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淮化24万吨年合成气制乙二醇项目初步设计（ID:2690399）
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| # | 文件名称 | 文件大小 |
|---|---|---|
| 1 | 17592317604183.zip | 136.65M |
| 2 | 1DesignSummary.doc | 1.22M |
| 3 | 1设计摘要.doc | 1.19M |
| 4 | 2可行性报告.doc | 2.67M |
| 5 | 3初步设计说明书.doc | 10.25M |
| 6 | 4创新性说明.doc | 595.50K |
| 7 | 5动态模拟与优化计算书-.doc | 2.44M |
| 8 | 6环境影响报告-.doc | 1.37M |
| 9 | 7设备一览表.doc | 531.00K |
| 10 | 8物料性质.doc | 756.00K |
| 11 | 9物料与能量平衡计算书.doc | 2.05M |
| 12 | 使用软件清单.txt | 483B |
| 13 | 设计图册.pdf | 11.50M |
| 14 | 乙二醇纯化工段厂区.png | 282.33K |
| 15 | 储罐区.png | 465.94K |
| 16 | 厂区全貌.png | 300.95K |
| 17 | 厂区车辆通道.png | 410.51K |
| 18 | 羰化车间.png | 474.28K |
| 19 | column2循环气回收塔T2012004.dwg | 2.95M |
| 20 | column2循环气回收塔T2012007.dwg | 3.31M |
| 21 | column2循环气回收塔T2032004.dwg | 2.94M |
| 22 | column2循环气回收塔T2032007.dwg | 3.33M |
| 23 | column2循环气回收塔T2042004.dwg | 2.93M |
| 24 | column2循环气回收塔T2042007.dwg | 3.30M |
| 25 | E-106冷却换热器2004.dwg | 276.23K |
| 26 | E-106冷却换热器2007.dwg | 307.78K |
| 27 | E-206冷却换热器2004.dwg | 328.44K |
| 28 | E-206冷却换热器2007.dwg | 356.69K |
| 29 | PFD图2004.dwg | 2.16M |
| 30 | PFD图2007.dwg | 2.10M |
| 31 | PID前工段2004.dwg | 2.93M |
| 32 | PID前工段2007.dwg | 3.01M |
| 33 | PID后工段2004.dwg | 2.34M |
| 34 | PID后工段2007.dwg | 2.36M |
| 35 | 轴测图2004.dwg | 548.38K |
| 36 | 轴测图2007.dwg | 564.69K |
| 37 | readme.txt | 185B |
| 38 | 乙二醇分离工段换热.hch | 240.08K |
| 39 | 亚硝酸甲酯再生换热优化.hch | 315.18K |
| 40 | 碳酸二甲酯和甲醇分离换热网络.hch | 208.05K |
| 41 | 草酸二甲酯加氢换热.hch | 212.67K |
| 42 | 草酸二甲酯合成分离换热网络.hch | 208.37K |
| 43 | aspen总流程换热网络.hch | 11.12M |
| 44 | 换热源文件.bkp | 927.08K |
| 45 | MN再生塔4bkp.bkp | 412.12K |
| 46 | MN再生塔4dyn.appdf | 465.33K |
| 47 | MN再生塔改进.dynf | 780.77K |
| 48 | mn再生塔4dyn.his | 2.70K |
| 49 | mn再生塔4dyn.rep | 0B |
| 50 | snapshot.bak | 2.15M |
| 51 | snpA0000.snp | 3.18M |
| 52 | snpA0001.snp | 4.22M |
| 53 | snpA0002.snp | 4.56M |
| 54 | snpA0003.snp | 2.79M |
| 55 | snpA0004.snp | 2.30M |
| 56 | snpA0005.snp | 4.91M |
| 57 | snpA0006.snp | 2.50M |
| 58 | snpA0007.snp | 2.50M |
| 59 | snpA0008.snp | 2.79M |
| 60 | snpA0009.snp | 4.55M |
| 61 | tasksnap.bak | 1.32K |
| 62 | mn再生塔4dyn.his | 2.70K |
| 63 | mn再生塔4dyn.rep | 0B |
