From ed80de3fbc4de714966d6b407715d100dddc5aa0 Mon Sep 17 00:00:00 2001 From: Sashi20 Date: Fri, 16 Feb 2024 00:20:16 +0550 Subject: Added(A)/Deleted(D) following Flowsheet file A Carbon_Capture_Process_From_Flue_Gas_By_Using_Mea_By_Mr_Abhishek_Anand/Abstract.pdf A Carbon_Capture_Process_From_Flue_Gas_By_Using_Mea_By_Mr_Abhishek_Anand/Flowsheet.dwxml A Process_Flowdiagram_For_Manufacture_Of_Formaldehyde_By_Ms_Ranjana_Soni/formaldehyde.dwxmz A Process_Flowdiagram_For_Manufacture_Of_Formaldehyde_By_Ms_Ranjana_Soni/formaldehyde.pdf A Rankine_Power_Plant_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_Dunstan_Chatumba,_Emmanuel_Mtatiro/Abstract_2.pdf A Rankine_Power_Plant_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_Dunstan_Chatumba,_Emmanuel_Mtatiro/COMPLETE_FLOWSHEET.dwxmz A Separation_Of_Separation_Of_Pyridine_And_Toluene_With_The_Help_Of_N_-_Propanol_By_Mr_Om_Pandey/Abstract.pdf A Separation_Of_Separation_Of_Pyridine_And_Toluene_With_The_Help_Of_N_-_Propanol_By_Mr_Om_Pandey/Flowsheet.dwxmz --- .../Abstract.pdf | Bin 0 -> 298877 bytes .../Flowsheet.dwxml | 13965 +++++++++++++++++++ .../formaldehyde.dwxmz | Bin 0 -> 111487 bytes .../formaldehyde.pdf | Bin 0 -> 475172 bytes .../Abstract_2.pdf | Bin 0 -> 112681 bytes .../COMPLETE_FLOWSHEET.dwxmz | Bin 0 -> 53210 bytes .../Abstract.pdf | Bin 0 -> 203370 bytes .../Flowsheet.dwxmz | Bin 0 -> 112575 bytes 8 files changed, 13965 insertions(+) create mode 100644 Carbon_Capture_Process_From_Flue_Gas_By_Using_Mea_By_Mr_Abhishek_Anand/Abstract.pdf create mode 100644 Carbon_Capture_Process_From_Flue_Gas_By_Using_Mea_By_Mr_Abhishek_Anand/Flowsheet.dwxml create mode 100644 Process_Flowdiagram_For_Manufacture_Of_Formaldehyde_By_Ms_Ranjana_Soni/formaldehyde.dwxmz create mode 100644 Process_Flowdiagram_For_Manufacture_Of_Formaldehyde_By_Ms_Ranjana_Soni/formaldehyde.pdf create mode 100644 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+ false + EN-46cbf572-c01f-4e37-a8ed-ec90e9876fd8 + E2 + 20 + 706.0651 + 345.413 + false + 0 + 2 + + + + + + + + + + + + + DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.MaterialStreamGraphic + false + 1 + true + #ff4682b4 + #fff5f5f5 + true + #ffffffff + #ffffffff + #ffd3d3d3 + #ffffffff + 10 + false + Bold + true + true + Material Stream + false + false + false + MaterialStream + 0 + DefaultShape + Calculated + false + 20 + false + MAT-b77eb592-349c-4607-91c3-1395dae64026 + S-06 + 20 + 856.1907 + 176.537 + false + 0 + 2 + + + + + + + + + + + + + DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.MaterialStreamGraphic + false + 1 + true + #ff4682b4 + #fff5f5f5 + true + #ffffffff + #ffffffff + #ffd3d3d3 + #ffffffff + 10 + false + Bold + true + true + Material Stream + false + false + false + MaterialStream + 0 + DefaultShape + Calculated + false + 20 + false + MAT-4f13085e-f0a3-4844-9dde-48b2e89a4758 + S-04 + 20 + 463.375 + 293.75 + false + 0 + 2 + + + + + + + + + + + + + + + PP-1e37eef4-3b36-471d-bec1-e3a7631125c5 + DWSIM.Thermodynamics.PropertyPackages.NRTLPropertyPackage + NRTL + Uses NRTL (Non-Random Two-Liquid) model to calculate liquid-phase activity coefficients. + NRTL (1) + true + true + 0.99999 + false + false + false + Rackett_and_ExpData + Rackett_and_ExpData + true + true + ExpData + Letsou_Stiel + true + MoleAverage + Ideal + FromLiquidFugacity + false + false + LiqCp_Excess + EOS + true + false + false + false + true + NestedLoops + [] + {} + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + DWSIM.Thermodynamics.BaseClasses.ConstantProperties + 0.344 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 7732-18-5 + 0.328 + 18.0674 + 0.0114198721442 + 0 + + + + 0.229 + 