PosY=0 );46 out outlet as wire (Brief = "Outlet", PosX=0.3529, PosY=1 );45 in inlet as wire (Brief = "Inlet", PosX=0.3831, PosY=0, Symbol="_{in}"); 46 out outlet as wire (Brief = "Outlet", PosX=0.3529, PosY=1, Symbol="_{out}"); 47 47 48 48 EQUATIONS … … 62 62 VARIABLES 63 63 q as charge; 64 in inlet as wire (Brief = "Inlet", PosX=0.3978, PosY=0 );65 out outlet as wire (Brief = "Outlet", PosX=0.3965, PosY=1 );64 in inlet as wire (Brief = "Inlet", PosX=0.3978, PosY=0, Symbol="_{in}"); 65 out outlet as wire (Brief = "Outlet", PosX=0.3965, PosY=1, Symbol="_{out}"); 66 66 67 67 EQUATIONS … … 81 81 82 82 VARIABLES 83 in inlet as wire (Brief = "Inlet", PosX=0.4638, PosY=0 );84 out outlet as wire (Brief = "Outlet", PosX=0.4638, PosY=1 );83 in inlet as wire (Brief = "Inlet", PosX=0.4638, PosY=0, Symbol="_{in}"); 84 out outlet as wire (Brief = "Outlet", PosX=0.4638, PosY=1, Symbol="_{out}"); 85 85 86 86 EQUATIONS … … 100 100 101 101 VARIABLES 102 in inlet as wire (Brief = "Inlet", PosX=0.3923, PosY=0 );103 out outlet as wire (Brief = "Outlet", PosX=0.3984, PosY=1 );102 in inlet as wire (Brief = "Inlet", PosX=0.3923, PosY=0, Symbol="_{in}"); 103 out outlet as wire (Brief = "Outlet", PosX=0.3984, PosY=1, Symbol="_{out}"); 104 104 105 105 EQUATIONS -
trunk/eml/heat_exchangers/DoublePipe.mso
r325 r352 57 57 VARIABLES 58 58 59 in InletInner as stream (Brief="Inlet Inner Stream", PosX=0, PosY=0.5225 );60 in InletOuter as stream (Brief="Inlet Outer Stream", PosX=0.2805, PosY=0 );61 out OutletInner as streamPH (Brief="Outlet Inner Stream", PosX=1, PosY=0.5225 );62 out OutletOuter as streamPH (Brief="Outlet Outer Stream", PosX=0.7264, PosY=1 );59 in InletInner as stream (Brief="Inlet Inner Stream", PosX=0, PosY=0.5225, Symbol="_{inInner}"); 60 in InletOuter as stream (Brief="Inlet Outer Stream", PosX=0.2805, PosY=0, Symbol="_{inOuter}"); 61 out OutletInner as streamPH (Brief="Outlet Inner Stream", PosX=1, PosY=0.5225, Symbol="_{outInner}"); 62 out OutletOuter as streamPH (Brief="Outlet Outer Stream", PosX=0.7264, PosY=1, Symbol="_{outOuter}"); 63 63 64 64 Details as Details_Main (Brief="Some Details in the Heat Exchanger"); -
trunk/eml/heat_exchangers/HeatExchangerDetailed.mso
r325 r352 33 33 VARIABLES 34 34 35 in InletTube as stream (Brief="Inlet Tube Stream", PosX=0, PosY=0.4915 );36 out OutletTube as streamPH (Brief="Outlet Tube Stream", PosX=1, PosY=0.4915 );37 in InletShell as stream (Brief="Inlet Shell Stream", PosX=0.5237, PosY=1 );38 out OutletShell as streamPH (Brief="Outlet Shell Stream", PosX=0.5237, PosY=0 );35 in InletTube as stream (Brief="Inlet Tube Stream", PosX=0, PosY=0.4915, Symbol="_{inTube}"); 36 out OutletTube as streamPH (Brief="Outlet Tube Stream", PosX=1, PosY=0.4915, Symbol="_{outTube}"); 37 in InletShell as stream (Brief="Inlet Shell Stream", PosX=0.5237, PosY=1, Symbol="_{inShell}"); 38 out OutletShell as streamPH (Brief="Outlet Shell Stream", PosX=0.5237, PosY=0, Symbol="_{outShell}"); 39 39 40 40 Details as Details_Main (Brief="Details in Heat Exchanger"); -
trunk/eml/heat_exchangers/HeatExchangerSimplified.mso
r325 r352 36 36 VARIABLES 37 37 38 in InletHot as stream (Brief="Inlet Hot Stream", PosX=0, PosY=0.4915 );39 out OutletHot as streamPH (Brief="Outlet Hot Stream", PosX=1, PosY=0.4915 );40 in InletCold as stream (Brief="Inlet Cold Stream", PosX=0.5237, PosY=1 );41 out OutletCold as streamPH (Brief="Outlet Cold Stream", PosX=0.5237, PosY=0 );38 in InletHot as stream (Brief="Inlet Hot Stream", PosX=0, PosY=0.4915, Symbol="_{inHot}"); 39 out OutletHot as streamPH (Brief="Outlet Hot Stream", PosX=1, PosY=0.4915, Symbol="_{outHot}"); 40 in InletCold as stream (Brief="Inlet Cold Stream", PosX=0.5237, PosY=1, Symbol="_{inCold}"); 41 out OutletCold as streamPH (Brief="Outlet Cold Stream", PosX=0.5237, PosY=0, Symbol="_{outCold}"); 42 42 43 43 xh(NComp) as fraction (Brief = "Liquid Molar Fraction in Hot Side"); -
