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Column_Reboiled_Kettle_Diagram.pfd @ 841

Last change on this file since 841 was 779, checked in by gerson bicca, 14 years ago
sample column updated
File size: 111.1 KB

Line
1	<?xml version="1.0"?>
2	<!-- VRTech xml file - http://www.vrtech.com.br -->
3	<Diagram version="1" revision="1">
4	<Physical_Properties>
5	<Component>isobutane</Component>
6	<Component>n-pentane</Component>
7	<Component>propylene</Component>
8	<Component>benzene</Component>
9	<Component>isobutene</Component>
10	<Liquid_Model>PR</Liquid_Model>
11	<Vapour_Model>PR</Vapour_Model>
12	</Physical_Properties>
13	<Options>
14	<Dynamic>1</Dynamic>
15	<Time_Start>0</Time_Start>
16	<Time_Step>0.1</Time_Step>
17	<Time_End>10</Time_End>
18	<Time_Unit>s</Time_Unit>
19	<Sparse_Algebra>1</Sparse_Algebra>
20	<Integration_Index>0</Integration_Index>
21	<Integration_Text>original</Integration_Text>
22	<NLASolver_File_Index>0</NLASolver_File_Index>
23	<NLASolver_File_Text>sundials</NLASolver_File_Text>
24	<DAESolver_File_Index>0</DAESolver_File_Index>
25	<DAESolver_File_Text>sundials</DAESolver_File_Text>
26	<DAESolver_Relative_Accuracy>1e-3</DAESolver_Relative_Accuracy>
27	<DAESolver_Absolute_Accuracy>1e-6</DAESolver_Absolute_Accuracy>
28	<DAESolver_Evt_Accuracy>1e-2</DAESolver_Evt_Accuracy>
29	</Options>
30	<Width>2000</Width>
31	<Height>1000</Height>
32	<Grid_Spacing>20</Grid_Spacing>
33	<View>
34	<Zoom_Level>1</Zoom_Level>
35	<Show_Grid>1</Show_Grid>
36	<Snap_to_Grid>1</Snap_to_Grid>
37	<Width>1250</Width>
38	<Height>558</Height>
39	<X>0</X>
40	<Y>0</Y>
41	</View>
42	<View>
43	<Zoom_Level>1</Zoom_Level>
44	<Show_Grid>1</Show_Grid>
45	<Snap_to_Grid>1</Snap_to_Grid>
46	<Width>1250</Width>
47	<Height>0</Height>
48	<X>0</X>
49	<Y>0</Y>
50	</View>
51	<Block>
52	<Type>simple_source</Type>
53	<Id_String>feed</Id_String>
54	<Image_File_Name>/home/bicca/apps/biblioteca/branches/gui/eml/icon/Source.png</Image_File_Name>
55	<X>67</X>
56	<Y>174</Y>
57	<Z>0</Z>
58	<Width>68</Width>
59	<Height>30</Height>
60	<Block_Properties>
61	<Model_File_Path>streams</Model_File_Path>
62	<Instance_Id>feed</Instance_Id>
63	<Model_Name>simple_source</Model_Name>
64	<T_Connection>0</T_Connection>
65	<Sub_Models>
66	<Block_Properties>
67	<Model_File_Path>streams</Model_File_Path>
68	<Instance_Id>Outlet</Instance_Id>
69	<Model_Name>Outlet</Model_Name>
70	<T_Connection>2</T_Connection>
71	<Base_Models>
72	<Block_Properties>
73	<Model_File_Path>streams</Model_File_Path>
74	<Instance_Id>Outlet</Instance_Id>
75	<Model_Name>stream</Model_Name>
76	<T_Connection>2</T_Connection>
77	<Parameters>
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79	<Index>0</Index>
80	<Values>5</Values>
81	<Status>0</Status>
82	</Parameters>
83	<Variables>
84	<Desc>F</Desc>
85	<Index>0</Index>
86	<Values>113.4</Values>
87	<Status>0</Status>
88	<Unit>kmol/h</Unit>
89	</Variables>
90	<Variables>
91	<Desc>T</Desc>
92	<Index>0</Index>
93	<Values>291</Values>
94	<Status>0</Status>
95	<Unit>K</Unit>
96	</Variables>
97	<Variables>
98	<Desc>P</Desc>
99	<Index>0</Index>
100	<Values>1.66099</Values>
101	<Status>0</Status>
102	<Unit>atm</Unit>
103	</Variables>
104	<Variables>
105	<Desc>h</Desc>
106	<Index>0</Index>
107	<Values>-15790.9</Values>
108	<Status>0</Status>
109	<Unit>kJ/kmol</Unit>
110	</Variables>
111	<Variables>
112	<Desc>v</Desc>
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114	<Values>0.429005</Values>
115	<Status>0</Status>
116	</Variables>
117	<Variables>
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122	<Index>1</Index>
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130	<Status>0</Status>
131	<Index>4</Index>
132	<Values>0.2</Values>
133	<Status>0</Status>
134	</Variables>
135	</Block_Properties>
136	</Base_Models>
137	</Block_Properties>
138	</Sub_Models>
139	<Parameters>
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141	<Index>0</Index>
142	<Values>PP</Values>
143	<Status>0</Status>
144	</Parameters>
145	<Parameters>
146	<Desc>NComp</Desc>
147	<Index>0</Index>
148	<Values>5</Values>
149	<Status>0</Status>
150	</Parameters>
151	<Parameters>
152	<Desc>M</Desc>
153	<Index>0</Index>
154	<Values>58.123</Values>
155	<Status>0</Status>
156	<Unit>kg/kmol</Unit>
157	<Index>1</Index>
158	<Values>72.1498</Values>
159	<Status>0</Status>
160	<Unit>kg/kmol</Unit>
161	<Index>2</Index>
162	<Values>42.0804</Values>
163	<Status>0</Status>
164	<Unit>kg/kmol</Unit>
165	<Index>3</Index>
166	<Values>78.1134</Values>
167	<Status>0</Status>
168	<Unit>kg/kmol</Unit>
169	<Index>4</Index>
170	<Values>56.1072</Values>
171	<Status>0</Status>
172	<Unit>kg/kmol</Unit>
173	</Parameters>
174	<Parameters>
175	<Desc>ValidPhases</Desc>
176	<Index>0</Index>
177	<Values>Vapour-Liquid</Values>
178	<Status>0</Status>
179	</Parameters>
180	<Variables>
181	<Desc>MolarComposition</Desc>
182	<Index>0</Index>
183	<Values>0.20</Values>
184	<Status>1</Status>
185	<Index>1</Index>
186	<Values>0.20</Values>
187	<Status>1</Status>
188	<Index>2</Index>
189	<Values>0.20</Values>
190	<Status>1</Status>
191	<Index>3</Index>
192	<Values>0.20</Values>
193	<Status>1</Status>
194	<Index>4</Index>
195	<Values>0.20</Values>
196	<Status>1</Status>
197	</Variables>
198	<Variables>
199	<Desc>SumOfComposition</Desc>
200	<Index>0</Index>
201	<Values>1</Values>
202	<Status>0</Status>
203	</Variables>
204	<Variables>
205	<Desc>F</Desc>
206	<Index>0</Index>
207	<Values>113.4</Values>
208	<Status>1</Status>
209	<Unit>kmol/h</Unit>
210	</Variables>
211	<Variables>
212	<Desc>T</Desc>
213	<Index>0</Index>
214	<Values>291</Values>
215	<Status>1</Status>
216	<Unit>K</Unit>
217	</Variables>
218	<Variables>
219	<Desc>T_Cdeg</Desc>
220	<Index>0</Index>
221	<Values>17.85</Values>
222	<Status>0</Status>
223	<Unit>K</Unit>
224	</Variables>
225	<Variables>
226	<Desc>P</Desc>
227	<Index>0</Index>
228	<Values>168.30</Values>
229	<Status>1</Status>
230	<Unit>kPa</Unit>
231	</Variables>
232	</Block_Properties>
233	</Block>
234	<Block>
235	<Type>simple_sink</Type>
236	<Id_String>vapour_Outlet</Id_String>
237	<Image_File_Name>/home/bicca/apps/biblioteca/branches/gui/eml/icon/Sink.png</Image_File_Name>
238	<X>118</X>
239	<Y>11</Y>
240	<Z>0</Z>
241	<Width>68</Width>
242	<Height>30</Height>
243	<Block_Properties>
244	<Model_File_Path>streams</Model_File_Path>
245	<Instance_Id>vapour_Outlet</Instance_Id>
246	<Model_Name>simple_sink</Model_Name>
247	<T_Connection>0</T_Connection>
