神华宁煤年产30万吨乙二醇项目初步设计(ID:2690030)
# | 文件名称 | 文件大小 |
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1 | 1759224458397.zip | 70.04M |
2 | 0-项目摘要.doc | 301.50K |
3 | 1-可行性研究报告.doc | 6.76M |
4 | 2-初步设计说明书.doc | 21.29M |
5 | 3-创新性说明书.doc | 480.50K |
6 | 4-设备选型一览表.doc | 427.00K |
7 | 5-1附录一:物料平衡计算书.doc | 933.50K |
8 | 5-2附录二:能量平衡计算书.doc | 1.10M |
9 | 5-3附录三:能量回收的换热网络设计.doc | 679.50K |
10 | 5-4附录四:物质MSDS.doc | 892.50K |
11 | 6-经济分析.doc | 1.43M |
12 | 7-安全预评价报告.doc | 1.63M |
13 | 8-环境影响评价报告书.doc | 1.77M |
14 | PFD2004.dwg | 681.27K |
15 | PID2004.dwg | 572.96K |
16 | SIS2004.dwg | 70.62K |
17 | 厂区布置图2004.dwg | 115.05K |
18 | 板式反应器2004.dwg | 177.99K |
19 | 精馏设备2004.dwg | 233.10K |
20 | 车间设备布置图2004.bak | 479.34K |
21 | 车间设备布置图2004.dwg | 456.97K |
22 | 首页图2004.dwg | 118.56K |
23 | PFD2010.dwg | 693.01K |
24 | PID2010.dwg | 590.76K |
25 | SIS2010.dwg | 80.84K |
26 | 厂区布置图2010.dwg | 126.49K |
27 | 板式反应器2010.dwg | 190.17K |
28 | 精馏设备2010.dwg | 244.76K |
29 | 车间设备布置图2010.dwg | 472.79K |
30 | 首页图2010.dwg | 131.66K |
31 | 设计图册.pdf | 18.72M |
32 | readme.txt | 388B |
33 | 中毒.alo | 4.73K |
34 | 喷射火热辐射.alo | 4.73K |
35 | 毗邻管道的热辐射.alo | 4.73K |
36 | 蒸气云爆炸.alo | 4.73K |
37 | 闪火.alo | 4.73K |
38 | 中毒.jpg | 178.06K |
39 | 喷射火热辐射.jpg | 182.74K |
40 | 毗邻管道的热辐射.jpg | 154.91K |
41 | 蒸气云爆炸.jpg | 182.62K |
42 | 闪火.jpg | 163.00K |
43 | 1.全流程模拟(不含换热网络).bkp | 1.74M |
44 | 2.流股提取(不含热泵精馏).xlsx | 11.47K |
45 | 3.不含热泵精馏.hch | 239.78K |
46 | 4.流股提取(含热泵精馏).xlsx | 11.54K |
47 | 5.全流程模拟(含换热网络,塔优化参数代入).bkp | 2.05M |
48 | 5.含热泵精馏.hch | 7.35M |
49 | 6.全流程模拟(含换热网络,引用热流,添加设计规定).bkp | 1.84M |
50 | E0102.DOC | 343.00K |
51 | E0102.EDR | 378.03K |
52 | E0102.pdf | 507.49K |
53 | E0103.DOC | 351.00K |
54 | E0103.EDR | 465.88K |
55 | E0103.pdf | 536.62K |
56 | E0104.DOC | 344.50K |
57 | E0104.EDR | 418.90K |
58 | E0104.pdf | 513.17K |
59 | E0105.DOC | 339.00K |
60 | E0105.EDR | 377.66K |
61 | E0105.pdf | 491.03K |
62 | E0204.DOC | 340.00K |
63 | E0204.EDR | 468.23K |
64 | E0204.pdf | 500.15K |
65 | E0205.DOC | 347.00K |
66 | E0205.EDR | 453.79K |
67 | E0205.pdf | 522.93K |
68 | E0207.DOC | 368.50K |
69 | E0207.EDR | 546.34K |
70 | E0207.pdf | 612.41K |
71 | E0303.DOC | 350.50K |
72 | E0303.EDR | 470.83K |
73 | E0303.pdf | 537.33K |
74 | E0304.DOC | 357.00K |
75 | E0304.EDR | 499.73K |
76 | E0304.pdf | 566.48K |
77 | E0308.DOC | 351.50K |
78 | E0308.EDR | 476.64K |
79 | E0308.pdf | 541.98K |
80 | E0309.DOC | 347.50K |
81 | E0309.EDR | 446.42K |
82 | E0309.pdf | 523.22K |
83 | E0101.DOC | 342.00K |
84 | E0101.EDR | 346.51K |
85 | E0101.pdf | 503.28K |
86 | E0201.DOC | 340.00K |
