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DPHE_series_diagram.pfd @ 494

Last change on this file since 494 was 479, checked in by gerson bicca, 15 years ago
added PFD sample with the option to solve a convergence problem in a series of double pipe
File size: 53.8 KB

Line
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627	<Values>0.00217</Values>
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629	<Unit>m^2*K/kW</Unit>
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634	<Values>0.0008</Values>
635	<Status>4</Status>
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663	<Values>counter</Values>
664	<Status>4</Status>
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839	<Model_Name>Properties_Average</Model_Name>
840	<T_Connection>0</T_Connection>
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844	<Instance_Id>Inner.Properties.Average.</Instance_Id>
845	<Model_Name>Average</Model_Name>
846	<T_Connection>0</T_Connection>
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895	<Model_Name>Main_DoublePipe</Model_Name>
896	<T_Connection>0</T_Connection>
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915	<Model_Name>DoublePipe_HeatTransfer</Model_Name>
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921	<Model_Name>HeatTransfer</Model_Name>
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931	<Model_Name>DoublePipe_PressureDrop</Model_Name>
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973	<Model_Name>Average</Model_Name>
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998	<Instance_Id>Outer.Properties.Wall.</Instance_Id>
999	<Model_Name>Properties_Wall</Model_Name>
1000	<T_Connection>0</T_Connection>
1001	</Block_Properties>
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1004	<Instance_Id>Outer.Properties.Wall.</Instance_Id>
1005	<Model_Name>Wall</Model_Name>
1006	<T_Connection>0</T_Connection>
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1010	<Instance_Id>Outer.Properties.</Instance_Id>
1011	<Model_Name>Physical_Properties</Model_Name>
1012	<T_Connection>0</T_Connection>
1013	</Block_Properties>
1014	</Base_Models>
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1016	<Instance_Id>Outer.Properties.</Instance_Id>
1017	<Model_Name>Properties</Model_Name>
1018	<T_Connection>0</T_Connection>
1019	</Block_Properties>
1020	</Sub_Models>
1021	<Model_File_Path>heat_exchangers/HEX_Engine</Model_File_Path>
1022	<Instance_Id>Outer.</Instance_Id>
1023	<Model_Name>Main_DoublePipe</Model_Name>
1024	<T_Connection>0</T_Connection>
1025	</Block_Properties>
1026	</Base_Models>
1027	<Model_File_Path>heat_exchangers/DoublePipe</Model_File_Path>
1028	<Instance_Id>Outer.</Instance_Id>
1029	<Model_Name>Outer</Model_Name>
1030	<T_Connection>0</T_Connection>
1031	</Block_Properties>
1032	</Sub_Models>
1033	<Model_File_Path>heat_exchangers/DoublePipe</Model_File_Path>
1034	<Instance_Id></Instance_Id>
1035	<Model_Name>DoublePipe_Basic</Model_Name>
1036	<T_Connection>0</T_Connection>
1037	<Parameters>
1038	<Desc>InnerLaminarCorrelation</Desc>
1039	<Index>0</Index>
1040	<Values>Schlunder</Values>
1041	<Status>4</Status>
1042	</Parameters>
1043	<Parameters>
1044	<Desc>InnerTransitionCorrelation</Desc>
1045	<Index>0</Index>
1046	<Values>Gnielinski</Values>
1047	<Status>4</Status>
1048	</Parameters>
1049	<Parameters>
1050	<Desc>InnerTurbulentCorrelation</Desc>
1051	<Index>0</Index>
1052	<Values>SiederTate</Values>
1053	<Status>4</Status>
1054	</Parameters>
1055	<Parameters>
1056	<Desc>OuterLaminarCorrelation</Desc>
1057	<Index>0</Index>
1058	<Values>Schlunder</Values>
1059	<Status>4</Status>
1060	</Parameters>
1061	<Parameters>
1062	<Desc>OuterTransitionCorrelation</Desc>
1063	<Index>0</Index>
1064	<Values>Gnielinski</Values>
1065	<Status>4</Status>
1066	</Parameters>
1067	<Parameters>
1068	<Desc>OuterTurbulentCorrelation</Desc>
1069	<Index>0</Index>
1070	<Values>SiederTate</Values>
1071	<Status>4</Status>
1072	</Parameters>
1073	<Parameters>
1074	<Desc>CalculationApproach</Desc>
1075	<Index>0</Index>
1076	<Values>Full</Values>
1077	<Status>4</Status>
1078	</Parameters>
1079	<Parameters>
1080	<Desc>Qestimated</Desc>
1081	<Index>0</Index>
1082	<Values>30</Values>
1083	<Status>4</Status>
1084	<Unit>kW</Unit>
1085	</Parameters>
1086	<Parameters>
1087	<Desc>DoInner</Desc>
1088	<Index>0</Index>
1089	<Values>42.16</Values>
1090	<Status>4</Status>
1091	<Unit>mm</Unit>
1092	</Parameters>
1093	<Parameters>
1094	<Desc>DiInner</Desc>
1095	<Index>0</Index>
1096	<Values>35.05</Values>
1097	<Status>4</Status>
1098	<Unit>mm</Unit>
1099	</Parameters>