trunk/eml/heat_exchangers/Mheatex.mso
r325 r352 38 38 VARIABLES 39 39 40 in InletHot(Nhot) as stream (Brief="Inlet Hot Streams", PosX=0, PosY=0.7156 );41 out OutletHot(Nhot) as streamPH (Brief="Outlet Hot Streams", PosX=1, PosY=0.7156 );42 in InletCold(Ncold) as stream (Brief="Inlet Cold Streams", PosX=1, PosY=0.2793 );43 out OutletCold(Ncold) as streamPH (Brief="Outlet Cold Streams", PosX=0, PosY=0.2793 );40 in InletHot(Nhot) as stream (Brief="Inlet Hot Streams", PosX=0, PosY=0.7156, Symbol="_{inHot}"); 41 out OutletHot(Nhot) as streamPH (Brief="Outlet Hot Streams", PosX=1, PosY=0.7156, Symbol="_{outHot}"); 42 in InletCold(Ncold) as stream (Brief="Inlet Cold Streams", PosX=1, PosY=0.2793, Symbol="_{inCold}"); 43 out OutletCold(Ncold) as streamPH (Brief="Outlet Cold Streams", PosX=0, PosY=0.2793, Symbol="_{outCold}"); 44 44 45 45 Method as LMTD_Basic (Brief="Log Mean Temperature Difference Method"); -
trunk/eml/heat_exchangers/PHE.mso
r325 r352 83 83 VARIABLES 84 84 85 in InletHot as stream (Brief="Inlet Hot Stream", PosX=0, PosY=0.7156 );86 in InletCold as stream (Brief="Inlet Cold Stream", PosX=1, PosY=0.7156 );87 out OutletHot as streamPH (Brief="Outlet Hot Stream", PosX=0, PosY=0.2793 );88 out OutletCold as streamPH (Brief="Outlet Cold Stream", PosX=1, PosY=0.2793 );85 in InletHot as stream (Brief="Inlet Hot Stream", PosX=0, PosY=0.7156, Symbol="_{inHot}"); 86 in InletCold as stream (Brief="Inlet Cold Stream", PosX=1, PosY=0.7156, Symbol="_{inCold}"); 87 out OutletHot as streamPH (Brief="Outlet Hot Stream", PosX=0, PosY=0.2793, Symbol="_{outHot}"); 88 out OutletCold as streamPH (Brief="Outlet Cold Stream", PosX=1, PosY=0.2793, Symbol="_{outCold}"); 89 89 90 90 HotSide as Main_PHE (Brief="Plate Heat Exchanger Hot Side"); -
trunk/eml/heat_exchangers/heater.mso
r326 r352 38 38 Lfrac as fraction (Brief = "Liquid fraction Outlet Stream"); 39 39 Kvalue(NComp) as Real (Brief = "Phase Equilibrium K-values"); 40 in Inlet(Ninlet ) as stream (Brief="Inlet Streams", PosX=0, PosY=0.4833 );41 out Outlet as streamPH (Brief="Outlet Stream", PosX=1, PosY=0.4782 );40 in Inlet(Ninlet ) as stream (Brief="Inlet Streams", PosX=0, PosY=0.4833, Symbol="_{in}"); 41 out Outlet as streamPH (Brief="Outlet Stream", PosX=1, PosY=0.4782, Symbol="_{out}"); 42 42 43 43 EQUATIONS … … 85 85 86 86 VARIABLES 87 in InletQ as energy_stream (Brief ="Inlet Heat Stream", PosX=0.1662, PosY=1 );87 in InletQ as energy_stream (Brief ="Inlet Heat Stream", PosX=0.1662, PosY=1, Symbol="_{out}"); 88 88 89 89 EQUATIONS … … 102 102 103 103 VARIABLES 104 in InletQ as energy_stream (Brief ="Inlet Heat Stream", PosX=0.8245, PosY=1 );104 in InletQ as energy_stream (Brief ="Inlet Heat Stream", PosX=0.8245, PosY=1, Symbol="_{out}"); 105 105 106 106 EQUATIONS -
trunk/eml/reactors/batch.mso
r325 r352 38 38 VARIABLES 39 39 40 in Inlet as stream (Brief="Inlet stream", PosX=0, PosY=0 );40 in Inlet as stream (Brief="Inlet stream", PosX=0, PosY=0, Symbol="_{in}"); 41 41 C(NComp) as conc_mol (Brief="Components concentration"); 42 42 r(NReac) as reaction_mol (Brief = "Reaction rates"); -
trunk/eml/reactors/cstr.mso
