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氧气直接氧化法年产30万吨环氧丙烷项目初步设计（ID:2689395）
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| # | 文件名称 | 文件大小 |
|---|---|---|
| 1 | 17592041166696.zip | 252.99M |
| 2 | 1-Summary.doc | 805.00K |
| 3 | 2-摘要.doc | 782.50K |
| 4 | 3-可行性研究报告.doc | 2.86M |
| 5 | 4-初步设计说明书.doc | 8.26M |
| 6 | 5-设计附录.doc | 10.75M |
| 7 | 6-能源评价.doc | 1.11M |
| 8 | 7-安全评价.doc | 1.35M |
| 9 | 8-环境影响评价.doc | 2.29M |
| 10 | 9-海之翼创新性说明.doc | 1.50M |
| 11 | 海之翼创新性说明.pdf | 956.67K |
| 12 | 1-可行性研究报告.jpg | 904.06K |
| 13 | 2-初步设计说明书.jpg | 918.54K |
| 14 | 3-环境影响评价.jpg | 922.55K |
| 15 | 4-安全评价.jpg | 893.90K |
| 16 | 5-能源评价.jpg | 893.35K |
| 17 | 6-附录.jpg | 895.55K |
| 18 | 7-创新性说明.jpg | 905.37K |
| 19 | 8-设计图册.jpg | 890.12K |
| 20 | 设计图册.pdf | 42.27M |
| 21 | 1-丙烯储罐.dwg | 40.98K |
| 22 | 2-乙醇储罐.dwg | 41.54K |
| 23 | 3-环氧丙烷储罐.dwg | 41.11K |
| 24 | 反应车间.dwg | 108.49K |
| 25 | 1-产品精制.dwg | 103.93K |
| 26 | 2-气液分离.dwg | 79.38K |
| 27 | 3-反应精馏塔.dwg | 74.03K |
| 28 | 1-丙烯储罐PID图.dwg | 70.06K |
| 29 | 2-环氧丙烷PID图.dwg | 74.50K |
| 30 | 3-乙醇储罐PID图.dwg | 69.46K |
| 31 | 填料塔反应器-1.dwg | 76.50K |
| 32 | 填料塔反应器-2.dwg | 76.60K |
| 33 | 填料塔反应器-3.dwg | 76.53K |
| 34 | 填料塔反应器-4.dwg | 76.60K |
| 35 | 填料塔反应器-56.dwg | 83.51K |
| 36 | 1-闪蒸罐.dwg | 100.92K |
| 37 | 2-脱丙烯塔.dwg | 96.89K |
| 38 | 3-脱环氧丙烷塔.dwg | 99.02K |
| 39 | 4-环氧丙烷精制塔.dwg | 125.40K |
| 40 | 5-多股进料塔.dwg | 113.42K |
| 41 | 6-丙烯醛脱水塔.dwg | 95.38K |
| 42 | 7-反应精馏塔.dwg | 101.27K |
| 43 | 1-反应车间EL0.00.dwg | 184.52K |
| 44 | 2-反应车间EL6.00.dwg | 84.28K |
| 45 | 3-反应车间主视图.dwg | 178.03K |
| 46 | 4-分离车间EL0.00.dwg | 198.30K |
| 47 | 5-分离车间EL6.00.dwg | 101.75K |
| 48 | 6-分离车间EL12.00.dwg | 88.23K |
| 49 | 7-分离车间主视图.dwg | 136.32K |
| 50 | 分离车间.dwg | 16.87M |
| 51 | 反应车间.dwg | 10.96M |
| 52 | acad.fas | 15.20K |
| 53 | 分离车间0001.dwg | 132.78K |
| 54 | 分离车间0002.DWG | 206.03K |
| 55 | 分离车间0003.DWG | 251.88K |
| 56 | 分离车间0004.DWG | 249.38K |
| 57 | 分离车间0005.DWG | 436.53K |
| 58 | 分离车间0006.DWG | 147.97K |
| 59 | 分离车间0007.DWG | 195.84K |
| 60 | 分离车间0008.DWG | 178.88K |
| 61 | 分离车间0009.DWG | 206.28K |
| 62 | 分离车间0010.DWG | 116.09K |
| 63 | 分离车间0011.DWG | 204.53K |
| 64 | 分离车间0012.DWG | 201.81K |
| 65 | 分离车间0013.DWG | 206.31K |
| 66 | 分离车间0014.dwg | 400.63K |
| 67 | 反应车间0001.DWG | 234.72K |
| 68 | 反应车间0002.DWG | 106.59K |