248	<Sub_Models>
249	<Block_Properties>
250	<Model_File_Path>streams</Model_File_Path>
251	<Instance_Id>Inlet</Instance_Id>
252	<Model_Name>Inlet</Model_Name>
253	<T_Connection>1</T_Connection>
254	<Base_Models>
255	<Block_Properties>
256	<Model_File_Path>streams</Model_File_Path>
257	<Instance_Id>Inlet</Instance_Id>
258	<Model_Name>stream</Model_Name>
259	<T_Connection>1</T_Connection>
260	<Parameters>
261	<Desc>NComp</Desc>
262	<Index>0</Index>
263	<Values>5</Values>
264	<Status>0</Status>
265	</Parameters>
266	<Variables>
267	<Desc>F</Desc>
268	<Index>0</Index>
269	<Values>5</Values>
270	<Status>0</Status>
271	<Unit>kmol/h</Unit>
272	</Variables>
273	<Variables>
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276	<Values>312.739</Values>
277	<Status>0</Status>
278	<Unit>K</Unit>
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280	<Variables>
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283	<Values>5.92779</Values>
284	<Status>0</Status>
285	<Unit>atm</Unit>
286	</Variables>
287	<Variables>
288	<Desc>h</Desc>
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290	<Values>219.595</Values>
291	<Status>0</Status>
292	<Unit>kJ/kmol</Unit>
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361	<Unit>kmol/h</Unit>
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367	<Status>0</Status>
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428	<Status>0</Status>
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442	<Index>4</Index>
443	<Values>56.1072</Values>
444	<Status>0</Status>
445	<Unit>kg/kmol</Unit>
446	</Parameters>
447	<Parameters>
448	<Desc>CompositionBasis</Desc>
449	<Index>0</Index>
450	<Values>Molar</Values>
451	<Status>4</Status>
452	</Parameters>
453	<Parameters>
454	<Desc>ValidPhases</Desc>
455	<Index>0</Index>
456	<Values>Liquid-Only</Values>
457	<Status>4</Status>
458	</Parameters>
459	<Variables>
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462	<Values>0.20</Values>
463	<Status>1</Status>
464	<Index>1</Index>
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487	<Status>1</Status>
488	<Unit>kmol/h</Unit>
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490	<Variables>
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493	<Values>4169.4</Values>
494	<Status>0</Status>
495	<Unit>kg/h</Unit>
496	</Variables>
497	<Variables>
498	<Desc>Fvol</Desc>
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500	<Values>6.1008</Values>
501	<Status>0</Status>
502	<Unit>m^3/h</Unit>
503	</Variables>
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509	<Unit>K</Unit>
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515	<Status>0</Status>
516	<Unit>K</Unit>
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529	<Status>0</Status>
530	<Unit>kg/kmol</Unit>
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535	<Values>8.97177e-05</Values>
536	<Status>0</Status>
537	<Unit>m^3/mol</Unit>
538	</Variables>
539	<Variables>
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543	<Status>0</Status>
544	<Unit>kg/m^3</Unit>
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546	<Variables>
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550	<Status>0</Status>
551	<Unit>kmol/m^3</Unit>
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1311	<Instance_Id>OutletLiquid</Instance_Id>
1312	<Model_Name>OutletLiquid</Model_Name>
1313	<T_Connection>2</T_Connection>
1314	<Base_Models>
1315	<Block_Properties>
1316	<Model_File_Path>streams</Model_File_Path>
1317	<Instance_Id>OutletLiquid</Instance_Id>
1318	<Model_Name>liquid_stream</Model_Name>
1319	<T_Connection>2</T_Connection>
1320	<Base_Models>
1321	<Block_Properties>
1322	<Model_File_Path>streams</Model_File_Path>
1323	<Instance_Id>OutletLiquid</Instance_Id>
1324	<Model_Name>stream</Model_Name>
1325	<T_Connection>2</T_Connection>
1326	</Block_Properties>
1327	</Base_Models>
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1329	<Desc>PP</Desc>
1330	<Index>0</Index>
1331	<Values>PP</Values>
1332	<Status>0</Status>
1333	</Parameters>
1334	</Block_Properties>
1335	</Base_Models>
1336	</Block_Properties>
1337	</Sub_Models>
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1339	<Block_Properties>
1340	<Model_File_Path>stage_separators/tray</Model_File_Path>
1341	<Instance_Id>OutletVapour</Instance_Id>
1342	<Model_Name>OutletVapour</Model_Name>
1343	<T_Connection>2</T_Connection>
1344	<Base_Models>
1345	<Block_Properties>
1346	<Model_File_Path>streams</Model_File_Path>
1347	<Instance_Id>OutletVapour</Instance_Id>
1348	<Model_Name>vapour_stream</Model_Name>
1349	<T_Connection>2</T_Connection>
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1351	<Block_Properties>
1352	<Model_File_Path>streams</Model_File_Path>
1353	<Instance_Id>OutletVapour</Instance_Id>
1354	<Model_Name>stream</Model_Name>
1355	<T_Connection>2</T_Connection>
1356	</Block_Properties>
1357	</Base_Models>
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1359	<Desc>PP</Desc>
1360	<Index>0</Index>
1361	<Values>PP</Values>
1362	<Status>0</Status>
1363	</Parameters>
1364	</Block_Properties>
1365	</Base_Models>
1366	</Block_Properties>
1367	</Sub_Models>
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1369	<Desc>PP</Desc>
1370	<Index>0</Index>
1371	<Values>PP</Values>
1372	<Status>0</Status>
1373	</Parameters>
1374	</Block_Properties>
1375	</Base_Models>
1376	</Block_Properties>
1377	</Base_Models>
1378	</Block_Properties>
1379	</Sub_Models>
1380	<Sub_Models>
1381	<Block_Properties>
1382	<Model_File_Path>stage_separators/column</Model_File_Path>
1383	<Instance_Id>TRAYS(1.</Instance_Id>
1384	<Model_Name>TRAYS</Model_Name>
1385	<T_Connection>0</T_Connection>
1386	<Base_Models>
1387	<Block_Properties>
1388	<Model_File_Path>stage_separators/tray</Model_File_Path>
1389	<Instance_Id>TRAYS(1.</Instance_Id>
1390	<Model_Name>tray</Model_Name>
1391	<T_Connection>0</T_Connection>
1392	<Base_Models>
1393	<Block_Properties>
1394	<Model_File_Path>stage_separators/tray</Model_File_Path>
1395	<Instance_Id>TRAYS(1.</Instance_Id>
1396	<Model_Name>trayBasic</Model_Name>
1397	<T_Connection>0</T_Connection>
1398	<Sub_Models>
1399	<Block_Properties>
1400	<Model_File_Path>stage_separators/tray</Model_File_Path>
1401	<Instance_Id>InletLiquid</Instance_Id>
1402	<Model_Name>InletLiquid</Model_Name>
1403	<T_Connection>1</T_Connection>
1404	<Base_Models>
1405	<Block_Properties>
1406	<Model_File_Path>streams</Model_File_Path>