r325 r352 37 37 VARIABLES 38 38 39 in Inlet as stream (Brief="Inlet Stream", PosX=0, PosY=0 );40 out Outlet as streamPH (Brief="Outlet Stream", PosX=1, PosY=1 );39 in Inlet as stream (Brief="Inlet Stream", PosX=0, PosY=0, Symbol="_{in}"); 40 out Outlet as streamPH (Brief="Outlet Stream", PosX=1, PosY=1, Symbol="_{out}"); 41 41 42 42 q as heat_rate (Brief="Heat"); -
trunk/eml/reactors/pfr.mso
r325 r352 50 50 VARIABLES 51 51 52 in Inlet as stream (Brief = "Inlet Stream", PosX=0, PosY=0.5076 );53 out Outlet as stream (Brief = "Outlet Stream", PosX=1, PosY=0.5236 );52 in Inlet as stream (Brief = "Inlet Stream", PosX=0, PosY=0.5076, Symbol="_{in}"); 53 out Outlet as stream (Brief = "Outlet Stream", PosX=1, PosY=0.5236, Symbol="_{out}"); 54 54 55 55 str(NDisc+1) as streamPH; -
trunk/eml/stage_separators/batch_dist.mso
r325 r352 48 48 49 49 VARIABLES 50 in Inlet as stream (Brief="Feed stream", PosX=0, PosY=0.9385 );51 in InletL as stream (Brief="Liquid inlet stream", PosX=0.5, PosY=0.1984 ); # FIXME52 out OutletV as vapour_stream (Brief="Vapour outlet stream", PosX=1, PosY=0.1984 );53 in InletQ as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.9578 );50 in Inlet as stream (Brief="Feed stream", PosX=0, PosY=0.9385, Symbol="_{in}"); 51 in InletL as stream (Brief="Liquid inlet stream", PosX=0.5, PosY=0.1984, Symbol="_{inL}"); # FIXME 52 out OutletV as vapour_stream (Brief="Vapour outlet stream", PosX=1, PosY=0.1984, Symbol="_{outV}"); 53 in InletQ as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.9578, Symbol="_{in}"); 54 54 55 55 M(NComp) as mol (Brief="Molar Holdup in the distillator"); -
trunk/eml/stage_separators/condenser.mso
r325 r352 48 48 49 49 VARIABLES 50 in InletV as stream(Brief="Vapour inlet stream", PosX=0.1164, PosY=0 );51 out OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4513, PosY=1 );52 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4723, PosY=0 );53 in InletQ as energy_stream (Brief="Cold supplied", PosX=1, PosY=0.6311 );50 in InletV as stream(Brief="Vapour inlet stream", PosX=0.1164, PosY=0, Symbol="_{inV}"); 51 out OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4513, PosY=1, Symbol="_{outL}"); 52 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4723, PosY=0, Symbol="_{outV}"); 53 in InletQ as energy_stream (Brief="Cold supplied", PosX=1, PosY=0.6311, Symbol="_{in}"); 54 54 55 55 M(NComp) as mol (Brief="Molar Holdup in the tray"); … … 127 127 128 128 VARIABLES 129 in InletV as stream(Brief="Vapour inlet stream", PosX=0.3431, PosY=0 );130 out OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.34375, PosY=1 );131 in InletQ as energy_stream (Brief="Cold supplied", PosX=1, PosY=0.5974 );129 in InletV as stream(Brief="Vapour inlet stream", PosX=0.3431, PosY=0, Symbol="_{inV}"); 130 out OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.34375, PosY=1, Symbol="_{outL}"); 131 in InletQ as energy_stream (Brief="Cold supplied", PosX=1, PosY=0.5974, Symbol="_{in}"); 132 132 DP as press_delta (Brief="Pressure Drop in the condenser"); 133 133 … … 181 181 182 182 VARIABLES 183 in InletV as stream(Brief="Vapour inlet stream", PosX=0.1164, PosY=0 );184 out OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4513, PosY=1 );185 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4723, PosY=0 );186 in InletQ as energy_stream (Brief="Cold supplied", PosX=1, PosY=0.6311 );183 in InletV as stream(Brief="Vapour inlet stream", PosX=0.1164, PosY=0, Symbol="_{inV}"); 184 out OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4513, PosY=1, Symbol="_{outL}"); 185 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4723, PosY=0, Symbol="_{outV}"); 186 in InletQ as energy_stream (Brief="Cold supplied", PosX=1, PosY=0.6311, Symbol="_{in}"); 187 187 188 188 M(NComp) as mol (Brief="Molar Holdup in the tray"); -
