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年产55万吨PX项目初步设计（ID:2685579）
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| # | 文件名称 | 文件大小 |
|---|---|---|
| 1 | 1759119469966.zip | 135.67M |
| 2 | 作品一览表.doc | 38.50K |
| 3 | ReadMe.txt | 558B |
| 4 | PFD工艺流程图.dwg | 586.35K |
| 5 | PFD工艺流程图.pdf | 366.46K |
| 6 | PID管道及仪表流程图.bak | 1.29M |
| 7 | PID管道及仪表流程图.dwg | 1.29M |
| 8 | 首页图.dwg | 230.16K |
| 9 | PID管道及仪表流程图.pdf | 1.14M |
| 10 | PDMS图1.png | 231.15K |
| 11 | PDMS图2.png | 316.24K |
| 12 | 俯视效果图.jpg | 681.98K |
| 13 | 车间效果图1.jpg | 643.37K |
| 14 | 车间效果图2.jpg | 594.24K |
| 15 | 车间效果图3.jpg | 596.51K |
| 16 | 厂区总平面布置图.dwg | 221.88K |
| 17 | 厂区总平面布置图.pdf | 122.60K |
| 18 | 1.抽提及烷基化工段.dwg | 920.57K |
| 19 | 2.异构化工段.dwg | 648.54K |
| 20 | 3.甲苯甲醇甲基化工段.dwg | 553.14K |
| 21 | 三甲化工段.pdf | 935.66K |
| 22 | 压缩机.pdf | 732.04K |
| 23 | 异构化工段.pdf | 1.09M |
| 24 | 抽提及烷基化工段.pdf | 1.56M |
| 25 | 总设备布置图.dwg | 704.92K |
| 26 | 第一工段设备布置图.dwg | 457.37K |
| 27 | 第三工段设备布置图.dwg | 392.63K |
| 28 | 第二工段设备布置图.dwg | 414.97K |
| 29 | 总设备布置图.pdf | 834.20K |
| 30 | 第一工段设备布置图.pdf | 317.44K |
| 31 | 第三工段设备布置图.pdf | 283.87K |
| 32 | 第二工段设备布置图.pdf | 319.33K |
| 33 | 原料初分离塔T0101.dwg | 389.45K |
| 34 | 反应器R0201.dwg | 256.47K |
| 35 | 换热器E0101.dwg | 287.02K |
| 36 | 原料初分离塔T0101.pdf | 426.21K |
| 37 | 反应器R0201.pdf | 160.54K |
| 38 | 换热器E0101.pdf | 163.96K |
| 39 | 二甲苯模拟移动吸附床说明书.pdf | 310.46K |
| 40 | 创新性说明.pdf | 883.00K |
| 41 | 初步设计说明书.pdf | 7.34M |
| 42 | 初步设计说明书附录.pdf | 1.85M |
| 43 | 可行性研究分析.pdf | 1.93M |
| 44 | 安全预评价.pdf | 1.56M |
| 45 | 环境评估报告.pdf | 1.23M |
| 46 | 设计摘要.pdf | 984.82K |
| 47 | 二甲苯模拟移动吸附床说明书.doc | 142.50K |
| 48 | 创新性说明.doc | 2.34M |
| 49 | 初步设计说明书.doc | 14.29M |
| 50 | 初步设计说明书附录.doc | 2.47M |
| 51 | 可行性研究分析.doc | 2.51M |
| 52 | 安全预评价.doc | 2.58M |
| 53 | 环境评估报告.doc | 1001.50K |
| 54 | 设计摘要.doc | 2.94M |
| 55 | readme.txt | 717B |
| 56 | PX4SMB.cra | 1.51M |
| 57 | PX4SMB稳新.cra | 2.09M |
| 58 | readme.txt | 529B |
| 59 | 运行说明.doc | 46.00K |
| 60 | readme.txt | 534B |
| 61 | 原料预分离塔.aprbkp | 191.29K |
| 62 | 原料预分离塔.bkp | 355.79K |
| 63 | 原料预分离塔.dynf | 1.06M |
| 64 | 原料预处理塔dyn.appdf | 365.15K |
| 65 | lsprst7.dll | 265B |
| 66 | lsprst7.tgz | 279B |
| 67 | propsplus.aprhis | 16.37K |
| 68 | propsplus.aprpdf | 253.36K |
| 69 | PropsPlus.def | 226B |
| 70 | PropsPlus.his | 2.26K |
| 71 | PropsPlus.rep | 0B |
| 72 | sysprs7.dll | 1.00K |
| 73 | sysprs7.tgz | 1.00K |
| 74 | 全厂换热网络（case）.hch | 746.30K |
| 75 | 全厂换热网络（project.hch | 1.71M |
| 76 | 1.bmp | 1.17M |
| 77 | 2.bmp | 695.63K |
| 78 | 3.png | 14.02K |
| 79 | 4.png | 13.64K |