1407	<Instance_Id>InletLiquid</Instance_Id>
1408	<Model_Name>stream</Model_Name>
1409	<T_Connection>1</T_Connection>
1410	</Block_Properties>
1411	</Base_Models>
1412	</Block_Properties>
1413	</Sub_Models>
1414	<Sub_Models>
1415	<Block_Properties>
1416	<Model_File_Path>stage_separators/tray</Model_File_Path>
1417	<Instance_Id>InletVapour</Instance_Id>
1418	<Model_Name>InletVapour</Model_Name>
1419	<T_Connection>1</T_Connection>
1420	<Base_Models>
1421	<Block_Properties>
1422	<Model_File_Path>streams</Model_File_Path>
1423	<Instance_Id>InletVapour</Instance_Id>
1424	<Model_Name>stream</Model_Name>
1425	<T_Connection>1</T_Connection>
1426	</Block_Properties>
1427	</Base_Models>
1428	</Block_Properties>
1429	</Sub_Models>
1430	<Sub_Models>
1431	<Block_Properties>
1432	<Model_File_Path>stage_separators/tray</Model_File_Path>
1433	<Instance_Id>OutletLiquid</Instance_Id>
1434	<Model_Name>OutletLiquid</Model_Name>
1435	<T_Connection>2</T_Connection>
1436	<Base_Models>
1437	<Block_Properties>
1438	<Model_File_Path>streams</Model_File_Path>
1439	<Instance_Id>OutletLiquid</Instance_Id>
1440	<Model_Name>liquid_stream</Model_Name>
1441	<T_Connection>2</T_Connection>
1442	<Base_Models>
1443	<Block_Properties>
1444	<Model_File_Path>streams</Model_File_Path>
1445	<Instance_Id>OutletLiquid</Instance_Id>
1446	<Model_Name>stream</Model_Name>
1447	<T_Connection>2</T_Connection>
1448	</Block_Properties>
1449	</Base_Models>
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1451	<Desc>PP</Desc>
1452	<Index>0</Index>
1453	<Values>PP</Values>
1454	<Status>0</Status>
1455	</Parameters>
1456	</Block_Properties>
1457	</Base_Models>
1458	</Block_Properties>
1459	</Sub_Models>
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1461	<Block_Properties>
1462	<Model_File_Path>stage_separators/tray</Model_File_Path>
1463	<Instance_Id>OutletVapour</Instance_Id>
1464	<Model_Name>OutletVapour</Model_Name>
1465	<T_Connection>2</T_Connection>
1466	<Base_Models>
1467	<Block_Properties>
1468	<Model_File_Path>streams</Model_File_Path>
1469	<Instance_Id>OutletVapour</Instance_Id>
1470	<Model_Name>vapour_stream</Model_Name>
1471	<T_Connection>2</T_Connection>
1472	<Base_Models>
1473	<Block_Properties>
1474	<Model_File_Path>streams</Model_File_Path>
1475	<Instance_Id>OutletVapour</Instance_Id>
1476	<Model_Name>stream</Model_Name>
1477	<T_Connection>2</T_Connection>
1478	</Block_Properties>
1479	</Base_Models>
1480	<Parameters>
1481	<Desc>PP</Desc>
1482	<Index>0</Index>
1483	<Values>PP</Values>
1484	<Status>0</Status>
1485	</Parameters>
1486	</Block_Properties>
1487	</Base_Models>
1488	</Block_Properties>
1489	</Sub_Models>
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1491	<Desc>PP</Desc>
1492	<Index>0</Index>
1493	<Values>PP</Values>
1494	<Status>0</Status>
1495	</Parameters>
1496	</Block_Properties>
1497	</Base_Models>
1498	</Block_Properties>
1499	</Base_Models>
1500	</Block_Properties>
1501	</Sub_Models>
1502	<Sub_Models>
1503	<Block_Properties>
1504	<Model_File_Path>stage_separators/column</Model_File_Path>
1505	<Instance_Id>TRAYS(1.</Instance_Id>
1506	<Model_Name>TRAYS</Model_Name>
1507	<T_Connection>0</T_Connection>
1508	<Base_Models>
1509	<Block_Properties>
1510	<Model_File_Path>stage_separators/tray</Model_File_Path>
1511	<Instance_Id>TRAYS(1.</Instance_Id>
1512	<Model_Name>tray</Model_Name>
1513	<T_Connection>0</T_Connection>
1514	<Base_Models>
1515	<Block_Properties>
1516	<Model_File_Path>stage_separators/tray</Model_File_Path>
1517	<Instance_Id>TRAYS(1.</Instance_Id>
1518	<Model_Name>trayBasic</Model_Name>
1519	<T_Connection>0</T_Connection>
1520	<Sub_Models>
1521	<Block_Properties>
1522	<Model_File_Path>stage_separators/tray</Model_File_Path>
1523	<Instance_Id>InletLiquid</Instance_Id>
1524	<Model_Name>InletLiquid</Model_Name>
1525	<T_Connection>1</T_Connection>
1526	<Base_Models>
1527	<Block_Properties>
1528	<Model_File_Path>streams</Model_File_Path>
1529	<Instance_Id>InletLiquid</Instance_Id>
1530	<Model_Name>stream</Model_Name>
1531	<T_Connection>1</T_Connection>
1532	</Block_Properties>
1533	</Base_Models>
1534	</Block_Properties>
1535	</Sub_Models>
1536	<Sub_Models>
1537	<Block_Properties>
1538	<Model_File_Path>stage_separators/tray</Model_File_Path>
1539	<Instance_Id>InletVapour</Instance_Id>
1540	<Model_Name>InletVapour</Model_Name>
1541	<T_Connection>1</T_Connection>
1542	<Base_Models>
1543	<Block_Properties>
1544	<Model_File_Path>streams</Model_File_Path>
1545	<Instance_Id>InletVapour</Instance_Id>
1546	<Model_Name>stream</Model_Name>
1547	<T_Connection>1</T_Connection>
1548	</Block_Properties>
1549	</Base_Models>
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1551	</Sub_Models>
1552	<Sub_Models>
1553	<Block_Properties>
1554	<Model_File_Path>stage_separators/tray</Model_File_Path>
1555	<Instance_Id>OutletLiquid</Instance_Id>
1556	<Model_Name>OutletLiquid</Model_Name>
1557	<T_Connection>2</T_Connection>
1558	<Base_Models>
1559	<Block_Properties>
1560	<Model_File_Path>streams</Model_File_Path>
1561	<Instance_Id>OutletLiquid</Instance_Id>
1562	<Model_Name>liquid_stream</Model_Name>
1563	<T_Connection>2</T_Connection>
1564	<Base_Models>
1565	<Block_Properties>
1566	<Model_File_Path>streams</Model_File_Path>
1567	<Instance_Id>OutletLiquid</Instance_Id>
1568	<Model_Name>stream</Model_Name>
1569	<T_Connection>2</T_Connection>
1570	</Block_Properties>
1571	</Base_Models>
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1573	<Desc>PP</Desc>
1574	<Index>0</Index>
1575	<Values>PP</Values>
1576	<Status>0</Status>
1577	</Parameters>
1578	</Block_Properties>
1579	</Base_Models>
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1581	</Sub_Models>
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1584	<Model_File_Path>stage_separators/tray</Model_File_Path>
1585	<Instance_Id>OutletVapour</Instance_Id>
1586	<Model_Name>OutletVapour</Model_Name>
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1590	<Model_File_Path>streams</Model_File_Path>
1591	<Instance_Id>OutletVapour</Instance_Id>
1592	<Model_Name>vapour_stream</Model_Name>
1593	<T_Connection>2</T_Connection>
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1595	<Block_Properties>
1596	<Model_File_Path>streams</Model_File_Path>
1597	<Instance_Id>OutletVapour</Instance_Id>
1598	<Model_Name>stream</Model_Name>
1599	<T_Connection>2</T_Connection>
1600	</Block_Properties>
1601	</Base_Models>
