25万吨年乙二醇项目初步设计(ID:2689766)
# | 文件名称 | 文件大小 |
---|---|---|
1 | 17592188512795.zip | 182.86M |
2 | 01-项目摘要.docx | 1.15M |
3 | 02-designabstract.docx | 1.12M |
4 | 03-初步设计说明书.docx | 6.69M |
5 | 04-可行性研究报告.docx | 4.27M |
6 | 05-环境影响评价.docx | 790.44K |
7 | 06-安全预评价报告.docx | 892.27K |
8 | 07-创新性说明.docx | 550.02K |
9 | 08-重大危险源物质泄漏报告.docx | 751.83K |
10 | 09-附录.docx | 20.90M |
11 | 致评委老师的一封信.doc | 27.00K |
12 | 换热网络.hch | 6.19M |
13 | 换热网络参考流程.bkp | 1.55M |
14 | 换热网络夹点分析.hch | 673.47K |
15 | 亚硝酸甲酯再生工段.bkp | 584.66K |
16 | 加氢工段.bkp | 741.50K |
17 | 工艺模拟.bkp | 376.38K |
18 | 精制工段.bkp | 527.28K |
19 | 羰化工段.bkp | 752.29K |
20 | 中间再沸器.bkp | 454.21K |
21 | 双效精馏.bkp | 508.24K |
22 | 变压精馏.bkp | 532.80K |
23 | T0205tiliuduan校核9.plc | 200.00K |
24 | T0205精馏段校核5.plc | 200.00K |
25 | T0301jingliuduan.plc | 200.00K |
26 | T0301提馏段.plc | 208.00K |
27 | T0302jingliuduan13.plc | 200.00K |
28 | T0302tiliuduan14.plc | 200.00K |
29 | T0303tiliu段29.plc | 200.00K |
30 | T0303精馏段21.plc | 200.00K |
31 | T0304tiliuduan48.plc | 200.00K |
32 | T0304精馏段31.plc | 200.00K |
33 | T0402tiliuduan36.plc | 200.00K |
34 | T0402精馏段20.plc | 200.00K |
35 | T0403jingliuduan26.plc | 200.00K |
36 | T0403提馏段49.plc | 200.00K |
37 | T102提馏段.plc | 224.00K |
38 | T102精馏段.plc | 216.00K |
39 | T103提馏段校核.plc | 200.00K |
40 | T103精馏段校核.plc | 200.00K |
41 | T201.CPS | 300B |
42 | T204提馏段.plc | 200.00K |
43 | T204精馏段.plc | 200.00K |
44 | 提馏段校核T0203.plc | 200.00K |
45 | 提馏段校核T202.plc | 200.00K |
46 | 精馏段校核T0203.plc | 200.00K |
47 | 精馏段校核T202.plc | 200.00K |
48 | cashflow.ics | 284.89K |
49 | cashflow.ict | 990.98K |
50 | CURRENCY.DAT | 8.20K |
51 | DefaultWB.xls | 20.29M |
52 | DESIGN.d01 | 52.10K |
53 | DESIGN.d02 | 10.23K |
54 | DESIGN.d03 | 72.81K |
55 | DESIGN.d04 | 16.80K |
56 | DESIGN.d05 | 36B |
57 | equip.ict | 38.15K |
58 | execsum.ics | 9.03K |
59 | execsum.ict | 7.36K |
60 | INV.d01 | 1.24K |
61 | INV.d02 | 10.55K |
62 | INV.d03 | 5.02K |
63 | INV.d04 | 4.98K |
64 | INV.d05 | 36B |
65 | ipeproc.d01 | 438B |
66 | ipeproc.d02 | 166B |
67 | ipeproc.d03 | 5.02K |
68 | ipeproc.d04 | 4.98K |
69 | ipeproc.d05 | 36B |
70 | ipeproj.d01 | 714B |
71 | ipeproj.d02 | 748B |
72 | ipeproj.d03 | 5.02K |
73 | ipeproj.d04 | 4.98K |
74 | ipeproj.d05 | 36B |
75 | IPEWB.XLS | 134.00K |
