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Column_ThermSubcoling.pfd @ 841

Last change on this file since 841 was 838, checked in by gerson bicca, 14 years ago
some modifications on models
File size: 207.0 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>propylene</Component>
6	<Component>propane</Component>
7	<Liquid_Model>PR</Liquid_Model>
8	<Vapour_Model>PR</Vapour_Model>
9	</Physical_Properties>
10	<Options>
11	<Dynamic>1</Dynamic>
12	<Time_Start>0</Time_Start>
13	<Time_Step>0.1</Time_Step>
14	<Time_End>1</Time_End>
15	<Time_Unit>h</Time_Unit>
16	<Sparse_Algebra>1</Sparse_Algebra>
17	<Integration_Index>0</Integration_Index>
18	<Integration_Text>original</Integration_Text>
19	<NLASolver_File_Index>0</NLASolver_File_Index>
20	<NLASolver_File_Text>sundials</NLASolver_File_Text>
21	<NLASolver_Relative_Accuracy>1e-2</NLASolver_Relative_Accuracy>
22	<DAESolver_File_Index>0</DAESolver_File_Index>
23	<DAESolver_File_Text>sundials</DAESolver_File_Text>
24	<DAESolver_Relative_Accuracy>1e-2</DAESolver_Relative_Accuracy>
25	<DAESolver_Absolute_Accuracy>1e-6</DAESolver_Absolute_Accuracy>
26	<DAESolver_Evt_Accuracy>1e-2</DAESolver_Evt_Accuracy>
27	</Options>
28	<Width>2000</Width>
29	<Height>1000</Height>
30	<Grid_Spacing>20</Grid_Spacing>
31	<View>
32	<Zoom_Level>1</Zoom_Level>
33	<Show_Grid>0</Show_Grid>
34	<Snap_to_Grid>0</Snap_to_Grid>
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36	<Height>486</Height>
37	<X>-326</X>
38	<Y>-529</Y>
39	</View>
40	<View>
41	<Zoom_Level>1</Zoom_Level>
42	<Show_Grid>0</Show_Grid>
43	<Snap_to_Grid>0</Snap_to_Grid>
44	<Width>921</Width>
45	<Height>0</Height>
46	<X>0</X>
47	<Y>0</Y>
48	</View>
49	<Block>
50	<Type>simple_source</Type>
51	<Id_String>feed</Id_String>
52	<Image_File_Name>/home/gerson/repositorio/alsoc/biblioteca/branches/gui/eml/icon/Source.png</Image_File_Name>
53	<X>132</X>
54	<Y>276</Y>
55	<Z>0</Z>
56	<Width>68</Width>
57	<Height>30</Height>
58	<Block_Properties>
59	<Model_File_Path>streams</Model_File_Path>
60	<Instance_Id>feed</Instance_Id>
61	<Model_Name>simple_source</Model_Name>
62	<T_Connection>0</T_Connection>
63	<Sub_Models>
64	<Block_Properties>
65	<Model_File_Path>streams</Model_File_Path>
66	<Instance_Id>Outlet</Instance_Id>
67	<Model_Name>Outlet</Model_Name>
68	<T_Connection>2</T_Connection>
69	<Base_Models>
70	<Block_Properties>
71	<Model_File_Path>streams</Model_File_Path>
72	<Instance_Id>Outlet</Instance_Id>
73	<Model_Name>stream</Model_Name>
74	<T_Connection>2</T_Connection>
75	<Parameters>
76	<Desc>NComp</Desc>
77	<Index>0</Index>
78	<Values>2</Values>
79	<Status>0</Status>
80	</Parameters>
81	<Variables>
82	<Desc>F</Desc>
83	<Index>0</Index>
84	<Values>700</Values>
85	<Status>0</Status>
86	<Unit>kmol/h</Unit>
87	</Variables>
88	<Variables>
89	<Desc>T</Desc>
90	<Index>0</Index>
91	<Values>323.15</Values>
92	<Status>0</Status>
93	<Unit>K</Unit>
94	</Variables>
95	<Variables>
96	<Desc>P</Desc>
97	<Index>0</Index>
98	<Values>20.4096</Values>
99	<Status>0</Status>
100	<Unit>atm</Unit>
101	</Variables>
102	<Variables>
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105	<Values>-12826.4</Values>
106	<Status>0</Status>
107	<Unit>kJ/kmol</Unit>
108	</Variables>
109	<Variables>
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113	<Status>0</Status>
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122	<Status>0</Status>
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124	</Block_Properties>
125	</Base_Models>
126	</Block_Properties>
127	</Sub_Models>
128	<Parameters>
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130	<Index>0</Index>
131	<Values>PP</Values>
132	<Status>0</Status>
133	</Parameters>
134	<Parameters>
135	<Desc>NComp</Desc>
