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Column_teste_Diagram.pfd @ 693

Last change on this file since 693 was 676, checked in by gerson bicca, 15 years ago
updates in column model
File size: 199.6 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>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>595</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>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>
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>Distillation_thermosyphon_subcooling</Type>
230	<Id_String>Distillation_thermosyphon_subcooling_1</Id_String>
231	<Image_File_Name>D:\Apps\repositorio\branches\gui\eml\stage_separators\icon/DistillationThermosyphonSubcooling.png</Image_File_Name>
232	<X>248</X>
233	<Y>39</Y>
234	<Z>0</Z>
235	<Width>240</Width>
236	<Height>451.5</Height>
237	<Block_Properties>
238	<Model_File_Path>stage_separators\column</Model_File_Path>
239	<Instance_Id>Distillation_thermosyphon_subcooling_1</Instance_Id>
240	<Model_Name>Distillation_thermosyphon_subcooling</Model_Name>
241	<T_Connection>0</T_Connection>
242	<Base_Models>
243	<Block_Properties>
244	<Model_File_Path>stage_separators\column</Model_File_Path>
245	<Instance_Id>Distillation_thermosyphon_subcooling_1</Instance_Id>
246	<Model_Name>Section_ColumnBasic</Model_Name>
247	<T_Connection>0</T_Connection>
248	<Sub_Models>
249	<Block_Properties>
250	<Model_File_Path>stage_separators\column</Model_File_Path>
251	<Instance_Id>FeedTray</Instance_Id>
252	<Model_Name>FeedTray</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>FeedTray</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>113.4</Values>
270	<Status>0</Status>
271	<Unit>kmol/h</Unit>
272	</Variables>
273	<Variables>
274	<Desc>T</Desc>
275	<Index>0</Index>
276	<Values>291</Values>
277	<Status>0</Status>
278	<Unit>K</Unit>
279	</Variables>
280	<Variables>
281	<Desc>P</Desc>
282	<Index>0</Index>
283	<Values>1.66099</Values>
284	<Status>0</Status>
285	<Unit>atm</Unit>
286	</Variables>
287	<Variables>
288	<Desc>h</Desc>
289	<Index>0</Index>
290	<Values>-15790.9</Values>
291	<Status>0</Status>
292	<Unit>kJ/kmol</Unit>
293	</Variables>
294	<Variables>
295	<Desc>v</Desc>
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297	<Values>0.429005</Values>
298	<Status>0</Status>
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317	</Variables>
318	</Block_Properties>
319	</Base_Models>
320	</Block_Properties>
321	</Sub_Models>
322	<Sub_Models>
323	<Block_Properties>
324	<Model_File_Path>stage_separators\column</Model_File_Path>
325	<Instance_Id>trays(1)</Instance_Id>
326	<Model_Name>trays</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>tray</Model_Name>
333	<T_Connection>0</T_Connection>
334	<Base_Models>
335	<Block_Properties>
336	<Model_File_Path>stage_separators\tray</Model_File_Path>
337	<Instance_Id>trays(1)</Instance_Id>
338	<Model_Name>trayBasic</Model_Name>
339	<T_Connection>0</T_Connection>
340	<Sub_Models>
341	<Block_Properties>
342	<Model_File_Path>stage_separators\tray</Model_File_Path>
343	<Instance_Id>InletL</Instance_Id>
344	<Model_Name>InletL</Model_Name>
345	<T_Connection>1</T_Connection>
346	<Base_Models>
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363	<Unit>kmol/h</Unit>
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4044	<Parameters>
4045	<Desc>FeedTrayLocation</Desc>
4046	<Index>0</Index>
4047	<Values>5</Values>
4048	<Status>4</Status>
4049	</Parameters>
4050	<Parameters>
4051	<Desc>LiquidSideStreamLocation</Desc>
4052	<Index>0</Index>
4053	<Values>3</Values>
4054	<Status>4</Status>
4055	</Parameters>
4056	<Parameters>
4057	<Desc>VapourSideStreamLocation</Desc>
4058	<Index>0</Index>
4059	<Values>2</Values>
4060	<Status>0</Status>
