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年产8万吨甲基丙烯酸甲酯项目初步设计（ID:2707620）
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| # | 文件名称 | 文件大小 |
|---|---|---|
| 1 | 17598871986835.zip | 282.59M |
| 2 | 4.现代设计方法评阅索引.pdf | 801.06K |
| 3 | 5.设计文档质量评阅索引.pdf | 680.32K |
| 4 | 致评委老师.txt | 1.96K |
| 5 | 1-复杂多相反应体系反应器模型化_渣油加氢裂化和萃取水合.caj | 6.36M |
| 6 | 2-Mo-Bi-Co-Fe基催化剂上异丁烯叔丁醇部分催化氧化制甲基丙烯醛.caj | 1.85M |
| 7 | 3-甲基丙烯醛一步氧化酯化制备甲基丙烯酸甲酯的研究_李桂花.caj | 3.24M |
| 8 | 4-KINETICSOFTHEOXIDATIONOFtert-BUTANOLTOMETHACROLEINONCALCIUMIONSPROMOTEDIRONTELLURIUM-MOLYBDENUMOXIDECATALYST.pdf | 270.76K |
| 9 | 动力学数据来源合理性说明.docx | 74.00K |
| 10 | 动力学数据来源合理性说明.pdf | 736.41K |
| 11 | 1-全流程模拟（不含双效精馏、不含换热网络、不含塔优化参数）.bkp | 4.87M |
| 12 | 2-全流程模拟（含双效精馏、不含换热网络、不含塔优化参数）.bkp | 3.02M |
| 13 | 3-全流程模拟（含双效精馏换热网络塔优化参数代入）.bkp | 2.97M |
| 14 | 1-复杂多相反应体系反应器模型化_渣油加氢裂化和萃取水合.caj | 6.36M |
| 15 | 2-Mo-Bi-Co-Fe基催化剂上异丁烯叔丁醇部分催化氧化制甲基丙烯醛.caj | 1.85M |
| 16 | 3-甲基丙烯醛一步氧化酯化制备甲基丙烯酸甲酯的研究_李桂花.caj | 3.24M |
| 17 | 4-KINETICSOFTHEOXIDATIONOFtert-BUTANOLTOMETHACROLEINONCALCIUMIONSPROMOTEDIRONTELLURIUM-MOLYBDENUMOXIDECATALYST.pdf | 270.76K |
| 18 | 动力学数据来源合理性说明.docx | 74.00K |
| 19 | 动力学数据来源合理性说明.pdf | 736.41K |
| 20 | T0306-D比F.apw | 1.50M |
| 21 | T0306-D比F.bkp | 617.03K |
| 22 | T0306-FEEDSTAGE.apw | 1.76M |
| 23 | T0306-FEEDSTAGE.bkp | 763.83K |
| 24 | T0306-NSTAGE.apw | 2.26M |
| 25 | T0306-NSTAGE.bkp | 1.57M |
| 26 | T0306-设计规定.apw | 2.15M |
| 27 | T0306-设计规定.bkp | 1.61M |
| 28 | T0306优化.doc | 191.50K |
| 29 | T0306优化.pdf | 367.84K |
| 30 | T0101-D比F.apw | 1.49M |
| 31 | T0101-D比F.bkp | 867.25K |
| 32 | T0101-FEEDSTAGE.apw | 1.40M |
| 33 | T0101-FEEDSTAGE.bkp | 798.63K |
| 34 | T0101-NSTAGE.apw | 1.47M |
| 35 | T0101-NSTAGE.bkp | 848.65K |
| 36 | T0101-回流比RR.apw | 1.49M |
| 37 | T0101-回流比RR.bkp | 873.80K |
| 38 | T0301优化.doc | 125.50K |
| 39 | T0301优化.pdf | 338.32K |
| 40 | T0201-总塔板数.apw | 1.36M |
| 41 | T0201-总塔板数.bkp | 537.82K |
| 42 | T0201-甲醇用量.apw | 1.40M |
| 43 | T0201-甲醇用量.bkp | 539.38K |
| 44 | T0201优化.doc | 122.50K |
| 45 | T0201优化.pdf | 306.20K |
| 46 | T0202-总塔板数.apw | 1.09M |
| 47 | T0202-总塔板数.bkp | 359.09K |
| 48 | T0202-甲醇用量.apw | 1.13M |
| 49 | T0202-甲醇用量.bkp | 384.05K |
| 50 | T0202优化.doc | 108.00K |
| 51 | T0202优化.pdf | 294.99K |
| 52 | T0305-FEEDSTEGE.apw | 1.49M |
| 53 | T0305-FEEDSTEGE.bkp | 610.50K |