136	<Index>0</Index>
137	<Values>2</Values>
138	<Status>0</Status>
139	</Parameters>
140	<Parameters>
141	<Desc>M</Desc>
142	<Index>0</Index>
143	<Values>42.0804</Values>
144	<Status>0</Status>
145	<Unit>kg/kmol</Unit>
146	<Index>1</Index>
147	<Values>44.0962</Values>
148	<Status>0</Status>
149	<Unit>kg/kmol</Unit>
150	</Parameters>
151	<Parameters>
152	<Desc>ValidPhases</Desc>
153	<Index>0</Index>
154	<Values>Vapour-Liquid</Values>
155	<Status>4</Status>
156	</Parameters>
157	<Variables>
158	<Desc>MolarComposition</Desc>
159	<Index>0</Index>
160	<Values>0.4</Values>
161	<Status>1</Status>
162	<Index>1</Index>
163	<Values>0.6</Values>
164	<Status>1</Status>
165	</Variables>
166	<Variables>
167	<Desc>SumOfComposition</Desc>
168	<Index>0</Index>
169	<Values>1</Values>
170	<Status>0</Status>
171	</Variables>
172	<Variables>
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176	<Status>1</Status>
177	<Unit>kmol/h</Unit>
178	</Variables>
179	<Variables>
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182	<Values>323.15</Values>
183	<Status>0</Status>
184	<Unit>K</Unit>
185	</Variables>
186	<Variables>
187	<Desc>T_Cdeg</Desc>
188	<Index>0</Index>
189	<Values>50</Values>
190	<Status>1</Status>
191	<Unit>K</Unit>
192	</Variables>
193	<Variables>
194	<Desc>P</Desc>
195	<Index>0</Index>
196	<Values>2068</Values>
197	<Status>1</Status>
198	<Unit>kPa</Unit>
199	</Variables>
200	</Block_Properties>
201	</Block>
202	<Block>
203	<Type>Distillation_thermosyphon_subcooling</Type>
204	<Id_String>T1</Id_String>
205	<Image_File_Name>/home/gerson/repositorio/alsoc/biblioteca/branches/gui/eml/stage_separators/icon/DistillationThermosyphonSubcooling.png</Image_File_Name>
206	<X>418</X>
207	<Y>43</Y>
208	<Z>0</Z>
209	<Width>306.5</Width>
210	<Height>664</Height>
211	<Block_Properties>
212	<Model_File_Path>stage_separators/column</Model_File_Path>
213	<Instance_Id>T1</Instance_Id>
214	<Model_Name>Distillation_thermosyphon_subcooling</Model_Name>
215	<T_Connection>0</T_Connection>
216	<Base_Models>
217	<Block_Properties>
218	<Model_File_Path>stage_separators/column</Model_File_Path>
219	<Instance_Id>T1</Instance_Id>
220	<Model_Name>ColumnBasic</Model_Name>
221	<T_Connection>0</T_Connection>
222	<Sub_Models>
223	<Block_Properties>
224	<Model_File_Path>stage_separators/column</Model_File_Path>
225	<Instance_Id>INITIALIZATION</Instance_Id>
226	<Model_Name>INITIALIZATION</Model_Name>
227	<T_Connection>0</T_Connection>
228	<Base_Models>
229	<Block_Properties>
230	<Model_File_Path>stage_separators/column</Model_File_Path>
231	<Instance_Id>INITIALIZATION</Instance_Id>
232	<Model_Name>InitializeSection</Model_Name>
233	<T_Connection>0</T_Connection>
234	<Parameters>
235	<Desc>NComp</Desc>
236	<Index>0</Index>
237	<Values>2</Values>
238	<Status>0</Status>
239	</Parameters>
240	<Parameters>
241	<Desc>TopTemperature</Desc>
242	<Index>0</Index>
243	<Values>300</Values>
244	<Status>4</Status>
245	<Unit>K</Unit>
246	</Parameters>
247	<Parameters>
248	<Desc>BottomTemperature</Desc>
249	<Index>0</Index>
250	<Values>330</Values>
251	<Status>4</Status>
252	<Unit>K</Unit>
253	</Parameters>
254	<Parameters>
255	<Desc>LevelFraction</Desc>
256	<Index>0</Index>
257	<Values>2</Values>
258	<Status>4</Status>
259	</Parameters>
260	<Parameters>
261	<Desc>TopComposition</Desc>
262	<Index>0</Index>
263	<Values>0.3</Values>
264	<Status>0</Status>
265	<Index>1</Index>
266	<Values>0.3</Values>
267	<Status>0</Status>
268	</Parameters>
269	<Parameters>
270	<Desc>BottomComposition</Desc>
271	<Index>0</Index>
272	<Values>0.3</Values>
273	<Status>0</Status>
274	<Index>1</Index>
275	<Values>0.3</Values>
276	<Status>0</Status>
277	</Parameters>
278	</Block_Properties>
279	</Base_Models>
