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Column_Distillation_Kettle_Diagram.pfd @ 838

Last change on this file since 838 was 838, checked in by gerson bicca, 14 years ago
some modifications on models
File size: 220.2 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>0.01</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	<NLASolver_Relative_Accuracy>1e-2</NLASolver_Relative_Accuracy>
25	<DAESolver_File_Index>0</DAESolver_File_Index>
26	<DAESolver_File_Text>sundials</DAESolver_File_Text>
27	<DAESolver_Relative_Accuracy>1e-2</DAESolver_Relative_Accuracy>
28	<DAESolver_Absolute_Accuracy>1e-6</DAESolver_Absolute_Accuracy>
29	<DAESolver_Evt_Accuracy>1e-2</DAESolver_Evt_Accuracy>
30	</Options>
31	<Width>2000</Width>
32	<Height>1000</Height>
33	<Grid_Spacing>20</Grid_Spacing>
34	<View>
35	<Zoom_Level>1</Zoom_Level>
36	<Show_Grid>1</Show_Grid>
37	<Snap_to_Grid>1</Snap_to_Grid>
38	<Width>921</Width>
39	<Height>486</Height>
40	<X>0</X>
41	<Y>-414</Y>
42	</View>
43	<View>
44	<Zoom_Level>1</Zoom_Level>
45	<Show_Grid>1</Show_Grid>
46	<Snap_to_Grid>1</Snap_to_Grid>
47	<Width>921</Width>
48	<Height>0</Height>
49	<X>0</X>
50	<Y>0</Y>
51	</View>
52	<Block>
53	<Type>simple_source</Type>
54	<Id_String>feed</Id_String>
55	<Image_File_Name>/home/gerson/repositorio/alsoc/biblioteca/branches/gui/eml/icon/Source.png</Image_File_Name>
56	<X>61</X>
57	<Y>415</Y>
58	<Z>0</Z>
59	<Width>68</Width>
60	<Height>30</Height>
61	<Block_Properties>
62	<Model_File_Path>streams</Model_File_Path>
63	<Instance_Id>feed</Instance_Id>
64	<Model_Name>simple_source</Model_Name>
65	<T_Connection>0</T_Connection>
66	<Sub_Models>
67	<Block_Properties>
68	<Model_File_Path>streams</Model_File_Path>
69	<Instance_Id>Outlet</Instance_Id>
70	<Model_Name>Outlet</Model_Name>
71	<T_Connection>2</T_Connection>
72	<Base_Models>
73	<Block_Properties>
74	<Model_File_Path>streams</Model_File_Path>
75	<Instance_Id>Outlet</Instance_Id>
76	<Model_Name>stream</Model_Name>
77	<T_Connection>2</T_Connection>
78	<Parameters>
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80	<Index>0</Index>
81	<Values>5</Values>
82	<Status>0</Status>
83	</Parameters>
84	<Variables>
85	<Desc>F</Desc>
86	<Index>0</Index>
87	<Values>113.4</Values>
88	<Status>0</Status>
89	<Unit>kmol/h</Unit>
90	</Variables>
91	<Variables>
92	<Desc>T</Desc>
93	<Index>0</Index>
94	<Values>291</Values>
95	<Status>0</Status>
96	<Unit>K</Unit>
97	</Variables>
98	<Variables>
99	<Desc>P</Desc>
100	<Index>0</Index>
101	<Values>1.66099</Values>
102	<Status>0</Status>
103	<Unit>atm</Unit>
104	</Variables>
105	<Variables>
106	<Desc>h</Desc>
107	<Index>0</Index>
108	<Values>-15790.9</Values>
109	<Status>0</Status>
110	<Unit>kJ/kmol</Unit>
111	</Variables>
112	<Variables>
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116	<Status>0</Status>
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131	<Status>0</Status>