4061	</Parameters>
4062	<Parameters>
4063	<Desc>VapourFlowModel</Desc>
4064	<Index>0</Index>
4065	<Values>Reepmeyer</Values>
4066	<Status>0</Status>
4067	</Parameters>
4068	<Parameters>
4069	<Desc>LiquidFlowModel</Desc>
4070	<Index>0</Index>
4071	<Values>default</Values>
4072	<Status>0</Status>
4073	</Parameters>
4074	<Parameters>
4075	<Desc>VolumeOfTray</Desc>
4076	<Index>0</Index>
4077	<Values>4</Values>
4078	<Status>4</Status>
4079	<Unit>ft^3</Unit>
4080	</Parameters>
4081	<Parameters>
4082	<Desc>HeatSupply</Desc>
4083	<Index>0</Index>
4084	<Values>0</Values>
4085	<Status>4</Status>
4086	<Unit>kW</Unit>
4087	</Parameters>
4088	<Parameters>
4089	<Desc>PlateArea</Desc>
4090	<Index>0</Index>
4091	<Values>3.94</Values>
4092	<Status>4</Status>
4093	<Unit>ft^2</Unit>
4094	</Parameters>
4095	<Parameters>
4096	<Desc>HolesArea</Desc>
4097	<Index>0</Index>
4098	<Values>0.394</Values>
4099	<Status>4</Status>
4100	<Unit>ft^2</Unit>
4101	</Parameters>
4102	<Parameters>
4103	<Desc>WeirLength</Desc>
4104	<Index>0</Index>
4105	<Values>20.94</Values>
4106	<Status>4</Status>
4107	<Unit>in</Unit>
4108	</Parameters>
4109	<Parameters>
4110	<Desc>WeirHeight</Desc>
4111	<Index>0</Index>
4112	<Values>0.125</Values>
4113	<Status>4</Status>
4114	<Unit>ft</Unit>
4115	</Parameters>
4116	<Parameters>
4117	<Desc>FeeheryCoeff</Desc>
4118	<Index>0</Index>
4119	<Values>1</Values>
4120	<Status>0</Status>
4121	<Unit>1/m^4</Unit>
4122	</Parameters>
4123	<Parameters>
4124	<Desc>ElgueCoeff</Desc>
4125	<Index>0</Index>
4126	<Values>1</Values>
4127	<Status>0</Status>
4128	<Unit>kg/m/mol^2</Unit>
4129	</Parameters>
4130	<Parameters>
4131	<Desc>OlsenCoeff</Desc>
4132	<Index>0</Index>
4133	<Values>1</Values>
4134	<Status>0</Status>
4135	</Parameters>
4136	<Parameters>
4137	<Desc>TrayLiquidPasses</Desc>
4138	<Index>0</Index>
4139	<Values>1</Values>
4140	<Status>0</Status>
4141	</Parameters>
4142	<Parameters>
4143	<Desc>TopTemperature</Desc>
4144	<Index>0</Index>
4145	<Values>295</Values>
4146	<Status>4</Status>
4147	<Unit>K</Unit>
4148	</Parameters>
4149	<Parameters>
4150	<Desc>TbottomTemperature</Desc>
4151	<Index>0</Index>
4152	<Values>330</Values>
4153	<Status>4</Status>
4154	<Unit>K</Unit>
4155	</Parameters>
4156	<Parameters>
4157	<Desc>LevelFraction</Desc>
4158	<Index>0</Index>
4159	<Values>0.2</Values>
4160	<Status>4</Status>
4161	</Parameters>
4162	<Parameters>
4163	<Desc>TopComposition</Desc>
4164	<Index>0</Index>
4165	<Values>0.5</Values>
4166	<Status>4</Status>
4167	<Index>1</Index>
4168	<Values>0.05</Values>
4169	<Status>4</Status>
4170	<Index>2</Index>
4171	<Values>0.01</Values>
4172	<Status>4</Status>
4173	<Index>3</Index>
4174	<Values>0.01</Values>
4175	<Status>4</Status>
4176	<Index>4</Index>
4177	<Values>0.5</Values>
4178	<Status>0</Status>
4179	</Parameters>
4180	<Parameters>
4181	<Desc>BottomComposition</Desc>
4182	<Index>0</Index>
4183	<Values>0.5</Values>
4184	<Status>4</Status>
4185	<Index>1</Index>
4186	<Values>0.05</Values>
4187	<Status>4</Status>
4188	<Index>2</Index>
4189	<Values>0.01</Values>
4190	<Status>4</Status>
4191	<Index>3</Index>
4192	<Values>0.01</Values>
4193	<Status>4</Status>
4194	<Index>4</Index>
4195	<Values>0.5</Values>
4196	<Status>0</Status>
4197	</Parameters>
4198	<Parameters>
4199	<Desc>beta</Desc>
4200	<Index>0</Index>
4201	<Values>0.6</Values>
4202	<Status>4</Status>
4203	</Parameters>
4204	<Parameters>
4205	<Desc>alfa</Desc>
4206	<Index>0</Index>
4207	<Values>4</Values>
4208	<Status>4</Status>
4209	</Parameters>
4210	<Variables>
4211	<Desc>VapourDrawOffFlow</Desc>
4212	<Index>0</Index>
4213	<Values>1</Values>
4214	<Status>1</Status>
4215	<Unit>kmol/h</Unit>
4216	</Variables>
4217	<Variables>
4218	<Desc>LiquidDrawOffFlow</Desc>
4219	<Index>0</Index>