280	</Block_Properties>
281	</Sub_Models>
282	<Sub_Models>
283	<Block_Properties>
284	<Model_File_Path>stage_separators/column</Model_File_Path>
285	<Instance_Id>CONTROL</Instance_Id>
286	<Model_Name>CONTROL</Model_Name>
287	<T_Connection>0</T_Connection>
288	<Base_Models>
289	<Block_Properties>
290	<Model_File_Path>stage_separators/column</Model_File_Path>
291	<Instance_Id>CONTROL</Instance_Id>
292	<Model_Name>ControlSection</Model_Name>
293	<T_Connection>0</T_Connection>
294	<Parameters>
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296	<Index>0</Index>
297	<Values>2</Values>
298	<Status>0</Status>
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300	<Parameters>
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306	<Parameters>
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309	<Values>1</Values>
310	<Status>0</Status>
311	</Parameters>
312	</Block_Properties>
313	</Base_Models>
314	</Block_Properties>
315	</Sub_Models>
316	<Sub_Models>
317	<Block_Properties>
318	<Model_File_Path>stage_separators/column</Model_File_Path>
319	<Instance_Id>TRAYS(1)</Instance_Id>
320	<Model_Name>TRAYS</Model_Name>
321	<T_Connection>0</T_Connection>
322	<Base_Models>
323	<Block_Properties>
324	<Model_File_Path>stage_separators/tray</Model_File_Path>
325	<Instance_Id>TRAYS(1)</Instance_Id>
326	<Model_Name>tray</Model_Name>
327	<T_Connection>0</T_Connection>
328	<Base_Models>
329	<Block_Properties>
330	<Model_File_Path>stage_separators/tray</Model_File_Path>
331	<Instance_Id>TRAYS(1)</Instance_Id>
332	<Model_Name>trayBasic</Model_Name>
333	<T_Connection>0</T_Connection>
334	<Sub_Models>
335	<Block_Properties>
336	<Model_File_Path>stage_separators/tray</Model_File_Path>
337	<Instance_Id>InletLiquid</Instance_Id>
338	<Model_Name>InletLiquid</Model_Name>
339	<T_Connection>1</T_Connection>
340	<Base_Models>
341	<Block_Properties>
342	<Model_File_Path>streams</Model_File_Path>
343	<Instance_Id>InletLiquid</Instance_Id>
344	<Model_Name>stream</Model_Name>
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346	<Parameters>
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357	<Unit>kmol/h</Unit>
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3376	<Index>0</Index>
3377	<Values>321.094</Values>
3378	<Status>0</Status>
3379	<Unit>K</Unit>
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3384	<Values>17.7904</Values>
3385	<Status>0</Status>
3386	<Unit>atm</Unit>
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3390	<Index>0</Index>
3391	<Values>-667.692</Values>
3392	<Status>0</Status>
3393	<Unit>kJ/kmol</Unit>
3394	</Variables>
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3398	<Values>1</Values>
3399	<Status>0</Status>
3400	</Variables>
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3404	<Values>0.529689</Values>
3405	<Status>0</Status>
3406	<Index>1</Index>
3407	<Values>0.470311</Values>
3408	<Status>0</Status>
3409	</Variables>
3410	</Block_Properties>
3411	</Base_Models>
3412	<Parameters>
3413	<Desc>PP</Desc>
3414	<Index>0</Index>
3415	<Values>PP</Values>
3416	<Status>0</Status>
3417	</Parameters>
3418	</Block_Properties>
3419	</Base_Models>
3420	</Block_Properties>
3421	</Sub_Models>
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3423	<Desc>PP</Desc>
3424	<Index>0</Index>
3425	<Values>PP</Values>
3426	<Status>0</Status>
3427	</Parameters>
3428	<Parameters>
3429	<Desc>NComp</Desc>
3430	<Index>0</Index>
3431	<Values>2</Values>
3432	<Status>0</Status>
3433	</Parameters>
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3435	<Desc>M</Desc>
3436	<Index>0</Index>
3437	<Values>0.747247</Values>
3438	<Status>0</Status>
3439	<Unit>kmol</Unit>
3440	<Index>1</Index>
3441	<Values>0.681871</Values>