87 | E0201.EDR | 411.56K |
88 | E0201.pdf | 493.05K |
89 | E0202.DOC | 343.50K |
90 | E0202.EDR | 378.20K |
91 | E0202.pdf | 508.52K |
92 | E0203.DOC | 339.50K |
93 | E0203.EDR | 355.85K |
94 | E0203.pdf | 491.54K |
95 | E0206.DOC | 350.00K |
96 | E0206.EDR | 456.73K |
97 | E0206.pdf | 531.47K |
98 | E0208.DOC | 342.50K |
99 | E0208.EDR | 362.07K |
100 | E0208.pdf | 502.50K |
101 | E0301.DOC | 340.00K |
102 | E0301.EDR | 381.87K |
103 | E0301.pdf | 493.02K |
104 | E0302.DOC | 341.00K |
105 | E0302.EDR | 406.55K |
106 | E0302.pdf | 498.33K |
107 | E0305.DOC | 339.00K |
108 | E0305.EDR | 375.90K |
109 | E0305.pdf | 492.43K |
110 | E0306.DOC | 343.00K |
111 | E0306.EDR | 409.97K |
112 | E0306.pdf | 505.12K |
113 | E0307.DOC | 342.00K |
114 | E0307.EDR | 353.67K |
115 | E0307.pdf | 503.75K |
116 | E0310.DOC | 349.50K |
117 | E0310.EDR | 528.16K |
118 | E0310.pdf | 521.38K |
119 | E0311.DOC | 356.50K |
120 | E0311.EDR | 479.77K |
121 | E0311.pdf | 558.91K |
122 | E0312.DOC | 342.50K |
123 | E0312.EDR | 424.74K |
124 | E0312.pdf | 503.43K |
125 | E0313.DOC | 348.00K |
126 | E0313.EDR | 438.29K |
127 | E0313.pdf | 523.99K |
128 | E0314.DOC | 347.00K |
129 | E0314.EDR | 393.62K |
130 | E0314.pdf | 519.52K |
131 | 1.全流程模拟(不含换热网络,添加设计规定).bkp | 1.74M |
132 | 2.全流程模拟(含换热网络,引用热流,添加设计规定).bkp | 1.84M |
133 | 3.全流程模拟(含换热网络,塔优化参数代入).bkp | 2.05M |
134 | R0101-压力.bkp | 413.86K |
135 | R0101-温度.bkp | 423.98K |
136 | 催化剂装填率.xlsx | 9.12K |
137 | T0102-反应压力.bkp | 341.71K |
138 | T0102-反应器体积.bkp | 348.97K |
139 | T0102-反应温度.bkp | 347.08K |
140 | T0102-氢气量.bkp | 353.41K |
141 | 不同压力下醇类沸点差异.xlsx | 165B |
142 | T0101-Design.bkp | 371.51K |
143 | T0101-Efficiency.bkp | 331.28K |
144 | T0101-RR.bkp | 327.54K |
145 | T0101-VFEEDSTAGE-REBDUTY.bkp | 325.01K |
146 | T0101-VFEEDSTAGE-分离效果.bkp | 330.18K |
147 | T0101-持液量.bkp | 358.71K |
148 | T0101-气液分别进料.bkp | 314.82K |
149 | T0101-氧气三股进料.bkp | 325.56K |
150 | 反应器塔.bkp | 377.22K |
151 | 塔设备优化(DSTWU简捷计算).bkp | 379.97K |
152 | 塔设备优化(回流比).bkp | 405.37K |
153 | 塔设备优化(设计规定).bkp | 397.17K |
154 | 塔设备优化(进料板位置).bkp | 405.80K |
155 | T0102-Design.bkp | 352.11K |
156 | T0102-DS.bkp | 237.03K |
157 | T0102-DSTWU.bkp | 236.18K |
158 | T0102-FEEDSTAGE.bkp | 320.20K |
159 | T0102-RR.bkp | 248.15K |
160 | T0201-Design.bkp | 434.75K |
161 | T0201-EFFIC.bkp | 408.98K |
162 | T0201-ME用量.bkp | 418.75K |
163 | T0201-NSTAGE.bkp | 429.12K |
164 | T0201-PRE.bkp | 409.80K |
165 | T0202-Design.bkp | 387.33K |
166 | T0202-DS.bkp | 237.39K |
167 | T0202-DSTWU.bkp | 289.25K |
168 | T0202-FEEDSTAGE.bkp | 339.95K |
169 | T0202-RR.bkp | 333.33K |