22064000 + 647.14 + 0.05595 + ChemSep + 6.17E-30 + 0 + 0 + 0 + 6.00174 + HOH + 59640000 + 0.86515 + -1.1134 + 0.67764 + -0.026925 + 647.28 + 273.15 + 0 + 1921 + 33200 + -878.9001 + 8.436956 + 0.00207627 + -6.467085E-07 + 16 + -13422.7167160322 + -2.4619941145636 + -12688.673170775 + + 0 + 0 + 0 + false + true + false + false + 0 + false + false + 0 + false + 32.51621 + -3.213004 + 7.92411 + -7.359898 + 2.703522 + 647.29 + 253.1 + 75539 + -22297 + 136.02 + -0.25622 + 0.00018273 + 533.15 + 273.1 + -1.5697 + -55.141 + 0.7832 + 0.0011484 + -1.8151E-06 + 633.15 + 273.1 + -133.7 + 6785.7 + 18.47 + -1.4736E-05 + 2 + 106 + 16 + 16 + 101 + 18.01528 + 0 + 0 + 0 + 0 + 0 + Water + 373.15 + + 0 + 373.15 + ChemSep + 0 + 0 + 0 + + 0 + 0 + O + 52.967 + -0.0075822 + 0 + 0 + 0 + 273.15 + 233.15 + -262.51 + 140.52 + -3.8869E-06 + -1.1996E-08 + 7.1879E-11 + 273.15 + 3.15 + 0 + 2 + 100 + 0 + 0 + 0 + 0 + -0.031819 + 167.09 + -3.6781 + 0.0053717 + -8.4188E-06 + 647.1 + 265.1 + 16 + 273.15 + 1.4 + 0.92 + 74.55502 + -7295.586 + -7.442448 + 4.2881E-06 + 2 + 647.29 + 263.15 + 6.5986E-06 + 1.3947 + 59.478 + -15484 + 0 + 1073.15 + 273.16 + 7.002327E-08 + 0.934576 + 195.6338 + -13045.99 + 0 + 1073.15 + 273.16 + 106 + 101 + 102 + 102 + 0.2338 + 13.11 + 2.52E-10 + 775 + 0.00926 + + -0.65445 + 0.04357 + false + 84 + + + + + + + + + + + + + + + + + DWSIM.Thermodynamics.BaseClasses.ConstantProperties + 0.223621 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 124-38-9 + 0.231 + 37.2744 + 0.0034785053748 + 0 + + + + 0.274 + 7383000 + 304.21 + 0.094 + ChemSep + 0 + 0 + 0 + 0 + 9.019 + OCO + 21092000 + 0.35366 + -0.46134 + 0.43554 + 0.037671 + 304.21 + 216.58 + 0 + 909 + 28933 + -494.28 + 10.658 + -2.7375E-05 + 3.3268E-09 + 16 + -8941.47854440518 + 0.0655416247361437 + -8961.01977982027 + + 0 + 0 + 0 + false + true + false + false + 0 + false + false + 0 + false + 2.768 + 0.26212 + 304.21 + 0.2908 + 0 + 304.21 + 216.58 + 80592 + 108.83 + -6.9126 + 0.059647 + 6.9922E-06 + 290 + 216.58 + -0.24975 + -55.106 + 0.41735 + -0.0051067 + 2.0157E-06 + 300 + 216.58 + -7.7022 + -166.34 + 0.38094 + -4.018E-05 + 2 + 105 + 16 + 16 + 101 + 44.0095 + 0 + 0 + 0 + 0 + 0 + Carbon dioxide + 194.686 + + 0 + 194.686 + ChemSep + 0 + 0 + 0 + + 0 + 0 + O=C=O + 42.04 + -0.034421 + -0.0002847 + 0 + 0 + 216.58 + 143.1 + -18283 + 1360.3 + -12.153 + 0.051584 + -7.6997E-05 + 216.58 + 25 + 0 + 2 + 100 + 0 + 0 + 0 + 0 + -0.011629 + -183.67 + 0.069773 + -0.012408 + -1.8232E-06 + 304.21 + 216.58 + 16 + 216.58 + 1.292 + 1.2986 + 95.478 + -4070 + -12.07 + 2.9505E-05 + 2 + 304.21 + 216.4 + 5.804 + -0.44522 + 794.13 + 2139600 + 0 + 1500 + 180 + 2.2464E-06 + 0.45495 + 292.64 + 1669.1 + 0 + 1900 + 170 + 106 + 101 + 102 + 102 + 0.270937 + 26.9 + 4.011624E-10 + 187.9268 + 0.0132 + + 0.231 + 0.104698 + false + 24 + + + + + + + + + + + DWSIM.Thermodynamics.BaseClasses.ConstantProperties + 0.245381 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 7446-09-5 + 0.2462 + 43.8228 + 0.0029313330734 + 0 + + + + 0.269 + 7884100 + 430.75 + 0.122 + ChemSep + 5.44E-30 + 0 + 0 + 0 + 7.401 + OSO + 48914000 + 1.8091 + -2.9053 + 2.2271 + -0.64793 + 430.75 + 197.67 + 0 + 910 + 33406 + -516.38 + 10.524 + 1.3143E-05 + -6.1535E-08 + 16 + -4633.50597373244 + 0.171722156752365 + -4684.70493476815 + + 0 + 0 + 0 + false + true + false + false + 0 + false + false + 0 + false + 1.8477 + 0.24254 + 430.75 + 0.27051 + 0 + 430.75 + 197.67 + 86911 + 53691 + -599.94 + 2.2025 + -0.0025885 + 350 + 197.67 + -0.21664 + -2.2484 + -0.50659 + -0.0009424 + -1.0218E-06 + 400 + 197.67 + 50.887 + -1574 + -9.4517 + 1.5898E-07 + 2 + 105 + 16 + 16 + 101 + 64.0638 + 0 + 0 + 0 + 0 + 0 + Sulfur dioxide + 263.13 + + 0 + 263.13 + ChemSep + 0 + 0 + 0 + + 0 + 0 + O=[S]=O + 32.096 + -0.018032 + 0 + 0 + 0 + 197.67 + 79.07 + -22618 + 1707.9 + -16.235 + 0.074564 + -0.00012295 + 197.68 + 30 + 0 + 2 + 100 + 0 + 0 + 0 + 0 + -0.011604 + 175.94 + -4.6965 + 0.008615 + -2.0963E-05 + 430.75 + 197.67 + 16 + 200 + 1.612 + 1.6961 + 53.52766 + -4260.124 + -4.670429 + 3.0272E-06 + 2 + 430.75 + 195.12 + 23.316 + -0.95324 + -1567.4 + 1330100 + 0 + 900 + 197.67 + 1.2144E-06 + 0.53923 + 315.41 + -2659.7 + 0 + 1250 + 197.67 + 106 + 101 + 102 + 102 + 0 + 41.8 + 4.04E-10 + 347 + 0.0181 + + 0.256 + 0.12522 + false + 24 + + + + + + + + + + + DWSIM.Thermodynamics.BaseClasses.ConstantProperties + 0.550815 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 141-43-5 + 0.446737 + 60.3415 + 0.00760246818 + 0 + + + + 0.284 + 8030000 + 671.4 + 0.225 + ChemSep + 2.59E-30 + 0 + 0 + 0 + 20.496 + HOCH2CH2NH2 + 101203100 + 1.976961 + -4.399887 + 4.906054 + -1.945886 + 595.14 + 283.65 + 0 + 1723 + 50668 + -516.86 + 12.167 + 8.641E-05 + 2.8656E-10 + 16 + -3208.74454922705 + -5.09007279094121 + -1691.13934660793 + + 0 + 0 + 0 + false + false + false + false + 0 + false + false + 0 + false + 0.648 + 0.18183 + 678.21 + 0.17947 + 0 + 678.2 + 283.15 + 78653.42 + 311.4162 + -0.0607137 + -2.713217E-06 + -1.7988E-05 + 443.15 + 293.15 + -0.37218 + 78.8 + -1.5916 + 0.0043895 + -5.3291E-06 + 583.15 + 283.65 + -370.3 + 17780 + 54.624 + -5.1065E-05 + 2 + 105 + 4 + 16 + 101 + 61.08308 + 0 + 0 + 0 + 0 + 0 + Monoethanolamine + 444.15 + + 0 + 444.15 + ChemSep + 0 + 0 + 0 + + 0 + 0 + NCCO + 21.251 + -0.0083183 + 0 + 0 + 0 + 283.65 + 113.46 + 15188 + 144.03 + 3.6142 + -0.019701 + 3.4165E-05 + 283.65 + 50 + 0 + 2 + 100 + 0 + 0 + 0 + 0 + -0.067139 + -7.9 + -1.90607 + -0.0004719 + -9.533E-07 + 600 + 270 + 16 + 283.65 + 2.976 + 3.0436 + 23.09274 + 4319.625 + -69.95024 + 0 + 0 + 678.2 + 283.65 + -9539.9 + 0.39852 + -1743300000 + -63715000000 + 0 + 1000 + 283.65 + 5.78881E-08 + 0.876532 + 75.00276 + 628.0161 + 0 + 1000 + 283.65 + 106 + 10 + 102 + 102 + 0.266147 + 51.539 + 5.140324E-10 + 431.8628 + 0.0284 + + 0.550815 + 0.20696 + false + 68 + + + + + + + + + + + + + + + + + + + + + + + + + DWSIM.Thermodynamics.BaseClasses.ConstantProperties + 0.037 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 7727-37-9 + 0.045 + 34.6723 + 0.00216918504124 + 0 + + + + 0.289 + 3398000 + 126.2 + 0.0901 + ChemSep + 0 + 0 + 0 + 0 + 0.72 + N2 + 27284000 + 7.8021 + -19.125 + 19.518 + -7.5428 + 126.26 + 63.15 + 0 + 905 + 29103.63 + -2305.946 + 11.31935 + -0.00100557 + 1.706099E-07 + 16 + 0 + 0 + 0 + + 0 + 0 + 0 + false + true + false + false + 0 + false + false + 0 + false + 2.435 + 0.25137 + 126.27 + 0.249 + 0 + 126.26 + 63.15 + 55135 + 217.45 + -0.9071 + 0.05327 + 0.00024166 + 115 + 63.15 + -0.21743 + 10.383 + -1.0631 + 0.00036245 + -2.3265E-05 + 124 + 60 + 3.4358 + -24.706 + -2.6748 + -4.1603E-05 + 2 + 105 + 16 + 16 + 101 + 28.0134 + 0 + 0 + 0 + 0 + 0 + Nitrogen + 77.35 + + 0 + 77.35 + ChemSep + 0 + 0 + 0 + + 0 + 0 + N#N + 37.87 + -0.06027 + 0 + 0 + 0 + 63.15 + 20.65 + 383890 + -28798 + 875.74 + -11.589 + 0.057106 + 63 + 32.8 + 0 + 2 + 100 + 0 + 0 + 0 + 0 + -0.0025409 + 96.836 + -7.6473 + 0.05313 + -0.00036553 + 126.2 + 63.15 + 16 + 63.149 + 1.088 + 1.0415 + 42.32946 + -965.9771 + -4.321774 + 7.97271E-05 + 2 + 126.26 + 60.81 + 0.0003395 + 0.76921 + 19.592 + 293.93 + 0 + 2000 + 50 + 4.6051E-07 + 0.65049 + 5.8019 + 2822.7 + 0 + 1970 + 63.15 + 106 + 101 + 102 + 102 + 0.2906 + 18.5 + 3.710301E-10 + 94.45061 + 0.0107 + + 0.0357998 + 0.0901499 + false + 74 + + + + + + + + + + + + DefaultSet + Default Set + Default Reaction Set + + + + + + + DWSIM.DynamicsManager.Manager + + + + + + + + + DWSIM.SharedClasses.Flowsheet.Optimization.OptimizationCase + optcase0 + + + AL_BRENT + 100 + 1E-06 + 0.001 + 0.001 + 0.001 + 0.001 + 0.0001 + 2 + false + Variable + Minimization + + + + + + + DWSIM.SharedClasses.Flowsheet.Optimization.SensitivityAnalysisCase + + DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable + + + + + 5 + + + 0 + + + DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable + + + + + 5 + + + 0 + + + DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable + + + + + 5 + + + 0 + + SACase0 + + + 1 + Variable + + + DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable + + + + + 5 + + + 0 + + + DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable + + + + + 5 + + + 0 + + + DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable + + + + + 5 + + + 0 + + + + + + + + + + + {"MAIN":"{\"?xml\":{\"@version\":\"1.0\"},\"grid\":{\"@xmlns:xsd\":\"http://www.w3.org/2001/XMLSchema\",\"@xmlns:xsi\":\"http://www.w3.org/2001/XMLSchema-instance\",\"head\":{\"meta\":{\"culture\":\"en-IN\",\"editor\":\"ReoGrid Core\",\"core-ver\":\"2.1.0.0\"},\"rows\":\"65536\",\"cols\":\"100\",\"default-row-height\":\"20\",\"default-col-width\":\"70\",\"focus-forward-direction\":\"down\",\"settings\":{\"@meta\":\"30475026398\"},\"script\":null},\"style\":{\"@font\":\"Arial\",\"@font-size\":\"10\",\"@align\":\"general\",\"@valign\":\"middle\"},\"rows\":null,\"cols\":null,\"v-borders\":null,\"h-borders\":null,\"cells\":null}}"} + + <?xml version="1.0" encoding="utf-8"?> +<!--DockPanel configuration file. Author: Weifen Luo, all rights reserved.--> +<!--!!! AUTOMATICALLY GENERATED FILE. DO NOT MODIFY !!!--> +<DockPanel FormatVersion="1.0" DockLeftPortion="450" DockRightPortion="0.203007518796992" DockTopPortion="0.25" DockBottomPortion="0.0508763545923176" ActiveDocumentPane="0" ActivePane="0"> + <Contents Count="14"> + <Content ID="0" PersistString="DWSIM.LogPanel" AutoHidePortion="0.152227705943669" IsHidden="False" IsFloat="False" /> + <Content ID="1" PersistString="DWSIM.MaterialStreamPanel" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" /> + <Content ID="2" PersistString="DWSIM.WatchPanel" AutoHidePortion="0.152227705943669" IsHidden="True" IsFloat="False" /> + <Content ID="3" PersistString="DWSIM.FormCharts" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" /> + <Content ID="4" PersistString="DWSIM.FormDynamicsManager" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" /> + <Content ID="5" PersistString="DWSIM.FormDynamicsIntegratorControl" AutoHidePortion="0.369804903093313" IsHidden="True" IsFloat="False" /> + <Content ID="6" PersistString="DWSIM.FormFileExplorer" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" /> + <Content ID="7" PersistString="DWSIM.FlowsheetSurface_SkiaSharp" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" /> + <Content ID="8" PersistString="DWSIM.FormNewSpreadsheet" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" /> + <Content ID="9" PersistString="DWSIM.FormScript" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" /> + <Content ID="10" PersistString="DWSIM.Thermodynamics.MaterialStreamEditor" AutoHidePortion="450" IsHidden="False" IsFloat="False" /> + <Content ID="11" PersistString="DWSIM.Thermodynamics.MaterialStreamEditor" AutoHidePortion="450" IsHidden="False" IsFloat="False" /> + <Content ID="12" PersistString="DWSIM.Thermodynamics.MaterialStreamEditor" AutoHidePortion="450" IsHidden="False" IsFloat="False" /> + <Content ID="13" PersistString="DWSIM.Thermodynamics.MaterialStreamEditor" AutoHidePortion="450" IsHidden="False" IsFloat="False" /> + </Contents> + <Panes Count="6"> + <Pane