3442	<Status>0</Status>
3443	<Unit>kmol</Unit>
3444	</Variables>
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3447	<Index>0</Index>
3448	<Values>0.328123</Values>
3449	<Status>0</Status>
3450	<Unit>kmol</Unit>
3451	</Variables>
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3454	<Index>0</Index>
3455	<Values>1.10099</Values>
3456	<Status>0</Status>
3457	<Unit>kmol</Unit>
3458	</Variables>
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3462	<Values>-7190.56</Values>
3463	<Status>0</Status>
3464	<Unit>kJ</Unit>
3465	</Variables>
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3468	<Index>0</Index>
3469	<Values>9.33852e-05</Values>
3470	<Status>0</Status>
3471	<Unit>m^3/mol</Unit>
3472	</Variables>
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3475	<Index>0</Index>
3476	<Values>0.00106788</Values>
3477	<Status>0</Status>
3478	<Unit>m^3/mol</Unit>
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3483	<Values>0.01905</Values>
3484	<Status>0</Status>
3485	<Unit>m</Unit>
3486	</Variables>
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3490	<Values>0.529689</Values>
3491	<Status>0</Status>
3492	<Index>1</Index>
3493	<Values>0.470311</Values>
3494	<Status>0</Status>
3495	</Variables>
3496	</Block_Properties>
3497	</Base_Models>
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3500	<Index>0</Index>
3501	<Values>461.404</Values>
3502	<Status>0</Status>
3503	<Unit>kg/m^3</Unit>
3504	</Variables>
3505	<Variables>
3506	<Desc>rhoV</Desc>
3507	<Index>0</Index>
3508	<Values>40.453</Values>
3509	<Status>0</Status>
3510	<Unit>kg/m^3</Unit>
3511	</Variables>
3512	</Block_Properties>
3513	</Base_Models>
3514	</Block_Properties>
3515	</Sub_Models>
3516	<Sub_Models>
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3518	<Model_File_Path>stage_separators/column</Model_File_Path>
3519	<Instance_Id>VapourDrawOff</Instance_Id>
3520	<Model_Name>VapourDrawOff</Model_Name>
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3522	<Base_Models>
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3524	<Model_File_Path>streams</Model_File_Path>
3525	<Instance_Id>VapourDrawOff</Instance_Id>
3526	<Model_Name>vapour_stream</Model_Name>
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3530	<Model_File_Path>streams</Model_File_Path>
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3538	<Status>0</Status>
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3543	<Values>0</Values>
3544	<Status>0</Status>
3545	<Unit>kmol/h</Unit>
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3550	<Values>320.156</Values>
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3552	<Unit>K</Unit>
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3557	<Values>17.4276</Values>
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3559	<Unit>atm</Unit>
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3564	<Values>-691.518</Values>
3565	<Status>0</Status>
3566	<Unit>kJ/kmol</Unit>
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3580	<Values>0.469983</Values>
3581	<Status>0</Status>
3582	</Variables>
3583	</Block_Properties>
3584	</Base_Models>
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3586	<Desc>PP</Desc>
3587	<Index>0</Index>
3588	<Values>PP</Values>
3589	<Status>0</Status>
3590	</Parameters>
3591	</Block_Properties>
3592	</Base_Models>
3593	</Block_Properties>
3594	</Sub_Models>
3595	<Sub_Models>
3596	<Block_Properties>
3597	<Model_File_Path>stage_separators/column</Model_File_Path>
3598	<Instance_Id>LiquidDrawOff</Instance_Id>
3599	<Model_Name>LiquidDrawOff</Model_Name>
3600	<T_Connection>2</T_Connection>
3601	<Base_Models>
3602	<Block_Properties>
3603	<Model_File_Path>streams</Model_File_Path>