trunk/eml/stage_separators/flash.mso
r334 r352 50 50 51 51 VARIABLES 52 in Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421 );53 out OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1 );54 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0 );55 in InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7559 );52 in Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421, Symbol="_{in}"); 53 out OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1, Symbol="_{outL}"); 54 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0, Symbol="_{outV}"); 55 in InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7559, Symbol="_{in}"); 56 56 57 57 M(NComp) as mol (Brief="Molar Holdup in the tray"); … … 63 63 Level as length (Brief="liquid height"); 64 64 Across as area (Brief="Flash Cross section area"); 65 vfrac as positive (Brief="Vapourization fraction" );65 vfrac as positive (Brief="Vapourization fraction", Symbol="\phi"); 66 66 67 67 EQUATIONS … … 146 146 147 147 VARIABLES 148 in Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421 );149 out OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1 );150 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0 );151 in InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7559 );152 vfrac as fraction (Brief="Vapourization fraction" );148 in Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421, Symbol="_{in}"); 149 out OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1, Symbol="_{outL}"); 150 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0, Symbol="_{outV}"); 151 in InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7559, Symbol="_{in}"); 152 vfrac as fraction (Brief="Vapourization fraction", Symbol="\phi"); 153 153 154 154 EQUATIONS … … 198 198 199 199 VARIABLES 200 in Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421 );201 out OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1 );202 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0 );203 in InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7559 );204 vfrac as fraction(Brief="Vaporization fraction" );200 in Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421, Symbol="_{in}"); 201 out OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1, Symbol="_{outL}"); 202 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0, Symbol="_{outV}"); 203 in InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7559, Symbol="_{in}"); 204 vfrac as fraction(Brief="Vaporization fraction", Symbol="\phi"); 205 205 h as enth_mol(Brief="Mixture enthalpy"); 206 206 … … 256 256 257 257 VARIABLES 258 in Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421 );259 out OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1 );260 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0 );261 in InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7559 );262 vfrac as fraction(Brief="Vaporization fraction" );263 vsat as Real(Lower=-0.1, Upper=1.1, Brief="Vaporization fraction if saturated" );258 in Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421, Symbol="_{in}"); 259 out OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1, Symbol="_{outL}"); 260 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0, Symbol="_{outV}"); 261 in InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7559, Symbol="_{in}"); 262 vfrac as fraction(Brief="Vaporization fraction", Symbol="\phi"); 263 vsat as Real(Lower=-0.1, Upper=1.1, Brief="Vaporization fraction if saturated", Symbol="\phi_{sat}"); 264 264 Tsat as temperature(Lower=173, Upper=1473, Brief="Temperature if saturated"); 265 265 xsat(NComp) as Real(Lower=0, Upper=1, Brief="Liquid composition if saturated"); -