ID="0" DockState="Document" ActiveContent="7"> + <Contents Count="7"> + <Content ID="0" RefID="6" /> + <Content ID="1" RefID="7" /> + <Content ID="2" RefID="4" /> + <Content ID="3" RefID="1" /> + <Content ID="4" RefID="8" /> + <Content ID="5" RefID="3" /> + <Content ID="6" RefID="9" /> + </Contents> + </Pane> + <Pane ID="1" DockState="DockBottom" ActiveContent="0"> + <Contents Count="1"> + <Content ID="0" RefID="0" /> + </Contents> + </Pane> + <Pane ID="2" DockState="DockBottom" ActiveContent="-1"> + <Contents Count="1"> + <Content ID="0" RefID="2" /> + </Contents> + </Pane> + <Pane ID="3" DockState="Float" ActiveContent="-1"> + <Contents Count="1"> + <Content ID="0" RefID="5" /> + </Contents> + </Pane> + <Pane ID="4" DockState="DockBottom" ActiveContent="-1"> + <Contents Count="1"> + <Content ID="0" RefID="5" /> + </Contents> + </Pane> + <Pane ID="5" DockState="DockLeft" ActiveContent="13"> + <Contents Count="4"> + <Content ID="0" RefID="10" /> + <Content ID="1" RefID="11" /> + <Content ID="2" RefID="12" /> + <Content ID="3" RefID="13" /> + </Contents> + </Pane> + </Panes> + <DockWindows> + <DockWindow ID="0" DockState="Document" ZOrderIndex="1"> + <NestedPanes Count="1"> + <Pane ID="0" RefID="0" PrevPane="-1" Alignment="Right" Proportion="0.5" /> + </NestedPanes> + </DockWindow> + <DockWindow ID="1" DockState="DockLeft" ZOrderIndex="3"> + <NestedPanes Count="1"> + <Pane ID="0" RefID="5" PrevPane="-1" Alignment="Bottom" Proportion="0.5" /> + </NestedPanes> + </DockWindow> + <DockWindow ID="2" DockState="DockRight" ZOrderIndex="4"> + <NestedPanes Count="0" /> + </DockWindow> + <DockWindow ID="3" DockState="DockTop" ZOrderIndex="5"> + <NestedPanes Count="0" /> + </DockWindow> + <DockWindow ID="4" DockState="DockBottom" ZOrderIndex="2"> + <NestedPanes Count="3"> + <Pane ID="0" RefID="1" PrevPane="-1" Alignment="Right" Proportion="0.5" /> + <Pane ID="1" RefID="4" PrevPane="1" Alignment="Top" Proportion="0.5" /> + <Pane ID="2" RefID="2" PrevPane="1" Alignment="Right" Proportion="0.261838440111421" /> + </NestedPanes> + </DockWindow> + </DockWindows> + <FloatWindows Count="1"> + <FloatWindow ID="0" Bounds="336, 370, 900, 155" ZOrderIndex="0"> + <NestedPanes Count="1"> + <Pane ID="0" RefID="3" PrevPane="-1" Alignment="Right" Proportion="0.5" /> + </NestedPanes> + </FloatWindow> + </FloatWindows> +</DockPanel> + + [03-02-2024 14:22:02] Estimated NRTL IP set for Water/Monoethanolamine: -563.53/198.39/0.2 + [03-02-2024 14:22:02] The flowsheet was calculated successfully. [3.678s] + [03-02-2024 14:22:14] The flowsheet was calculated successfully. [0.05993s] + [03-02-2024 14:22:23] The flowsheet was calculated successfully. [0.02294s] + [03-02-2024 14:22:39] The flowsheet was calculated successfully. [0.03161s] + [03-02-2024 14:23:20] The flowsheet was calculated successfully. [0.02622s] + [03-02-2024 14:23:58] The flowsheet was calculated successfully. [0.01497s] + [03-02-2024 14:24:16] It is recommended that the column propertiy editing be carried out with the calculator disabled. + [03-02-2024 14:24:16] When editing the column connections, remember to click any cell other than the one being edited, so that changes are recognized by DWSIM. + [03-02-2024 14:24:16] Remember to set the pressure of the intermediate stages of the column. + [03-02-2024 14:25:23] The flowsheet was calculated successfully. [0.6281s] + [03-02-2024 14:26:45] It is recommended that the column propertiy editing be carried out with the calculator disabled. + [03-02-2024 14:26:45] When editing the column connections, remember to click any cell other than the one being edited, so that changes are recognized by