76 | IPEWB_TRA.XLS | 22.50K |
77 | IPSUNTUN.d01 | 852B |
78 | IPSUNTUN.d02 | 341B |
79 | IPSUNTUN.d03 | 5.02K |
80 | IPSUNTUN.d04 | 4.98K |
81 | IPSUNTUN.d05 | 36B |
82 | map.d01 | 1.10K |
83 | map.d02 | 7.42K |
84 | map.d03 | 5.02K |
85 | map.d04 | 20.74K |
86 | map.d05 | 36B |
87 | OP.d01 | 714B |
88 | OP.d02 | 2.37K |
89 | OP.d03 | 5.02K |
90 | OP.d04 | 4.98K |
91 | OP.d05 | 36B |
92 | PFDDIG.d01 | 438B |
93 | PFDDIG.d02 | 166B |
94 | PFDDIG.d03 | 5.02K |
95 | PFDDIG.d04 | 4.98K |
96 | PFDDIG.d05 | 36B |
97 | proc.d01 | 2.72K |
98 | proc.d02 | 1.59K |
99 | proc.d03 | 5.02K |
100 | proc.d04 | 4.98K |
101 | proc.d05 | 36B |
102 | procAZ.d01 | 990B |
103 | procAZ.d02 | 268B |
104 | procAZ.d03 | 5.02K |
105 | procAZ.d04 | 4.98K |
106 | procAZ.d05 | 36B |
107 | PROCCN.d01 | 438B |
108 | PROCCN.d02 | 166B |
109 | PROCCN.d03 | 5.02K |
110 | PROCCN.d04 | 4.98K |
111 | PROCCN.d05 | 36B |
112 | ProcessTemplateProject.KBW | 43B |
113 | PROD.d01 | 1.51K |
114 | PROD.d02 | 6.81K |
115 | PROD.d03 | 5.02K |
116 | PROD.d04 | 4.98K |
117 | PROD.d05 | 36B |
118 | ProdRes.txt | 127B |
119 | proj.d01 | 1.78K |
120 | proj.d02 | 1.29K |
121 | proj.d03 | 5.02K |
122 | proj.d04 | 4.98K |
123 | proj.d05 | 36B |
124 | projinfo.d01 | 714B |
125 | projinfo.d02 | 1.93K |
126 | projinfo.d03 | 5.02K |
127 | projinfo.d04 | 4.98K |
128 | projinfo.d05 | 36B |
129 | PROJL.d01 | 438B |
130 | PROJL.d02 | 166B |
131 | PROJL.d03 | 5.02K |
132 | PROJL.d04 | 4.98K |
133 | PROJL.d05 | 36B |
134 | projmap.d01 | 852B |
135 | projmap.d02 | 166B |
136 | projmap.d03 | 5.02K |
137 | projmap.d04 | 4.98K |
138 | projmap.d05 | 36B |
139 | PROJNAZ.d01 | 438B |
140 | PROJNAZ.d02 | 166B |
141 | PROJNAZ.d03 | 5.02K |
142 | PROJNAZ.d04 | 4.98K |
143 | PROJNAZ.d05 | 36B |
144 | PROJNBD.d01 | 438B |
145 | PROJNBD.d02 | 166B |
146 | PROJNBD.d03 | 5.02K |
147 | PROJNBD.d04 | 4.98K |
148 | PROJNBD.d05 | 36B |
149 | PROJNBG.d01 | 438B |
150 | PROJNBG.d02 | 166B |
151 | PROJNBG.d03 | 5.02K |
152 | PROJNBG.d04 | 4.98K |
153 | PROJNBG.d05 | 36B |
154 | PROJNBI.d01 | 438B |
155 | PROJNBI.d02 | 166B |
156 | PROJNBI.d03 | 5.02K |
157 | PROJNBI.d04 | 4.98K |
158 | PROJNBI.d05 | 36B |
159 | PROJNBM.d01 | 438B |
160 | PROJNBM.d02 | 166B |
161 | PROJNBM.d03 | 5.02K |
162 | PROJNBM.d04 | 4.98K |