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134	<Status>0</Status>
135	</Variables>
136	</Block_Properties>
137	</Base_Models>
138	</Block_Properties>
139	</Sub_Models>
140	<Parameters>
141	<Desc>PP</Desc>
142	<Index>0</Index>
143	<Values>PP</Values>
144	<Status>0</Status>
145	</Parameters>
146	<Parameters>
147	<Desc>NComp</Desc>
148	<Index>0</Index>
149	<Values>5</Values>
150	<Status>0</Status>
151	</Parameters>
152	<Parameters>
153	<Desc>M</Desc>
154	<Index>0</Index>
155	<Values>58.123</Values>
156	<Status>0</Status>
157	<Unit>kg/kmol</Unit>
158	<Index>1</Index>
159	<Values>72.1498</Values>
160	<Status>0</Status>
161	<Unit>kg/kmol</Unit>
162	<Index>2</Index>
163	<Values>42.0804</Values>
164	<Status>0</Status>
165	<Unit>kg/kmol</Unit>
166	<Index>3</Index>
167	<Values>78.1134</Values>
168	<Status>0</Status>
169	<Unit>kg/kmol</Unit>
170	<Index>4</Index>
171	<Values>56.1072</Values>
172	<Status>0</Status>
173	<Unit>kg/kmol</Unit>
174	</Parameters>
175	<Parameters>
176	<Desc>ValidPhases</Desc>
177	<Index>0</Index>
178	<Values>Vapour-Liquid</Values>
179	<Status>0</Status>
180	</Parameters>
181	<Variables>
182	<Desc>MolarComposition</Desc>
183	<Index>0</Index>
184	<Values>0.20</Values>
185	<Status>1</Status>
186	<Index>1</Index>
187	<Values>0.20</Values>
188	<Status>1</Status>
189	<Index>2</Index>
190	<Values>0.20</Values>
191	<Status>1</Status>
192	<Index>3</Index>
193	<Values>0.20</Values>
194	<Status>1</Status>
195	<Index>4</Index>
196	<Values>0.20</Values>
197	<Status>1</Status>
198	</Variables>
199	<Variables>
200	<Desc>SumOfComposition</Desc>
201	<Index>0</Index>
202	<Values>1</Values>
203	<Status>0</Status>
204	</Variables>
205	<Variables>
206	<Desc>F</Desc>
207	<Index>0</Index>
208	<Values>113.4</Values>
209	<Status>1</Status>
210	<Unit>kmol/h</Unit>
211	</Variables>
212	<Variables>
213	<Desc>T</Desc>
214	<Index>0</Index>
215	<Values>291</Values>
216	<Status>1</Status>
217	<Unit>K</Unit>
218	</Variables>
219	<Variables>
220	<Desc>T_Cdeg</Desc>
221	<Index>0</Index>
222	<Values>17.85</Values>
223	<Status>0</Status>
224	<Unit>K</Unit>
225	</Variables>
226	<Variables>
227	<Desc>P</Desc>
228	<Index>0</Index>
229	<Values>168.30</Values>
230	<Status>1</Status>
231	<Unit>kPa</Unit>
232	</Variables>
233	</Block_Properties>
234	</Block>
235	<Block>
236	<Type>Distillation_kettle_cond</Type>
237	<Id_String>Column_KC</Id_String>
238	<Image_File_Name>/home/gerson/repositorio/alsoc/biblioteca/branches/gui/eml/stage_separators/icon/DistillationKettleCond.png</Image_File_Name>
239	<X>269</X>
240	<Y>131</Y>
241	<Z>0</Z>
242	<Width>274</Width>
243	<Height>607</Height>
244	<Block_Properties>
245	<Model_File_Path>stage_separators/column</Model_File_Path>
246	<Instance_Id>Column_KC</Instance_Id>
247	<Model_Name>Distillation_kettle_cond</Model_Name>
248	<T_Connection>0</T_Connection>
249	<Base_Models>
250	<Block_Properties>
251	<Model_File_Path>stage_separators/column</Model_File_Path>