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1603	<Desc>PP</Desc>
1604	<Index>0</Index>
1605	<Values>PP</Values>
1606	<Status>0</Status>
1607	</Parameters>
1608	</Block_Properties>
1609	</Base_Models>
1610	</Block_Properties>
1611	</Sub_Models>
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1613	<Desc>PP</Desc>
1614	<Index>0</Index>
1615	<Values>PP</Values>
1616	<Status>0</Status>
1617	</Parameters>
1618	</Block_Properties>
1619	</Base_Models>
1620	</Block_Properties>
1621	</Base_Models>
1622	</Block_Properties>
1623	</Sub_Models>
1624	<Sub_Models>
1625	<Block_Properties>
1626	<Model_File_Path>stage_separators/column</Model_File_Path>
1627	<Instance_Id>TRAYS(1.</Instance_Id>
1628	<Model_Name>TRAYS</Model_Name>
1629	<T_Connection>0</T_Connection>
1630	<Base_Models>
1631	<Block_Properties>
1632	<Model_File_Path>stage_separators/tray</Model_File_Path>
1633	<Instance_Id>TRAYS(1.</Instance_Id>
1634	<Model_Name>tray</Model_Name>
1635	<T_Connection>0</T_Connection>
1636	<Base_Models>
1637	<Block_Properties>
1638	<Model_File_Path>stage_separators/tray</Model_File_Path>
1639	<Instance_Id>TRAYS(1.</Instance_Id>
1640	<Model_Name>trayBasic</Model_Name>
1641	<T_Connection>0</T_Connection>
1642	<Sub_Models>
1643	<Block_Properties>
1644	<Model_File_Path>stage_separators/tray</Model_File_Path>
1645	<Instance_Id>InletLiquid</Instance_Id>
1646	<Model_Name>InletLiquid</Model_Name>
1647	<T_Connection>1</T_Connection>
1648	<Base_Models>
1649	<Block_Properties>
1650	<Model_File_Path>streams</Model_File_Path>
1651	<Instance_Id>InletLiquid</Instance_Id>
1652	<Model_Name>stream</Model_Name>
1653	<T_Connection>1</T_Connection>
1654	</Block_Properties>
1655	</Base_Models>
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1657	</Sub_Models>
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1660	<Model_File_Path>stage_separators/tray</Model_File_Path>
1661	<Instance_Id>InletVapour</Instance_Id>
1662	<Model_Name>InletVapour</Model_Name>
1663	<T_Connection>1</T_Connection>
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1666	<Model_File_Path>streams</Model_File_Path>
1667	<Instance_Id>InletVapour</Instance_Id>
1668	<Model_Name>stream</Model_Name>
1669	<T_Connection>1</T_Connection>
1670	</Block_Properties>
1671	</Base_Models>
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1675	<Block_Properties>
1676	<Model_File_Path>stage_separators/tray</Model_File_Path>
1677	<Instance_Id>OutletLiquid</Instance_Id>
1678	<Model_Name>OutletLiquid</Model_Name>
1679	<T_Connection>2</T_Connection>
1680	<Base_Models>
1681	<Block_Properties>
1682	<Model_File_Path>streams</Model_File_Path>
1683	<Instance_Id>OutletLiquid</Instance_Id>
1684	<Model_Name>liquid_stream</Model_Name>
1685	<T_Connection>2</T_Connection>
1686	<Base_Models>
1687	<Block_Properties>
1688	<Model_File_Path>streams</Model_File_Path>
1689	<Instance_Id>OutletLiquid</Instance_Id>
1690	<Model_Name>stream</Model_Name>
1691	<T_Connection>2</T_Connection>
1692	</Block_Properties>
1693	</Base_Models>
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1695	<Desc>PP</Desc>
1696	<Index>0</Index>
1697	<Values>PP</Values>
1698	<Status>0</Status>
1699	</Parameters>
1700	</Block_Properties>
1701	</Base_Models>
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1703	</Sub_Models>
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1706	<Model_File_Path>stage_separators/tray</Model_File_Path>
1707	<Instance_Id>OutletVapour</Instance_Id>
1708	<Model_Name>OutletVapour</Model_Name>
1709	<T_Connection>2</T_Connection>
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1711	<Block_Properties>
1712	<Model_File_Path>streams</Model_File_Path>
1713	<Instance_Id>OutletVapour</Instance_Id>
1714	<Model_Name>vapour_stream</Model_Name>
1715	<T_Connection>2</T_Connection>
1716	<Base_Models>
1717	<Block_Properties>
1718	<Model_File_Path>streams</Model_File_Path>
1719	<Instance_Id>OutletVapour</Instance_Id>
1720	<Model_Name>stream</Model_Name>
1721	<T_Connection>2</T_Connection>
1722	</Block_Properties>
1723	</Base_Models>
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1725	<Desc>PP</Desc>
1726	<Index>0</Index>
1727	<Values>PP</Values>
1728	<Status>0</Status>
1729	</Parameters>
1730	</Block_Properties>
1731	</Base_Models>
1732	</Block_Properties>
1733	</Sub_Models>
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1735	<Desc>PP</Desc>
1736	<Index>0</Index>
1737	<Values>PP</Values>
1738	<Status>0</Status>
1739	</Parameters>
1740	</Block_Properties>
1741	</Base_Models>
1742	</Block_Properties>
1743	</Base_Models>
1744	</Block_Properties>
1745	</Sub_Models>
1746	<Sub_Models>
1747	<Block_Properties>
1748	<Model_File_Path>stage_separators/column</Model_File_Path>
1749	<Instance_Id>TRAYS(1.</Instance_Id>
1750	<Model_Name>TRAYS</Model_Name>
1751	<T_Connection>0</T_Connection>
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1753	<Block_Properties>
1754	<Model_File_Path>stage_separators/tray</Model_File_Path>
1755	<Instance_Id>TRAYS(1.</Instance_Id>
1756	<Model_Name>tray</Model_Name>
1757	<T_Connection>0</T_Connection>
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1759	<Block_Properties>
1760	<Model_File_Path>stage_separators/tray</Model_File_Path>
1761	<Instance_Id>TRAYS(1.</Instance_Id>
1762	<Model_Name>trayBasic</Model_Name>
1763	<T_Connection>0</T_Connection>
1764	<Sub_Models>
1765	<Block_Properties>
1766	<Model_File_Path>stage_separators/tray</Model_File_Path>
1767	<Instance_Id>InletLiquid</Instance_Id>
1768	<Model_Name>InletLiquid</Model_Name>
1769	<T_Connection>1</T_Connection>
1770	<Base_Models>
1771	<Block_Properties>
1772	<Model_File_Path>streams</Model_File_Path>
1773	<Instance_Id>InletLiquid</Instance_Id>
1774	<Model_Name>stream</Model_Name>
1775	<T_Connection>1</T_Connection>
1776	</Block_Properties>
1777	</Base_Models>
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1779	</Sub_Models>
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1782	<Model_File_Path>stage_separators/tray</Model_File_Path>
1783	<Instance_Id>InletVapour</Instance_Id>
1784	<Model_Name>InletVapour</Model_Name>
1785	<T_Connection>1</T_Connection>
1786	<Base_Models>
1787	<Block_Properties>
1788	<Model_File_Path>streams</Model_File_Path>
1789	<Instance_Id>InletVapour</Instance_Id>
1790	<Model_Name>stream</Model_Name>
1791	<T_Connection>1</T_Connection>
1792	</Block_Properties>
1793	</Base_Models>
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1798	<Model_File_Path>stage_separators/tray</Model_File_Path>