3604	<Instance_Id>LiquidDrawOff</Instance_Id>
3605	<Model_Name>liquid_stream</Model_Name>
3606	<T_Connection>2</T_Connection>
3607	<Base_Models>
3608	<Block_Properties>
3609	<Model_File_Path>streams</Model_File_Path>
3610	<Instance_Id>LiquidDrawOff</Instance_Id>
3611	<Model_Name>stream</Model_Name>
3612	<T_Connection>2</T_Connection>
3613	<Parameters>
3614	<Desc>NComp</Desc>
3615	<Index>0</Index>
3616	<Values>2</Values>
3617	<Status>0</Status>
3618	</Parameters>
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3621	<Index>0</Index>
3622	<Values>0</Values>
3623	<Status>0</Status>
3624	<Unit>kmol/h</Unit>
3625	</Variables>
3626	<Variables>
3627	<Desc>T</Desc>
3628	<Index>0</Index>
3629	<Values>320.156</Values>
3630	<Status>0</Status>
3631	<Unit>K</Unit>
3632	</Variables>
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3634	<Desc>P</Desc>
3635	<Index>0</Index>
3636	<Values>17.4276</Values>
3637	<Status>0</Status>
3638	<Unit>atm</Unit>
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3642	<Index>0</Index>
3643	<Values>-13175.3</Values>
3644	<Status>0</Status>
3645	<Unit>kJ/kmol</Unit>
3646	</Variables>
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3650	<Values>0</Values>
3651	<Status>0</Status>
3652	</Variables>
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3654	<Desc>z</Desc>
3655	<Index>0</Index>
3656	<Values>0.5</Values>
3657	<Status>0</Status>
3658	<Index>1</Index>
3659	<Values>0.5</Values>
3660	<Status>0</Status>
3661	</Variables>
3662	</Block_Properties>
3663	</Base_Models>
3664	<Parameters>
3665	<Desc>PP</Desc>
3666	<Index>0</Index>
3667	<Values>PP</Values>
3668	<Status>0</Status>
3669	</Parameters>
3670	</Block_Properties>
3671	</Base_Models>
3672	</Block_Properties>
3673	</Sub_Models>
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3675	<Desc>PP</Desc>
3676	<Index>0</Index>
3677	<Values>PP</Values>
3678	<Status>0</Status>
3679	</Parameters>
3680	<Parameters>
3681	<Desc>NComp</Desc>
3682	<Index>0</Index>
3683	<Values>2</Values>
3684	<Status>0</Status>
3685	</Parameters>
3686	<Parameters>
3687	<Desc>NumberOfFeeds</Desc>
3688	<Index>0</Index>
3689	<Values>1</Values>
3690	<Status>0</Status>
3691	</Parameters>
3692	<Parameters>
3693	<Desc>FeedTrayLocation</Desc>
3694	<Index>0</Index>
3695	<Values>19</Values>
3696	<Status>4</Status>
3697	<Index>1</Index>
3698	<Values>2</Values>
3699	<Status>0</Status>
3700	<Index>2</Index>
3701	<Values>2</Values>
3702	<Status>0</Status>
3703	</Parameters>
3704	<Parameters>
3705	<Desc>NumberOfTrays</Desc>
3706	<Index>0</Index>
3707	<Values>33</Values>
3708	<Status>4</Status>
3709	</Parameters>
3710	<Parameters>
3711	<Desc>LiquidSideStreamLocation</Desc>
3712	<Index>0</Index>
3713	<Values>2</Values>
3714	<Status>0</Status>
3715	</Parameters>
3716	<Parameters>
3717	<Desc>VapourSideStreamLocation</Desc>
3718	<Index>0</Index>
3719	<Values>2</Values>
3720	<Status>0</Status>
3721	</Parameters>
3722	<Parameters>
3723	<Desc>VapourFlowModel</Desc>
3724	<Index>0</Index>
3725	<Values>Reepmeyer</Values>
3726	<Status>0</Status>
3727	</Parameters>
3728	<Parameters>
3729	<Desc>LiquidFlowModel</Desc>
3730	<Index>0</Index>
3731	<Values>default</Values>
3732	<Status>0</Status>
3733	</Parameters>
3734	<Parameters>
3735	<Desc>TrayDiameter</Desc>
3736	<Index>0</Index>
3737	<Values>1.6</Values>
3738	<Status>0</Status>
3739	<Unit>m</Unit>
3740	</Parameters>
3741	<Parameters>
3742	<Desc>TraySpacing</Desc>
3743	<Index>0</Index>
3744	<Values>0.6</Values>
3745	<Status>0</Status>
3746	<Unit>m</Unit>
3747	</Parameters>
3748	<Parameters>
3749	<Desc>Fraction_HoleArea</Desc>
3750	<Index>0</Index>
3751	<Values>0.1</Values>
3752	<Status>0</Status>
3753	</Parameters>
3754	<Parameters>