| 80 | 437-2.EDR | 389.89K |
| 81 | lsprst7.dll | 265B |
| 82 | lsprst7.tgz | 279B |
| 83 | sysprs7.dll | 1.00K |
| 84 | sysprs7.tgz | 1.00K |
| 85 | 1.bmp | 1.17M |
| 86 | 2.bmp | 695.63K |
| 87 | 3.png | 13.85K |
| 88 | 4.png | 13.77K |
| 89 | 冷凝器1.EDR | 418.47K |
| 90 | 1.bmp | 1.17M |
| 91 | 2.bmp | 695.63K |
| 92 | 3.png | 13.28K |
| 93 | 4.png | 13.73K |
| 94 | 再沸器01.EDR | 431.93K |
| 95 | 1.bmp | 1.17M |
| 96 | 2.bmp | 695.63K |
| 97 | 3.png | 13.54K |
| 98 | 4.png | 13.72K |
| 99 | 冷凝器2.EDR | 354.25K |
| 100 | 1.bmp | 1.17M |
| 101 | 2.bmp | 695.63K |
| 102 | 3.png | 13.71K |
| 103 | 4.png | 13.59K |
| 104 | 再沸器2.EDR | 510.75K |
| 105 | 1.bmp | 1.17M |
| 106 | 2.bmp | 695.63K |
| 107 | 3.png | 13.22K |
| 108 | 4.png | 13.72K |
| 109 | E0106.EDR | 455.05K |
| 110 | 1.bmp | 1.17M |
| 111 | 2.bmp | 695.63K |
| 112 | 3.png | 13.83K |
| 113 | 4.png | 13.60K |
| 114 | 再沸器3.EDR | 439.37K |
| 115 | 1.bmp | 737.47K |
| 116 | 2.bmp | 1.24M |
| 117 | 3.png | 13.03K |
| 118 | 4.png | 13.65K |
| 119 | 冷凝器4.EDR | 333.56K |
| 120 | 1.bmp | 1.17M |
| 121 | 2.bmp | 695.63K |
| 122 | 3.png | 14.07K |
| 123 | 4.png | 13.63K |
| 124 | 再沸器4.EDR | 485.38K |
| 125 | 1.bmp | 1.17M |
| 126 | 100.1.EDR | 413.26K |
| 127 | 2.bmp | 695.63K |
| 128 | 3.png | 13.49K |
| 129 | 4.png | 13.83K |
| 130 | 1.bmp | 1.17M |
| 131 | 2.bmp | 695.63K |
| 132 | 3.png | 13.21K |
| 133 | 4.png | 13.88K |
| 134 | 437-1.EDR | 330.47K |
| 135 | 1.bmp | 1.17M |
| 136 | 2.bmp | 695.63K |
| 137 | 3.png | 13.94K |
| 138 | 395-4.EDR | 420.17K |
| 139 | 4.png | 13.80K |
| 140 | 1.bmp | 1.17M |
| 141 | 2.bmp | 695.63K |
| 142 | 3.png | 13.63K |
| 143 | 395-3.EDR | 471.25K |
| 144 | 4.png | 13.88K |
| 145 | 1.bmp | 1.17M |
| 146 | 2.bmp | 695.63K |
| 147 | 3.png | 13.24K |
| 148 | 395-1.EDR | 371.69K |
| 149 | 4.png | 13.80K |
| 150 | 1.bmp | 1.17M |
| 151 | 2.bmp | 695.63K |
| 152 | 3.png | 13.34K |
| 153 | 395-2.EDR | 385.35K |
| 154 | 4.png | 13.71K |
| 155 | 1.bmp | 1.17M |
| 156 | 2.bmp | 695.63K |
| 157 | 3.png | 13.40K |
| 158 | 4.png | 13.80K |
| 159 | 冷凝器8.EDR | 377.20K |
| 160 | 1.bmp | 1.17M |
| 161 | 2.bmp | 695.63K |
| 162 | 3.png | 13.15K |
| 163 | 4.png | 13.65K |
| 164 | 490-2.EDR | 458.51K |
| 165 | 1.bmp | 1.17M |
| 166 | 2.bmp | 695.63K |
| 167 | 3.png | 13.25K |
| 168 | 4.png | 13.80K |
| 169 | 490-1.EDR | 381.93K |
| 170 | 1.bmp | 1.17M |
| 171 | 2.bmp | 695.63K |
| 172 | 3.png | 13.54K |
| 173 | 4.png | 13.68K |
| 174 | 490-3.EDR | 403.19K |
| 175 | 1.bmp | 1.17M |
| 176 | 2.bmp | 695.63K |
| 177 | 3.png | 13.78K |