| 69 | 反应车间0003.DWG | 209.78K |
| 70 | 反应车间0004.DWG | 278.03K |
| 71 | 反应车间0005.DWG | 203.81K |
| 72 | 反应车间0006.DWG | 223.22K |
| 73 | 反应车间0007.DWG | 260.81K |
| 74 | 反应车间0008.DWG | 392.69K |
| 75 | 反应车间0009.DWG | 149.25K |
| 76 | 反应车间0010.DWG | 147.22K |
| 77 | 反应车间0011.dwg | 246.38K |
| 78 | 1-填料塔反应器.dwg | 279.67K |
| 79 | 2-板式塔.dwg | 233.35K |
| 80 | 3-换热器.dwg | 175.31K |
| 81 | 4-反应精馏塔.dwg | 118.92K |
| 82 | 厂区分布总图.dwg | 214.03K |
| 83 | 1.jpg | 53.58K |
| 84 | 10.jpg | 43.63K |
| 85 | 11.jpg | 51.80K |
| 86 | 12.jpg | 50.95K |
| 87 | 13.jpg | 43.36K |
| 88 | 14.jpg | 57.90K |
| 89 | 2.jpg | 53.58K |
| 90 | 3.jpg | 55.91K |
| 91 | 4.jpg | 55.91K |
| 92 | 5.jpg | 52.87K |
| 93 | 6.jpg | 52.87K |
| 94 | 7.jpg | 45.64K |
| 95 | 8.jpg | 45.64K |
| 96 | 9.jpg | 42.85K |
| 97 | 图例1.dwg | 43.58K |
| 98 | 图例2.dwg | 34.36K |
| 99 | 图例3.dwg | 39.36K |
| 100 | 流程方框图.dwg | 29.38K |
| 101 | 1-丙烯储罐.bak | 56.94K |
| 102 | 1-丙烯储罐.dwg | 41.95K |
| 103 | 2-乙醇储罐.bak | 41.54K |
| 104 | 2-乙醇储罐.dwg | 41.48K |
| 105 | 3-环氧丙烷储罐.bak | 41.11K |
| 106 | 3-环氧丙烷储罐.dwg | 41.23K |
| 107 | acaddoc.lsp | 3.13M |
| 108 | plot.log | 914B |
| 109 | acad.vlx | 2.93K |
| 110 | acaddoc.lsp | 3.13M |
| 111 | plot.log | 365B |
| 112 | 反应车间.bak | 138.65K |
| 113 | 反应车间.dwg | 138.65K |
| 114 | 1-产品精制.bak | 160.11K |
| 115 | 1-产品精制.dwg | 160.11K |
| 116 | 2-气液分离.bak | 131.15K |
| 117 | 2-气液分离.dwg | 131.21K |
| 118 | 3-反应精馏塔.bak | 99.91K |
| 119 | 3-反应精馏塔.dwg | 99.91K |
| 120 | acad.vlx | 2.93K |
| 121 | acaddoc.lsp | 3.13M |
| 122 | 1-丙烯储罐PID图.bak | 90.44K |
| 123 | 1-丙烯储罐PID图.dwg | 75.31K |
| 124 | 2-环氧丙烷PID图.bak | 95.91K |
| 125 | 2-环氧丙烷PID图.dwg | 81.06K |
| 126 | 3-乙醇储罐PID图.bak | 74.78K |
| 127 | 3-乙醇储罐PID图.dwg | 74.81K |
| 128 | acad.vlx | 2.93K |
| 129 | acaddoc.lsp | 3.13M |
| 130 | acad.vlx | 2.93K |
| 131 | acaddoc.lsp | 2.38M |
| 132 | plot.log | 865B |
| 133 | 填料塔反应器-1.bak | 114.19K |
| 134 | 填料塔反应器-1.dwg | 80.09K |
| 135 | 填料塔反应器-2.bak | 95.06K |
| 136 | 填料塔反应器-2.dwg | 76.41K |
| 137 | 填料塔反应器-3.bak | 91.09K |
| 138 | 填料塔反应器-3.dwg | 76.41K |
| 139 | 填料塔反应器-4.bak | 94.56K |
| 140 | 填料塔反应器-4.dwg | 76.44K |
| 141 | 填料塔反应器-56.bak | 103.78K |
| 142 | 填料塔反应器-56.dwg | 83.51K |
| 143 | 1-闪蒸罐.bak | 131.22K |
| 144 | 1-闪蒸罐.dwg | 109.11K |
| 145 | 2-脱丙烯塔.bak | 96.73K |