| 64 | MN再生塔4.dynf | 781.36K |
| 65 | MN再生塔4dyn.appdf | 465.33K |
| 66 | fort.91 | 2.70K |
| 67 | mn再生塔4dyn.his | 2.70K |
| 68 | mn再生塔4dyn.rep | 0B |
| 69 | snapshot.bak | 4.92M |
| 70 | snpA0000.snp | 2.47M |
| 71 | snpA0001.snp | 2.15M |
| 72 | snpA0002.snp | 2.49M |
| 73 | snpA0003.snp | 2.49M |
| 74 | snpA0004.snp | 2.14M |
| 75 | snpA0005.snp | 2.14M |
| 76 | snpA0006.snp | 2.14M |
| 77 | snpA0007.snp | 2.83M |
| 78 | snpA0008.snp | 3.53M |
| 79 | snpA0009.snp | 2.49M |
| 80 | snpA0010.snp | 3.51M |
| 81 | tasksnap.bak | 9.59K |
| 82 | tasksnap.tsnp | 9.59K |
| 83 | DV型控制方案.appdf | 465.43K |
| 84 | 亚硝酸甲酯甲醇与水分离塔2.dynf | 551.32K |
| 85 | 亚硝酸甲酯甲醇与水分离塔dyn.appdf | 464.09K |
| 86 | 亚硝酸甲酯甲醇与水分离塔dyn2.appdf | 465.43K |
| 87 | snapshot.bak | 2.72M |
| 88 | snpA0000.snp | 1.59M |
| 89 | snpA0001.snp | 1.89M |
| 90 | tasksnap.bak | 3.37K |
| 91 | 亚硝酸甲酯甲醇与水分离塔dyn.his | 2.70K |
| 92 | 亚硝酸甲酯甲醇与水分离塔dyn.rep | 0B |
| 93 | LV型控制方案.appdf | 465.43K |
| 94 | LV型控制方案.dynf | 531.63K |
| 95 | 亚硝酸甲酯甲醇与水分离塔.bkp | 233.47K |
| 96 | snapshot.bak | 2.17M |
| 97 | snpA0000.snp | 1.89M |
| 98 | snpA0001.snp | 2.14M |
| 99 | snpA0002.snp | 2.14M |
| 100 | snpA0003.snp | 3.87M |
| 101 | snpA0004.snp | 3.85M |
| 102 | snpA0005.snp | 3.07M |
| 103 | tasksnap.bak | 2.33K |
| 104 | 亚硝酸甲酯甲醇与水分离塔dyn.his | 2.70K |
| 105 | 亚硝酸甲酯甲醇与水分离塔dyn.rep | 0B |
| 106 | 亚硝酸甲酯甲醇与水分离塔.bkp | 152.56K |
| 107 | 亚硝酸甲酯甲醇与水分离塔2.dynf | 563.75K |
| 108 | 亚硝酸甲酯甲醇与水分离塔dyn.appdf | 464.09K |
| 109 | 亚硝酸甲酯甲醇与水分离塔dyn2.appdf | 465.43K |
| 110 | AM_SAI.appdf | 465.38K |
| 111 | AspenAMLock.aml | 0B |
| 112 | dv浓度控制dyn.his | 2.70K |
| 113 | dv浓度控制dyn.rep | 0B |
| 114 | PlotData.cpd | 448.50K |
| 115 | snapshot.bak | 1.63M |
| 116 | snapshot.snp | 1.64M |
| 117 | snpA0000.snp | 1.89M |
| 118 | snpA0001.snp | 2.36M |
| 119 | snpA0002.snp | 1.93M |
| 120 | snpA0003.snp | 1.93M |
| 121 | snpA0004.snp | 2.69M |
| 122 | snpA0005.snp | 1.88M |
| 123 | snpA0006.snp | 1.59M |
| 124 | snpA0007.snp | 1.88M |
| 125 | snpA0008.snp | 2.18M |
| 126 | snpA0009.snp | 2.62M |
| 127 | snpA0010.snp | 3.50M |
| 128 | snpA0011.snp | 1.92M |
| 129 | snpA0012.snp | 2.11M |
| 130 | snpA0013.snp | 1.89M |
| 131 | snpA0014.snp | 1.89M |