1799	<Instance_Id>OutletLiquid</Instance_Id>
1800	<Model_Name>OutletLiquid</Model_Name>
1801	<T_Connection>2</T_Connection>
1802	<Base_Models>
1803	<Block_Properties>
1804	<Model_File_Path>streams</Model_File_Path>
1805	<Instance_Id>OutletLiquid</Instance_Id>
1806	<Model_Name>liquid_stream</Model_Name>
1807	<T_Connection>2</T_Connection>
1808	<Base_Models>
1809	<Block_Properties>
1810	<Model_File_Path>streams</Model_File_Path>
1811	<Instance_Id>OutletLiquid</Instance_Id>
1812	<Model_Name>stream</Model_Name>
1813	<T_Connection>2</T_Connection>
1814	</Block_Properties>
1815	</Base_Models>
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1817	<Desc>PP</Desc>
1818	<Index>0</Index>
1819	<Values>PP</Values>
1820	<Status>0</Status>
1821	</Parameters>
1822	</Block_Properties>
1823	</Base_Models>
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1825	</Sub_Models>
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1828	<Model_File_Path>stage_separators/tray</Model_File_Path>
1829	<Instance_Id>OutletVapour</Instance_Id>
1830	<Model_Name>OutletVapour</Model_Name>
1831	<T_Connection>2</T_Connection>
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1833	<Block_Properties>
1834	<Model_File_Path>streams</Model_File_Path>
1835	<Instance_Id>OutletVapour</Instance_Id>
1836	<Model_Name>vapour_stream</Model_Name>
1837	<T_Connection>2</T_Connection>
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1839	<Block_Properties>
1840	<Model_File_Path>streams</Model_File_Path>
1841	<Instance_Id>OutletVapour</Instance_Id>
1842	<Model_Name>stream</Model_Name>
1843	<T_Connection>2</T_Connection>
1844	</Block_Properties>
1845	</Base_Models>
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1847	<Desc>PP</Desc>
1848	<Index>0</Index>
1849	<Values>PP</Values>
1850	<Status>0</Status>
1851	</Parameters>
1852	</Block_Properties>
1853	</Base_Models>
1854	</Block_Properties>
1855	</Sub_Models>
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1857	<Desc>PP</Desc>
1858	<Index>0</Index>
1859	<Values>PP</Values>
1860	<Status>0</Status>
1861	</Parameters>
1862	</Block_Properties>
1863	</Base_Models>
1864	</Block_Properties>
1865	</Base_Models>
1866	</Block_Properties>
1867	</Sub_Models>
1868	<Sub_Models>
1869	<Block_Properties>
1870	<Model_File_Path>stage_separators/column</Model_File_Path>
1871	<Instance_Id>TRAYS(1.</Instance_Id>
1872	<Model_Name>TRAYS</Model_Name>
1873	<T_Connection>0</T_Connection>
1874	<Base_Models>
1875	<Block_Properties>
1876	<Model_File_Path>stage_separators/tray</Model_File_Path>
1877	<Instance_Id>TRAYS(1.</Instance_Id>
1878	<Model_Name>tray</Model_Name>
1879	<T_Connection>0</T_Connection>
1880	<Base_Models>
1881	<Block_Properties>
1882	<Model_File_Path>stage_separators/tray</Model_File_Path>
1883	<Instance_Id>TRAYS(1.</Instance_Id>
1884	<Model_Name>trayBasic</Model_Name>
1885	<T_Connection>0</T_Connection>
1886	<Sub_Models>
1887	<Block_Properties>
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1889	<Instance_Id>InletLiquid</Instance_Id>
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1927	<Instance_Id>OutletLiquid</Instance_Id>
1928	<Model_Name>liquid_stream</Model_Name>
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1957	<Instance_Id>OutletVapour</Instance_Id>
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1981	<Values>PP</Values>
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1994	<Model_Name>TRAYS</Model_Name>
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1996	<Base_Models>
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2000	<Model_Name>tray</Model_Name>
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2005	<Instance_Id>TRAYS(1.</Instance_Id>
2006	<Model_Name>trayBasic</Model_Name>
2007	<T_Connection>0</T_Connection>
2008	<Sub_Models>
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2011	<Instance_Id>InletLiquid</Instance_Id>
2012	<Model_Name>InletLiquid</Model_Name>
2013	<T_Connection>1</T_Connection>
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2015	<Block_Properties>
2016	<Model_File_Path>streams</Model_File_Path>
2017	<Instance_Id>InletLiquid</Instance_Id>
2018	<Model_Name>stream</Model_Name>
2019	<T_Connection>1</T_Connection>
2020	</Block_Properties>
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2044	<Model_Name>OutletLiquid</Model_Name>
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2049	<Instance_Id>OutletLiquid</Instance_Id>
2050	<Model_Name>liquid_stream</Model_Name>
2051	<T_Connection>2</T_Connection>
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2055	<Instance_Id>OutletLiquid</Instance_Id>
2056	<Model_Name>stream</Model_Name>
2057	<T_Connection>2</T_Connection>
2058	</Block_Properties>
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2063	<Values>PP</Values>
2064	<Status>0</Status>
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2074	<Model_Name>OutletVapour</Model_Name>
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2079	<Instance_Id>OutletVapour</Instance_Id>
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2085	<Instance_Id>OutletVapour</Instance_Id>
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2087	<T_Connection>2</T_Connection>
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2093	<Values>PP</Values>
2094	<Status>0</Status>
2095	</Parameters>
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2102	<Index>0</Index>
2103	<Values>PP</Values>
2104	<Status>0</Status>
2105	</Parameters>
2106	</Block_Properties>
2107	</Base_Models>
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2109	</Base_Models>
2110	</Block_Properties>
2111	</Sub_Models>
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2113	<Block_Properties>
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2115	<Instance_Id>TRAYS(1.</Instance_Id>
2116	<Model_Name>TRAYS</Model_Name>
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2121	<Instance_Id>TRAYS(1.</Instance_Id>
2122	<Model_Name>tray</Model_Name>
2123	<T_Connection>0</T_Connection>
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2125	<Block_Properties>
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2127	<Instance_Id>TRAYS(1.</Instance_Id>
2128	<Model_Name>trayBasic</Model_Name>
2129	<T_Connection>0</T_Connection>
2130	<Sub_Models>
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2133	<Instance_Id>InletLiquid</Instance_Id>
2134	<Model_Name>InletLiquid</Model_Name>