| 146 | 2-脱丙烯塔.dwg | 96.76K |
| 147 | 3-脱环氧丙烷塔.bak | 137.06K |
| 148 | 3-脱环氧丙烷塔.dwg | 98.04K |
| 149 | 4-环氧丙烷精制塔.bak | 161.72K |
| 150 | 4-环氧丙烷精制塔.dwg | 134.50K |
| 151 | 5-多股进料塔.bak | 165.84K |
| 152 | 5-多股进料塔.dwg | 121.49K |
| 153 | 6-丙烯醛脱水塔.bak | 127.31K |
| 154 | 6-丙烯醛脱水塔.dwg | 95.42K |
| 155 | 7-反应精馏塔.bak | 118.13K |
| 156 | 7-反应精馏塔.dwg | 119.13K |
| 157 | plot.log | 1.51K |
| 158 | 1.pdf | 27.06K |
| 159 | 2.pdf | 34.92K |
| 160 | 3.pdf | 55.05K |
| 161 | 4.pdf | 35.22K |
| 162 | 5.pdf | 35.62K |
| 163 | 6.pdf | 41.47K |
| 164 | 7.pdf | 40.95K |
| 165 | 8.pdf | 34.03K |
| 166 | 9.pdf | 36.85K |
| 167 | 1-反应车间EL0.00.dwg | 184.52K |
| 168 | 2-反应车间EL6.00.dwg | 84.28K |
| 169 | 3-反应车间主视图.dwg | 178.03K |
| 170 | 4-分离车间EL0.00.dwg | 198.30K |
| 171 | 5-分离车间EL6.00.dwg | 101.75K |
| 172 | 6-分离车间EL12.00.dwg | 88.23K |
| 173 | 7-分离车间主视图.dwg | 136.32K |
| 174 | 低温余热发电.bak | 51.56K |
| 175 | 低温余热发电.dwg | 68.50K |
| 176 | 氨吸收式制冷.bak | 75.50K |
| 177 | 氨吸收式制冷.dwg | 75.50K |
| 178 | 1-填料塔反应器.bak | 264.75K |
| 179 | 1-填料塔反应器.dwg | 264.75K |
| 180 | 2-板式塔.bak | 312.34K |
| 181 | 2-板式塔.dwg | 312.84K |
| 182 | 3-换热器.bak | 204.69K |
| 183 | 3-换热器.dwg | 204.69K |
| 184 | 4-反应精馏塔.bak | 135.56K |
| 185 | 4-反应精馏塔.dwg | 152.28K |
| 186 | 图例1.bak | 58.44K |
| 187 | 图例1.dwg | 58.44K |
| 188 | 图例2.bak | 49.22K |
| 189 | 图例2.dwg | 49.22K |
| 190 | 图例3.bak | 39.36K |
| 191 | 图例3.dwg | 53.94K |
| 192 | 流程方框图.bak | 44.22K |
| 193 | 流程方框图.dwg | 44.22K |
| 194 | 厂区分布总图.dwg | 206.72K |
| 195 | Readme.txt | 83B |
| 196 | 优化后水集成网络.png | 21.63K |
| 197 | 初步设计水集成网络.png | 13.21K |
| 198 | 浓度组合曲线和最佳供水线.jpg | 74.40K |
| 199 | 浓度间隔表.jpg | 54.64K |
| 200 | 软件使用说明.txt | 136B |
| 201 | acad.fas | 15.20K |
| 202 | 分离车间0001.dwg | 132.78K |
| 203 | 分离车间0002.DWG | 206.03K |
| 204 | 分离车间0003.DWG | 251.88K |
| 205 | 分离车间0004.DWG | 249.38K |
| 206 | 分离车间0005.DWG | 436.53K |
| 207 | 分离车间0006.DWG | 147.97K |
| 208 | 分离车间0007.DWG | 195.84K |
| 209 | 分离车间0008.DWG | 178.88K |
| 210 | 分离车间0009.DWG | 206.28K |
| 211 | 分离车间0010.DWG | 116.09K |
| 212 | 分离车间0011.DWG | 204.53K |
| 213 | 分离车间0012.DWG | 201.81K |
| 214 | 分离车间0013.DWG | 206.31K |
| 215 | 分离车间0014.dwg | 400.63K |
| 216 | 反应车间0001.DWG | 234.72K |
| 217 | 反应车间0002.DWG | 106.59K |
| 218 | 反应车间0003.DWG | 209.78K |
| 219 | 反应车间0004.DWG | 278.03K |