| 178 | 4.png | 13.82K |
| 179 | 冷凝器7.EDR | 404.44K |
| 180 | 1.bmp | 1.17M |
| 181 | 2.bmp | 695.63K |
| 182 | 3.png | 14.14K |
| 183 | 4.png | 13.49K |
| 184 | 再沸器7.EDR | 396.06K |
| 185 | 1.jpg | 90.36K |
| 186 | 2.jpg | 101.67K |
| 187 | 3.jpg | 66.17K |
| 188 | 4.jpg | 57.12K |
| 189 | E0211.EDR | 444.99K |
| 190 | 1.bmp | 1.17M |
| 191 | 2.bmp | 695.63K |
| 192 | 3.png | 14.20K |
| 193 | 4.png | 13.65K |
| 194 | 再沸器8.EDR | 488.23K |
| 195 | .1.bmp | 1.17M |
| 196 | .2.bmp | 695.63K |
| 197 | 1.png | 12.71K |
| 198 | 2.png | 13.72K |
| 199 | 78-PX2.EDR | 442.01K |
| 200 | .1.bmp | 1.17M |
| 201 | .2.bmp | 695.63K |
| 202 | 1.png | 12.36K |
| 203 | 2.png | 13.70K |
| 204 | 46-PX1.edr | 356.02K |
| 205 | 1.bmp | 1.17M |
| 206 | 2.bmp | 695.63K |
| 207 | 3.png | 12.89K |
| 208 | 4.png | 13.77K |
| 209 | 冷凝器5.EDR | 344.50K |
| 210 | 1.bmp | 1.17M |
| 211 | 2.bmp | 695.63K |
| 212 | 3.png | 13.19K |
| 213 | 4.png | 13.89K |
| 214 | 再沸器5.EDR | 374.67K |
| 215 | 1.bmp | 1.17M |
| 216 | 2.bmp | 695.63K |
| 217 | 3.png | 13.76K |
| 218 | 4.png | 13.71K |
| 219 | 冷凝器6.EDR | 429.40K |
| 220 | 1.bmp | 1.17M |
| 221 | 2.bmp | 695.63K |
| 222 | 3.png | 13.07K |
| 223 | 4.png | 13.71K |
| 224 | 再沸器6.EDR | 377.34K |
| 225 | IPEWB.XLS | 134.00K |
| 226 | IPEWB_TRA.XLS | 22.50K |
| 227 | RESULTS.xls | 873.50K |
| 228 | SPECS.xls | 3.25M |
| 229 | 全厂换热网络.bkp | 728.98K |
| 230 | C6C9烷基化工段.bkp | 688.26K |
| 231 | 全流程模拟.bkp | 1.48M |
| 232 | 异构化工段.bkp | 719.17K |
| 233 | 甲苯甲醇烷基化工段.bkp | 539.08K |
| 234 | T0303塔优化（回流比）.bkp | 303.35K |
| 235 | T0303塔优化（塔板数）.bkp | 316.95K |
| 236 | T0303塔优化（进料位置）.bkp | 303.83K |
| 237 | PX精馏双塔优化（塔1采出率）.bkp | 341.96K |
| 238 | PX精馏双塔优化（塔2回流比）.bkp | 341.93K |
| 239 | T0101塔优化（回流比）.bkp | 287.01K |
| 240 | T0101塔优化（塔板数）.bkp | 301.63K |
| 241 | T0101塔优化（进料位置）.bkp | 287.34K |
| 242 | readme.txt | 106B |
| 243 | 停留时间.rxn | 45.62K |
| 244 | 直径1.2m高10m.mph | 373.08K |
| 245 | 直径1.5m高6.5m.mph | 424.25K |
| 246 | 直径1.7m高5m.mph | 470.56K |
| 247 | 1.png | 64.96K |
| 248 | 10.pdf | 188.75K |
| 249 | 2.png | 86.57K |
| 250 | 3.png | 58.21K |
| 251 | 4.png | 58.10K |
| 252 | 5.png | 58.24K |
| 253 | 6.png | 199.86K |
| 254 | 7.pdf | 188.69K |
| 255 | 8.pdf | 188.70K |
| 256 | 9.pdf | 188.75K |
| 257 | T0101原料初分离塔.kgt | 2.01K |
| 258 | 1.png | 54.66K |
| 259 | 2.png | 72.95K |
| 260 | 3.png | 52.66K |
| 261 | 4.png | 54.66K |
| 262 | 5.png | 55.69K |
| 263 | 6.png | 190.86K |
| 264 | 7.tif | 328.82K |
| 265 | 8.tif | 328.64K |
| 266 | 9.tif | 328.35K |
| 267 | T0102苯精馏塔.kgt | 1.64K |
| 268 | 1.png | 46.50K |
