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Column_Rectifier_Diagram.pfd @ 698

Last change on this file since 698 was 678, checked in by gerson bicca, 15 years ago
updates in column.mso
File size: 80.4 KB

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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>100</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>0</Show_Grid>
36	<Snap_to_Grid>0</Snap_to_Grid>
37	<Width>1260</Width>
38	<Height>607</Height>
39	<X>0</X>
40	<Y>0</Y>
41	</View>
42	<View>
43	<Zoom_Level>1</Zoom_Level>
44	<Show_Grid>0</Show_Grid>
45	<Snap_to_Grid>0</Snap_to_Grid>
46	<Width>1260</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>D:\Apps\repositorio\branches\gui\eml\icon/Source.png</Image_File_Name>
55	<X>30</X>
56	<Y>252</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>
78	<Desc>NComp</Desc>
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>
113	<Index>0</Index>
114	<Values>0.429005</Values>
115	<Status>0</Status>
116	</Variables>
117	<Variables>
118	<Desc>z</Desc>
119	<Index>0</Index>
120	<Values>0.2</Values>
121	<Status>0</Status>
122	<Index>1</Index>
123	<Values>0.2</Values>
124	<Status>0</Status>
125	<Index>2</Index>
126	<Values>0.2</Values>
127	<Status>0</Status>
128	<Index>3</Index>
129	<Values>0.2</Values>
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>
140	<Desc>PP</Desc>
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>F</Desc>
200	<Index>0</Index>
201	<Values>113.4</Values>
202	<Status>1</Status>
203	<Unit>kmol/h</Unit>
204	</Variables>
205	<Variables>
206	<Desc>T</Desc>
207	<Index>0</Index>
208	<Values>291</Values>
209	<Status>1</Status>
210	<Unit>K</Unit>
211	</Variables>
212	<Variables>
213	<Desc>T_Cdeg</Desc>
214	<Index>0</Index>
215	<Values>17.85</Values>
216	<Status>0</Status>
217	<Unit>K</Unit>
218	</Variables>
219	<Variables>
220	<Desc>P</Desc>
221	<Index>0</Index>
222	<Values>168.30</Values>
223	<Status>1</Status>
224	<Unit>kPa</Unit>
225	</Variables>
226	</Block_Properties>
227	</Block>
228	<Block>
229	<Type>reboiler</Type>
230	<Id_String>ReboilerDevice</Id_String>
231	<Image_File_Name>D:\Apps\repositorio\branches\gui\eml\stage_separators\icon/Reboiler.png</Image_File_Name>
232	<X>363</X>
233	<Y>528</Y>
234	<Z>0</Z>
235	<Width>179</Width>
236	<Height>55</Height>
237	<Block_Properties>
238	<Model_File_Path>stage_separators\reboiler</Model_File_Path>
239	<Instance_Id>ReboilerDevice</Instance_Id>
240	<Model_Name>reboiler</Model_Name>
241	<T_Connection>0</T_Connection>
242	<Sub_Models>
243	<Block_Properties>
244	<Model_File_Path>stage_separators\reboiler</Model_File_Path>
245	<Instance_Id>Inlet</Instance_Id>
246	<Model_Name>Inlet</Model_Name>
247	<T_Connection>1</T_Connection>
248	<Base_Models>
249	<Block_Properties>
250	<Model_File_Path>streams</Model_File_Path>
251	<Instance_Id>Inlet</Instance_Id>
252	<Model_Name>stream</Model_Name>
253	<T_Connection>1</T_Connection>
254	<Parameters>
255	<Desc>NComp</Desc>
256	<Index>0</Index>
257	<Values>5</Values>
258	<Status>0</Status>
259	</Parameters>
260	<Variables>
261	<Desc>F</Desc>
262	<Index>0</Index>
263	<Values>0</Values>
264	<Status>0</Status>
265	<Unit>kmol/h</Unit>
266	</Variables>
267	<Variables>
268	<Desc>T</Desc>
269	<Index>0</Index>
270	<Values>300</Values>
271	<Status>0</Status>
272	<Unit>K</Unit>
273	</Variables>
274	<Variables>
275	<Desc>P</Desc>
276	<Index>0</Index>
277	<Values>1</Values>
278	<Status>0</Status>
279	<Unit>atm</Unit>
280	</Variables>
281	<Variables>
282	<Desc>h</Desc>
283	<Index>0</Index>
284	<Values>0</Values>
285	<Status>0</Status>
286	<Unit>kJ/kmol</Unit>
287	</Variables>
288	<Variables>
289	<Desc>v</Desc>
290	<Index>0</Index>
291	<Values>0</Values>
292	<Status>0</Status>
293	</Variables>
294	<Variables>
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296	<Index>0</Index>
297	<Values>0.2</Values>
298	<Status>0</Status>
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307	<Status>0</Status>
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310	<Status>0</Status>
311	</Variables>
312	</Block_Properties>
313	</Base_Models>
314	</Block_Properties>