2135	<T_Connection>1</T_Connection>
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2139	<Instance_Id>InletLiquid</Instance_Id>
2140	<Model_Name>stream</Model_Name>
2141	<T_Connection>1</T_Connection>
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2165	<Instance_Id>OutletLiquid</Instance_Id>
2166	<Model_Name>OutletLiquid</Model_Name>
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2170	<Model_File_Path>streams</Model_File_Path>
2171	<Instance_Id>OutletLiquid</Instance_Id>
2172	<Model_Name>liquid_stream</Model_Name>
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2177	<Instance_Id>OutletLiquid</Instance_Id>
2178	<Model_Name>stream</Model_Name>
2179	<T_Connection>2</T_Connection>
2180	</Block_Properties>
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2185	<Values>PP</Values>
2186	<Status>0</Status>
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2201	<Instance_Id>OutletVapour</Instance_Id>
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2215	<Values>PP</Values>
2216	<Status>0</Status>
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2225	<Values>PP</Values>
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2255	<Instance_Id>InletLiquid</Instance_Id>
2256	<Model_Name>InletLiquid</Model_Name>
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2261	<Instance_Id>InletLiquid</Instance_Id>
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2293	<Instance_Id>OutletLiquid</Instance_Id>
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2299	<Instance_Id>OutletLiquid</Instance_Id>
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2301	<T_Connection>2</T_Connection>
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2307	<Values>PP</Values>
2308	<Status>0</Status>
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2331	<T_Connection>2</T_Connection>
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2337	<Values>PP</Values>
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2347	<Values>PP</Values>
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2429	<Values>PP</Values>
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2453	<T_Connection>2</T_Connection>
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2459	<Values>PP</Values>
2460	<Status>0</Status>
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2469	<Values>PP</Values>
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2477	</Sub_Models>
2478	<Parameters>
2479	<Desc>PP</Desc>
2480	<Index>0</Index>
2481	<Values>PP</Values>
2482	<Status>0</Status>
2483	</Parameters>
2484	<Parameters>
2485	<Desc>NComp</Desc>
2486	<Index>0</Index>
2487	<Values>5</Values>
2488	<Status>0</Status>
2489	</Parameters>
2490	<Parameters>
2491	<Desc>NumberOfTrays</Desc>
2492	<Index>0</Index>
2493	<Values>12</Values>
2494	<Status>4</Status>
2495	</Parameters>
2496	<Parameters>
2497	<Desc>FeedTrayTopLocation</Desc>
2498	<Index>0</Index>
2499	<Values>3</Values>
2500	<Status>4</Status>
2501	</Parameters>
2502	<Parameters>
2503	<Desc>FeedTrayBottomLocation</Desc>
2504	<Index>0</Index>
2505	<Values>9</Values>
2506	<Status>4</Status>
2507	</Parameters>
2508	<Parameters>
2509	<Desc>LiquidSideStreamLocation</Desc>
2510	<Index>0</Index>
2511	<Values>2</Values>
2512	<Status>4</Status>
2513	</Parameters>
2514	<Parameters>
2515	<Desc>VapourSideStreamLocation</Desc>
2516	<Index>0</Index>
2517	<Values>2</Values>
2518	<Status>4</Status>
2519	</Parameters>
2520	<Parameters>
2521	<Desc>VapourFlowModel</Desc>
2522	<Index>0</Index>
2523	<Values>Reepmeyer</Values>
2524	<Status>0</Status>
2525	</Parameters>
2526	<Parameters>
2527	<Desc>LiquidFlowModel</Desc>
2528	<Index>0</Index>
2529	<Values>default</Values>
2530	<Status>0</Status>
2531	</Parameters>
2532	<Parameters>
2533	<Desc>VolumeOfTray</Desc>
2534	<Index>0</Index>
2535	<Values>4</Values>
2536	<Status>4</Status>
2537	<Unit>ft^3</Unit>
2538	</Parameters>
2539	<Parameters>
2540	<Desc>HeatSupply</Desc>
2541	<Index>0</Index>
2542	<Values>0</Values>
2543	<Status>4</Status>
2544	<Unit>kW</Unit>
2545	</Parameters>
2546	<Parameters>
2547	<Desc>PlateArea</Desc>
2548	<Index>0</Index>
2549	<Values>3.94</Values>
2550	<Status>4</Status>
2551	<Unit>ft^2</Unit>
2552	</Parameters>
2553	<Parameters>
2554	<Desc>HolesArea</Desc>
2555	<Index>0</Index>
2556	<Values>0.394</Values>
2557	<Status>4</Status>
2558	<Unit>ft^2</Unit>
2559	</Parameters>
2560	<Parameters>
2561	<Desc>WeirLength</Desc>
2562	<Index>0</Index>
2563	<Values>20.94</Values>
2564	<Status>4</Status>
2565	<Unit>in</Unit>
2566	</Parameters>
2567	<Parameters>
2568	<Desc>WeirHeight</Desc>
2569	<Index>0</Index>
2570	<Values>0.125</Values>
2571	<Status>4</Status>
2572	<Unit>ft</Unit>
2573	</Parameters>
2574	<Parameters>
2575	<Desc>FeeheryCoeff</Desc>
2576	<Index>0</Index>
2577	<Values>1</Values>
2578	<Status>0</Status>
2579	<Unit>1/m^4</Unit>
2580	</Parameters>
2581	<Parameters>
2582	<Desc>ElgueCoeff</Desc>
2583	<Index>0</Index>
2584	<Values>1</Values>
2585	<Status>0</Status>
2586	<Unit>kg/m/mol^2</Unit>
2587	</Parameters>
2588	<Parameters>
2589	<Desc>OlsenCoeff</Desc>
2590	<Index>0</Index>
2591	<Values>1</Values>
2592	<Status>0</Status>
2593	</Parameters>
2594	<Parameters>
2595	<Desc>TrayLiquidPasses</Desc>
2596	<Index>0</Index>
2597	<Values>1</Values>
2598	<Status>0</Status>
2599	</Parameters>
2600	<Parameters>
2601	<Desc>beta</Desc>
2602	<Index>0</Index>
2603	<Values>0.6</Values>
2604	<Status>4</Status>
2605	</Parameters>
2606	<Parameters>
2607	<Desc>alfa</Desc>
2608	<Index>0</Index>
2609	<Values>4</Values>
2610	<Status>4</Status>
2611	</Parameters>
2612	<Variables>
2613	<Desc>VapourDrawOffFlow</Desc>
2614	<Index>0</Index>
2615	<Values>0</Values>
2616	<Status>1</Status>
2617	<Unit>kmol/h</Unit>
2618	</Variables>
2619	<Variables>
2620	<Desc>LiquidDrawOffFlow</Desc>
2621	<Index>0</Index>
2622	<Values>0</Values>
2623	<Status>1</Status>
2624	<Unit>kmol/h</Unit>
2625	</Variables>
2626	<Variables>
2627	<Desc>MurphreeEff</Desc>
2628	<Index>0</Index>
2629	<Values>1</Values>
2630	<Status>1</Status>
2631	</Variables>
2632	</Block_Properties>
2633	</Base_Models>
2634	<Sub_Models>
2635	<Block_Properties>
2636	<Model_File_Path>stage_separators/column</Model_File_Path>
2637	<Instance_Id>VapourDrawOff</Instance_Id>
2638	<Model_Name>VapourDrawOff</Model_Name>
2639	<T_Connection>2</T_Connection>
2640	<Base_Models>
2641	<Block_Properties>
2642	<Model_File_Path>streams</Model_File_Path>
2643	<Instance_Id>VapourDrawOff</Instance_Id>
