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Double_Pipe_Multitubular.rlt @ 136

Last change on this file since 136 was 136, checked in by gerson bicca, 16 years ago
solved convergence problem for multitubular heat exchanger
File size: 4.1 KB

Line
1	Double_Pipe_Multitubular
2	1 0 Double_Pipe_Multitubular
3	0
4	0
5
6	3
7	Pipe
8	0
9	1
10	Multitubular_Basic_LMTD
11	3
12	DT0
13	1 2 1 22 1 18.436
14	DTL
15	1 2 1 18.436 1 15.453
16	LMTD
17	1 2 1 20.1656 1 16.9007
18	1
19	Multitubular_Basic
20	0
21	0
22
23	1
24	Unity
25	0
26	0
27
28	7
29	Inlet
30	0
31	0
32
33	2
34	Hot
35	6
36	F
37	2 2 1 1 10 1 10
38	T
39	2 2 1 1 315 1 314.067
40	P
41	2 2 1 1 4.93462 1 4.93456
42	z
43	2 2 2 1 1 1 0 1 1 1 0
44	h
45	2 2 1 1 -38699.2 1 -38806.2
46	v
47	2 2 1 1 0 1 0
48	0
49
50	0
51	Cold
52	6
53	F
54	2 2 1 1 5 1 5
55	T
56	2 2 1 1 293 1 295.631
57	P
58	2 2 1 1 4.93462 1 4.93461
59	z
60	2 2 2 1 0 1 1 1 0 1 1
61	h
62	2 2 1 1 -46183.2 1 -45969.4
63	v
64	2 2 1 1 0 1 0
65	0
66
67	0
68	Outlet
69	0
70	0
71
72	2
73	Hot
74	0
75	1
76	stream
77	6
78	F
79	2 2 1 1 10 1 10
80	T
81	2 2 1 1 314.067 1 313.285
82	P
83	2 2 1 1 4.93456 1 4.9345
84	z
85	2 2 2 1 1 1 0 1 1 1 0
86	h
87	2 2 1 1 -38806.2 1 -38895.6
88	v
89	2 2 1 1 0 1 0
90	0
91
92	0
93
94	0
95	Cold
96	0
97	1
98	stream
99	6
100	F
101	2 2 1 1 5 1 5
102	T
103	2 2 1 1 295.631 1 297.832
104	P
105	2 2 1 1 4.93461 1 4.93461
106	z
107	2 2 2 1 0 1 1 1 0 1 1
108	h
109	2 2 1 1 -45969.4 1 -45790.5
110	v
111	2 2 1 1 0 1 0
112	0
113
114	0
115
116	0
117	Properties
118	0
119	0
120
121	2
122	Hot
123	0
124	0
125
126	4
127	Inlet
128	5
129	Fw
130	2 2 1 1 320.42 1 320.42
131	rho
132	2 2 1 1 659.065 1 659.808
133	Mu
134	2 2 1 1 0.414062 1 0.418544
135	Cp
136	2 2 1 1 114.614 1 114.494
137	K
138	2 2 1 1 0.183362 1 0.18374
139	0
140
141	0
142	Average
143	7
144	Mw
145	2 2 1 1 32.042 1 32.042
146	T
147	2 2 1 1 314.533 1 313.676
148	P
149	2 2 1 1 4.93459 1 4.93453
150	rho
151	2 2 1 1 659.437 1 660.117
152	Mu
153	2 2 1 1 0.416293 1 0.420445
154	Cp
155	2 2 1 1 114.554 1 114.445
156	K
157	2 2 1 1 0.183551 1 0.183898
158	0
159
160	0
161	Outlet
162	5
163	Fw
164	2 2 1 1 320.42 1 320.42
165	rho
166	2 2 1 1 659.808 1 660.426
167	Mu
168	2 2 1 1 0.418544 1 0.422361
169	Cp
170	2 2 1 1 114.494 1 114.395
171	K
172	2 2 1 1 0.18374 1 0.184057
173	0
174
175	0
176	Wall
177	4
178	Mu
179	2 2 1 1 0.47011 1 0.465555
180	Cp
181	2 2 1 1 113.347 1 113.434
182	K
183	2 2 1 1 0.187657 1 0.18734
184	Twall
185	2 2 1 1 304.424 1 305.204
186	0
187
188	0
189	Cold
190	0
191	0
192
193	4
194	Inlet
195	5
196	Fw
197	2 2 1 1 90.076 1 90.076
198	rho
199	2 2 1 1 851.284 1 849.844
200	Mu
201	2 2 1 1 0.999361 1 0.941034
202	Cp
203	2 2 1 1 81.3013 1 81.2837
204	K
205	2 2 1 1 0.60885 1 0.612809