252	<Instance_Id>Column_KC</Instance_Id>
253	<Model_Name>ColumnBasic</Model_Name>
254	<T_Connection>0</T_Connection>
255	<Sub_Models>
256	<Block_Properties>
257	<Model_File_Path>stage_separators/column</Model_File_Path>
258	<Instance_Id>INITIALIZATION</Instance_Id>
259	<Model_Name>INITIALIZATION</Model_Name>
260	<T_Connection>0</T_Connection>
261	<Base_Models>
262	<Block_Properties>
263	<Model_File_Path>stage_separators/column</Model_File_Path>
264	<Instance_Id>INITIALIZATION</Instance_Id>
265	<Model_Name>InitializeSection</Model_Name>
266	<T_Connection>0</T_Connection>
267	<Parameters>
268	<Desc>NComp</Desc>
269	<Index>0</Index>
270	<Values>5</Values>
271	<Status>0</Status>
272	</Parameters>
273	<Parameters>
274	<Desc>TopTemperature</Desc>
275	<Index>0</Index>
276	<Values>329</Values>
277	<Status>4</Status>
278	<Unit>K</Unit>
279	</Parameters>
280	<Parameters>
281	<Desc>BottomTemperature</Desc>
282	<Index>0</Index>
283	<Values>330</Values>
284	<Status>4</Status>
285	<Unit>K</Unit>
286	</Parameters>
287	<Parameters>
288	<Desc>LevelFraction</Desc>
289	<Index>0</Index>
290	<Values>1</Values>
291	<Status>4</Status>
292	</Parameters>
293	<Parameters>
294	<Desc>TopComposition</Desc>
295	<Index>0</Index>
296	<Values>0.3</Values>
297	<Status>0</Status>
298	<Index>1</Index>
299	<Values>0.3</Values>
300	<Status>0</Status>
301	<Index>2</Index>
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303	<Status>0</Status>
304	<Index>3</Index>
305	<Values>0.3</Values>
306	<Status>0</Status>
307	<Index>4</Index>
308	<Values>0.3</Values>
309	<Status>0</Status>
310	</Parameters>
311	<Parameters>
312	<Desc>BottomComposition</Desc>
313	<Index>0</Index>
314	<Values>0.3</Values>
315	<Status>0</Status>
316	<Index>1</Index>
317	<Values>0.3</Values>
318	<Status>0</Status>
319	<Index>2</Index>
320	<Values>0.3</Values>
321	<Status>0</Status>
322	<Index>3</Index>
323	<Values>0.3</Values>
324	<Status>0</Status>
325	<Index>4</Index>
326	<Values>0.3</Values>
327	<Status>0</Status>
328	</Parameters>
329	</Block_Properties>
330	</Base_Models>
331	</Block_Properties>
332	</Sub_Models>
333	<Sub_Models>
334	<Block_Properties>
335	<Model_File_Path>stage_separators/column</Model_File_Path>
336	<Instance_Id>CONTROL</Instance_Id>
337	<Model_Name>CONTROL</Model_Name>
338	<T_Connection>0</T_Connection>
339	<Base_Models>
340	<Block_Properties>
341	<Model_File_Path>stage_separators/column</Model_File_Path>
342	<Instance_Id>CONTROL</Instance_Id>
343	<Model_Name>ControlSection</Model_Name>
344	<T_Connection>0</T_Connection>
345	<Parameters>
346	<Desc>NComp</Desc>
347	<Index>0</Index>
348	<Values>5</Values>
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351	<Parameters>
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357	<Parameters>
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361	<Status>0</Status>
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363	</Block_Properties>
364	</Base_Models>