| 220 | 反应车间0005.DWG | 203.81K |
| 221 | 反应车间0006.DWG | 223.22K |
| 222 | 反应车间0007.DWG | 260.81K |
| 223 | 反应车间0008.DWG | 392.69K |
| 224 | 反应车间0009.DWG | 149.25K |
| 225 | 反应车间0010.DWG | 147.22K |
| 226 | 反应车间0011.dwg | 246.38K |
| 227 | 分离车间.dwg | 17.43M |
| 228 | 反应车间.dwg | 15.16M |
| 229 | 1.pdf | 990.93K |
| 230 | 2.pdf | 563.79K |
| 231 | 3.pdf | 732.41K |
| 232 | 4.pdf | 599.22K |
| 233 | 分离车间管道图.pdf | 747.79K |
| 234 | 反应车间配管图.pdf | 809.93K |
| 235 | 1.jpg | 53.58K |
| 236 | 10.jpg | 43.63K |
| 237 | 11.jpg | 51.80K |
| 238 | 12.jpg | 50.95K |
| 239 | 13.jpg | 43.36K |
| 240 | 14.jpg | 57.90K |
| 241 | 2.jpg | 53.58K |
| 242 | 3.jpg | 55.91K |
| 243 | 4.jpg | 55.91K |
| 244 | 5.jpg | 52.87K |
| 245 | 6.jpg | 52.87K |
| 246 | 7.jpg | 45.64K |
| 247 | 8.jpg | 45.64K |
| 248 | 9.jpg | 42.85K |
| 249 | 厂区3D漫游.max | 107.52M |
| 250 | 1-换热网络.bkp | 803.70K |
| 251 | 2-Cost最小的换热网络.hch | 4.68M |
| 252 | 3-换热网络.appdf | 392.31K |
| 253 | 液相催化反应器工段.bkp | 283.86K |
| 254 | 液相催化反应器工段英文版.bkp | 283.87K |
| 255 | 1-丙烯醛脱水塔.bkp | 138.90K |
| 256 | 2-加压精馏分离DMF与丙烯酸.bkp | 194.08K |
| 257 | 3-分离预处理工段.bkp | 288.57K |
| 258 | 1-反应精馏塔.bkp | 83.87K |
| 259 | 2-环氧丙烷精制塔.bkp | 196.92K |
| 260 | 反应精馏塔英文版.bkp | 170.78K |
| 261 | 环氧丙烷精制塔英文版.bkp | 196.93K |
| 262 | T20110进料板优化.bkp | 111.14K |
| 263 | T20113进料板优化.bkp | 485.28K |
| 264 | T20114进料板优化.bkp | 485.04K |
| 265 | T201回流比优化.bkp | 492.62K |
| 266 | T201回流比优化.his | 45.96K |
| 267 | T201塔板数优化.bkp | 489.41K |
| 268 | T202回流比优化.bkp | 488.16K |
| 269 | T202塔板数优化.bkp | 488.56K |
| 270 | T2塔板数优化.bkp | 111.12K |
| 271 | T3回流比优化.bkp | 482.36K |
| 272 | T3进料板优化.bkp | 480.76K |
| 273 | T4回流比优化.bkp | 479.75K |
| 274 | T4塔板数优化.bkp | 496.07K |
| 275 | T4进料板优化.bkp | 479.51K |
| 276 | T5回流比优化.bkp | 478.77K |
| 277 | T5塔板数优化.bkp | 477.22K |
| 278 | T6塔板数优化.bkp | 112.05K |
| 279 | TI01回流比优化.bkp | 485.19K |
| 280 | TI01回流比全部灵敏度分析优化.bkp | 487.53K |
| 281 | TI01塔板数优化.bkp | 496.47K |
| 282 | TI01塔板数全部灵敏度分析优化.bkp | 111.86K |
| 283 | TI01进料板优化.bkp | 484.72K |
| 284 | TI01进料板数全部灵敏度分析优化.bkp | 486.95K |
| 285 | 回流1.bkp | 236.63K |
| 286 | 回流2.bkp | 550.69K |
| 287 | 回流3.bkp | 509.99K |
| 288 | 回流4.bkp | 532.62K |
| 289 | 回流5.bkp | 557.35K |
| 290 | 回流6.bkp | 117.56K |
| 291 | 回流7.bkp | 509.92K |
| 292 | 回流成功.bkp | 124.49K |
| 293 | 回流成功2.bkp | 550.71K |