163 | PROJNBM.d05 | 36B |
164 | PROJNBP.d01 | 438B |
165 | PROJNBP.d02 | 166B |
166 | PROJNBP.d03 | 5.02K |
167 | PROJNBP.d04 | 4.98K |
168 | PROJNBP.d05 | 36B |
169 | PROJNCN.d01 | 438B |
170 | PROJNCN.d02 | 166B |
171 | PROJNCN.d03 | 5.02K |
172 | PROJNCN.d04 | 4.98K |
173 | PROJNCN.d05 | 36B |
174 | PROJP.d01 | 438B |
175 | PROJP.d02 | 166B |
176 | PROJP.d03 | 5.02K |
177 | PROJP.d04 | 4.98K |
178 | PROJP.d05 | 36B |
179 | PROJSUM.ICS | 28.64K |
180 | projsum.ict | 232.10K |
181 | RAW.d01 | 1.51K |
182 | RAW.d02 | 6.74K |
183 | RAW.d03 | 5.02K |
184 | RAW.d04 | 4.98K |
185 | RAW.d05 | 36B |
186 | RawRes.txt | 132B |
187 | REP_GEN.d01 | 438B |
188 | REP_GEN.d02 | 166B |
189 | REP_GEN.d03 | 5.02K |
190 | REP_GEN.d04 | 4.98K |
191 | REP_GEN.d05 | 36B |
192 | RESULTS.xls | 873.50K |
193 | Scenario1.izp | 3.40M |
194 | Scenario1.szp | 10.75M |
195 | SCHD.d01 | 162B |
196 | SCHD.d02 | 77B |
197 | SCHD.d03 | 5.02K |
198 | SCHD.d04 | 4.98K |
199 | SCHD.d05 | 36B |
200 | SPECS.xls | 3.25M |
201 | STD.d01 | 9.73K |
202 | STD.d02 | 21.65K |
203 | STD.d03 | 20.97K |
204 | STD.d04 | 20.74K |
205 | STD.d05 | 36B |
206 | US_MET.KBW | 46B |
207 | US_Metric.KBW | 28B |
208 | UTILITY.d01 | 3.26K |
209 | UTILITY.d02 | 17.76K |
210 | UTILITY.d03 | 5.02K |
211 | UTILITY.d04 | 28.62K |
212 | UTILITY.d05 | 36B |
213 | cashflow.ics | 284.89K |
214 | cashflow.ict | 990.98K |
215 | CURRENCY.DAT | 8.20K |
216 | DESIGN.d01 | 52.10K |
217 | DESIGN.d02 | 10.23K |
218 | DESIGN.d03 | 72.81K |
219 | DESIGN.d04 | 16.80K |
220 | DESIGN.d05 | 36B |
221 | equip.ict | 38.15K |
222 | execsum.ics | 9.03K |
223 | execsum.ict | 7.36K |
224 | Flag.txt | 0B |
225 | INV.d01 | 1.24K |
226 | INV.d02 | 10.55K |
227 | INV.d03 | 5.02K |
228 | INV.d04 | 4.98K |
229 | INV.d05 | 36B |
230 | ipeproc.d01 | 438B |
231 | ipeproc.d02 | 166B |
232 | ipeproc.d03 | 5.02K |
233 | ipeproc.d04 | 4.98K |
234 | ipeproc.d05 | 36B |
235 | ipeproj.d01 | 714B |
236 | ipeproj.d02 | 748B |
237 | ipeproj.d03 | 5.02K |
238 | ipeproj.d04 | 4.98K |
239 | ipeproj.d05 | 36B |
240 | IPEWB.XLS | 134.00K |
241 | IPEWB_TRA.XLS | 22.50K |
242 | IPSUNTUN.d01 | 852B |
243 | IPSUNTUN.d02 | 341B |
244 | IPSUNTUN.d03 | 5.02K |
245 | IPSUNTUN.d04 | 4.98K |
246 | IPSUNTUN.d05 | 36B |
247 | map.d01 | 1.10K |