trunk/eml/stage_separators/reboiler.mso
r325 r352 56 56 57 57 VARIABLES 58 in Inlet as stream(Brief="Feed Stream", PosX=0.8127, PosY=0 );59 in InletL as stream(Brief="Liquid inlet stream", PosX=0, PosY=0.5254 );60 out OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.2413, PosY=1 );61 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.5079, PosY=0 );62 in InletQ as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.6123 );58 in Inlet as stream(Brief="Feed Stream", PosX=0.8127, PosY=0, Symbol="_{in}"); 59 in InletL as stream(Brief="Liquid inlet stream", PosX=0, PosY=0.5254, Symbol="_{inL}"); 60 out OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.2413, PosY=1, Symbol="_{outL}"); 61 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.5079, PosY=0, Symbol="_{outV}"); 62 in InletQ as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.6123, Symbol="_{in}"); 63 63 64 64 M(NComp) as mol (Brief="Molar Holdup in the tray"); … … 141 141 142 142 VARIABLES 143 in InletL as stream(Brief="Liquid inlet stream", PosX=0.3345, PosY=1 );144 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.3369, PosY=0 );145 in InletQ as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.6111 );143 in InletL as stream(Brief="Liquid inlet stream", PosX=0.3345, PosY=1, Symbol="_{inL}"); 144 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.3369, PosY=0, Symbol="_{outV}"); 145 in InletQ as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.6111, Symbol="_{in}"); 146 146 vV as volume_mol (Brief="Vapour Molar volume"); 147 147 rhoV as dens_mass (Brief="Vapour Density"); … … 188 188 189 189 VARIABLES 190 in InletL as stream(Brief="Liquid inlet stream", PosX=0.3345, PosY=1 );191 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.3369, PosY=0 );192 in InletQ as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.6111 );190 in InletL as stream(Brief="Liquid inlet stream", PosX=0.3345, PosY=1, Symbol="_{inL}"); 191 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.3369, PosY=0, Symbol="_{outV}"); 192 in InletQ as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.6111, Symbol="_{in}"); 193 193 194 194 EQUATIONS … … 252 252 253 253 VARIABLES 254 in Inlet as stream(Brief="Feed Stream", PosX=0.8127, PosY=0 );255 in InletL as stream(Brief="Liquid inlet stream", PosX=0, PosY=0.5254 );256 out OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.2413, PosY=1 );257 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.5079, PosY=0 );258 in InletQ as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.6123 );254 in Inlet as stream(Brief="Feed Stream", PosX=0.8127, PosY=0, Symbol="_{in}"); 255 in InletL as stream(Brief="Liquid inlet stream", PosX=0, PosY=0.5254, Symbol="_{inL}"); 256 out OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.2413, PosY=1, Symbol="_{outL}"); 257 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.5079, PosY=0, Symbol="_{outV}"); 258 in InletQ as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.6123, Symbol="_{in}"); 259 259 260 260 M(NComp) as mol (Brief="Molar Holdup in the tray"); -