170 | T0202-气相出口.bkp | 328.84K |
171 | T0203-Design.bkp | 465.47K |
172 | T0203-DS.bkp | 380.83K |
173 | T0203-DSTWU.bkp | 289.60K |
174 | T0203-FEEDSTAGE.bkp | 380.90K |
175 | T0203-RR.bkp | 392.44K |
176 | T0301-Design.bkp | 356.73K |
177 | T0301-DS.bkp | 333.88K |
178 | T0301-DSTWU.bkp | 304.54K |
179 | T0301-FEEDSTAGE.bkp | 250.26K |
180 | T0301-RR.bkp | 350.63K |
181 | T0302-Design.bkp | 628.72K |
182 | T0302-DS.bkp | 460.27K |
183 | T0302-DSTWU.bkp | 320.07K |
184 | T0302-FEEDSTAGE.bkp | 467.13K |
185 | T0302-RR.bkp | 469.06K |
186 | T0303-Design.bkp | 445.94K |
187 | T0303-DSTWU-BPRE.bkp | 281.82K |
188 | T0303-DSTWU.bkp | 308.55K |
189 | T0303-FEEDSTAGE.bkp | 247.46K |
190 | T0303-RR.bkp | 348.88K |
191 | T0304-Design.bkp | 601.96K |
192 | T0304-DS.bkp | 270.81K |
193 | T0304-DSTWU.bkp | 333.79K |
194 | T0304-FEEDSTAGE.bkp | 507.14K |
195 | T0304-RR.bkp | 501.21K |
196 | T0305-Design.bkp | 548.60K |
197 | T0305-DSTWU.bkp | 283.28K |
198 | T0305-FEEDSTAGE.bkp | 415.23K |
199 | T0305-RE-RR.bkp | 414.75K |
200 | T0305-RR.bkp | 368.77K |
201 | V0201-PRE.bkp | 343.79K |
202 | V0201-TEM.bkp | 338.80K |
203 | V0301-PRE.bkp | 303.84K |
204 | V0301-TEM.bkp | 316.23K |
205 | EconomicAnalysis.izp | 1.97M |
206 | EconomicAnalysis.szp | 1.41M |
207 | Results.xls | 286.50K |
208 | Risksystem甲醇储罐泄漏模拟.pdf | 881.34K |
209 | 两相流泄漏.rsm | 95B |
210 | 典型泄漏事故.rsm | 526B |
211 | 气体泄漏.rsm | 73B |
212 | 池火事故.rsm | 204B |
213 | 池火事故伤害范围.rsp | 444.00K |
214 | 泄漏扩散.rsm | 491B |
215 | 液体泄漏.rsm | 108B |
216 | 火球BLEVE.rsm | 211B |
217 | 火球BLEVE伤害范围.rsp | 444.00K |
218 | 热量蒸发.rsm | 56B |
219 | 蒸汽云爆炸.rsm | 174B |
220 | 蒸汽云爆炸伤害范围.rsp | 444.00K |
221 | 质量蒸发.rsm | 56B |
222 | 闪蒸.rsm | 54B |
223 | designnew.ses | 6.58M |
224 | SP3D布置图-1.pdf | 65.96K |
225 | SP3D布置图-10.pdf | 29.51K |
226 | SP3D布置图-11.pdf | 34.12K |
227 | SP3D布置图-12.pdf | 18.72K |
228 | SP3D布置图-2.pdf | 65.11K |
229 | SP3D布置图-3.pdf | 57.65K |
230 | SP3D布置图-4.pdf | 57.67K |
231 | SP3D布置图-5.pdf | 24.33K |
232 | SP3D布置图-6.pdf | 32.20K |
233 | SP3D布置图-7.pdf | 37.47K |
234 | SP3D布置图-8.pdf | 29.47K |
235 | SP3D布置图-9.pdf | 51.06K |
236 | 管道轴测图-1.dwg | 46.41K |
237 | 管道轴测图-10.dwg | 46.57K |
238 | 管道轴测图-101.tif | 58.01K |
239 | 管道轴测图-11.dwg | 44.96K |
240 | 管道轴测图-11.tif | 58.59K |
241 | 管道轴测图-111.tif | 58.13K |
242 | 管道轴测图-12.dwg | 44.76K |
243 | 管道轴测图-121.tif | 58.04K |
244 | 管道轴测图-13.dwg | 45.86K |
245 | 管道轴测图-131.tif | 57.94K |
246 | 管道轴测图-14.dwg | 50.11K |
247 | 管道轴测图-141.tif | 57.94K |
248 | 管道轴测图-15.dwg | 46.04K |
249 | 管道轴测图-151.tif | 57.88K |
250 | 管道轴测图-2.dwg | 47.28K |