| 54 | T0305-NSTAGE.apw | 1.62M |
| 55 | T0305-NSTAGE.bkp | 749.03K |
| 56 | T0305-设计规定.apw | 1.39M |
| 57 | T0305-设计规定.bkp | 546.19K |
| 58 | T0305优化.doc | 154.00K |
| 59 | T0305优化.pdf | 337.98K |
| 60 | 1.T0202粗MAL吸收塔设计源文件.bkp | 3.62M |
| 61 | 2.T0202粗MAL吸收塔水力学校核书.pdf | 384.79K |
| 62 | 3.T0202粗MAL吸收塔设备条件图.dwg | 481.99K |
| 63 | 4.T0202粗MAL吸收塔机械强度校核书.pdf | 397.68K |
| 64 | 5.T0202粗MAL吸收塔机械强度校核书.doc | 632.94K |
| 65 | 6.T0202粗MAL吸收塔机械强度校核源文件.cn2 | 32.58K |
| 66 | 三包.apw | 3.24M |
| 67 | 三包.bkp | 2.37M |
| 68 | 两包.apw | 3.19M |
| 69 | 两包.bkp | 2.44M |
| 70 | 先反应后精馏.apw | 3.23M |
| 71 | 先反应后精馏.bkp | 2.63M |
| 72 | 四包.apw | 3.88M |
| 73 | 四包.bkp | 2.98M |
| 74 | 单塔.apw | 1.16M |
| 75 | 单塔.bkp | 384.54K |
| 76 | 多效精馏.apw | 3.35M |
| 77 | 多效精馏.bkp | 2.84M |
| 78 | 熔盐蒸汽发生器.apw | 728.00K |
| 79 | 熔盐蒸汽发生器.bkp | 111.76K |
| 80 | T0202粗MAL吸收塔机械强度校核书.doc | 632.94K |
| 81 | T0202粗MAL吸收塔机械强度校核书.pdf | 397.68K |
| 82 | T0202粗MAL吸收塔机械强度校核源文件.cn2 | 32.58K |
| 83 | 1-E0312校核源文件.fx3 | 25.63K |
| 84 | 2-E0312校核说明书.docx | 694.96K |
| 85 | 1-E0405校核源文件.fx3 | 25.63K |
| 86 | 2-E0405校核说明书.docx | 715.20K |
| 87 | 反应器R0101.ra2 | 23.58K |
| 88 | 反应器R0101校核书.doc | 165.50K |
| 89 | 反应器R0201校核.fx3 | 25.63K |
| 90 | 反应器R0201校核书.doc | 1.69M |
| 91 | 反应器R0301.doc | 191.50K |
| 92 | 反应器R0301.ra2 | 23.58K |
| 93 | 反应器R0303.ra2 | 23.58K |
| 94 | 反应器R0303校核书.doc | 191.50K |
| 95 | V0102.docx | 57.58K |
| 96 | V0102.ra2 | 23.58K |
| 97 | readme.txt | 563B |
| 98 | 1.全厂车间-ISO面.PNG | 186.24K |
| 99 | 10.管道模块操作截图.png | 212.75K |
| 100 | 2.全厂车间-侧视图.PNG | 56.25K |
| 101 | 3.全厂车间-平面.PNG | 45.03K |
| 102 | 4.全厂车间-前视图.PNG | 85.02K |
| 103 | 5.甲基丙烯酸甲酯合成及精制车间-ISO图.PNG | 108.85K |
| 104 | 6.甲基丙烯酸甲酯合成及精制车间-侧视图.PNG | 73.05K |
| 105 | 7.甲基丙烯酸甲酯合成及精制车间-平面.PNG | 61.29K |
| 106 | 8.甲基丙烯酸甲酯合成及精制车间-前视图.PNG | 46.65K |
| 107 | 9.设备模块操作截图.png | 103.51K |
| 108 | equipment.dgn | 3.05M |
| 109 | process.dgn | 2.15M |
| 110 | stream.dgn | 67.00K |
| 111 | water.dgn | 37.00K |
| 112 | 1.png | 49.09K |
| 113 | 2.jpg | 35.95K |
| 114 | 3.png | 19.19K |
| 115 | dimian.FBX | 4.20M |
| 116 | equipment.fbx | 13.10M |
| 117 | equipmname.FBX | 1.50M |
| 118 | gate.FBX | 2.88M |
| 119 | pipe-process.fbx | 27.35M |
| 120 | pipe-stream.fbx | 564.95K |
| 121 | pipe-water.fbx | 198.47K |
| 122 | 1.jpg | 173.33K |
| 123 | 2.jpg | 110.95K |