| 132 | tasksnap.bak | 856B |
| 133 | tasksnap.tsnp | 856B |
| 134 | snapshot.bak | 2.74M |
| 135 | snpA0000.snp | 1.59M |
| 136 | snpA0001.snp | 1.59M |
| 137 | snpA0002.snp | 1.86M |
| 138 | snpA0003.snp | 1.88M |
| 139 | snpA0004.snp | 1.88M |
| 140 | snpA0005.snp | 1.86M |
| 141 | snpA0006.snp | 1.88M |
| 142 | snpA0007.snp | 1.88M |
| 143 | snpA0008.snp | 1.59M |
| 144 | snpA0009.snp | 1.59M |
| 145 | snpA0010.snp | 1.88M |
| 146 | snpA0011.snp | 1.86M |
| 147 | snpA0012.snp | 1.88M |
| 148 | snpA0013.snp | 1.88M |
| 149 | snpA0014.snp | 2.11M |
| 150 | snpA0015.snp | 2.11M |
| 151 | snpA0016.snp | 1.83M |
| 152 | tasksnap.bak | 3.35K |
| 153 | 亚硝酸甲酯甲醇与水分离塔dyn.his | 2.70K |
| 154 | 亚硝酸甲酯甲醇与水分离塔dyn.rep | 0B |
| 155 | 乙二醇提纯分离工段.bkp | 305.96K |
| 156 | 亚硝酸甲酯再生工段.bkp | 312.00K |
| 157 | 碳酸二甲酯与甲醇分离工段.bkp | 267.92K |
| 158 | 草酸二甲酯加氢工段.bkp | 226.57K |
| 159 | 草酸二甲酯合成分离工段.bkp | 456.06K |
| 160 | 总流程.bkp | 929.24K |
| 161 | 总流程优化版.bkp | 927.08K |
| 162 | 亚硝酸甲酯再生T101.bkp | 408.21K |
| 163 | 循环气回收塔column2.bkp | 291.74K |
| 164 | 甲醇与水分离塔.bkp | 242.63K |
| 165 | 甲醇回收塔.bkp | 240.81K |
| 166 | 碳酸二甲酯与甲醇分离加压塔.bkp | 249.30K |
| 167 | 碳酸二甲酯与甲醇分离常压塔.bkp | 256.40K |
| 168 | 脱轻组分塔.bkp | 242.52K |
| 169 | 草酸二甲酯与乙醇酸甲酯回收塔.bkp | 213.47K |
| 170 | 草酸二甲酯分离精馏塔.bkp | 272.47K |
| 171 | 草酸二甲酯合成产物冷凝吸收塔.bkp | 271.30K |
| 172 | C.xls | 18.00K |
| 173 | DCPCENTRIF.xls | 17.00K |
| 174 | DGCCENTRIF.xls | 14.50K |
| 175 | DHEFLOATHEAD.xls | 16.50K |
| 176 | DHTHORIZDRUM.xls | 16.00K |
| 177 | DRBUTUBE.xls | 19.00K |
| 178 | DTWTRAYED.xls | 18.00K |
| 179 | DVTCYLINDER.xls | 15.00K |
| 180 | Equipment.xls | 22.00K |
| 181 | IPEWB1.xls | 214.50K |
| 182 | IPEWB_TRA.XLS | 22.50K |
| 183 | RESULTS.xls | 873.50K |
| 184 | SPECS.xls | 3.25M |
| 185 | 经济分析总流程.bkp | 930.02K |
| 186 | cashflow.ics | 284.89K |
| 187 | cashflow.ict | 990.98K |
| 188 | CURRENCY.DAT | 8.20K |
| 189 | DESIGN.d01 | 52.10K |
| 190 | DESIGN.d02 | 10.23K |
| 191 | DESIGN.d03 | 72.81K |
| 192 | DESIGN.d04 | 16.80K |
| 193 | DESIGN.d05 | 36B |
| 194 | equip.ict | 38.15K |
| 195 | execsum.ics | 9.03K |
| 196 | execsum.ict | 7.36K |
| 197 | INV.d01 | 1.24K |
| 198 | INV.d02 | 10.55K |
| 199 | INV.d03 | 5.02K |
| 200 | INV.d04 | 4.98K |