2644	<Model_Name>vapour_stream</Model_Name>
2645	<T_Connection>2</T_Connection>
2646	<Base_Models>
2647	<Block_Properties>
2648	<Model_File_Path>streams</Model_File_Path>
2649	<Instance_Id>VapourDrawOff</Instance_Id>
2650	<Model_Name>stream</Model_Name>
2651	<T_Connection>2</T_Connection>
2652	<Parameters>
2653	<Desc>NComp</Desc>
2654	<Index>0</Index>
2655	<Values>5</Values>
2656	<Status>0</Status>
2657	</Parameters>
2658	<Variables>
2659	<Desc>F</Desc>
2660	<Index>0</Index>
2661	<Values>0</Values>
2662	<Status>0</Status>
2663	<Unit>kmol/h</Unit>
2664	</Variables>
2665	<Variables>
2666	<Desc>T</Desc>
2667	<Index>0</Index>
2668	<Values>314.942</Values>
2669	<Status>0</Status>
2670	<Unit>K</Unit>
2671	</Variables>
2672	<Variables>
2673	<Desc>P</Desc>
2674	<Index>0</Index>
2675	<Values>5.92799</Values>
2676	<Status>0</Status>
2677	<Unit>atm</Unit>
2678	</Variables>
2679	<Variables>
2680	<Desc>h</Desc>
2681	<Index>0</Index>
2682	<Values>402.964</Values>
2683	<Status>0</Status>
2684	<Unit>kJ/kmol</Unit>
2685	</Variables>
2686	<Variables>
2687	<Desc>v</Desc>
2688	<Index>0</Index>
2689	<Values>1</Values>
2690	<Status>0</Status>
2691	</Variables>
2692	<Variables>
2693	<Desc>z</Desc>
2694	<Index>0</Index>
2695	<Values>0.198532</Values>
2696	<Status>0</Status>
2697	<Index>1</Index>
2698	<Values>0.0447686</Values>
2699	<Status>0</Status>
2700	<Index>2</Index>
2701	<Values>0.5732</Values>
2702	<Status>0</Status>
2703	<Index>3</Index>
2704	<Values>0.013302</Values>
2705	<Status>0</Status>
2706	<Index>4</Index>
2707	<Values>0.170198</Values>
2708	<Status>0</Status>
2709	</Variables>
2710	</Block_Properties>
2711	</Base_Models>
2712	<Parameters>
2713	<Desc>PP</Desc>
2714	<Index>0</Index>
2715	<Values>PP</Values>
2716	<Status>0</Status>
2717	</Parameters>
2718	</Block_Properties>
2719	</Base_Models>
2720	</Block_Properties>
2721	</Sub_Models>
2722	<Sub_Models>
2723	<Block_Properties>
2724	<Model_File_Path>stage_separators/column</Model_File_Path>
2725	<Instance_Id>LiquidDrawOff</Instance_Id>
2726	<Model_Name>LiquidDrawOff</Model_Name>
2727	<T_Connection>2</T_Connection>
2728	<Base_Models>
2729	<Block_Properties>
2730	<Model_File_Path>streams</Model_File_Path>
2731	<Instance_Id>LiquidDrawOff</Instance_Id>
2732	<Model_Name>liquid_stream</Model_Name>
2733	<T_Connection>2</T_Connection>
2734	<Base_Models>
2735	<Block_Properties>
2736	<Model_File_Path>streams</Model_File_Path>
2737	<Instance_Id>LiquidDrawOff</Instance_Id>
2738	<Model_Name>stream</Model_Name>
2739	<T_Connection>2</T_Connection>
2740	<Parameters>
2741	<Desc>NComp</Desc>
2742	<Index>0</Index>
2743	<Values>5</Values>
2744	<Status>0</Status>
2745	</Parameters>
2746	<Variables>
2747	<Desc>F</Desc>
2748	<Index>0</Index>
2749	<Values>0</Values>
2750	<Status>0</Status>
2751	<Unit>kmol/h</Unit>
2752	</Variables>
2753	<Variables>
2754	<Desc>T</Desc>
2755	<Index>0</Index>
2756	<Values>314.942</Values>
2757	<Status>0</Status>
2758	<Unit>K</Unit>
2759	</Variables>
2760	<Variables>
2761	<Desc>P</Desc>
2762	<Index>0</Index>
2763	<Values>5.92799</Values>
2764	<Status>0</Status>
2765	<Unit>atm</Unit>
2766	</Variables>
2767	<Variables>
2768	<Desc>h</Desc>
2769	<Index>0</Index>
2770	<Values>-20499.7</Values>
2771	<Status>0</Status>
2772	<Unit>kJ/kmol</Unit>
2773	</Variables>
2774	<Variables>
2775	<Desc>v</Desc>
2776	<Index>0</Index>
2777	<Values>0</Values>
2778	<Status>0</Status>
2779	</Variables>
2780	<Variables>
2781	<Desc>z</Desc>
2782	<Index>0</Index>
2783	<Values>0.205363</Values>
2784	<Status>0</Status>
2785	<Index>1</Index>
2786	<Values>0.18259</Values>
2787	<Status>0</Status>
2788	<Index>2</Index>
2789	<Values>0.233723</Values>
2790	<Status>0</Status>
2791	<Index>3</Index>
2792	<Values>0.176691</Values>
2793	<Status>0</Status>
2794	<Index>4</Index>
2795	<Values>0.201633</Values>
2796	<Status>0</Status>
2797	</Variables>
2798	</Block_Properties>
2799	</Base_Models>
2800	<Parameters>
2801	<Desc>PP</Desc>
2802	<Index>0</Index>
2803	<Values>PP</Values>
2804	<Status>0</Status>
2805	</Parameters>
2806	</Block_Properties>
2807	</Base_Models>
2808	</Block_Properties>
2809	</Sub_Models>
2810	<Sub_Models>
2811	<Block_Properties>
2812	<Model_File_Path>stage_separators/column</Model_File_Path>
2813	<Instance_Id>REBOILER</Instance_Id>
2814	<Model_Name>REBOILER</Model_Name>
2815	<T_Connection>0</T_Connection>
2816	<Base_Models>
2817	<Block_Properties>
2818	<Model_File_Path>stage_separators/reboiler</Model_File_Path>
2819	<Instance_Id>REBOILER</Instance_Id>
2820	<Model_Name>reboiler</Model_Name>
2821	<T_Connection>0</T_Connection>
2822	<Sub_Models>
2823	<Block_Properties>
2824	<Model_File_Path>stage_separators/reboiler</Model_File_Path>
2825	<Instance_Id>InletLiquid</Instance_Id>
2826	<Model_Name>InletLiquid</Model_Name>
2827	<T_Connection>1</T_Connection>
2828	<Base_Models>
2829	<Block_Properties>
2830	<Model_File_Path>streams</Model_File_Path>
2831	<Instance_Id>InletLiquid</Instance_Id>
2832	<Model_Name>stream</Model_Name>
2833	<T_Connection>1</T_Connection>
2834	</Block_Properties>
2835	</Base_Models>
2836	</Block_Properties>
2837	</Sub_Models>
2838	<Sub_Models>
2839	<Block_Properties>
2840	<Model_File_Path>stage_separators/reboiler</Model_File_Path>
2841	<Instance_Id>OutletLiquid</Instance_Id>
2842	<Model_Name>OutletLiquid</Model_Name>
2843	<T_Connection>2</T_Connection>
2844	<Base_Models>
2845	<Block_Properties>
2846	<Model_File_Path>streams</Model_File_Path>
2847	<Instance_Id>OutletLiquid</Instance_Id>
2848	<Model_Name>liquid_stream</Model_Name>
2849	<T_Connection>2</T_Connection>
2850	<Base_Models>
2851	<Block_Properties>
2852	<Model_File_Path>streams</Model_File_Path>
2853	<Instance_Id>OutletLiquid</Instance_Id>
2854	<Model_Name>stream</Model_Name>
2855	<T_Connection>2</T_Connection>
2856	<Variables>
2857	<Desc>F</Desc>
2858	<Index>0</Index>
2859	<Values>28.4</Values>
2860	<Status>1</Status>
2861	<Unit>kmol/h</Unit>
2862	</Variables>
2863	</Block_Properties>
2864	</Base_Models>
2865	<Parameters>
2866	<Desc>PP</Desc>
2867	<Index>0</Index>
2868	<Values>PP</Values>
2869	<Status>0</Status>
2870	</Parameters>
2871	</Block_Properties>
2872	</Base_Models>
2873	</Block_Properties>
2874	</Sub_Models>
2875	<Sub_Models>
2876	<Block_Properties>
2877	<Model_File_Path>stage_separators/reboiler</Model_File_Path>
2878	<Instance_Id>OutletVapour</Instance_Id>
2879	<Model_Name>OutletVapour</Model_Name>
2880	<T_Connection>2</T_Connection>
2881	<Base_Models>