| 269 | 2.png | 49.36K |
| 270 | 3.png | 74.25K |
| 271 | 4.png | 52.87K |
| 272 | 5.png | 52.31K |
| 273 | 6.png | 190.07K |
| 274 | 7.tif | 328.52K |
| 275 | 8.tif | 328.90K |
| 276 | 9.tif | 328.49K |
| 277 | T0103二甲苯精馏塔.kgt | 1.64K |
| 278 | 1.png | 45.87K |
| 279 | 2.png | 82.17K |
| 280 | 3.png | 52.90K |
| 281 | 4.png | 55.53K |
| 282 | 5.png | 55.23K |
| 283 | 6.png | 195.97K |
| 284 | 7.tif | 328.68K |
| 285 | 8.tif | 328.43K |
| 286 | 9.tif | 328.54K |
| 287 | T0104重芳烃精馏塔.kgt | 1.64K |
| 288 | 1.png | 58.60K |
| 289 | 10.pdf | 184.09K |
| 290 | 2.png | 89.70K |
| 291 | 3.png | 60.28K |
| 292 | 4.png | 61.08K |
| 293 | 5.png | 60.74K |
| 294 | 6.png | 195.58K |
| 295 | 7.pdf | 184.11K |
| 296 | 8.pdf | 184.11K |
| 297 | 9.pdf | 184.08K |
| 298 | PDEB分离塔.kgt | 2.01K |
| 299 | 1.png | 61.15K |
| 300 | 2.png | 83.85K |
| 301 | 3.png | 60.48K |
| 302 | 4.png | 61.09K |
| 303 | 5.png | 58.09K |
| 304 | 6.png | 201.64K |
| 305 | 7.tif | 327.40K |
| 306 | 8.tif | 328.57K |
| 307 | 9.tif | 328.45K |
| 308 | T0205PX精馏塔一段.kgt | 1.64K |
| 309 | 1.png | 55.14K |
| 310 | 2.png | 76.64K |
| 311 | 3.png | 50.35K |
| 312 | 4.png | 51.22K |
| 313 | 5.png | 50.81K |
| 314 | 6.png | 190.18K |
| 315 | 7.tif | 328.94K |
| 316 | 8.tif | 328.32K |
| 317 | 9.tif | 328.38K |
| 318 | T0206PX精馏塔二段.kgt | 1.63K |
| 319 | 1.png | 61.67K |
| 320 | 2.png | 82.14K |
| 321 | 3.png | 55.84K |
| 322 | 4.png | 56.97K |
| 323 | 5.png | 191.58K |
| 324 | 6.tif | 328.13K |
| 325 | 7.tif | 327.63K |
| 326 | 8.tif | 328.62K |
| 327 | T0302甲醇精馏塔.kgt | 1.64K |
| 328 | 1.png | 57.62K |
| 329 | 2.png | 56.11K |
| 330 | 3.png | 60.00K |
| 331 | 4.png | 78.59K |
| 332 | 5.png | 55.94K |
| 333 | 6.png | 197.00K |
| 334 | 7.tif | 332.02K |
| 335 | 8.tif | 328.68K |
| 336 | 9.tif | 328.83K |
| 337 | T0303PX精馏塔.kgt | 1.65K |
| 338 | readme.txt | 677B |
| 339 | Project_Description_IMP.txt | 0B |
| 340 | imp0001_0001 | 26.00K |
| 341 | imp0002_0001 | 26.00K |
| 342 | imp0003_0001 | 26.00K |
| 343 | imp0004_0001 | 26.00K |
| 344 | imp0005_0001 | 26.00K |
| 345 | imp0006_0001 | 26.00K |
| 346 | imp0007_0001 | 26.00K |
| 347 | imp0009_0001 | 26.00K |
| 348 | imp0010_0001 | 20.00K |
| 349 | imp0011_0001 | 20.00K |
| 350 | imp0012_0001 | 20.00K |
| 351 | imp0013_0001 | 20.00K |
| 352 | imp0014_0001 | 20.00K |
| 353 | imp0015_0001 | 20.00K |
| 354 | imp0016_0001 | 20.00K |
| 355 | imp0017_0001 | 20.00K |
| 356 | imp0018_0001 | 20.00K |
| 357 | imp0019_0001 | 20.00K |
| 358 | imp0020_0001 | 20.00K |
| 359 | imp0021_0001 | 20.00K |
| 360 | imp0022_0001 | 20.00K |