4220	<Values>1</Values>
4221	<Status>1</Status>
4222	<Unit>kmol/h</Unit>
4223	</Variables>
4224	<Variables>
4225	<Desc>MurphreeEff</Desc>
4226	<Index>0</Index>
4227	<Values>1</Values>
4228	<Status>1</Status>
4229	</Variables>
4230	</Block_Properties>
4231	</Base_Models>
4232	<Sub_Models>
4233	<Block_Properties>
4234	<Model_File_Path>stage_separators\column</Model_File_Path>
4235	<Instance_Id>VapourDrawOff</Instance_Id>
4236	<Model_Name>VapourDrawOff</Model_Name>
4237	<T_Connection>2</T_Connection>
4238	<Base_Models>
4239	<Block_Properties>
4240	<Model_File_Path>streams</Model_File_Path>
4241	<Instance_Id>VapourDrawOff</Instance_Id>
4242	<Model_Name>vapour_stream</Model_Name>
4243	<T_Connection>2</T_Connection>
4244	<Base_Models>
4245	<Block_Properties>
4246	<Model_File_Path>streams</Model_File_Path>
4247	<Instance_Id>VapourDrawOff</Instance_Id>
4248	<Model_Name>stream</Model_Name>
4249	<T_Connection>2</T_Connection>
4250	<Parameters>
4251	<Desc>NComp</Desc>
4252	<Index>0</Index>
4253	<Values>5</Values>
4254	<Status>0</Status>
4255	</Parameters>
4256	<Variables>
4257	<Desc>F</Desc>
4258	<Index>0</Index>
4259	<Values>1</Values>
4260	<Status>0</Status>
4261	<Unit>kmol/h</Unit>
4262	</Variables>
4263	<Variables>
4264	<Desc>T</Desc>
4265	<Index>0</Index>
4266	<Values>300</Values>
4267	<Status>0</Status>
4268	<Unit>K</Unit>
4269	</Variables>
4270	<Variables>
4271	<Desc>P</Desc>
4272	<Index>0</Index>
4273	<Values>3.31662</Values>
4274	<Status>0</Status>
4275	<Unit>atm</Unit>
4276	</Variables>
4277	<Variables>
4278	<Desc>h</Desc>
4279	<Index>0</Index>
4280	<Values>-594.877</Values>
4281	<Status>0</Status>
4282	<Unit>kJ/kmol</Unit>
4283	</Variables>
4284	<Variables>
4285	<Desc>v</Desc>
4286	<Index>0</Index>
4287	<Values>1</Values>
4288	<Status>0</Status>
4289	</Variables>
4290	<Variables>
4291	<Desc>z</Desc>
4292	<Index>0</Index>
4293	<Values>0.542699</Values>
4294	<Status>0</Status>
4295	<Index>1</Index>
4296	<Values>0.0124123</Values>
4297	<Status>0</Status>
4298	<Index>2</Index>
4299	<Values>0.0305563</Values>
4300	<Status>0</Status>
4301	<Index>3</Index>
4302	<Values>0.00079801</Values>
4303	<Status>0</Status>
4304	<Index>4</Index>
4305	<Values>0.413534</Values>
4306	<Status>0</Status>
4307	</Variables>
4308	</Block_Properties>
4309	</Base_Models>
4310	<Parameters>
4311	<Desc>PP</Desc>
4312	<Index>0</Index>
4313	<Values>PP</Values>
4314	<Status>0</Status>
4315	</Parameters>
4316	</Block_Properties>
4317	</Base_Models>
4318	</Block_Properties>
4319	</Sub_Models>
4320	<Sub_Models>
4321	<Block_Properties>
4322	<Model_File_Path>stage_separators\column</Model_File_Path>
4323	<Instance_Id>LiquidDrawOff</Instance_Id>
4324	<Model_Name>LiquidDrawOff</Model_Name>
4325	<T_Connection>2</T_Connection>
4326	<Base_Models>
4327	<Block_Properties>
4328	<Model_File_Path>streams</Model_File_Path>
4329	<Instance_Id>LiquidDrawOff</Instance_Id>
4330	<Model_Name>liquid_stream</Model_Name>
4331	<T_Connection>2</T_Connection>
4332	<Base_Models>
4333	<Block_Properties>
4334	<Model_File_Path>streams</Model_File_Path>
4335	<Instance_Id>LiquidDrawOff</Instance_Id>
4336	<Model_Name>stream</Model_Name>
4337	<T_Connection>2</T_Connection>
4338	<Parameters>
4339	<Desc>NComp</Desc>
4340	<Index>0</Index>
4341	<Values>5</Values>
4342	<Status>0</Status>
4343	</Parameters>
4344	<Variables>
4345	<Desc>F</Desc>
4346	<Index>0</Index>
4347	<Values>1</Values>
4348	<Status>0</Status>
4349	<Unit>kmol/h</Unit>
4350	</Variables>
4351	<Variables>
4352	<Desc>T</Desc>
4353	<Index>0</Index>
4354	<Values>305</Values>
4355	<Status>0</Status>
4356	<Unit>K</Unit>
4357	</Variables>
4358	<Variables>
4359	<Desc>P</Desc>
4360	<Index>0</Index>
4361	<Values>3.82561</Values>
4362	<Status>0</Status>
4363	<Unit>atm</U