315	</Sub_Models>
316	<Sub_Models>
317	<Block_Properties>
318	<Model_File_Path>stage_separators\reboiler</Model_File_Path>
319	<Instance_Id>InletL</Instance_Id>
320	<Model_Name>InletL</Model_Name>
321	<T_Connection>1</T_Connection>
322	<Base_Models>
323	<Block_Properties>
324	<Model_File_Path>streams</Model_File_Path>
325	<Instance_Id>InletL</Instance_Id>
326	<Model_Name>stream</Model_Name>
327	<T_Connection>1</T_Connection>
328	<Parameters>
329	<Desc>NComp</Desc>
330	<Index>0</Index>
331	<Values>5</Values>
332	<Status>0</Status>
333	</Parameters>
334	<Variables>
335	<Desc>F</Desc>
336	<Index>0</Index>
337	<Values>0</Values>
338	<Status>0</Status>
339	<Unit>kmol/h</Unit>
340	</Variables>
341	<Variables>
342	<Desc>T</Desc>
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344	<Values>298</Values>
345	<Status>0</Status>
346	<Unit>K</Unit>
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348	<Variables>
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352	<Status>0</Status>
353	<Unit>atm</Unit>
354	</Variables>
355	<Variables>
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358	<Values>-25225.5</Values>
359	<Status>0</Status>
360	<Unit>kJ/kmol</Unit>
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440	<Unit>kJ/kmol</Unit>
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467	</Base_Models>
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496	<Parameters>
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502	<Variables>
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506	<Status>0</Status>
507	<Unit>kmol/h</Unit>
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509	<Variables>
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512	<Values>350</Values>
513	<Status>0</Status>
514	<Unit>K</Unit>
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520	<Status>0</Status>
521	<Unit>atm</Unit>
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527	<Status>0</Status>
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563	</Base_Models>
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572	<Parameters>
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578	<Parameters>
579	<Desc>Across</Desc>
580	<Index>0</Index>
581	<Values>1</Values>
582	<Status>4</Status>
583	<Unit>m^2</Unit>
584	</Parameters>
585	<Parameters>
586	<Desc>V</Desc>
587	<Index>0</Index>
588	<Values>2</Values>
589	<Status>4</Status>
590	<Unit>m^3</Unit>
591	</Parameters>
592	<Variables>
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595	<Values>1047.22</Values>
596	<Status>0</Status>
597	<Unit>kW</Unit>
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599	<Variables>
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648	<Unit>m^3/mol</Unit>
649	</Variables>
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653	<Values>0.00400763</Values>
654	<Status>0</Status>
655	<Unit>m^3/mol</Unit>
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661	<Status>2</Status>
662	<Unit>m</Unit>
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664	<Variables>
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667	<Values>14.4692</Values>
668	<Status>0</Status>
669	<Unit>kg/m^3</Unit>
670	</Variables>
671	</Block_Properties>
672	</Block>
673	<Block>
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676	<Image_File_Name>D:\Apps\repositorio\branches\gui\eml\icon/Sink.png</Image_File_Name>
677	<X>946</X>
678	<Y>521</Y>
679	<Z>0</Z>
680	<Width>68</Width>
681	<Height>30</Height>
682	<Block_Properties>
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684	<Instance_Id>LiquidOut</Instance_Id>
685	<Model_Name>simple_sink</Model_Name>
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687	<Sub_Models>
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1428	<Model_Name>trayBasic</Model_Name>
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1472	<Model_Name>liquid_stream</Model_Name>
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1525	<Values>PP</Values>
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1593	<Instance_Id>OutletL</Instance_Id>
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1637	<Values>PP</Values>