| 124 | 3.jpg | 70.21K |
| 125 | 4.png | 2.02M |
| 126 | Lumion全厂渲染源文件.ls8 | 111.61M |
| 127 | 1-换热网络初始设计（不含双效精馏）.hch | 2.72M |
| 128 | 2-流股信息提取不含双效精馏.xlsx | 9.81K |
| 129 | 3-全流程模拟（不含双效精馏）.appdf | 1.49M |
| 130 | 3-全流程模拟（不含双效精馏）.bkp | 4.87M |
| 131 | 4-换热网络最终设计（含双效精馏）.hch | 4.20M |
| 132 | 5-流股信息提取含双效精馏.xlsx | 9.86K |
| 133 | 6-全流程模拟（含双效精馏，无换热网络）.bkp | 3.03M |
| 134 | 7-全流程模拟（含双效精馏换热网络塔优化参数代入）.bkp | 2.97M |
| 135 | 8-附录三换热网络设计.pdf | 1.98M |
| 136 | 3-污垢热阻来源于《化工工艺设计手册》第四版.png | 356.93K |
| 137 | 1-E0405.edr | 255.61K |
| 138 | 2-E0405校核说明书.docx | 715.20K |
| 139 | 3-E0405校核源文件.fx3 | 25.63K |
| 140 | 4-（04版本）设备条件图-循环甲醇冷却器E0405.dwg | 280.80K |
| 141 | 5-（16版本）设备条件图-循环甲醇冷却器E0405.dwg | 265.61K |
| 142 | 1-E0312.edr | 261.47K |
| 143 | 2-E0312校核说明书.docx | 694.96K |
| 144 | 3-E0312校核源文件.fx3 | 25.63K |
| 145 | 01.png | 146.23K |
| 146 | 02.png | 226.40K |
| 147 | 03.png | 183.14K |
| 148 | 04.png | 86.94K |
| 149 | distributor1.FCStd | 6.50K |
| 150 | distributor2-1.FCStd | 301.11K |
| 151 | distributor2.FCStd | 206.24K |
| 152 | distributor2.FCStd1 | 177.25K |
| 153 | distributor2.step | 1.92M |
| 154 | inlet.step | 3.28K |
| 155 | outlet.step | 3.35K |
| 156 | ste.step | 1.92M |
| 157 | wall1.step | 15.56K |
| 158 | wall2.step | 2.11M |
| 159 | epsilon | 1.34K |
| 160 | epsilon~ | 1.35K |
| 161 | k | 1.33K |
| 162 | k~ | 1.33K |
| 163 | nut | 1.35K |
| 164 | nut~ | 1.36K |
| 165 | p | 1.22K |
| 166 | p~ | 1.23K |
| 167 | U | 1.25K |
| 168 | U~ | 1.32K |
| 169 | epsilon | 1.19M |
| 170 | k | 1.26M |
| 171 | nut | 1.59M |
| 172 | p | 948.48K |
| 173 | phi | 4.13M |
| 174 | U | 3.67M |
| 175 | time | 968B |
| 176 | porosityProperties | 1.37K |
| 177 | porosityProperties~ | 1.37K |
| 178 | RASProperties | 935B |
| 179 | transportProperties | 1.34K |
| 180 | boundary | 1.29K |
| 181 | boundary~ | 2.14K |
| 182 | cellLevel | 241.04K |
| 183 | cellZones | 378.91K |
| 184 | faces | 10.66M |
| 185 | faceZones | 877B |
| 186 | level0Edge | 947B |
| 187 | neighbour | 2.12M |
| 188 | owner | 2.27M |
| 189 | pointLevel | 299.21K |
| 190 | points | 5.77M |
| 191 | pointZones | 878B |
| 192 | refinementHistory | 924B |
| 193 | surfaceIndex | 1.10M |
| 194 | c0 | 443.27K |
| 195 | dis1.foam | 0B |
| 196 | initialiseFields_parallel.run | 647B |
| 197 | initialiseFields_serial.run | 647B |