248 | map.d02 | 7.42K |
249 | map.d03 | 5.02K |
250 | map.d04 | 20.74K |
251 | map.d05 | 36B |
252 | OP.d01 | 714B |
253 | OP.d02 | 2.37K |
254 | OP.d03 | 5.02K |
255 | OP.d04 | 4.98K |
256 | OP.d05 | 36B |
257 | PFDDIG.d01 | 438B |
258 | PFDDIG.d02 | 166B |
259 | PFDDIG.d03 | 5.02K |
260 | PFDDIG.d04 | 4.98K |
261 | PFDDIG.d05 | 36B |
262 | proc.d01 | 2.72K |
263 | proc.d02 | 1.59K |
264 | proc.d03 | 5.02K |
265 | proc.d04 | 4.98K |
266 | proc.d05 | 36B |
267 | procAZ.d01 | 990B |
268 | procAZ.d02 | 268B |
269 | procAZ.d03 | 5.02K |
270 | procAZ.d04 | 4.98K |
271 | procAZ.d05 | 36B |
272 | PROCCN.d01 | 438B |
273 | PROCCN.d02 | 166B |
274 | PROCCN.d03 | 5.02K |
275 | PROCCN.d04 | 4.98K |
276 | PROCCN.d05 | 36B |
277 | ProcessTemplateProject.KBW | 43B |
278 | PROD.d01 | 1.51K |
279 | PROD.d02 | 6.81K |
280 | PROD.d03 | 5.02K |
281 | PROD.d04 | 4.98K |
282 | PROD.d05 | 36B |
283 | ProdRes.txt | 127B |
284 | proj.d01 | 1.78K |
285 | proj.d02 | 1.29K |
286 | proj.d03 | 5.02K |
287 | proj.d04 | 4.98K |
288 | proj.d05 | 36B |
289 | projinfo.d01 | 714B |
290 | projinfo.d02 | 1.93K |
291 | projinfo.d03 | 5.02K |
292 | projinfo.d04 | 4.98K |
293 | projinfo.d05 | 36B |
294 | PROJL.d01 | 438B |
295 | PROJL.d02 | 166B |
296 | PROJL.d03 | 5.02K |
297 | PROJL.d04 | 4.98K |
298 | PROJL.d05 | 36B |
299 | projmap.d01 | 852B |
300 | projmap.d02 | 166B |
301 | projmap.d03 | 5.02K |
302 | projmap.d04 | 4.98K |
303 | projmap.d05 | 36B |
304 | PROJNAZ.d01 | 438B |
305 | PROJNAZ.d02 | 166B |
306 | PROJNAZ.d03 | 5.02K |
307 | PROJNAZ.d04 | 4.98K |
308 | PROJNAZ.d05 | 36B |
309 | PROJNBD.d01 | 438B |
310 | PROJNBD.d02 | 166B |
311 | PROJNBD.d03 | 5.02K |
312 | PROJNBD.d04 | 4.98K |
313 | PROJNBD.d05 | 36B |
314 | PROJNBG.d01 | 438B |
315 | PROJNBG.d02 | 166B |
316 | PROJNBG.d03 | 5.02K |
317 | PROJNBG.d04 | 4.98K |
318 | PROJNBG.d05 | 36B |
319 | PROJNBI.d01 | 438B |
320 | PROJNBI.d02 | 166B |
321 | PROJNBI.d03 | 5.02K |
322 | PROJNBI.d04 | 4.98K |
323 | PROJNBI.d05 | 36B |
324 | PROJNBM.d01 | 438B |
325 | PROJNBM.d02 | 166B |
326 | PROJNBM.d03 | 5.02K |
327 | PROJNBM.d04 | 4.98K |
328 | PROJNBM.d05 | 36B |
329 | PROJNBP.d01 | 438B |
330 | PROJNBP.d02 | 166B |
331 | PROJNBP.d03 | 5.02K |
332 | PROJNBP.d04 | 4.98K |
333 | PROJNBP.d05 | 36B |
334 | PROJNCN.d01 | 438B |