3755	<Desc>Fraction_DowncomerArea</Desc>
3756	<Index>0</Index>
3757	<Values>0.2</Values>
3758	<Status>0</Status>
3759	</Parameters>
3760	<Parameters>
3761	<Desc>WeirLength</Desc>
3762	<Index>0</Index>
3763	<Values>20.94</Values>
3764	<Status>4</Status>
3765	<Unit>in</Unit>
3766	</Parameters>
3767	<Parameters>
3768	<Desc>WeirHeight</Desc>
3769	<Index>0</Index>
3770	<Values>0.125</Values>
3771	<Status>4</Status>
3772	<Unit>ft</Unit>
3773	</Parameters>
3774	<Parameters>
3775	<Desc>TrayLiquidPasses</Desc>
3776	<Index>0</Index>
3777	<Values>1</Values>
3778	<Status>4</Status>
3779	</Parameters>
3780	<Parameters>
3781	<Desc>HeatSupply</Desc>
3782	<Index>0</Index>
3783	<Values>0</Values>
3784	<Status>4</Status>
3785	<Unit>kW</Unit>
3786	</Parameters>
3787	<Parameters>
3788	<Desc>AerationFraction</Desc>
3789	<Index>0</Index>
3790	<Values>1</Values>
3791	<Status>0</Status>
3792	</Parameters>
3793	<Parameters>
3794	<Desc>DryPdropCoeff</Desc>
3795	<Index>0</Index>
3796	<Values>0.6</Values>
3797	<Status>0</Status>
3798	</Parameters>
3799	<Parameters>
3800	<Desc>PlateArea</Desc>
3801	<Index>0</Index>
3802	<Values>3.94</Values>
3803	<Status>4</Status>
3804	<Unit>ft^2</Unit>
3805	</Parameters>
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3807	<Desc>TrayVolume</Desc>
3808	<Index>0</Index>
3809	<Values>1.20637</Values>
3810	<Status>0</Status>
3811	<Unit>m^3</Unit>
3812	</Parameters>
3813	<Parameters>
3814	<Desc>HolesArea</Desc>
3815	<Index>0</Index>
3816	<Values>0.394</Values>
3817	<Status>4</Status>
3818	<Unit>ft^2</Unit>
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3823	<Values>320</Values>
3824	<Status>0</Status>
3825	</Variables>
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3828	<Index>0</Index>
3829	<Values>17.3677</Values>
3830	<Status>0</Status>
3831	</Variables>
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3835	<Values>0</Values>
3836	<Status>1</Status>
3837	<Unit>kmol/h</Unit>
3838	</Variables>
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3842	<Values>0</Values>
3843	<Status>1</Status>
3844	<Unit>kmol/h</Unit>
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3849	<Values>1</Values>
3850	<Status>1</Status>
3851	</Variables>
3852	</Block_Properties>
3853	</Base_Models>
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3856	<Model_File_Path>stage_separators/column</Model_File_Path>
3857	<Instance_Id>CONDENSER</Instance_Id>
3858	<Model_Name>CONDENSER</Model_Name>
3859	<T_Connection>0</T_Connection>
3860	<Base_Models>
3861	<Block_Properties>
3862	<Model_File_Path>stage_separators/condenser</Model_File_Path>
3863	<Instance_Id>CONDENSER</Instance_Id>
3864	<Model_Name>condenserSteady</Model_Name>
3865	<T_Connection>0</T_Connection>
3866	<Sub_Models>
3867	<Block_Properties>
3868	<Model_File_Path>stage_separators/condenser</Model_File_Path>
3869	<Instance_Id>InletVapour</Instance_Id>
3870	<Model_Name>InletVapour</Model_Name>
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3873	<Block_Properties>
3874	<Model_File_Path>streams</Model_File_Path>
3875	<Instance_Id>InletVapour</Instance_Id>
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3882	<Status>0</Status>
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3887	<Values>127.694</Values>
3888	<Status>0</Status>
3889	<Unit>kmol/h</Unit>
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3896	<Unit>K</Unit>
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3901	<Values>17.3677</Values>
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3903	<Unit>atm</Unit>
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3908	<Values>-695.557</Values>
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3910	<Unit>kJ/kmol</Unit>