| 201 | INV.d05 | 36B |
| 202 | ipeproc.d01 | 438B |
| 203 | ipeproc.d02 | 166B |
| 204 | ipeproc.d03 | 5.02K |
| 205 | ipeproc.d04 | 4.98K |
| 206 | ipeproc.d05 | 36B |
| 207 | ipeproj.d01 | 714B |
| 208 | ipeproj.d02 | 748B |
| 209 | ipeproj.d03 | 5.02K |
| 210 | ipeproj.d04 | 4.98K |
| 211 | ipeproj.d05 | 36B |
| 212 | IPSUNTUN.d01 | 852B |
| 213 | IPSUNTUN.d02 | 341B |
| 214 | IPSUNTUN.d03 | 5.02K |
| 215 | IPSUNTUN.d04 | 4.98K |
| 216 | IPSUNTUN.d05 | 36B |
| 217 | map.d01 | 1.10K |
| 218 | map.d02 | 7.42K |
| 219 | map.d03 | 5.02K |
| 220 | map.d04 | 20.74K |
| 221 | map.d05 | 36B |
| 222 | OP.d01 | 714B |
| 223 | OP.d02 | 2.37K |
| 224 | OP.d03 | 5.02K |
| 225 | OP.d04 | 4.98K |
| 226 | OP.d05 | 36B |
| 227 | PFDDIG.d01 | 438B |
| 228 | PFDDIG.d02 | 166B |
| 229 | PFDDIG.d03 | 5.02K |
| 230 | PFDDIG.d04 | 4.98K |
| 231 | PFDDIG.d05 | 36B |
| 232 | proc.d01 | 2.72K |
| 233 | proc.d02 | 1.59K |
| 234 | proc.d03 | 5.02K |
| 235 | proc.d04 | 4.98K |
| 236 | proc.d05 | 36B |
| 237 | procAZ.d01 | 990B |
| 238 | procAZ.d02 | 268B |
| 239 | procAZ.d03 | 5.02K |
| 240 | procAZ.d04 | 4.98K |
| 241 | procAZ.d05 | 36B |
| 242 | PROCCN.d01 | 438B |
| 243 | PROCCN.d02 | 166B |
| 244 | PROCCN.d03 | 5.02K |
| 245 | PROCCN.d04 | 4.98K |
| 246 | PROCCN.d05 | 36B |
| 247 | ProcessTemplateProject.KBW | 43B |
| 248 | PROD.d01 | 1.51K |
| 249 | PROD.d02 | 6.81K |
| 250 | PROD.d03 | 5.02K |
| 251 | PROD.d04 | 4.98K |
| 252 | PROD.d05 | 36B |
| 253 | ProdRes.txt | 127B |
| 254 | proj.d01 | 1.78K |
| 255 | proj.d02 | 1.29K |
| 256 | proj.d03 | 5.02K |
| 257 | proj.d04 | 4.98K |
| 258 | proj.d05 | 36B |
| 259 | projinfo.d01 | 714B |
| 260 | projinfo.d02 | 1.93K |
| 261 | projinfo.d03 | 5.02K |
| 262 | projinfo.d04 | 4.98K |
| 263 | projinfo.d05 | 36B |
| 264 | PROJL.d01 | 438B |
| 265 | PROJL.d02 | 166B |
| 266 | PROJL.d03 | 5.02K |
| 267 | PROJL.d04 | 4.98K |
| 268 | PROJL.d05 | 36B |
| 269 | projmap.d01 | 852B |
| 270 | projmap.d02 | 166B |
| 271 | projmap.d03 | 5.02K |
| 272 | projmap.d04 | 4.98K |
| 273 | projmap.d05 | 36B |
| 274 | PROJNAZ.d01 | 438B |
| 275 | PROJNAZ.d02 | 166B |
| 276 | PROJNAZ.d03 | 5.02K |
| 277 | PROJNAZ.d04 | 4.98K |
| 278 | PROJNAZ.d05 | 36B |
| 279 | PROJNBD.d01 | 438B |