335 | PROJNCN.d02 | 166B |
336 | PROJNCN.d03 | 5.02K |
337 | PROJNCN.d04 | 4.98K |
338 | PROJNCN.d05 | 36B |
339 | PROJP.d01 | 438B |
340 | PROJP.d02 | 166B |
341 | PROJP.d03 | 5.02K |
342 | PROJP.d04 | 4.98K |
343 | PROJP.d05 | 36B |
344 | PROJSUM.ICS | 28.64K |
345 | projsum.ict | 232.10K |
346 | RAW.d01 | 1.51K |
347 | RAW.d02 | 6.74K |
348 | RAW.d03 | 5.02K |
349 | RAW.d04 | 4.98K |
350 | RAW.d05 | 36B |
351 | RawRes.txt | 132B |
352 | REP_GEN.d01 | 438B |
353 | REP_GEN.d02 | 166B |
354 | REP_GEN.d03 | 5.02K |
355 | REP_GEN.d04 | 4.98K |
356 | REP_GEN.d05 | 36B |
357 | RESULTS.xls | 873.50K |
358 | Scenario1.izp | 1.02M |
359 | Scenario1.szp | 796.06K |
360 | SCHD.d01 | 162B |
361 | SCHD.d02 | 77B |
362 | SCHD.d03 | 5.02K |
363 | SCHD.d04 | 4.98K |
364 | SCHD.d05 | 36B |
365 | SPECS.xls | 3.25M |
366 | STD.d01 | 9.73K |
367 | STD.d02 | 21.65K |
368 | STD.d03 | 20.97K |
369 | STD.d04 | 20.74K |
370 | STD.d05 | 36B |
371 | US_MET.KBW | 46B |
372 | US_Metric.KBW | 28B |
373 | UTILITY.d01 | 3.26K |
374 | UTILITY.d02 | 17.76K |
375 | UTILITY.d03 | 5.02K |
376 | UTILITY.d04 | 28.62K |
377 | UTILITY.d05 | 36B |
378 | E101.EDR | 432.45K |
379 | E104.EDR | 503.22K |
380 | E106T102冷凝器.EDR | 497.80K |
381 | E201.EDR | 451.34K |
382 | E202.EDR | 638.47K |
383 | E203.EDR | 357.05K |
384 | E206.EDR | 371.51K |
385 | E207.EDR | 348.42K |
386 | E208.EDR | 395.01K |
387 | E210T203冷凝器.EDR | 391.74K |
388 | E211.EDR | 340.54K |
389 | E213T204冷凝器.EDR | 384.61K |
390 | E214.EDR | 338.05K |
391 | E215.EDR | 364.26K |
392 | E217T215冷凝器.EDR | 365.95K |
393 | E301.EDR | 488.22K |
394 | E302.EDR | 401.91K |
395 | E303.EDR | 531.83K |
396 | E305T301冷凝器.EDR | 506.03K |
397 | E307T302冷凝器.EDR | 481.59K |
398 | E309T303冷凝器.EDR | 355.26K |
399 | E311T304冷凝器.EDR | 364.14K |
400 | E402T402冷凝器.EDR | 506.24K |
401 | E403(T403冷凝器).EDR | 469.59K |
402 | 器设备一览表.docx | 162B |
403 | DMO加氢工段.dwg | 2.83M |
404 | 乙二醇精制工段.dwg | 226.85K |
405 | 加氢工段.dwg | 412.02K |
406 | 精制工段1.dwg | 1.84M |
407 | 羰化工段.dwg | 380.53K |
408 | 羰化提纯工段.dwg | 2.84M |
409 | 脂化工段.dwg | 288.51K |
410 | 酯化工段.dwg | 2.09M |
411 | 一氧化氮在大气中的扩散预测.rsm | 506B |
412 | 一氧化氮气体泄露量.rsm | 75B |
413 | 甲苯储罐BLEVE模型伤害范围.rsp | 396.00K |
414 | 甲苯储罐BLEVE模型伤害范围计算.rsm | 205B |
415 | 甲苯储罐典型泄漏事故模拟.rsm | 493B |