| 198 | mesh_parallel.run | 882B |
| 199 | mesh_serial.run | 745B |
| 200 | solver_parallel.run | 698B |
| 201 | solver_serial.run | 659B |
| 202 | dynamicMeshDict | 715B |
| 203 | MRFProperties | 681B |
| 204 | turbulenceProperties | 688B |
| 205 | boundary | 2.14K |
| 206 | cellLevel | 241.04K |
| 207 | cellZones | 877B |
| 208 | faces | 10.66M |
| 209 | faceZones | 877B |
| 210 | level0Edge | 947B |
| 211 | neighbour | 2.12M |
| 212 | owner | 2.27M |
| 213 | pointLevel | 299.21K |
| 214 | points | 5.77M |
| 215 | pointZones | 878B |
| 216 | refinementHistory | 924B |
| 217 | surfaceIndex | 1.10M |
| 218 | inlet.stl | 9.36K |
| 219 | outlet.stl | 12.35K |
| 220 | wall1.stl | 633.40K |
| 221 | snappyHexMesh.log | 43.68K |
| 222 | blockMeshDict | 1.37K |
| 223 | controlDict | 1020B |
| 224 | customNodeDict | 839B |
| 225 | decomposeParDict | 875B |
| 226 | fvOptions | 675B |
| 227 | fvSchemes | 766B |
| 228 | fvSolution | 701B |
| 229 | mapFieldsDict | 679B |
| 230 | projectDict | 1.41K |
| 231 | setFieldsDict | 679B |
| 232 | snappyHexMeshDict | 3.29K |
| 233 | stretchMeshDict | 681B |
| 234 | controlDict | 1.19K |
| 235 | controlDict~ | 1.19K |
| 236 | fvSchemes | 1.49K |
| 237 | fvSolution | 1.76K |
| 238 | fvSolution~ | 1.76K |
| 239 | topoSetDict | 11.35K |
| 240 | topoSetDict~ | 11.35K |
| 241 | epsilon | 1.34K |
| 242 | epsilon~ | 1.35K |
| 243 | k | 1.33K |
| 244 | k~ | 1.33K |
| 245 | nut | 1.35K |
| 246 | nut~ | 1.36K |
| 247 | p | 1.22K |
| 248 | p~ | 1.23K |
| 249 | U | 1.25K |
| 250 | U~ | 1.32K |
| 251 | epsilon | 2.25M |
| 252 | k | 2.40M |
| 253 | nut | 2.99M |
| 254 | p | 1.62M |
| 255 | phi | 7.44M |
| 256 | U | 6.19M |
| 257 | time | 972B |
| 258 | epsilon | 2.24M |
| 259 | k | 2.40M |
| 260 | nut | 2.99M |
| 261 | p | 1.62M |
| 262 | phi | 7.44M |
| 263 | U | 6.19M |
| 264 | time | 968B |
| 265 | porosityProperties | 1.37K |
| 266 | porosityProperties~ | 1.37K |
| 267 | RASProperties | 935B |
| 268 | transportProperties | 1.34K |
| 269 | boundary | 1.44K |
| 270 | boundary~ | 2.29K |
| 271 | cellLevel | 421.02K |
| 272 | cellZones | 378.85K |
| 273 | faces | 20.62M |
| 274 | faceZones | 877B |
| 275 | level0Edge | 947B |
| 276 | neighbour | 4.10M |
| 277 | owner | 4.41M |
| 278 | pointLevel | 569.16K |
| 279 | points | 11.08M |