365	</Block_Properties>
366	</Sub_Models>
367	<Sub_Models>
368	<Block_Properties>
369	<Model_File_Path>stage_separators/column</Model_File_Path>
370	<Instance_Id>TRAYS(1)</Instance_Id>
371	<Model_Name>TRAYS</Model_Name>
372	<T_Connection>0</T_Connection>
373	<Base_Models>
374	<Block_Properties>
375	<Model_File_Path>stage_separators/tray</Model_File_Path>
376	<Instance_Id>TRAYS(1)</Instance_Id>
377	<Model_Name>tray</Model_Name>
378	<T_Connection>0</T_Connection>
379	<Base_Models>
380	<Block_Properties>
381	<Model_File_Path>stage_separators/tray</Model_File_Path>
382	<Instance_Id>TRAYS(1)</Instance_Id>
383	<Model_Name>trayBasic</Model_Name>
384	<T_Connection>0</T_Connection>
385	<Sub_Models>
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387	<Model_File_Path>stage_separators/tray</Model_File_Path>
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4001	<Status>0</Status>
4002	</Variables>
4003	</Block_Properties>
4004	</Base_Models>
4005	<Variables>
4006	<Desc>rhoL</Desc>
4007	<Index>0</Index>
4008	<Values>626.528</Values>
4009	<Status>0</Status>
4010	<Unit>kg/m^3</Unit>
4011	</Variables>
4012	<Variables>
4013	<Desc>rhoV</Desc>
4014	<Index>0</Index>
4015	<Values>14.8882</Values>
4016	<Status>0</Status>
4017	<Unit>kg/m^3</Unit>
4018	</Variables>
4019	</Block_Properties>
4020	</Base_Models>
4021	</Block_Properties>
4022	</Sub_Models>
4023	<Sub_Models>
4024	<Block_Properties>
4025	<Model_File_Path>stage_separators/column</Model_File_Path>
4026	<Instance_Id>VapourDrawOff</Instance_Id>
4027	<Model_Name>VapourDrawOff</Model_Name>
4028	<T_Connection>2</T_Connection>
4029	<Base_Models>
4030	<Block_Properties>
4031	<Model_File_Path>streams</Model_File_Path>
4032	<Instance_Id>VapourDrawOff</Instance_Id>
4033	<Model_Name>vapour_stream</Model_Name>
4034	<T_Connection>2</T_Connection>
4035	<Base_Models>
4036	<Block_Properties>
4037	<Model_File_Path>streams</Model_File_Path>
4038	<Instance_Id>VapourDrawOff</Instance_Id>
4039	<Model_Name>stream</Model_Name>
4040	<T_Connection>2</T_Connection>
4041	<Parameters>
4042	<Desc>NComp</Desc>
4043	<Index>0</Index>
4044	<Values>5</Values>
4045	<Status>0</Status>
4046	</Parameters>
4047	<Variables>
4048	<Desc>F</Desc>
4049	<Index>0</Index>
4050	<Values>0</Values>
4051	<Status>0</Status>
4052	<Unit>kmol/h</Unit>
4053	</Variables>
4054	<Variables>
4055	<Desc>T</Desc>
4056	<Index>0</Index>
4057	<Values>322.598</Values>
4058	<Status>0</Status>
4059	<Unit>K</Unit>
4060	</Variables>
4061	<Variables>
4062	<Desc>P</Desc>
4063	<Index>0</Index>
4064	<Values>6.87948</Values>
4065	<Status>0</Status>
4066	<Unit>atm</Unit>
4067	</Variables>
4068	<Variables>
4069	<Desc>h</Desc>
4070	<Index>0</Index>
4071	<Values>929.08</Values>
4072	<Status>0</Status>
4073	<Unit>kJ/kmol</Unit>
4074	</Variables>
4075	<Variables>
4076	<Desc>v</Desc>
4077	<Index>0</Index>
4078	<Values>1</Values>
4079	<Status>0</Status>
4080	</Variables>
4081	<Variables>