206	0
207
208	0
209	Average
210	7
211	Mw
212	2 2 1 1 18.0152 1 18.0152
213	T
214	2 2 1 1 294.315 1 296.731
215	P
216	2 2 1 1 4.93461 1 4.93461
217	rho
218	2 2 1 1 850.565 1 849.237
219	Mu
220	2 2 1 1 0.969572 1 0.918067
221	Cp
222	2 2 1 1 81.292 1 81.2775
223	K
224	2 2 1 1 0.61084 1 0.614439
225	0
226
227	0
228	Outlet
229	5
230	Fw
231	2 2 1 1 90.076 1 90.076
232	rho
233	2 2 1 1 849.844 1 848.628
234	Mu
235	2 2 1 1 0.941034 1 0.895895
236	Cp
237	2 2 1 1 81.2837 1 81.2721
238	K
239	2 2 1 1 0.612809 1 0.616054
240	0
241
242	0
243	Wall
244	4
245	Mu
246	2 2 1 1 0.777997 1 0.765576
247	Cp
248	2 2 1 1 81.2544 1 81.2541
249	K
250	2 2 1 1 0.625404 1 0.626472
251	Twall
252	2 2 1 1 304.424 1 305.204
253	0
254
255	0
256	Details
257	10
258	A
259	2 2 1 1 0.257743 1 0.257743
260	Q
261	2 2 1 1 0.297007 1 0.248501
262	Uc
263	2 2 1 1 0.0571381 1 0.0570421
264	Ud
265	2 2 1 1 0.057144 1 0.0570478
266	Ch
267	2 2 1 1 318.205 1 317.902
268	Cc
269	2 2 1 1 112.906 1 112.885
270	Cr
271	2 2 1 1 0.35482 1 0.355095
272	Cmin
273	2 2 1 1 112.906 1 112.885
274	Cmax
275	2 2 1 1 318.205 1 317.902
276	NTU
277	2 2 1 1 0.130449 1 0.130253
278	0
279
280	0
281	Inner
282	0
283	0
284
285	2
286	HeatTransfer
287	5
288	Re
289	2 2 1 1 6657.5 1 6591.75
290	hcoeff
291	2 2 1 1 0.264631 1 0.264003
292	PR
293	2 2 1 1 8.10833 1 8.16595
294	Phi
295	2 2 1 1 0.983123 1 0.985833
296	Vmean
297	2 2 1 1 0.102783 1 0.102677
298	0
299
300	0
301	PressureDrop
302	3
303	Pdrop
304	2 2 1 1 5.84033e-005 1 5.8341e-005
305	fi
306	2 2 1 1 0.0100435 1 0.0100709
307	Re
308	2 2 1 1 6657.5 1 6591.75
309	0
310
311	0
312	Outer
313	0
314	0
315
316	2
317	HeatTransfer
318	5
319	Re
320	2 2 1 1 680.846 1 719.043
321	hcoeff
322	2 2 1 1 0.0771037 1 0.0769914
323	PR
324	2 2 1 1 7.16244 1 6.74104
325	Phi
326	2 2 1 1 1.0313 1 1.02576
327	Vmean
328	2 2 1 1 0.0100038 1 0.0100195
329	0
330
331	0
332	PressureDrop
333	3
334	Pdrop
335	2 2 1 1 5.73601e-006 1 5.46919e-006
336	fi
337	2 2 1 1 0.0614481 1 0.0581839
338	Re
339	2 2 1 1 260.382 1 274.99
340	0
341
342	0
343	Resistances
344	5
345	Rtube
346	2 2 1 1 4.45995 1 4.47056
347	Rwall
348	2 2 1 1 0.0701538 1 0.0701538
349	Rshell
350	2 2 1 1 12.9696 1 12.9885
351	Rfi
352	2 2 1 1 0 1 0
353	Rfo
354	2 2 1 1 0 1 0
355	0
356
357	0
358
359	0
360
361	0
362	streamhot
363	0
364	1
365	stream
366	6
367	F
368	1 1 1 10
369	T
370	1 1 1 315
371	P
372	1 1 1 4.93462
373	z
374	1 2 1 1 1 0
375	h
376	1 1 1 -38699.2
377	v
378	1 1 1 0
379	0
380
381	0
382
383	0
384	streamcold
385	0
386	1
387	stream
388	6
389	F
390	1 1 1 5
391	T
392	1 1 1 293
393	P
394	1 1 1 4.93462
395	z
396	1 2 1 0 1 1
397	h
398	1 1 1 -46183.2
399	v
400	1 1 1 0
401	0
402
403	0
404
405	0

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