| 280 | PROJNBD.d02 | 166B |
| 281 | PROJNBD.d03 | 5.02K |
| 282 | PROJNBD.d04 | 4.98K |
| 283 | PROJNBD.d05 | 36B |
| 284 | PROJNBG.d01 | 438B |
| 285 | PROJNBG.d02 | 166B |
| 286 | PROJNBG.d03 | 5.02K |
| 287 | PROJNBG.d04 | 4.98K |
| 288 | PROJNBG.d05 | 36B |
| 289 | PROJNBI.d01 | 438B |
| 290 | PROJNBI.d02 | 166B |
| 291 | PROJNBI.d03 | 5.02K |
| 292 | PROJNBI.d04 | 4.98K |
| 293 | PROJNBI.d05 | 36B |
| 294 | PROJNBM.d01 | 438B |
| 295 | PROJNBM.d02 | 166B |
| 296 | PROJNBM.d03 | 5.02K |
| 297 | PROJNBM.d04 | 4.98K |
| 298 | PROJNBM.d05 | 36B |
| 299 | PROJNBP.d01 | 438B |
| 300 | PROJNBP.d02 | 166B |
| 301 | PROJNBP.d03 | 5.02K |
| 302 | PROJNBP.d04 | 4.98K |
| 303 | PROJNBP.d05 | 36B |
| 304 | PROJNCN.d01 | 438B |
| 305 | PROJNCN.d02 | 166B |
| 306 | PROJNCN.d03 | 5.02K |
| 307 | PROJNCN.d04 | 4.98K |
| 308 | PROJNCN.d05 | 36B |
| 309 | PROJP.d01 | 438B |
| 310 | PROJP.d02 | 166B |
| 311 | PROJP.d03 | 5.02K |
| 312 | PROJP.d04 | 4.98K |
| 313 | PROJP.d05 | 36B |
| 314 | PROJSUM.ICS | 28.64K |
| 315 | projsum.ict | 232.10K |
| 316 | RAW.d01 | 1.51K |
| 317 | RAW.d02 | 6.74K |
| 318 | RAW.d03 | 5.02K |
| 319 | RAW.d04 | 4.98K |
| 320 | RAW.d05 | 36B |
| 321 | RawRes.txt | 132B |
| 322 | REP_GEN.d01 | 438B |
| 323 | REP_GEN.d02 | 166B |
| 324 | REP_GEN.d03 | 5.02K |
| 325 | REP_GEN.d04 | 4.98K |
| 326 | REP_GEN.d05 | 36B |
| 327 | Scenario1.izp | 2.10M |
| 328 | Scenario1.szp | 2.60M |
| 329 | SCHD.d01 | 162B |
| 330 | SCHD.d02 | 77B |
| 331 | SCHD.d03 | 5.02K |
| 332 | SCHD.d04 | 4.98K |
| 333 | SCHD.d05 | 36B |
| 334 | STD.d01 | 9.73K |
| 335 | STD.d02 | 21.65K |
| 336 | STD.d03 | 20.97K |
| 337 | STD.d04 | 20.74K |
| 338 | STD.d05 | 36B |
| 339 | US_MET.KBW | 46B |
| 340 | US_Metric.KBW | 28B |
| 341 | UTILITY.d01 | 3.26K |
| 342 | UTILITY.d02 | 17.76K |
| 343 | UTILITY.d03 | 5.02K |
| 344 | UTILITY.d04 | 28.62K |
| 345 | UTILITY.d05 | 36B |
| 346 | HEAT01.dxf | 91.95K |
| 347 | HEAT01.EDR | 380.24K |
| 348 | HEAT01.XLS | 183.00K |
| 349 | HEAT01中文版.XLS | 154.00K |
| 350 | HTFSGraphicalOutput.tif | 26.92K |
| 351 | HTFSGraphicalOutput2.TIF | 20.46K |
| 352 | 换热器01.bkp | 188.64K |
| 353 | HEAT02.EDR | 405.11K |
| 354 | HEAT02.XLS | 164.00K |