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1759	<Values>PP</Values>
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1837	<Instance_Id>OutletL</Instance_Id>
1838	<Model_Name>liquid_stream</Model_Name>
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1851	<Values>PP</Values>
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1862	<Model_Name>OutletV</Model_Name>
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1867	<Instance_Id>OutletV</Instance_Id>
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1874	<Model_Name>stream</Model_Name>
1875	<T_Connection>2</T_Connection>
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1881	<Values>PP</Values>
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1891	<Values>PP</Values>
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1903	<Values>PP</Values>
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1909	<Values>8</Values>
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1916	<Status>4</Status>
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1921	<Values>2</Values>
1922	<Status>4</Status>
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1927	<Values>2</Values>
1928	<Status>4</Status>
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1933	<Values>Reepmeyer</Values>
1934	<Status>0</Status>
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1945	<Values>0</Values>
1946	<Status>1</Status>
1947	<Unit>kmol/h</Unit>
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1952	<Values>0</Values>
1953	<Status>1</Status>
1954	<Unit>kmol/h</Unit>
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1987	<Values>PP</Values>
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2003	<Instance_Id>LiquidDrawOff</Instance_Id>
2004	<Model_Name>liquid_stream</Model_Name>
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2061	<Instance_Id>OutletL</Instance_Id>
2062	<Model_Name>liquid_stream</Model_Name>
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2075	<Values>PP</Values>
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2105	<Unit>kmol/h</Unit>
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2128	<Values>2</Values>
2129	<Status>4</Status>
2130	<Unit>m^3</Unit>
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2135	<Values>1</Values>
2136	<Status>4</Status>
2137	<Unit>m^2</Unit>
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2142	<Values>-3.75E6</Values>
2143	<Status>1</Status>
2144	<Unit>kJ/h</Unit>
2145	</Variables>
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2515	<X1>98</X1>
2516	<Y1>267.768</Y1>
2517	<X2>194</X2>
2518	<Y2>309.75</Y2>
2519	<Block_Source>feed</Block_Source>
2520	<Port_Source>Outlet</Port_Source>
2521	<Block_Target>Rectifier_1</Block_Target>
2522	<Port_Target>FeedTray</Port_Target>
2523	</Line>
2524	<Line>
2525	<Line_Name>2</Line_Name>
2526	<X1>253.75</X1>
2527	<Y1>492</Y1>
2528	<X2>363</X2>
2529	<Y2>556.897</Y2>
2530	<Block_Source>Rectifier_1</Block_Source>
2531	<Port_Source>LiquidOutlet</Port_Source>
2532	<Block_Target>ReboilerDevice</Block_Target>
2533	<Port_Target>InletL</Port_Target>
2534	</Line>
2535	<Line>
2536	<Line_Name>3</Line_Name>
2537	<X1>453.914</X1>
2538	<Y1>528</Y1>
2539	<X2>237.02</X2>
2540	<Y2>492</Y2>
2541	<Block_Source>ReboilerDevice</Block_Source>
2542	<Port_Source>OutletV</Port_Source>
2543	<Block_Target>Rectifier_1</Block_Target>
2544	<Port_Target>VapourInlet</Port_Target>
2545	</Line>
2546	<Line>
2547	<Line_Name>7</Line_Name>
2548	<X1>433</X1>
2549	<Y1>220.65</Y1>
2550	<X2>752</X2>
2551	<Y2>117.924</Y2>
2552	<Block_Source>Rectifier_1</Block_Source>
2553	<Port_Source>LiquidDistillate</Port_Source>
2554	<Block_Target>simple_sink_1</Block_Target>
2555	<Port_Target>Inlet</Port_Target>
2556	</Line>
2557	<Line>
2558	<Line_Name>8</Line_Name>
2559	<X1>354.13</X1>
2560	<Y1>87</Y1>
2561	<X2>589</X2>
2562	<Y2>29</Y2>
2563	<Block_Source>Rectifier_1</Block_Source>
2564	<Port_Source>VapourDistillate</Port_Source>
2565	<Block_Target>simple_sink_2</Block_Target>
2566	<Port_Target>Inlet</Port_Target>
2567	</Line>
2568	</Diagram>

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