| 361 | imp0023_0001 | 20.00K |
| 362 | imp0024_0001 | 20.00K |
| 363 | imp0025_0001 | 20.00K |
| 364 | imp0026_0001 | 6.29M |
| 365 | imp0027_0001 | 6.29M |
| 366 | imp0028_0001 | 26.00K |
| 367 | imp0029_0001 | 26.00K |
| 368 | imp0030_0001 | 6.29M |
| 369 | imp0032_0001 | 6.29M |
| 370 | imp0033_0001 | 6.29M |
| 371 | imp0034_0001 | 6.29M |
| 372 | imp0035_0001 | 6.29M |
| 373 | imp0036_0001 | 6.29M |
| 374 | imp0037_0001 | 142.00K |
| 375 | imp0038_0001 | 142.00K |
| 376 | imp0039_0001 | 142.00K |
| 377 | imp0040_0001 | 142.00K |
| 378 | imp0041_0001 | 142.00K |
| 379 | imp0042_0001 | 2.71M |
| 380 | imp0043_0001 | 142.00K |
| 381 | imp0044_0001 | 142.00K |
| 382 | imp0045_0001 | 142.00K |
| 383 | imp0046_0001 | 26.00K |
| 384 | imp0047_0001 | 26.00K |
| 385 | imp0048_0001 | 26.00K |
| 386 | imp0049_0001 | 26.00K |
| 387 | imp0050_0001 | 26.00K |
| 388 | imp0051_0001 | 26.00K |
| 389 | imp0052_0001 | 26.00K |
| 390 | imp0053_0001 | 26.00K |
| 391 | imp7011_0001 | 1.67M |
| 392 | imp7017_0001 | 2.44M |
| 393 | imp7019_0001 | 36.00K |
| 394 | imp7020_0001 | 1.45M |
| 395 | imp7030_0001 | 38.00K |
| 396 | imp7032_0001 | 18.00K |
| 397 | imp7033_0001 | 18.00K |
| 398 | imp7110_0001 | 26.00K |
| 399 | imp7111_0001 | 20.00K |
| 400 | imp7120_0001 | 26.00K |
| 401 | imp7121_0001 | 20.00K |
| 402 | imp7130_0001 | 26.00K |
| 403 | imp7131_0001 | 20.00K |
| 404 | imp7140_0001 | 26.00K |
| 405 | imp7141_0001 | 20.00K |
| 406 | imp7143_0001 | 20.00K |
| 407 | imp7144_0001 | 52.00K |
| 408 | imp7150_0001 | 26.00K |
| 409 | imp7151_0001 | 20.00K |
| 410 | imp7160_0001 | 26.00K |
| 411 | imp7161_0001 | 20.00K |
| 412 | imp7162_0001 | 20.00K |
| 413 | imp7204_0001 | 1.45M |
| 414 | imp7205_0001 | 32.00K |
| 415 | imp7207_0001 | 34.00K |
| 416 | imp7596_0001 | 1.69M |
| 417 | imp7598_0001 | 48.00K |
| 418 | impcom | 30.00K |
| 419 | impmis | 14.00K |
| 420 | impsys | 1.83M |
| 421 | ADVANCED.IMP | 3.67K |
| 422 | ADVANCED.MET | 3.66K |
| 423 | BASIC.IMP | 287B |
| 424 | BASIC.MET | 262B |
| 425 | BASICSYS.IMP | 290B |
| 426 | BASICSYS.MET | 281B |
| 427 | M15212-224-7020-240 | 14.50K |
| 428 | M15212-2848-7020-1 | 23.88K |
| 429 | M15212-2880-7020-1 | 18.25K |
| 430 | M15212-2912-7020-1 | 14.63K |
| 431 | M15212-1058-7020-245 | 47.13K |
| 432 | M15212-290-7020-240 | 17.25K |
| 433 | M15212-2307-7020-1 | 19.75K |
| 434 | M15212-2339-7020-1 | 17.50K |
| 435 | M15212-2371-7020-1 | 13.63K |
| 436 | M15212-1156-7020-244 | 37.50K |
| 437 | M15212-132-7020-240 | 17.25K |
| 438 | M15212-2405-7020-1 | 25.50K |
| 439 | M15212-2437-7020-1 | 22.00K |