DWSIM. + [03-02-2024 14:26:45] Remember to set the pressure of the intermediate stages of the column. + [03-02-2024 14:28:48] Errors occurred during the calculation of the flowsheet, please read the following messages for more details. + [03-02-2024 14:28:48] Error in 'ABS-2': Please set the Column Stage for Feed Stream '8'. (RigorousColumn.vb, 4381) + [03-02-2024 14:29:01] Errors occurred during the calculation of the flowsheet, please read the following messages for more details. + [03-02-2024 14:29:01] Error in 'ABS-2': Please set the Column Stage for Feed Stream '8'. (RigorousColumn.vb, 4381) + [03-02-2024 14:29:28] Errors occurred during the calculation of the flowsheet, please read the following messages for more details. + [03-02-2024 14:29:28] Error in 'ABS-2': Please set the Column Stage for Feed Stream '8'. (RigorousColumn.vb, 4381) + [03-02-2024 14:30:19] Errors occurred during the calculation of the flowsheet, please read the following messages for more details. + [03-02-2024 14:30:19] Error in 'ABS-2': Please set the Column Stage for Feed Stream '8'. (RigorousColumn.vb, 4381) + [03-02-2024 14:31:11] ABS-2: Column Solver did not converge. Will reset some parameters and try again shortly... + [03-02-2024 14:31:11] Errors occurred during the calculation of the flowsheet, please read the following messages for more details. + [03-02-2024 14:31:11] Error in 'ABS-2': Converged to an invalid temperature at stage 6 (Tcalc = -64.2553174521587 K). (SumRates.vb, 720) + [03-02-2024 14:31:34] ABS-2: Column Solver did not converge. Will reset some parameters and try again shortly... + [03-02-2024 14:31:34] Errors occurred during the calculation of the flowsheet, please read the following messages for more details. + [03-02-2024 14:31:34] Error in 'ABS-2': Converged to an invalid temperature at stage 4 (Tcalc = -24.0692138664524 K). (SumRates.vb, 720) + [03-02-2024 14:31:38] ABS-2: Column Solver did not converge. Will reset some parameters and try again shortly... + [03-02-2024 14:31:39] Errors occurred during the calculation of the flowsheet, please read the following messages for more details. + [03-02-2024 14:31:39] Error in 'ABS-2': Converged to an invalid temperature at stage 4 (Tcalc = -24.0692138664524 K). (SumRates.vb, 720) + [03-02-2024 14:32:12] ABS-2: Column Solver did not converge. Will reset some parameters and try again shortly... + [03-02-2024 14:32:12] Errors occurred during the calculation of the flowsheet, please read the following messages for more details. + [03-02-2024 14:32:12] Error in 'ABS-2': Converged to an invalid temperature at stage 7 (Tcalc = -134.736524832954 K). (SumRates.vb, 720) + [03-02-2024 14:32:23] The flowsheet was calculated successfully. [0.9824s] + [03-02-2024 14:34:17] Errors occurred during the calculation of the flowsheet, please read the following messages for more details. + [03-02-2024 14:34:17] Error in 'PUMP-1': Check the connections of the object. (Pump.vb, 511) + [03-02-2024 14:34:59] The flowsheet was calculated successfully. [1.49s] + [03-02-2024 14:36:11] Errors occurred during the calculation of the flowsheet, please read the following messages for more details. + [03-02-2024 14:36:11] Error in 'HT-1': Check the connections of the object. (Heater.vb, 360) + [03-02-2024 14:36:58] The flowsheet was calculated successfully. [1.303s] + [03-02-2024 14:43:57] Errors occurred during the calculation of the flowsheet, please read the following messages for more details. + [03-02-2024 14:43:57] Error in 'ABS-1': Please set the Column Stage for Feed Stream 'S-06'. (RigorousColumn.vb, 4381) + [03-02-2024 14:44:29] ABS-1: Column Solver did