| 294 | 回流成功、DMF.bkp | 124.49K |
| 295 | 回流收敛上.bkp | 533.32K |
| 296 | 回流收敛下.bkp | 122.21K |
| 297 | Cost最小的换热网络.hch | 4.68M |
| 298 | 全厂换热网络.apw | 941.50K |
| 299 | 换热网络.appdf | 392.31K |
| 300 | 换热网络.bkp | 145.95K |
| 301 | 1-总流程.bkp | 827.14K |
| 302 | 2-总流程.bkp | 826.64K |
| 303 | 1-丙烯醛脱水塔中间冷凝器.bkp | 79.73K |
| 304 | 2-多股进料塔中间再沸器.bkp | 204.91K |
| 305 | 3-脱PO塔中间再沸器.bkp | 170.99K |
| 306 | 4-塔顶蒸汽直接压缩式热泵精馏.bkp | 238.77K |
| 307 | 5-塔底液体闪蒸再沸式热泵精馏.bkp | 240.64K |
| 308 | 6-复叠式制冷系统.bkp | 256.25K |
| 309 | 7-双级氨吸收式制冷.bkp | 266.27K |
| 310 | 8-氨低温余热发电有机朗肯循环技术.bkp | 96.99K |
| 311 | 塔底液体闪蒸再沸式设计步骤1.bkp | 89.20K |
| 312 | 塔底液体闪蒸再沸式设计步骤2.bkp | 229.52K |
| 313 | 塔底液体闪蒸再沸式设计步骤3.bkp | 92.25K |
| 314 | lai.bkp | 827.11K |
| 315 | PROJECTS.OBI | 35B |
| 316 | RESULTS.xls | 873.50K |
| 317 | cashflow.ics | 284.89K |
| 318 | cashflow.ict | 990.98K |
| 319 | CURRENCY.DAT | 8.20K |
| 320 | DESIGN.d01 | 52.10K |
| 321 | DESIGN.d02 | 10.23K |
| 322 | DESIGN.d03 | 72.81K |
| 323 | DESIGN.d04 | 16.80K |
| 324 | DESIGN.d05 | 36B |
| 325 | equip.ict | 38.15K |
| 326 | execsum.ics | 9.03K |
| 327 | execsum.ict | 7.36K |
| 328 | Flag.txt | 0B |
| 329 | INV.d01 | 1.24K |
| 330 | INV.d02 | 10.55K |
| 331 | INV.d03 | 5.02K |
| 332 | INV.d04 | 4.98K |
| 333 | INV.d05 | 36B |
| 334 | ipeproc.d01 | 438B |
| 335 | ipeproc.d02 | 166B |
| 336 | ipeproc.d03 | 5.02K |
| 337 | ipeproc.d04 | 4.98K |
| 338 | ipeproc.d05 | 36B |
| 339 | ipeproj.d01 | 714B |
| 340 | ipeproj.d02 | 748B |
| 341 | ipeproj.d03 | 5.02K |
| 342 | ipeproj.d04 | 4.98K |
| 343 | ipeproj.d05 | 36B |
| 344 | IPEWB.XLS | 145.00K |
| 345 | IPEWB_TRA.XLS | 22.50K |
| 346 | IPSUNTUN.d01 | 852B |
| 347 | IPSUNTUN.d02 | 341B |
| 348 | IPSUNTUN.d03 | 5.02K |
| 349 | IPSUNTUN.d04 | 4.98K |
| 350 | IPSUNTUN.d05 | 36B |
| 351 | map.d01 | 1.10K |
| 352 | map.d02 | 7.42K |
| 353 | map.d03 | 5.02K |
| 354 | map.d04 | 20.74K |
| 355 | map.d05 | 36B |
| 356 | OP.d01 | 714B |
| 357 | OP.d02 | 2.37K |
| 358 | OP.d03 | 5.02K |
| 359 | OP.d04 | 4.98K |
| 360 | OP.d05 | 36B |
| 361 | PFDDIG.d01 | 438B |
| 362 | PFDDIG.d02 | 166B |
| 363 | PFDDIG.d03 | 5.02K |
| 364 | PFDDIG.d04 | 4.98K |
| 365 | PFDDIG.d05 | 36B |
| 366 | proc.d01 | 2.72K |
| 367 | proc.d02 | 1.59K |
| 368 | proc.d03 | 5.02K |
| 369 | proc.d04 | 4.98K |
| 370 | proc.d05 | 36B |