| 440 | M15212-2469-7020-1 | 16.88K |
| 441 | M15212-198-7020-240 | 18.38K |
| 442 | M15212-2502-7020-1 | 27.25K |
| 443 | M15212-38-7020-240 | 18.88K |
| 444 | M15212-6-7020-240 | 21.13K |
| 445 | M15397-6-7205-18 | 1.38M |
| 446 | M15212-71-7020-240 | 15.13K |
| 447 | M15212-2568-7020-1 | 20.13K |
| 448 | M15212-264-7020-240 | 19.50K |
| 449 | M15212-3944-7020-1 | 4.25K |
| 450 | M15212-329-7020-240 | 11.88K |
| 451 | M15212-106-7020-240 | 19.50K |
| 452 | M15212-171-7020-240 | 11.88K |
| 453 | M15212-875-7020-240 | 4.00K |
| 454 | M15212-237-7020-240 | 13.50K |
| 455 | M15212-2638-7020-1 | 25.63K |
| 456 | M15212-2670-7020-1 | 22.13K |
| 457 | M15212-2702-7020-1 | 17.00K |
| 458 | M15212-2735-7020-1 | 25.63K |
| 459 | M15212-2767-7020-1 | 22.13K |
| 460 | M15212-2799-7020-1 | 16.88K |
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| 520 | mas7016_0001 | 66.00K |
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| 703 | V23996-9-7612-1.vtx | 138.00K |
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| 709 | 氢气热量蒸发量计算.rsm | 50B |
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| 711 | 氢气闪蒸计算.rsm | 54B |
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| 717 | 甲醇两相流泄漏量计算.rsm | 86B |
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| 719 | 甲醇液体泄漏量计算.rsm | 107B |
| 720 | 甲醇热量蒸发量计算.rsm | 50B |
| 721 | 甲醇质量蒸发量计算.rsm | 56B |
| 722 | 甲醇闪蒸量计算.rsm | 54B |
| 723 | 甲醇池火事故模型预测－事故源.rsm | 194B |
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| 729 | 苯气体泄漏量计算.rsm | 73B |
| 730 | 苯液体泄漏量计算.rsm | 105B |
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| 735 | 苯沸腾液体扩展蒸汽爆炸（火球ＢＬＥＶＥ）模型预测.rsm | 203B |
| 736 | 苯蒸汽云爆炸模型预测（ＴＮＴ当量法）.rsm | 167B |
| 737 | readme.txt | 452B |
| 738 | 反应器R0201校核.doc | 264.50K |
| 739 | 反应器R0201校核.ra2 | 23.24K |
| 740 | T0101原料初分离塔.doc | 615.50K |
| 741 | T0102苯精馏塔.doc | 630.50K |
| 742 | T0103二甲苯精馏塔.doc | 630.00K |
| 743 | T0104重芳烃精馏塔.doc | 613.00K |
| 744 | T0202PDEB分离塔.doc | 621.00K |
| 745 | T0205PX精馏塔一段.doc | 613.50K |
| 746 | T0206PX精馏塔二段.doc | 613.50K |
| 747 | T0302甲醇精馏塔.doc | 613.50K |
| 748 | T0303PX精馏塔.doc | 613.50K |
| 749 | T0101原料初分离塔.cn2 | 30.20K |
| 750 | T0102苯精馏塔.cn2 | 30.20K |
| 751 | T0103二甲苯精馏塔.cn2 | 30.20K |
| 752 | T0104重芳烃精馏塔.cn2 | 30.20K |
| 753 | T0202PDEB分离塔.cn2 | 30.20K |
| 754 | T0205PX精馏塔一段.cn2 | 30.20K |
| 755 | T0206PX精馏塔二段.cn2 | 30.20K |
| 756 | T0302甲醇精馏塔.cn2 | 30.20K |
| 757 | T0303PX精馏塔.cn2 | 30.20K |
| 758 | 换热器E0101文档.doc | 2.38M |
| 759 | 换热器E0101校核源文件.fx2 | 24.00K |
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