not converge. Will reset some parameters and try again shortly... + [03-02-2024 14:44:31] Errors occurred during the calculation of the flowsheet, please read the following messages for more details. + [03-02-2024 14:44:31] Error in 'ABS-1': Solver reached the maximum number of iterations without converging. (SumRates.vb, 808) + [03-02-2024 14:46:34] ABS-1: Column Solver did not converge. Will reset some parameters and try again shortly... + [03-02-2024 14:46:36] Errors occurred during the calculation of the flowsheet, please read the following messages for more details. + [03-02-2024 14:46:36] Error in 'ABS-1': Solver reached the maximum number of iterations without converging. (SumRates.vb, 808) + [03-02-2024 14:47:09] ABS-1: Column Solver did not converge. Will reset some parameters and try again shortly... + [03-02-2024 14:47:12] Errors occurred during the calculation of the flowsheet, please read the following messages for more details. + [03-02-2024 14:47:12] Error in 'ABS-1': Solver reached the maximum number of iterations without converging. (SumRates.vb, 808) + [03-02-2024 15:09:15] ABS-1: Column Solver did not converge. Will reset some parameters and try again shortly... + [03-02-2024 15:09:17] Errors occurred during the calculation of the flowsheet, please read the following messages for more details. + [03-02-2024 15:09:17] Error in 'ABS-1': Solver reached the maximum number of iterations without converging. (SumRates.vb, 808) + [03-02-2024 15:10:21] File C:\Users\pc\AppData\Local\DWSIM\DWSIM12.dwxmz saved successfully. + [03-02-2024 15:11:55] The flowsheet was calculated successfully. [0.3253s] + [03-02-2024 15:12:01] The flowsheet was calculated successfully. [1.27s] + [03-02-2024 15:13:36] The flowsheet was calculated successfully. [1.417s] + [03-02-2024 15:17:38] ABS-2: Column Solver did not converge. Will reset some parameters and try again shortly... + [03-02-2024 15:17:38] Errors occurred during the calculation of the flowsheet, please read the following messages for more details. + [03-02-2024 15:17:38] Error in 'ABS-2': Converged to an invalid temperature at stage 8 (Tcalc = -6.83388802861742 K). (SumRates.vb, 720) + [03-02-2024 15:17:42] ABS-2: Column Solver did not converge. Will reset some parameters and try again shortly... + [03-02-2024 15:17:43] Errors occurred during the calculation of the flowsheet, please read the following messages for more details. + [03-02-2024 15:17:43] Error in 'ABS-2': Converged to an invalid temperature at stage 8 (Tcalc = -6.83388802861742 K). (SumRates.vb, 720) + [03-02-2024 15:17:55] The flowsheet was calculated successfully. [1.082s] + [03-02-2024 15:18:11] The flowsheet was calculated successfully. [1.467s] + [03-02-2024 15:22:58] The flowsheet was calculated successfully. [0.01858s] + [03-02-2024 15:23:38] The flowsheet was calculated successfully. [0.01359s] + [03-02-2024 15:23:56] The flowsheet was calculated successfully. [0.01962s] + [03-02-2024 15:24:10] The flowsheet was calculated successfully. [0.02029s] + [03-02-2024 15:25:42] ABS-1: Column Solver did not converge. Will reset some parameters and try again shortly... + [03-02-2024 15:25:44] Errors occurred during the calculation of the flowsheet, please read the following messages for more details. + [03-02-2024 15:25:44] Error in 'ABS-1': Solver reached the maximum number of iterations without converging. (SumRates.vb, 808) + [03-02-2024 15:27:33] Errors occurred during the calculation of the flowsheet, please read the following messages for more details. + [03-02-2024 15:27:33] Error in 'PUMP-1': Check the connections of the object. (Pump.vb, 451) + [03-02-2024 