| 371 | procAZ.d01 | 990B |
| 372 | procAZ.d02 | 268B |
| 373 | procAZ.d03 | 5.02K |
| 374 | procAZ.d04 | 4.98K |
| 375 | procAZ.d05 | 36B |
| 376 | PROCCN.d01 | 438B |
| 377 | PROCCN.d02 | 166B |
| 378 | PROCCN.d03 | 5.02K |
| 379 | PROCCN.d04 | 4.98K |
| 380 | PROCCN.d05 | 36B |
| 381 | ProcessTemplateProject.KBW | 43B |
| 382 | PROD.d01 | 1.51K |
| 383 | PROD.d02 | 6.81K |
| 384 | PROD.d03 | 5.02K |
| 385 | PROD.d04 | 4.98K |
| 386 | PROD.d05 | 36B |
| 387 | ProdRes.txt | 127B |
| 388 | proj.d01 | 1.78K |
| 389 | proj.d02 | 1.29K |
| 390 | proj.d03 | 5.02K |
| 391 | proj.d04 | 4.98K |
| 392 | proj.d05 | 36B |
| 393 | projinfo.d01 | 714B |
| 394 | projinfo.d02 | 1.93K |
| 395 | projinfo.d03 | 5.02K |
| 396 | projinfo.d04 | 4.98K |
| 397 | projinfo.d05 | 36B |
| 398 | PROJL.d01 | 438B |
| 399 | PROJL.d02 | 166B |
| 400 | PROJL.d03 | 5.02K |
| 401 | PROJL.d04 | 4.98K |
| 402 | PROJL.d05 | 36B |
| 403 | projmap.d01 | 852B |
| 404 | projmap.d02 | 166B |
| 405 | projmap.d03 | 5.02K |
| 406 | projmap.d04 | 4.98K |
| 407 | projmap.d05 | 36B |
| 408 | PROJNAZ.d01 | 438B |
| 409 | PROJNAZ.d02 | 166B |
| 410 | PROJNAZ.d03 | 5.02K |
| 411 | PROJNAZ.d04 | 4.98K |
| 412 | PROJNAZ.d05 | 36B |
| 413 | PROJNBD.d01 | 438B |
| 414 | PROJNBD.d02 | 166B |
| 415 | PROJNBD.d03 | 5.02K |
| 416 | PROJNBD.d04 | 4.98K |
| 417 | PROJNBD.d05 | 36B |
| 418 | PROJNBG.d01 | 438B |
| 419 | PROJNBG.d02 | 166B |
| 420 | PROJNBG.d03 | 5.02K |
| 421 | PROJNBG.d04 | 4.98K |
| 422 | PROJNBG.d05 | 36B |
| 423 | PROJNBI.d01 | 438B |
| 424 | PROJNBI.d02 | 166B |
| 425 | PROJNBI.d03 | 5.02K |
| 426 | PROJNBI.d04 | 4.98K |
| 427 | PROJNBI.d05 | 36B |
| 428 | PROJNBM.d01 | 438B |
| 429 | PROJNBM.d02 | 166B |
| 430 | PROJNBM.d03 | 5.02K |
| 431 | PROJNBM.d04 | 4.98K |
| 432 | PROJNBM.d05 | 36B |
| 433 | PROJNBP.d01 | 438B |
| 434 | PROJNBP.d02 | 166B |
| 435 | PROJNBP.d03 | 5.02K |
| 436 | PROJNBP.d04 | 4.98K |
| 437 | PROJNBP.d05 | 36B |
| 438 | PROJNCN.d01 | 438B |
| 439 | PROJNCN.d02 | 166B |
| 440 | PROJNCN.d03 | 5.02K |
| 441 | PROJNCN.d04 | 4.98K |
| 442 | PROJNCN.d05 | 36B |
| 443 | PROJP.d01 | 438B |
| 444 | PROJP.d02 | 166B |
| 445 | PROJP.d03 | 5.02K |
| 446 | PROJP.d04 | 4.98K |
| 447 | PROJP.d05 | 36B |
| 448 | PROJSUM.ICS | 28.64K |
| 449 | projsum.ict | 232.10K |