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3921	<Values>0.530072</Values>
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3924	<Values>0.469928</Values>
3925	<Status>0</Status>
3926	</Variables>
3927	</Block_Properties>
3928	</Base_Models>
3929	</Block_Properties>
3930	</Sub_Models>
3931	<Sub_Models>
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3933	<Model_File_Path>stage_separators/condenser</Model_File_Path>
3934	<Instance_Id>OutletLiquid</Instance_Id>
3935	<Model_Name>OutletLiquid</Model_Name>
3936	<T_Connection>2</T_Connection>
3937	<Base_Models>
3938	<Block_Properties>
3939	<Model_File_Path>streams</Model_File_Path>
3940	<Instance_Id>OutletLiquid</Instance_Id>
3941	<Model_Name>liquid_stream</Model_Name>
3942	<T_Connection>2</T_Connection>
3943	<Base_Models>
3944	<Block_Properties>
3945	<Model_File_Path>streams</Model_File_Path>
3946	<Instance_Id>OutletLiquid</Instance_Id>
3947	<Model_Name>stream</Model_Name>
3948	<T_Connection>2</T_Connection>
3949	<Parameters>
3950	<Desc>NComp</Desc>
3951	<Index>0</Index>
3952	<Values>2</Values>
3953	<Status>0</Status>
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3957	<Index>0</Index>
3958	<Values>127.694</Values>
3959	<Status>0</Status>
3960	<Unit>kmol/h</Unit>
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3963	<Desc>T</Desc>
3964	<Index>0</Index>
3965	<Values>309.344</Values>
3966	<Status>0</Status>
3967	<Unit>K</Unit>
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3972	<Values>16.8347</Values>
3973	<Status>0</Status>
3974	<Unit>atm</Unit>
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3977	<Desc>h</Desc>
3978	<Index>0</Index>
3979	<Values>-14609.1</Values>
3980	<Status>0</Status>
3981	<Unit>kJ/kmol</Unit>
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3984	<Desc>v</Desc>
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3986	<Values>0</Values>
3987	<Status>0</Status>
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3991	<Index>0</Index>
3992	<Values>0.530072</Values>
3993	<Status>0</Status>
3994	<Index>1</Index>
3995	<Values>0.469928</Values>
3996	<Status>0</Status>
3997	</Variables>
3998	</Block_Properties>
3999	</Base_Models>
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4002	<Index>0</Index>
4003	<Values>PP</Values>
4004	<Status>0</Status>
4005	</Parameters>
4006	</Block_Properties>
4007	</Base_Models>
4008	</Block_Properties>
4009	</Sub_Models>
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4011	<Desc>PP</Desc>
4012	<Index>0</Index>
4013	<Values>PP</Values>
4014	<Status>0</Status>
4015	</Parameters>
4016	<Parameters>
4017	<Desc>NComp</Desc>
4018	<Index>0</Index>
4019	<Values>2</Values>
4020	<Status>0</Status>
4021	</Parameters>
4022	<Parameters>
4023	<Desc>Pdrop</Desc>
4024	<Index>0</Index>
4025	<Values>54</Values>
4026	<Status>4</Status>
4027	<Unit>kPa</Unit>
4028	</Parameters>
4029	<Variables>
4030	<Desc>InletQ</Desc>
4031	<Index>0</Index>
4032	<Values>-493.52</Values>
4033	<Status>0</Status>
4034	<Unit>kW</Unit>
4035	</Variables>
4036	<Variables>
4037	<Desc>Tbubble</Desc>
4038	<Index>0</Index>
4039	<Values>318.344</Values>
4040	<Status>0</Status>
4041	<Unit>K</Unit>
4042	</Variables>
4043	<Variables>
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4045	<Index>0</Index>
4046	<Values>9</Values>
4047	<Status>1</Status>
4048	<Unit>K</Unit>
4049	</Variables>
4050	<Variables>
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4052	<Index>0</Index>
4053	<Values>309.344</Values>
4054	<Status>0</Status>
4055	</Variables>
4056	<Variables>
4057	<Desc>PI</Desc>
4058	<Index>0</Index>
4059	<Values>16.8347</Values>
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4232	<Status>0</Status>
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