15:28:10] ABS-1: Column Solver did not converge. Will reset some parameters and try again shortly... + [03-02-2024 15:28:13] Errors occurred during the calculation of the flowsheet, please read the following messages for more details. + [03-02-2024 15:28:13] Error in 'ABS-1': Solver reached the maximum number of iterations without converging. (SumRates.vb, 808) + [03-02-2024 15:29:57] The flowsheet was calculated successfully. [0.02471s] + [03-02-2024 15:31:00] The flowsheet was calculated successfully. [0.01522s] + [03-02-2024 15:32:45] ABS-1: Column Solver did not converge. Will reset some parameters and try again shortly... + [03-02-2024 15:32:47] Errors occurred during the calculation of the flowsheet, please read the following messages for more details. + [03-02-2024 15:32:47] Error in 'ABS-1': Solver reached the maximum number of iterations without converging. (SumRates.vb, 808) + [03-02-2024 15:34:32] The flowsheet was calculated successfully. [1.034s] + [03-02-2024 17:01:57] File C:\Users\pc\AppData\Local\DWSIM\DWSIM12.dwxmz saved successfully. + + \ No newline at end of file diff --git a/Process_Flowdiagram_For_Manufacture_Of_Formaldehyde_By_Ms_Ranjana_Soni/formaldehyde.dwxmz b/Process_Flowdiagram_For_Manufacture_Of_Formaldehyde_By_Ms_Ranjana_Soni/formaldehyde.dwxmz new file mode 100644 index 0000000..71a5b02 Binary files /dev/null and b/Process_Flowdiagram_For_Manufacture_Of_Formaldehyde_By_Ms_Ranjana_Soni/formaldehyde.dwxmz differ diff --git a/Process_Flowdiagram_For_Manufacture_Of_Formaldehyde_By_Ms_Ranjana_Soni/formaldehyde.pdf b/Process_Flowdiagram_For_Manufacture_Of_Formaldehyde_By_Ms_Ranjana_Soni/formaldehyde.pdf new file mode 100644 index 0000000..98ec9d3 Binary files /dev/null and b/Process_Flowdiagram_For_Manufacture_Of_Formaldehyde_By_Ms_Ranjana_Soni/formaldehyde.pdf differ diff --git a/Rankine_Power_Plant_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_Dunstan_Chatumba,_Emmanuel_Mtatiro/Abstract_2.pdf b/Rankine_Power_Plant_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_Dunstan_Chatumba,_Emmanuel_Mtatiro/Abstract_2.pdf new file mode 100644 index 0000000..4452778 Binary files /dev/null and b/Rankine_Power_Plant_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_Dunstan_Chatumba,_Emmanuel_Mtatiro/Abstract_2.pdf differ diff --git a/Rankine_Power_Plant_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_Dunstan_Chatumba,_Emmanuel_Mtatiro/COMPLETE_FLOWSHEET.dwxmz b/Rankine_Power_Plant_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_Dunstan_Chatumba,_Emmanuel_Mtatiro/COMPLETE_FLOWSHEET.dwxmz new file mode 100644 index 0000000..46f4ed1 Binary files /dev/null and b/Rankine_Power_Plant_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_Dunstan_Chatumba,_Emmanuel_Mtatiro/COMPLETE_FLOWSHEET.dwxmz differ diff --git a/Separation_Of_Separation_Of_Pyridine_And_Toluene_With_The_Help_Of_N_-_Propanol_By_Mr_Om_Pandey/Abstract.pdf b/Separation_Of_Separation_Of_Pyridine_And_Toluene_With_The_Help_Of_N_-_Propanol_By_Mr_Om_Pandey/Abstract.pdf new file mode 100644 index 0000000..021e089 Binary files /dev/null and b/Separation_Of_Separation_Of_Pyridine_And_Toluene_With_The_Help_Of_N_-_Propanol_By_Mr_Om_Pandey/Abstract.pdf differ diff --git a/Separation_Of_Separation_Of_Pyridine_And_Toluene_With_The_Help_Of_N_-_Propanol_By_Mr_Om_Pandey/Flowsheet.dwxmz b/Separation_Of_Separation_Of_Pyridine_And_Toluene_With_The_Help_Of_N_-_Propanol_By_Mr_Om_Pandey/Flowsheet.dwxmz new file mode 100644 index 0000000..58dc7c1 Binary files /dev/null and b/Separation_Of_Separation_Of_Pyridine_And_Toluene_With_The_Help_Of_N_-_Propanol_By_Mr_Om_Pandey/Flowsheet.dwxmz differ -- cgit