| 280 | pointZones | 878B |
| 281 | refinementHistory | 924B |
| 282 | surfaceIndex | 2.00M |
| 283 | c0 | 443.20K |
| 284 | dis2.foam | 0B |
| 285 | initialiseFields_parallel.run | 647B |
| 286 | initialiseFields_serial.run | 647B |
| 287 | mesh_parallel.run | 882B |
| 288 | mesh_serial.run | 745B |
| 289 | solver_parallel.run | 698B |
| 290 | solver_serial.run | 659B |
| 291 | epsilon | 1.34K |
| 292 | epsilon~ | 1.35K |
| 293 | k | 1.33K |
| 294 | k~ | 1.33K |
| 295 | nut | 1.35K |
| 296 | nut~ | 1.36K |
| 297 | p | 1.22K |
| 298 | p~ | 1.23K |
| 299 | U | 1.25K |
| 300 | U~ | 1.32K |
| 301 | dynamicMeshDict | 715B |
| 302 | porosityProperties | 1.37K |
| 303 | porosityProperties~ | 1.37K |
| 304 | RASProperties | 935B |
| 305 | transportProperties | 1.34K |
| 306 | boundary | 2.29K |
| 307 | cellLevel | 421.02K |
| 308 | cellZones | 877B |
| 309 | faces | 20.62M |
| 310 | faceZones | 877B |
| 311 | level0Edge | 947B |
| 312 | neighbour | 4.10M |
| 313 | owner | 4.41M |
| 314 | pointLevel | 569.16K |
| 315 | points | 11.08M |
| 316 | pointZones | 878B |
| 317 | refinementHistory | 924B |
| 318 | surfaceIndex | 2.00M |
| 319 | inlet.stl | 9.36K |
| 320 | outlet.stl | 12.35K |
| 321 | wall1.stl | 633.28K |
| 322 | wall2.stl | 342.84K |
| 323 | snappyHexMesh.log | 44.39K |
| 324 | blockMeshDict | 1.37K |
| 325 | controlDict | 1020B |
| 326 | customNodeDict | 839B |
| 327 | decomposeParDict | 874B |
| 328 | fvOptions | 675B |
| 329 | fvSchemes | 766B |
| 330 | fvSolution | 701B |
| 331 | mapFieldsDict | 679B |
| 332 | projectDict | 1.77K |
| 333 | setFieldsDict | 679B |
| 334 | snappyHexMeshDict | 3.37K |
| 335 | stretchMeshDict | 681B |
| 336 | controlDict | 1.19K |
| 337 | controlDict~ | 1.19K |
| 338 | fvSchemes | 1.49K |
| 339 | fvSolution | 1.76K |
| 340 | fvSolution~ | 1.76K |
| 341 | topoSetDict | 11.35K |
| 342 | topoSetDict~ | 11.35K |
| 343 | inlet.step | 3.22K |
| 344 | inlet.stl | 16.84K |
| 345 | outlet.step | 3.29K |
| 346 | outlet.stl | 16.84K |
| 347 | wall1.step | 15.38K |
| 348 | wall1.stl | 928.55K |
| 349 | inlet.step | 3.22K |
| 350 | inlet.stl | 16.84K |
| 351 | outlet.step | 3.29K |
| 352 | outlet.stl | 16.84K |
| 353 | wall1.step | 13.44K |
| 354 | wall1.stl | 928.55K |
| 355 | wall2.step | 2.11M |
| 356 | wall2.stl | 596.26K |