| 450 | RAW.d01 | 1.51K |
| 451 | RAW.d02 | 6.74K |
| 452 | RAW.d03 | 5.02K |
| 453 | RAW.d04 | 4.98K |
| 454 | RAW.d05 | 36B |
| 455 | RawRes.txt | 132B |
| 456 | REP_GEN.d01 | 438B |
| 457 | REP_GEN.d02 | 166B |
| 458 | REP_GEN.d03 | 5.02K |
| 459 | REP_GEN.d04 | 4.98K |
| 460 | REP_GEN.d05 | 36B |
| 461 | RESULTS.xls | 873.50K |
| 462 | Scenario1.izp | 1.92M |
| 463 | Scenario1.szp | 2.42M |
| 464 | SCHD.d01 | 162B |
| 465 | SCHD.d02 | 77B |
| 466 | SCHD.d03 | 5.02K |
| 467 | SCHD.d04 | 4.98K |
| 468 | SCHD.d05 | 36B |
| 469 | SPECS.xls | 3.25M |
| 470 | STD.d01 | 9.73K |
| 471 | STD.d02 | 21.65K |
| 472 | STD.d03 | 20.97K |
| 473 | STD.d04 | 20.74K |
| 474 | STD.d05 | 36B |
| 475 | US_MET.KBW | 46B |
| 476 | US_Metric.KBW | 28B |
| 477 | UTILITY.d01 | 3.26K |
| 478 | UTILITY.d02 | 17.76K |
| 479 | UTILITY.d03 | 5.02K |
| 480 | UTILITY.d04 | 28.62K |
| 481 | UTILITY.d05 | 36B |
| 482 | fanyingqi-0100.cas | 1.17M |
| 483 | fanyingqi-0100.dat | 6.24M |
| 484 | fanyingqi-0200.cas | 1.17M |
| 485 | fanyingqi-0200.dat | 6.24M |
| 486 | fanyingqi-0300.cas | 1.17M |
| 487 | fanyingqi-0300.dat | 6.24M |
| 488 | fanyingqi-0400.cas | 1.17M |
| 489 | fanyingqi-0400.dat | 6.24M |
| 490 | fanyingqi-0500.cas | 1.17M |
| 491 | fanyingqi-0500.dat | 6.24M |
| 492 | fanyingqi-0600.cas | 1.17M |
| 493 | fanyingqi-0600.dat | 6.24M |
| 494 | fanyingqi-0700.cas | 1.17M |
| 495 | fanyingqi-0700.dat | 6.24M |
| 496 | fanyingqi-0800.cas | 1.17M |
| 497 | fanyingqi-0800.dat | 6.24M |
| 498 | fanyingqi-0900.cas | 1.17M |
| 499 | fanyingqi-0900.dat | 6.24M |
| 500 | fanyingqi-1000.cas | 1.17M |
| 501 | fanyingqi-1000.dat | 6.24M |
| 502 | fanyingqi-1100.cas | 1.17M |
| 503 | fanyingqi-1100.dat | 6.24M |
| 504 | fanyingqi-1200.cas | 1.17M |
| 505 | fanyingqi-1200.dat | 6.24M |
| 506 | fanyingqi-1300.cas | 1.17M |
| 507 | fanyingqi-1300.dat | 6.24M |
| 508 | fanyingqi-1400.cas | 1.17M |
| 509 | fanyingqi-1400.dat | 6.24M |
| 510 | fanyingqi-1500.cas | 1.17M |
| 511 | fanyingqi-1500.dat | 6.24M |
| 512 | fanyingqi-1600.cas | 1.17M |
| 513 | fanyingqi-1600.dat | 6.24M |
| 514 | E101.EDR | 295.62K |
| 515 | E102.EDR | 282.63K |
| 516 | E103.EDR | 297.22K |
| 517 | E104.EDR | 294.10K |
| 518 | E105.EDR | 283.36K |
| 519 | E106.EDR | 283.38K |
| 520 | E114.EDR | 285.27K |
| 521 | E109.EDR | 300.09K |