| 355 | HEAT02中文版.XLS | 154.00K |
| 356 | HTFSGraphicalOutput.tif | 20.56K |
| 357 | HTFSGraphicalOutput1.TIF | 39.42K |
| 358 | 换热器02.bkp | 187.97K |
| 359 | 换热器02.dxf | 84.36K |
| 360 | 换热器设计02tubesheetlayout.dxf | 91.08K |
| 361 | HEAT03.EDR | 436.74K |
| 362 | HEAT03.XLS | 179.00K |
| 363 | HEAT03中文版.XLS | 154.00K |
| 364 | HTFSGraphicalOutput.tif | 20.32K |
| 365 | HTFSGraphicalOutput1.TIF | 44.50K |
| 366 | 换热器03.bkp | 187.43K |
| 367 | HEAT04.EDR | 467.44K |
| 368 | HEAT04.XLS | 178.50K |
| 369 | HEAT04中文版.XLS | 157.00K |
| 370 | HTFSGraphicalOutput.tif | 20.58K |
| 371 | HTFSGraphicalOutput1.TIF | 75.71K |
| 372 | 换热器04.bkp | 188.40K |
| 373 | heat05.dxf | 90.48K |
| 374 | HEAT05.EDR | 355.93K |
| 375 | HEAT05.XLS | 178.50K |
| 376 | HEAT05中文版.XLS | 154.00K |
| 377 | HTFSGraphicalOutput.tif | 20.41K |
| 378 | HTFSGraphicalOutput1.TIF | 42.08K |
| 379 | 换热器05.bkp | 186.77K |
| 380 | HEAT06.EDR | 396.55K |
| 381 | HEAT06.XLS | 178.50K |
| 382 | HEAT06中文版.XLS | 154.00K |
| 383 | HTFSGraphicalOutput.tif | 20.87K |
| 384 | HTFSGraphicalOutput1.TIF | 53.41K |
| 385 | 换热器06.bkp | 187.21K |
| 386 | column2循环气回收塔T2012004.dwg | 2.95M |
| 387 | column2循环气回收塔T2012007.dwg | 3.31M |
| 388 | E-206冷却换热器2004.dwg | 328.44K |
| 389 | E-206冷却换热器2007.dwg | 356.69K |
| 390 | PFD图2004.dwg | 2.12M |
| 391 | PFD图2007.dwg | 2.04M |
| 392 | PID前工段2004.dwg | 2.83M |
| 393 | PID前工段2007.dwg | 7.98M |
| 394 | PID后工段2004.dwg | 2.32M |
| 395 | PID后工段2007.dwg | 2.34M |
| 396 | 轴测图2004.dwg | 546.97K |
| 397 | 轴测图2007.dwg | 560.94K |
| 398 | Plant3D乙二醇纯化车间源文件.dwg | 1.36M |
| 399 | Plant3D加氢车间源文件.dwg | 1.50M |
| 400 | Plant3D羰化车间源文件.dwg | 5.44M |
| 401 | Plant3D酯化车间源文件.dwg | 1.23M |
| 402 | 乙二醇纯化车间平面布置图.dwg | 1.26M |
| 403 | 厂区平面图.dwg | 466.03K |
| 404 | 羰化车间平面布置图.bak | 1.26M |
| 405 | 羰化车间平面布置图.dwg | 1.26M |
| 406 | 乙二醇纯化车间平面布置图.dwg | 1.31M |
| 407 | 厂区平面图.bak | 501.63K |
| 408 | 厂区平面图.dwg | 501.13K |
| 409 | 羰化车间平面布置图.dwg | 1.31M |
| 410 | 乙二醇纯化车间平面布置图.dwg | 1.26M |
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| 412 | 羰化车间平面布置图.dwg | 2.29M |
| 413 | CO101.dwg | 160.47K |
| 414 | DMO101-1-1.dwg | 138.53K |
| 415 | DMO101-2.dwg | 88.06K |
| 416 | DMO101-3.dwg | 114.05K |
| 417 | DMO101-4-1.dwg | 96.48K |