| 357 | Risksystem环境风险评价.docx | 10.04M |
| 358 | Risksystem环境风险评价.pdf | 4.13M |
| 359 | Thumbs.db | 15.50K |
| 360 | MMA液体泄漏量计算.png | 133.73K |
| 361 | MMA液体泄漏量计算.rsm | 118B |
| 362 | Thumbs.db | 8.00K |
| 363 | MMA池火事故模型预测.png | 122.72K |
| 364 | MMA池火事故模型预测.rsm | 215B |
| 365 | MMA池火事故模型预测2.png | 104.65K |
| 366 | MMA池火事故模型预测3.png | 65.14K |
| 367 | MMA池火事故模型预测4.png | 124.11K |
| 368 | MMA池火事故模型预测5.png | 68.84K |
| 369 | Thumbs.db | 18.00K |
| 370 | MMA沸腾液体扩展蒸汽爆炸.rsm | 227B |
| 371 | MMA沸腾液体扩展蒸汽爆炸1.png | 110.29K |
| 372 | MMA沸腾液体扩展蒸汽爆炸2.png | 107.69K |
| 373 | MMA沸腾液体扩展蒸汽爆炸3.png | 84.95K |
| 374 | MMA沸腾液体扩展蒸汽爆炸4.png | 105.98K |
| 375 | MMA沸腾液体扩展蒸汽爆炸5.png | 218.91K |
| 376 | Thumbs.db | 7.00K |
| 377 | MMA蒸汽云爆炸模型预测.rsm | 189B |
| 378 | MMA蒸汽云爆炸模型预测1.png | 97.27K |
| 379 | MMA蒸汽云爆炸模型预测2.png | 106.98K |
| 380 | MMA蒸汽云爆炸模型预测3.png | 57.98K |
| 381 | MMA蒸汽云爆炸模型预测4.png | 83.03K |
| 382 | MMA蒸汽云爆炸模型预测5.png | 210.65K |
| 383 | MMA在大气中扩散预测.rsm | 521B |
| 384 | MMA在大气中扩散预测1.png | 115.14K |
| 385 | MMA在大气中扩散预测2.png | 152.11K |
| 386 | MMA在大气中扩散预测3.png | 134.43K |
| 387 | MMA在大气中扩散预测4.png | 157.58K |
| 388 | MMA在大气中扩散预测5.png | 216.15K |
| 389 | MMA在大气中扩散预测6.png | 91.29K |
| 390 | MMA在大气中扩散预测7.png | 82.54K |
| 391 | MMA典型泄露事故模拟.rsm | 546B |
| 392 | MMA典型泄露事故模拟1.png | 231.77K |
| 393 | MMA典型泄露事故模拟2.png | 165.46K |
| 394 | MMA典型泄露事故模拟3.png | 141.71K |
| 395 | MMA典型泄露事故模拟4.png | 160.48K |
| 396 | MMA典型泄露事故模拟5.png | 554.91K |
| 397 | MMA典型泄露事故模拟6.png | 233.20K |
| 398 | MMA典型泄露事故模拟7.png | 85.46K |
| 399 | MMA典型泄露事故模拟8.png | 78.33K |
| 400 | 甲醇液体泄漏量计算.png | 137.58K |
| 401 | 甲醇液体泄漏量计算.rsm | 107B |
| 402 | 甲醇池火事故模型预测.png | 117.84K |
| 403 | 甲醇池火事故模型预测.rsm | 200B |
| 404 | 甲醇池火事故模型预测2.png | 102.33K |
| 405 | 甲醇池火事故模型预测3.png | 64.38K |
| 406 | 甲醇池火事故模型预测4.png | 111.38K |
| 407 | 甲醇池火事故模型预测5.png | 211.46K |
| 408 | 甲醇沸腾液体扩展蒸汽爆炸.rsm | 207B |
| 409 | 甲醇沸腾液体扩展蒸汽爆炸1.png | 105.69K |
| 410 | 甲醇沸腾液体扩展蒸汽爆炸2.png | 107.59K |
| 411 | 甲醇沸腾液体扩展蒸汽爆炸3.png | 90.91K |
| 412 | 甲醇沸腾液体扩展蒸汽爆炸4.png | 97.11K |
| 413 | 甲醇沸腾液体扩展蒸汽爆炸5.png | 206.00K |
| 414 | 甲醇蒸汽云爆炸模型预测.rsm | 169B |
| 415 | 甲醇蒸汽云爆炸模型预测1.png | 93.64K |
| 416 | 甲醇蒸汽云爆炸模型预测2.png | 107.28K |
| 417 | 甲醇蒸汽云爆炸模型预测3.png | 58.77K |
| 418 | 甲醇蒸汽云爆炸模型预测4.png | 85.31K |
| 419 | 甲醇蒸汽云爆炸模型预测5.png | 208.58K |
| 420 | 甲醇在大气中的扩散预测.rsm | 491B |
| 421 | 甲醇在大气中的扩散预测1.png | 115.16K |