4082	<Desc>z</Desc>
4083	<Index>0</Index>
4084	<Values>0.205865</Values>
4085	<Status>0</Status>
4086	<Index>1</Index>
4087	<Values>0.0512219</Values>
4088	<Status>0</Status>
4089	<Index>2</Index>
4090	<Values>0.547613</Values>
4091	<Status>0</Status>
4092	<Index>3</Index>
4093	<Values>0.0160766</Values>
4094	<Status>0</Status>
4095	<Index>4</Index>
4096	<Values>0.179224</Values>
4097	<Status>0</Status>
4098	</Variables>
4099	</Block_Properties>
4100	</Base_Models>
4101	<Parameters>
4102	<Desc>PP</Desc>
4103	<Index>0</Index>
4104	<Values>PP</Values>
4105	<Status>0</Status>
4106	</Parameters>
4107	</Block_Properties>
4108	</Base_Models>
4109	</Block_Properties>
4110	</Sub_Models>
4111	<Sub_Models>
4112	<Block_Properties>
4113	<Model_File_Path>stage_separators/column</Model_File_Path>
4114	<Instance_Id>LiquidDrawOff</Instance_Id>
4115	<Model_Name>LiquidDrawOff</Model_Name>
4116	<T_Connection>2</T_Connection>
4117	<Base_Models>
4118	<Block_Properties>
4119	<Model_File_Path>streams</Model_File_Path>
4120	<Instance_Id>LiquidDrawOff</Instance_Id>
4121	<Model_Name>liquid_stream</Model_Name>
4122	<T_Connection>2</T_Connection>
4123	<Base_Models>
4124	<Block_Properties>
4125	<Model_File_Path>streams</Model_File_Path>
4126	<Instance_Id>LiquidDrawOff</Instance_Id>
4127	<Model_Name>stream</Model_Name>
4128	<T_Connection>2</T_Connection>
4129	<Parameters>
4130	<Desc>NComp</Desc>
4131	<Index>0</Index>
4132	<Values>5</Values>
4133	<Status>0</Status>
4134	</Parameters>
4135	<Variables>
4136	<Desc>F</Desc>
4137	<Index>0</Index>
4138	<Values>0</Values>
4139	<Status>0</Status>
4140	<Unit>kmol/h</Unit>
4141	</Variables>
4142	<Variables>
4143	<Desc>T</Desc>
4144	<Index>0</Index>
4145	<Values>322.598</Values>
4146	<Status>0</Status>
4147	<Unit>K</Unit>
4148	</Variables>
4149	<Variables>
4150	<Desc>P</Desc>
4151	<Index>0</Index>
4152	<Values>6.87948</Values>
4153	<Status>0</Status>
4154	<Unit>atm</Unit>
4155	</Variables>
4156	<Variables>
4157	<Desc>h</Desc>
4158	<Index>0</Index>
4159	<Values>-19570.2</Values>
4160	<Status>0</Status>
4161	<Unit>kJ/kmol</Unit>
4162	</Variables>
4163	<Variables>
4164	<Desc>v</Desc>
4165	<Index>0</Index>
4166	<Values>0</Values>
4167	<Status>0</Status>
4168	</Variables>
4169	<Variables>
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4171	<Index>0</Index>
4172	<Values>0.204584</Values>
4173	<Status>0</Status>
4174	<Index>1</Index>
4175	<Values>0.187521</Values>
4176	<Status>0</Status>
4177	<Index>2</Index>
4178	<Values>0.223831</Values>
4179	<Status>0</Status>
4180	<Index>3</Index>
4181	<Values>0.181863</Values>
4182	<Status>0</Status>
4183	<Index>4</Index>
4184	<Values>0.202202</Values>
4185	<Status>0</Status>
4186	</Variables>
4187	</Block_Properties>
4188	</Base_Models>
4189	<Parameters>
4190	<Desc>PP</Desc>
4191	<Index>0</Index>
4192	<Values>PP</Values>
4193	<Status>0</Status>
4194	</Parameters>
4195	</Block_Properties>
4196	</Base_Models>