| 418 | DMO101-4-2.dwg | 99.00K |
| 419 | G102-2-1.dwg | 111.95K |
| 420 | G103-1.dwg | 94.97K |
| 421 | G104-1-1.dwg | 91.06K |
| 422 | G104-2.dwg | 117.04K |
| 423 | G105-1.dwg | 107.16K |
| 424 | G105-2.dwg | 107.25K |
| 425 | L103-2.dwg | 127.95K |
| 426 | L103-3-2.dwg | 136.87K |
| 427 | L103-4-1.dwg | 128.08K |
| 428 | L104-1-1.dwg | 131.21K |
| 429 | L104-2-1.dwg | 121.23K |
| 430 | L104-2-2.dwg | 135.49K |
| 431 | L104-3-1.dwg | 122.38K |
| 432 | L105-1-1.dwg | 129.18K |
| 433 | L105-1-2.dwg | 110.79K |
| 434 | L105-2.dwg | 95.94K |
| 435 | L105-3.dwg | 128.62K |
| 436 | CO101.dwg | 188.28K |
| 437 | DMO101-1-1.dwg | 167.38K |
| 438 | DMO101-2.dwg | 115.03K |
| 439 | DMO101-3.dwg | 143.19K |
| 440 | DMO101-4-1.dwg | 124.03K |
| 441 | DMO101-4-2.dwg | 126.53K |
| 442 | G101-3.dwg | 146.06K |
| 443 | G102-2-1.dwg | 141.81K |
| 444 | G103-1.dwg | 123.84K |
| 445 | G104-1-1.dwg | 120.88K |
| 446 | G104-2.dwg | 146.56K |
| 447 | G105-1.dwg | 137.56K |
| 448 | G105-2.dwg | 136.59K |
| 449 | L103-2.dwg | 139.06K |
| 450 | L103-3-2.dwg | 168.47K |
| 451 | L103-4-1.dwg | 158.75K |
| 452 | L104-1-1.dwg | 163.75K |
| 453 | L104-2-1.dwg | 152.06K |
| 454 | L104-2-2.dwg | 167.47K |
| 455 | L104-3-1.dwg | 152.78K |
| 456 | L105-1-1.dwg | 159.00K |
| 457 | L105-1-2.dwg | 141.06K |
| 458 | L105-2.dwg | 127.34K |
| 459 | L105-3.dwg | 158.25K |
| 460 | CO101.dwg | 150.80K |
| 461 | DMO101-1-1.dwg | 124.20K |
| 462 | DMO101-2.dwg | 99.17K |
| 463 | DMO101-3.dwg | 99.12K |
| 464 | DMO101-4-1.dwg | 127.54K |
| 465 | DMO101-4-2.dwg | 132.08K |
| 466 | G101-3.dwg | 95.80K |
| 467 | G102-2-1.dwg | 93.03K |
| 468 | G103-1.dwg | 98.50K |
| 469 | G104-1-1.dwg | 93.55K |
| 470 | G104-2.dwg | 97.46K |
| 471 | G105-1.dwg | 87.70K |
| 472 | G105-2.dwg | 87.76K |
| 473 | L103-2.dwg | 89.71K |
| 474 | L103-3-2.dwg | 120.04K |
| 475 | L103-4-1.dwg | 109.07K |
| 476 | L104-1-1.dwg | 115.07K |
| 477 | L104-2-1.dwg | 103.03K |
| 478 | L104-2-2.dwg | 118.26K |
| 479 | L104-3-1.dwg | 105.41K |
| 480 | L105-1-1.dwg | 111.66K |
| 481 | L105-1-2.dwg | 92.93K |
| 482 | L105-2.dwg | 79.99K |
| 483 | L105-3.dwg | 110.35K |
| 484 | B4-T101.doc | 233.00K |
| 485 | B4-T101.xls | 61.00K |