2882	<Block_Properties>
2883	<Model_File_Path>streams</Model_File_Path>
2884	<Instance_Id>OutletVapour</Instance_Id>
2885	<Model_Name>vapour_stream</Model_Name>
2886	<T_Connection>2</T_Connection>
2887	<Base_Models>
2888	<Block_Properties>
2889	<Model_File_Path>streams</Model_File_Path>
2890	<Instance_Id>OutletVapour</Instance_Id>
2891	<Model_Name>stream</Model_Name>
2892	<T_Connection>2</T_Connection>
2893	</Block_Properties>
2894	</Base_Models>
2895	<Parameters>
2896	<Desc>PP</Desc>
2897	<Index>0</Index>
2898	<Values>PP</Values>
2899	<Status>0</Status>
2900	</Parameters>
2901	</Block_Properties>
2902	</Base_Models>
2903	</Block_Properties>
2904	</Sub_Models>
2905	<Parameters>
2906	<Desc>PP</Desc>
2907	<Index>0</Index>
2908	<Values>PP</Values>
2909	<Status>0</Status>
2910	</Parameters>
2911	<Parameters>
2912	<Desc>NComp</Desc>
2913	<Index>0</Index>
2914	<Values>5</Values>
2915	<Status>0</Status>
2916	</Parameters>
2917	<Parameters>
2918	<Desc>Across</Desc>
2919	<Index>0</Index>
2920	<Values>1</Values>
2921	<Status>4</Status>
2922	<Unit>m^2</Unit>
2923	</Parameters>
2924	<Parameters>
2925	<Desc>V</Desc>
2926	<Index>0</Index>
2927	<Values>2</Values>
2928	<Status>4</Status>
2929	<Unit>m^3</Unit>
2930	</Parameters>
2931	<Parameters>
2932	<Desc>Initial_Level</Desc>
2933	<Index>0</Index>
2934	<Values>1</Values>
2935	<Status>0</Status>
2936	<Unit>m</Unit>
2937	</Parameters>
2938	<Parameters>
2939	<Desc>Initial_Temperature</Desc>
2940	<Index>0</Index>
2941	<Values>300</Values>
2942	<Status>0</Status>
2943	<Unit>K</Unit>
2944	</Parameters>
2945	<Parameters>
2946	<Desc>Initial_Composition</Desc>
2947	<Index>0</Index>
2948	<Values>0.5</Values>
2949	<Status>0</Status>
2950	<Index>1</Index>
2951	<Values>0.5</Values>
2952	<Status>0</Status>
2953	<Index>2</Index>
2954	<Values>0.5</Values>
2955	<Status>0</Status>
2956	<Index>3</Index>
2957	<Values>0.5</Values>
2958	<Status>0</Status>
2959	<Index>4</Index>
2960	<Values>0.5</Values>
2961	<Status>0</Status>
2962	</Parameters>
2963	<Variables>
2964	<Desc>InletQ</Desc>
2965	<Index>0</Index>
2966	<Values>1047.22</Values>
2967	<Status>0</Status>
2968	<Unit>kW</Unit>
2969	</Variables>
2970	<Variables>
2971	<Desc>M</Desc>
2972	<Index>0</Index>
2973	<Values>2.1749</Values>
2974	<Status>0</Status>
2975	<Unit>kmol</Unit>
2976	<Index>1</Index>
2977	<Values>2.14865</Values>
2978	<Status>0</Status>
2979	<Unit>kmol</Unit>
2980	<Index>2</Index>
2981	<Values>2.23447</Values>
2982	<Status>0</Status>
2983	<Unit>kmol</Unit>
2984	<Index>3</Index>
2985	<Values>2.14331</Values>
2986	<Status>0</Status>
2987	<Unit>kmol</Unit>
2988	<Index>4</Index>
2989	<Values>2.16993</Values>
2990	<Status>0</Status>
2991	<Unit>kmol</Unit>
2992	</Variables>
2993	<Variables>
2994	<Desc>ML</Desc>
2995	<Index>0</Index>
2996	<Values>10.6784</Values>
2997	<Status>0</Status>
2998	<Unit>kmol</Unit>
2999	</Variables>
3000	<Variables>
3001	<Desc>MV</Desc>
3002	<Index>0</Index>
3003	<Values>0.192851</Values>
3004	<Status>0</Status>
3005	<Unit>kmol</Unit>
3006	</Variables>
3007	<Variables>
3008	<Desc>E</Desc>
3009	<Index>0</Index>
3010	<Values>-237105</Values>
3011	<Status>0</Status>
3012	<Unit>kJ</Unit>
3013	</Variables>
3014	<Variables>
3015	<Desc>vL</Desc>
3016	<Index>0</Index>
3017	<Values>9.40302e-05</Values>
3018	<Status>0</Status>
3019	<Unit>m^3/mol</Unit>
3020	</Variables>
3021	<Variables>
3022	<Desc>vV</Desc>
3023	<Index>0</Index>
3024	<Values>0.00516414</Values>
3025	<Status>0</Status>
3026	<Unit>m^3/mol</Unit>
3027	</Variables>
3028	<Variables>
3029	<Desc>Level</Desc>
3030	<Index>0</Index>
3031	<Values>1.00409</Values>
3032	<Status>0</Status>
3033	<Unit>m</Unit>
3034	</Variables>
3035	<Variables>
3036	<Desc>rhoV</Desc>
3037	<Index>0</Index>
3038	<Values>9.65584</Values>
3039	<Status>0</Status>
3040	<Unit>kg/m^3</Unit>
3041	</Variables>
3042	</Block_Properties>
3043	</Base_Models>
3044	</Block_Properties>
3045	</Sub_Models>
3046	<Sub_Models>
3047	<Block_Properties>
3048	<Model_File_Path>stage_separators/column</Model_File_Path>
3049	<Instance_Id>LiquidInlet</Instance_Id>
3050	<Model_Name>LiquidInlet</Model_Name>
3051	<T_Connection>1</T_Connection>
3052	<Base_Models>
3053	<Block_Properties>
3054	<Model_File_Path>streams</Model_File_Path>
3055	<Instance_Id>LiquidInlet</Instance_Id>
3056	<Model_Name>stream</Model_Name>
3057	<T_Connection>1</T_Connection>
3058	<Parameters>
3059	<Desc>NComp</Desc>
3060	<Index>0</Index>
3061	<Values>5</Values>
3062	<Status>0</Status>
3063	</Parameters>
3064	<Variables>
3065	<Desc>F</Desc>
3066	<Index>0</Index>
3067	<Values>68</Values>
3068	<Status>0</Status>
3069	<Unit>kmol/h</Unit>
3070	</Variables>
3071	<Variables>
3072	<Desc>T</Desc>
3073	<Index>0</Index>
3074	<Values>281.75</Values>
3075	<Status>0</Status>
3076	<Unit>K</Unit>
3077	</Variables>
3078	<Variables>
3079	<Desc>P</Desc>
3080	<Index>0</Index>
3081	<Values>1.48038</Values>
3082	<Status>0</Status>
3083	<Unit>atm</Unit>
3084	</Variables>
3085	<Variables>
3086	<Desc>h</Desc>
3087	<Index>0</Index>
3088	<Values>-25383.9</Values>
3089	<Status>0</Status>
3090	<Unit>kJ/kmol</Unit>
3091	</Variables>
3092	<Variables>
3093	<Desc>v</Desc>
3094	<Index>0</Index>
3095	<Values>0</Values>
3096	<Status>0</Status>
3097	</Variables>
3098	<Variables>
3099	<Desc>z</Desc>
3100	<Index>0</Index>
3101	<Values>0.2</Values>
3102	<Status>0</Status>
3103	<Index>1</Index>
3104	<Values>0.2</Values>
3105	<Status>0</Status>
3106	<Index>2</Index>
3107	<Values>0.2</Values>
3108	<Status>0</Status>
3109	<Index>3</Index>
3110	<Values>0.2</Values>
3111	<Status>0</Status>
3112	<Index>4</Index>
3113	<Values>0.2</Values>
3114	<Status>0</Status>
3115	</Variables>
3116	</Block_Properties>
3117	</Base_Models>
3118	</Block_Properties>
3119	</Sub_Models>
3120	<Sub_Models>
3121	<Block_Properties>
3122	<Model_File_Path>stage_separators/column</Model_File_Path>
3123	<Instance_Id>VapourOutlet</Instance_Id>
3124	<Model_Name>VapourOutlet</Model_Name>
3125	<T_Connection>2</T_Connection>
3126	<Base_Models>
3127	<Block_Properties>
3128	<Model_File_Path>streams</Model_File_Path>
3129	<Instance_Id>VapourOutlet</Instance_Id>
3130	<Model_Name>vapour_stream</Model_Name>
3131	<T_Connection>2</T_Connection>
3132	<Base_Models>
3133	<Block_Properties>
3134	<Model_File_Path>streams</Model_File_Path>
3135	<Instance_Id>VapourOutlet</Instance_Id>
3136	<Model_Name>stream</Model_Name>
3137	<T_Connection>2</T_Connection>
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