251 | 管道轴测图-21.tif | 58.04K |
252 | 管道轴测图-3.dwg | 41.33K |
253 | 管道轴测图-31.tif | 58.38K |
254 | 管道轴测图-4.dwg | 45.82K |
255 | 管道轴测图-41.tif | 58.13K |
256 | 管道轴测图-5.dwg | 40.21K |
257 | 管道轴测图-51.tif | 58.09K |
258 | 管道轴测图-6.dwg | 51.64K |
259 | 管道轴测图-61.tif | 58.00K |
260 | 管道轴测图-7.dwg | 40.28K |
261 | 管道轴测图-71.tif | 58.03K |
262 | 管道轴测图-8.dwg | 57.92K |
263 | 管道轴测图-81.tif | 58.10K |
264 | 管道轴测图-9.dwg | 43.24K |
265 | 管道轴测图-91.tif | 58.15K |
266 | 管道轴测图-1.pdf | 65.39K |
267 | 管道轴测图-10.pdf | 60.52K |
268 | 管道轴测图-11.pdf | 65.76K |
269 | 管道轴测图-12.pdf | 64.89K |
270 | 管道轴测图-13.pdf | 61.22K |
271 | 管道轴测图-15.pdf | 65.74K |
272 | 管道轴测图-2.pdf | 66.17K |
273 | 管道轴测图-3.pdf | 58.55K |
274 | 管道轴测图-4.pdf | 65.69K |
275 | 管道轴测图-5.pdf | 58.42K |
276 | 管道轴测图-6.pdf | 66.44K |
277 | 管道轴测图-7.pdf | 58.69K |
278 | 管道轴测图-8.pdf | 61.78K |
279 | 管道轴测图-9.pdf | 59.85K |
280 | R0201.docx | 157.53K |
281 | R0301.docx | 157.65K |
282 | T0101.docx | 267.49K |
283 | T0102.docx | 267.27K |
284 | T0201.docx | 172.93K |
285 | T0202.docx | 305.93K |
286 | T0203.docx | 267.17K |
287 | T0301.docx | 172.10K |
288 | T0302.docx | 284.19K |
289 | T0303.docx | 189.31K |
290 | T0304.docx | 188.20K |
291 | T0305.docx | 283.19K |
292 | E0101.docx | 478.42K |
293 | E0102.docx | 477.90K |
294 | E0103.docx | 478.56K |
295 | E0104.docx | 478.17K |
296 | E0105.docx | 477.50K |
297 | E0201.docx | 479.14K |
298 | E0202.docx | 478.45K |
299 | E0203.docx | 478.36K |
300 | E0204.docx | 477.90K |
301 | E0205.docx | 478.58K |
302 | E0206.docx | 477.79K |
303 | E0207.docx | 477.88K |
304 | E0208.docx | 478.09K |
305 | E0301.docx | 477.99K |
306 | E0302.docx | 477.81K |
307 | E0303.docx | 478.29K |
308 | E0304.docx | 477.92K |
309 | E0305.docx | 477.81K |
310 | E0306.docx | 432.72K |
311 | E0307.docx | 209.87K |
312 | E0308.docx | 208.58K |
313 | E0309.docx | 208.33K |
314 | E0310.docx | 208.52K |
315 | E0311.docx | 207.78K |
316 | E0312.docx | 225.55K |
317 | E0313.docx | 209.41K |
318 | E0314.docx | 208.98K |
319 | R0201.ra2 | 23.24K |
320 | R0301.ra2 | 23.24K |
321 | T0101.cn2 | 30.20K |
322 | T0102.cn2 | 30.20K |
323 | T0201.cn2 | 30.20K |
324 | T0202.cn2 | 30.20K |
325 | T0203.cn2 | 30.20K |
326 | T0301.cn2 | 30.20K |
327 | T0302.cn2 | 30.20K |
328 | T0303.cn2 | 30.20K |
329 | T0304.cn2 | 30.20K |
330 | T0305.cn2 | 30.20K |
331 | E0101.fx2 | 24.00K |
332 | E0102.fx2 | 24.00K |
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334 | E0104.fx2 | 24.00K |
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336 | E0201.fx2 | 24.00K |
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