trunk/eml/stage_separators/tank.mso
r325 r352 59 59 60 60 VARIABLES 61 in Inlet as stream (Brief = "Inlet stream", PosX=0.3037, PosY=0 );62 out Outlet as liquid_stream (Brief = "Outlet liquid stream", PosX=1, PosY=1 );63 in InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7859 );61 in Inlet as stream (Brief = "Inlet stream", PosX=0.3037, PosY=0, Symbol="_{in}"); 62 out Outlet as liquid_stream (Brief = "Outlet liquid stream", PosX=1, PosY=1, Symbol="_{out}"); 63 in InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7859, Symbol="_{in}"); 64 64 Level as length(Brief="Tank level"); 65 65 M(NComp) as mol (Brief="Molar Holdup in the tank"); … … 119 119 120 120 VARIABLES 121 in Inlet as stream (Brief = "Inlet stream", PosX=0.1825, PosY=0 );122 out Outlet as liquid_stream (Brief = "Outlet liquid stream", PosX=1, PosY=1 );123 in InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.6160 );121 in Inlet as stream (Brief = "Inlet stream", PosX=0.1825, PosY=0, Symbol="_{in}"); 122 out Outlet as liquid_stream (Brief = "Outlet liquid stream", PosX=1, PosY=1, Symbol="_{out}"); 123 in InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.6160, Symbol="_{in}"); 124 124 Level as length(Brief="Tank level"); 125 125 Across as area (Brief="Tank cross section area", Default=2); … … 209 209 210 210 VARIABLES 211 in Feed as stream (Brief = "Feed stream", PosX=0.32, PosY=0 );212 in Inlet as stream (Brief = "Inlet stream", PosX=0.3037, PosY=0 );213 out Outlet as liquid_stream (Brief = "Outlet liquid stream", PosX=1, PosY=1 );214 in InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7859 );211 in Feed as stream (Brief = "Feed stream", PosX=0.32, PosY=0, Symbol="_{feed}"); 212 in Inlet as stream (Brief = "Inlet stream", PosX=0.3037, PosY=0, Symbol="_{in}"); 213 out Outlet as liquid_stream (Brief = "Outlet liquid stream", PosX=1, PosY=1, Symbol="_{out}"); 214 in InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7859, Symbol="_{in}"); 215 215 216 216 Level as length(Brief="Tank level"); -
trunk/eml/streams.mso
r346 r352 156 156 157 157 VARIABLES 158 out Outlet as stream (Brief = "Outlet stream", PosX=1, PosY=0.5256 );158 out Outlet as stream (Brief = "Outlet stream", PosX=1, PosY=0.5256, Symbol="_{out}"); 159 159 x(NComp) as fraction (Brief = "Liquid Molar Fraction"); 160 160 y(NComp) as fraction (Brief = "Vapour Molar Fraction"); … … 246 246 247 247 VARIABLES 248 out Outlet as stream (Brief = "Outlet stream", PosX=1, PosY=0.5256 );248 out Outlet as stream (Brief = "Outlet stream", PosX=1, PosY=0.5256, Symbol="_{out}"); 249 249 x(NComp) as fraction (Brief = "Liquid Molar Fraction"); 250 250 y(NComp) as fraction (Brief = "Vapour Molar Fraction"); … … 308 308 309 309 VARIABLES 310 in Inlet as stream (Brief = "Inlet Stream", PosX=0, PosY=0.5308 );310 in Inlet as stream (Brief = "Inlet Stream", PosX=0, PosY=0.5308, Symbol="_{in}"); 311 311 v as fraction (Brief = "Vapourization fraction"); 312 312 x(NComp) as fraction (Brief = "Liquid Molar Fraction"); … … 369 369 370 370 VARIABLES 371 in Inlet as stream (Brief = "Inlet Stream", PosX=0, PosY=0.5308 );371 in Inlet as stream (Brief = "Inlet Stream", PosX=0, PosY=0.5308, Symbol="_{in}"); 372 372 end 373 373 … … 392 392 393 393 VARIABLES 394 out OutletQ as energy_stream (Brief = "Outlet energy stream", PosX=1, PosY=0.5349 );395 end 394 out OutletQ as energy_stream (Brief = "Outlet energy stream", PosX=1, PosY=0.5349, Symbol="_{out}"); 395 end
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