1100	<Parameters>
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1102	<Index>0</Index>
1103	<Values>52.5</Values>
1104	<Status>4</Status>
1105	<Unit>mm</Unit>
1106	</Parameters>
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1109	<Index>0</Index>
1110	<Values>9</Values>
1111	<Status>4</Status>
1112	<Unit>m</Unit>
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1115	<Desc>Kwall</Desc>
1116	<Index>0</Index>
1117	<Values>0.057</Values>
1118	<Status>4</Status>
1119	<Unit>kW/m/K</Unit>
1120	</Parameters>
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1122	<Desc>Rfi</Desc>
1123	<Index>0</Index>
1124	<Values>0.00217</Values>
1125	<Status>4</Status>
1126	<Unit>m^2*K/kW</Unit>
1127	</Parameters>
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1130	<Index>0</Index>
1131	<Values>0.0008</Values>
1132	<Status>4</Status>
1133	<Unit>m^2*K/kW</Unit>
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1142	<Instance_Id>Method.</Instance_Id>
1143	<Model_Name>LMTD_Basic</Model_Name>
1144	<T_Connection>0</T_Connection>
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1148	<Instance_Id>Method.</Instance_Id>
1149	<Model_Name>Method</Model_Name>
1150	<T_Connection>0</T_Connection>
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1154	<Instance_Id></Instance_Id>
1155	<Model_Name>DoublePipe_LMTD</Model_Name>
1156	<T_Connection>0</T_Connection>
1157	<Parameters>
1158	<Desc>FlowDirection</Desc>
1159	<Index>0</Index>
1160	<Values>counter</Values>
1161	<Status>4</Status>
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1169	<Image_File_Name>/home/bicca/Desktop/biblioteca/biblioteca/trunk/eml/heat_exchangers/icon/DoublePipe.png</Image_File_Name>
1170	<X>209.429</X>
1171	<Y>146.143</Y>
1172	<Z>0</Z>
1173	<Width>266</Width>
1174	<Height>70</Height>
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1183	<Instance_Id>InletInner.</Instance_Id>
1184	<Model_Name>stream</Model_Name>
1185	<T_Connection>1</T_Connection>
1186	</Block_Properties>
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1189	<Instance_Id>InletInner.</Instance_Id>
1190	<Model_Name>InletInner</Model_Name>
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1748	<Port_Target>DoublePipe_LMTD_1_1_1.InletInner</Port_Target>
1749	</Line>
1750	<Line>
1751	<Line_Name>line_18</Line_Name>
1752	<X1>95.9286</X1>
1753	<Y1>44.7329</Y1>
1754	<X2>284.286</X2>
1755	<Y2>148.571</Y2>
1756	<Block_Source>simple_source_2</Block_Source>
1757	<Port_Source>simple_source_2.Outlet</Port_Source>
1758	<Block_Target>DoublePipe_LMTD_1_1_2</Block_Target>
1759	<Port_Target>DoublePipe_LMTD_1_1_2.InletOuter</Port_Target>
1760	</Line>
1761	<Line>
1762	<Line_Name>line_19</Line_Name>
1763	<X1>95.9285</X1>
1764	<Y1>408.447</Y1>
1765	<X2>210</X2>
1766	<Y2>184.286</Y2>
1767	<Block_Source>simple_source_1</Block_Source>
1768	<Port_Source>simple_source_1.Outlet</Port_Source>
1769	<Block_Target>DoublePipe_LMTD_1_1_2</Block_Target>
1770	<Port_Target>DoublePipe_LMTD_1_1_2.InletInner</Port_Target>
1771	</Line>
1772	<Line>
1773	<Line_Name>line_20</Line_Name>
1774	<X1>402.651</X1>
1775	<Y1>216.143</Y1>
1776	<X2>561.429</X2>
1777	<Y2>345.714</Y2>
1778	<Block_Source>DoublePipe_LMTD_1_1_2</Block_Source>
1779	<Port_Source>DoublePipe_LMTD_1_1_2.OutletOuter</Port_Source>
1780	<Block_Target>DoublePipe_LMTD_1_1</Block_Target>
1781	<Port_Target>DoublePipe_LMTD_1_1.InletOuter</Port_Target>
1782	</Line>
1783	<Line>
1784	<Line_Name>line_21</Line_Name>
1785	<X1>475.429</X1>
1786	<Y1>182.718</Y1>
1787	<X2>497.143</X2>
1788	<Y2>368.571</Y2>
1789	<Block_Source>DoublePipe_LMTD_1_1_2</Block_Source>
1790	<Port_Source>DoublePipe_LMTD_1_1_2.OutletInner</Port_Source>
1791	<Block_Target>DoublePipe_LMTD_1_1</Block_Target>
1792	<Port_Target>DoublePipe_LMTD_1_1.InletInner</Port_Target>
1793	</Line>
1794	<Line>
1795	<Line_Name>line_22</Line_Name>
1796	<X1>1158.57</X1>
1797	<Y1>395.354</Y1>
1798	<X2>1118.57</X2>
1799	<Y2>604.286</Y2>
1800	<Block_Source>simple_sink_5</Block_Source>
1801	<Port_Source>simple_sink_5.Inlet</Port_Source>
1802	<Block_Target>DoublePipe_LMTD_1_1_1</Block_Target>
1803	<Port_Target>DoublePipe_LMTD_1_1_1.OutletInner</Port_Target>
1804	</Line>
1805	<Line>
1806	<Line_Name>line_23</Line_Name>
1807	<X1>1051.22</X1>
1808	<Y1>639</Y1>
1809	<X2>1174.29</X2>
1810	<Y2>707.143</Y2>
1811	<Block_Source>DoublePipe_LMTD_1_1_1</Block_Source>
1812	<Port_Source>DoublePipe_LMTD_1_1_1.OutletOuter</Port_Source>
1813	<Block_Target>simple_sink_6</Block_Target>
1814	<Port_Target>simple_sink_6.Inlet</Port_Target>
1815	</Line>
1816	</Diagram>

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