| 522 | E110.EDR | 285.39K |
| 523 | E111.EDR | 287.64K |
| 524 | E112.EDR | 278.18K |
| 525 | EDR.apw | 2.39M |
| 526 | EDR.bkp | 813.19K |
| 527 | 总流程.apw | 2.55M |
| 528 | 总流程.bkp | 853.42K |
| 529 | 热泵精馏换热器.EDR | 417.47K |
| 530 | A-0406.EDR | 1.18M |
| 531 | E-0401.EDR | 468.94K |
| 532 | E-0402.EDR | 503.74K |
| 533 | E-0403.EDR | 622.68K |
| 534 | E-0404.EDR | 545.90K |
| 535 | E-0405.EDR | 530.48K |
| 536 | 1.png | 67.20K |
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| 553 | 脱丙烯塔浮阀塔.kgt | 3.50K |
| 554 | 脱丙烯塔筛板塔.kgt | 3.52K |
| 555 | 1.png | 71.42K |
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| 562 | 8.png | 76.45K |
| 563 | 9.png | 76.52K |
| 564 | 多股进料塔.kgt | 3.51K |
| 565 | 脱氧气、丙烯多股进料塔.kgt | 2.98K |
| 566 | 1.png | 46.60K |
| 567 | 2.png | 52.50K |
| 568 | 3.png | 73.62K |
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| 573 | 脱环氧丙烷塔.kgt | 2.98K |
| 574 | 环氧丙烷精制塔.kgt | 3.51K |
| 575 | 丙烯酸、乙醇反应精馏塔.kgt | 1.80K |
| 576 | readme.txt | 236B |
| 577 | 环境风险评价.doc | 4.17M |
| 578 | 丙烯在大气中的扩散预测.rsm | 490B |
| 579 | 丙烯泄漏事故模拟.rsm | 501B |
| 580 | 丙烯两相流泄漏量计算.rsm | 95B |
| 581 | 丙烯气体泄漏量计算.rsm | 72B |
| 582 | 丙烯液体泄漏量计算.rsm | 105B |
| 583 | 丙烯热量蒸发量计算.rsm | 53B |
| 584 | 丙烯质量蒸发量计算.rsm | 58B |
| 585 | 丙烯闪蒸量计算.rsm | 63B |
| 586 | 丙烯池火事故模型预测.rsm | 200B |
| 587 | 丙烯沸腾液体扩展蒸汽爆炸.rsm | 207B |
| 588 | 丙烯蒸汽云爆炸模型预测.rsm | 170B |
| 589 | R1环氧丙烷反应器.doc | 139.00K |
| 590 | R2环氧丙烷反应器.doc | 139.00K |
| 591 | R3环氧丙烷反应器.doc | 139.00K |
| 592 | R4环氧丙烷反应器.doc | 139.00K |
| 593 | R5环氧丙烷反应器.doc | 139.00K |
| 594 | R6环氧丙烷反应器.doc | 139.00K |
| 595 | T0101脱丙烯塔.doc | 504.50K |
| 596 | T201脱氧气、丙烯多股进料塔.doc | 326.00K |
| 597 | T202脱环氧丙烷塔.doc | 325.00K |
| 598 | T203环氧丙烷精制塔.doc | 325.00K |
| 599 | T204丙烯醛脱水塔.doc | 325.00K |
| 600 | T301丙烯酸、乙醇反应精馏塔.doc | 325.00K |
| 601 | R1环氧丙烷反应器.ra1 | 10.21K |
| 602 | R2环氧丙烷反应器.ra1 | 10.21K |
| 603 | R3环氧丙烷反应器.ra1 | 10.21K |
| 604 | R4环氧丙烷反应器.ra1 | 10.21K |
| 605 | R5环氧丙烷反应器.ra1 | 10.21K |
| 606 | R6环氧丙烷反应器.ra1 | 10.21K |
| 607 | T0101脱丙烯塔.co1 | 10.21K |
| 608 | T201脱氧气、丙烯多股进料塔.co1 | 10.21K |
| 609 | T202脱环氧丙烷塔.co1 | 10.21K |
| 610 | T203环氧丙烷精制塔.col | 10.21K |
| 611 | T204丙烯醛脱水塔.col | 10.21K |
| 612 | T301丙烯酸、乙醇反应精馏塔.co1 | 10.21K |
| 613 | 团队海报.jpg | 751.08K |
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