416 | 甲苯液体泄漏量.rsm | 105B |
417 | 甲苯蒸汽云爆炸模型伤害范围.rsp | 396.00K |
418 | 甲苯蒸汽云爆炸模型伤害范围计算.rsm | 160B |
419 | 甲醇储罐BLEVE模型伤害范围.rsp | 396.00K |
420 | 甲醇储罐BLEVE模型伤害范围计算.rsm | 206B |
421 | 甲醇储罐典型泄漏事故模拟.rsm | 495B |
422 | 甲醇液体泄漏量.rsm | 105B |
423 | 甲醇火球模型伤害范围.rsp | 396.00K |
424 | 甲醇蒸汽云爆炸模型伤害范围.rsp | 396.00K |
425 | 甲醇蒸汽云爆炸模型伤害范围计算.rsm | 159B |
426 | 甲醇储罐.ra2 | 23.24K |
427 | T101.cn2 | 30.20K |
428 | T102.cn2 | 30.20K |
429 | T103.cn2 | 30.20K |
430 | T202.cn2 | 30.20K |
431 | T203.cn2 | 30.20K |
432 | T204.cn2 | 30.20K |
433 | T205.cn2 | 30.20K |
434 | T301.cn2 | 30.20K |
435 | T302.cn2 | 30.20K |
436 | T303.cn2 | 30.20K |
437 | T304.cn2 | 30.20K |
438 | T402.cn2 | 30.20K |
439 | T403.cn2 | 30.20K |
440 | E101.fx2 | 24.00K |
441 | E102.fx2 | 24.00K |
442 | E103.fx2 | 24.00K |
443 | 智能选泵.pdf | 1.53M |
444 | 总图.pdf | 111.10M |
445 | PFD2004.dwg | 397.17K |
446 | PID2004.dwg | 1.29M |
447 | R201反应器.dwg | 260.67K |
448 | 乙二醇储罐设备条件图.dwg | 134.66K |
449 | 塔设备条件图.dwg | 127.33K |
450 | 酯化工段.dwg | 1.53M |
451 | 羰化工段.dwg | 2.03M |
452 | DMO加氢工段.dwg | 1.92M |
453 | 精制工段.dwg | 1.61M |
454 | 厂区布置图(2004).dwg | 788.66K |
455 | 酯化工段.dwg | 471.16K |
456 | 酯化工段材料规格表.dwg | 126.27K |
457 | Thumbs.db | 15.00K |
458 | 羰化提纯工段.dwg | 936.79K |
459 | 羰化提纯工段材料规格表.dwg | 127.74K |
460 | DMO加氢工段.dwg | 724.11K |
461 | DMO加氢工段材料规格表.dwg | 130.55K |
462 | Thumbs.db | 4.00K |
463 | 精制工段.dwg | 350.36K |
464 | 精制工段材料规格表.dwg | 150.02K |
465 | DMO加氢工段设备图-1.png | 43.24K |
466 | DMO加氢工段设备图-2.png | 37.42K |
467 | DMO加氢工段设备图-3.png | 34.96K |
468 | 精制工段设备图-1.png | 17.21K |
469 | 精制工段设备图-2.png | 15.71K |
470 | 精制工段设备图-3.png | 28.91K |
471 | 精制工段配管图-1.png | 20.96K |
472 | 精制工段配管图-2.png | 40.31K |
473 | 羰化工段设备图-1.png | 48.40K |
474 | 羰化工段设备图-2.png | 41.62K |
475 | 羰化工段设备图-3.png | 64.08K |
476 | 羰化工段配管图-1.png | 17.50K |
477 | 羰化工段配管图-2.png | 14.96K |
478 | 羰化工段配管图-3.png | 14.55K |
479 | 酯化工段设备图-1.png | 28.16K |
480 | 酯化工段设备图-2.png | 28.44K |
481 | 酯化工段配管图-1.png | 31.58K |
482 | 酯化工段配管图-2.png | 21.18K |
此图纸下载需要520金币
立即下载
发布者
静
创作: 12900
粉丝: 6
加入时间:2025-05-27

模型信息
图纸格式:dwg,pdf
文件大小:187.25M
所需金币:520
上传时间:2025-09-30 15:56:37
是否可编辑:可修改,包括参数
版本:AutoCAD 2004
标签
图纸简介
版权说明
用户在本站上传的作品如侵犯到您的权益,请与本站管理员联系删除。用户在本站下载的原创作品,只拥有作品的使用权,著作权归原作者所有,未经合法授权,用户不得以任何形式发布、传播、复制、转售该作品。
作者其它图纸 查看更多
猜你喜欢