4197	</Block_Properties>
4198	</Sub_Models>
4199	<Parameters>
4200	<Desc>PP</Desc>
4201	<Index>0</Index>
4202	<Values>PP</Values>
4203	<Status>0</Status>
4204	</Parameters>
4205	<Parameters>
4206	<Desc>NComp</Desc>
4207	<Index>0</Index>
4208	<Values>5</Values>
4209	<Status>0</Status>
4210	</Parameters>
4211	<Parameters>
4212	<Desc>NumberOfFeeds</Desc>
4213	<Index>0</Index>
4214	<Values>1</Values>
4215	<Status>0</Status>
4216	</Parameters>
4217	<Parameters>
4218	<Desc>FeedTrayLocation</Desc>
4219	<Index>0</Index>
4220	<Values>9</Values>
4221	<Status>4</Status>
4222	<Index>1</Index>
4223	<Values>2</Values>
4224	<Status>0</Status>
4225	<Index>2</Index>
4226	<Values>2</Values>
4227	<Status>0</Status>
4228	</Parameters>
4229	<Parameters>
4230	<Desc>NumberOfTrays</Desc>
4231	<Index>0</Index>
4232	<Values>16</Values>
4233	<Status>4</Status>
4234	</Parameters>
4235	<Parameters>
4236	<Desc>LiquidSideStreamLocation</Desc>
4237	<Index>0</Index>
4238	<Values>2</Values>
4239	<Status>0</Status>
4240	</Parameters>
4241	<Parameters>
4242	<Desc>VapourSideStreamLocation</Desc>
4243	<Index>0</Index>
4244	<Values>2</Values>
4245	<Status>0</Status>
4246	</Parameters>
4247	<Parameters>
4248	<Desc>VapourFlowModel</Desc>
4249	<Index>0</Index>
4250	<Values>Reepmeyer</Values>
4251	<Status>0</Status>
4252	</Parameters>
4253	<Parameters>
4254	<Desc>LiquidFlowModel</Desc>
4255	<Index>0</Index>
4256	<Values>default</Values>
4257	<Status>0</Status>
4258	</Parameters>
4259	<Parameters>
4260	<Desc>TrayDiameter</Desc>
4261	<Index>0</Index>
4262	<Values>1.6</Values>
4263	<Status>0</Status>
4264	<Unit>m</Unit>
4265	</Parameters>
4266	<Parameters>
4267	<Desc>TraySpacing</Desc>
4268	<Index>0</Index>
4269	<Values>0.6</Values>
4270	<Status>0</Status>
4271	<Unit>m</Unit>
4272	</Parameters>
4273	<Parameters>
4274	<Desc>Fraction_HoleArea</Desc>
4275	<Index>0</Index>
4276	<Values>0.1</Values>
4277	<Status>0</Status>
4278	</Parameters>
4279	<Parameters>
4280	<Desc>Fraction_DowncomerArea</Desc>
4281	<Index>0</Index>
4282	<Values>0.2</Values>
4283	<Status>0</Status>
4284	</Parameters>
4285	<Parameters>
4286	<Desc>WeirLength</Desc>
4287	<Index>0</Index>
4288	<Values>0.53</Values>
4289	<Status>4</Status>
4290	<Unit>m</Unit>
4291	</Parameters>
4292	<Parameters>
4293	<Desc>WeirHeight</Desc>
4294	<Index>0</Index>
4295	<Values>0.038</Values>
4296	<Status>4</Status>
4297	<Unit>m</Unit>
4298	</Parameters>
4299	<Parameters>
4300	<Desc>TrayLiquidPasses</Desc>
4301	<Index>0</Index>
4302	<Values>1</Values>
4303	<Status>0</Status>
4304	</Parameters>
4305	<Parameters>
4306	<Desc>HeatSupply</Desc>
4307	<Index>0</Index>
4308	<Values>0</Values>
4309	<Status>4</Status>
4310	<Unit>kW</Unit>
4311	</Parameters>
4312	<Parameters>
4313	<Desc>AerationFraction</Desc>
4314	<Index>0</Index>
4315	<Values>1</Values>
4316	<Status>0</Status>
4317	</Parameters>
4318	<Parameters>
4319	<Desc>DryPdropCoeff</Desc>
4320	<Index>0</Index>
4321