| 422 | 甲醇在大气中的扩散预测2.png | 162.25K |
| 423 | 甲醇在大气中的扩散预测3.png | 139.17K |
| 424 | 甲醇在大气中的扩散预测4.png | 160.46K |
| 425 | 甲醇在大气中的扩散预测5.png | 204.27K |
| 426 | 甲醇在大气中的扩散预测6.png | 89.15K |
| 427 | 甲醇在大气中的扩散预测7.png | 89.90K |
| 428 | 甲醇典型泄漏事故模拟.rsm | 506B |
| 429 | 甲醇典型泄漏事故模拟1.png | 225.99K |
| 430 | 甲醇典型泄漏事故模拟2.png | 166.09K |
| 431 | 甲醇典型泄漏事故模拟3.png | 135.74K |
| 432 | 甲醇典型泄漏事故模拟4.png | 203.61K |
| 433 | 甲醇典型泄漏事故模拟5.png | 685.54K |
| 434 | 甲醇典型泄漏事故模拟6.png | 196.52K |
| 435 | 甲醇典型泄漏事故模拟7.png | 85.36K |
| 436 | 甲醇典型泄漏事故模拟8.png | 84.25K |
| 437 | BLEVE.png | 81.22K |
| 438 | MMA储罐.alo | 4.73K |
| 439 | 有毒气体泄露.png | 82.12K |
| 440 | 池火.png | 87.77K |
| 441 | 甲醇储罐.alo | 4.73K |
| 442 | 储罐区火灾爆炸.ffta | 13.93K |
| 443 | 储罐区火灾爆炸.jpg | 84.17K |
| 444 | 反应器压力异常升高.ffta | 11.54K |
| 445 | 反应器压力异常升高.jpg | 62.69K |
| 446 | 反应器火灾爆炸.ffta | 23.97K |
| 447 | 反应器火灾爆炸.jpg | 195.36K |
| 448 | 管道完整性失效.ffta | 15.35K |
| 449 | 管道完整性失效.jpg | 89.50K |
| 450 | 罐区中毒事故.ffta | 11.80K |
| 451 | 罐区中毒事故.jpg | 62.38K |
| 452 | A计权声级分布.png | 187.92K |
| 453 | 噪声分布.png | 29.07K |
| 454 | 噪声级分布计算.ein | 2.65K |
| 455 | 工业噪声预测.ein | 2.30K |
| 456 | 工业噪声预测.png | 30.71K |
| 457 | 技术经济分析.xlsx | 111.73K |
| 458 | 0-摘要.doc | 5.71M |
| 459 | 1-可行性报告.doc | 6.94M |
| 460 | 2-初步设计说明书（含附录）.doc | 11.11M |
| 461 | 3-典型设备设计说明书（含设备选型一览表）.doc | 20.90M |
| 462 | 4-创新性说明书.doc | 4.89M |
| 463 | 5-安全预评价.doc | 4.81M |
| 464 | 6-环境影响评价报告.doc | 5.04M |
| 465 | 7-经济分析.doc | 6.17M |
| 466 | 8-Risksystem环境风险评价.doc | 11.09M |
| 467 | 1-Eureka-物料流程PFD图.dwg | 1.93M |
| 468 | 1-Eureka-物料流程PFD图.pdf | 6.75M |
| 469 | 2-Eureka-工艺管道及仪表流程PID图.dwg | 875.70K |
| 470 | 2-Eureka-工艺管道及仪表流程PID图.pdf | 2.95M |
| 471 | 3-Eureka-甲基丙烯酸甲酯合成及精制车间设备布置图.dwg | 611.12K |
| 472 | 3-Eureka-甲基丙烯酸甲酯合成及精制车间设备布置图.pdf | 2.54M |
| 473 | 4-Eureka-厂区总平面布置图.dwg | 368.80K |
| 474 | 4-Eureka-厂区总平面布置图.pdf | 1.87M |
| 475 | 5-设备条件图-循环甲醇冷却器E0405.dwg | 281.26K |
| 476 | 5-设备条件图-甲基丙烯醛反应器R0201.dwg | 382.52K |
| 477 | 5-设备条件图-甲基丙烯醛吸收塔T0202.dwg | 395.06K |
| 478 | 5-设备条件图.pdf | 2.29M |
| 479 | 6-Eureka-管道平立面图.dwg | 2.51M |
| 480 | 6-Eureka-管道平立面图.pdf | 2.78M |
| 481 | 7-Eureka-管道轴测图.dwg | 198.19K |
| 482 | 7-Eureka-管道轴测图.pdf | 1.71M |
| 483 | gbcbig.shx | 881.68K |
| 484 | readme.txt | 362B |
| 485 | 首页图册集.pdf | 13.26M |
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