| 486 | B4101（填料塔）-T101.xls | 30.00K |
| 487 | B4填料塔-T101.CPR | 211B |
| 488 | T101.plc | 196.00K |
| 489 | 亚硝酸甲酯结束后的甲醇精馏塔T101.xlsx | 12.17K |
| 490 | 浮阀设计_亚硝酸甲酯结束后的甲醇精馏塔T101：（实际板号：2＃—14＃）.xls | 186.00K |
| 491 | T102.plc | 204.00K |
| 492 | T102.xlsx | 14.78K |
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| 495 | B4-T201.xls | 61.00K |
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| 497 | B4填料塔-T201.CPR | 211B |
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| 499 | T201.plc | 200.00K |
| 500 | 浮阀设计_column2循环气回收塔T201：（实际板号：1＃—35＃）.xls | 179.50K |
| 501 | T202.plc | 204.00K |
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| 503 | 亚硝酸甲酯结束后的甲醇精馏塔T202.xlsx | 12.17K |
| 504 | 浮阀设计_DMO分离精馏T202：（实际板号：1＃—30＃）.xls | 186.50K |
| 505 | 浮阀设计_亚硝酸甲酯结束后的甲醇精馏塔T202：（实际板号：2＃—14＃）.xls | 186.00K |
| 506 | column2循环气回收塔T203.xls | 30.50K |
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| 508 | 浮阀设计_column2循环气回收塔T203：（实际板号：1＃—35＃）.xls | 179.50K |
| 509 | 碳酸二甲酯与甲醇分离常压塔.doc | 233.00K |
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| 512 | T302.plc | 200.00K |
| 513 | T302水利数据.xls | 26.00K |
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| 517 | 甲醇回收塔T501.plc | 200.00K |
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| 523 | 草酸二甲酯与乙醇酸甲酯负荷性能图.dot | 233.00K |
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| 526 | 甲醇有毒有害气体物质在大气中扩散预测源文件.rsm | 495B |
| 527 | 对二甲苯两相流泄漏量计算.rsm | 104B |
| 528 | 对二甲苯气体泄漏量计算.rsm | 79B |
| 529 | 对二甲苯液体泄漏量计算.rsm | 118B |
| 530 | 对二甲苯热量蒸发量计算.rsm | 58B |
| 531 | 对二甲苯质量蒸发量计算.rsm | 65B |
| 532 | 对二甲苯闪蒸量计算.rsm | 66B |
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| 534 | 甲醇气体泄漏量计算源文件.rsm | 77B |
| 535 | 甲醇液体泄漏量计算源文件.rsm | 111B |
| 536 | 甲醇热量蒸发量计算源文件.rsm | 51B |
| 537 | 甲醇质量蒸发量计算源文件.rsm | 65B |
| 538 | 甲醇闪蒸量计算源文件.rsm | 57B |
| 539 | 甲醇池火事故模型预测源文件.rsm | 322B |
| 540 | 甲醇沸腾液体扩散蒸汽爆炸模型预测源文件.rsm | 228B |
| 541 | 甲醇蒸气云爆炸模型预测源文件.rsm | 196B |
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| 574 | T202.cn2 | 30.20K |
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| 598 | V401下封头.docx | 30.60K |
| 599 | V401筒体.docx | 28.46K |
| 600 | 厂区3D布置.max | 628.00M |
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