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100kta丙烷制环氧丙烷生产项目初步设计（ID:2686578）
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| # | 文件名称 | 文件大小 |
|---|---|---|
| 1 | 17591338171129.zip | 253.88M |
| 2 | readme.txt | 1.44K |
| 3 | 现代设计方法评阅索引.pdf | 631.91K |
| 4 | 项目摘要.pdf | 937.69K |
| 5 | 设计图册.pdf | 22.00M |
| 6 | 1-可行性研究报告.pdf | 2.34M |
| 7 | 2-初步设计说明书.pdf | 8.80M |
| 8 | 3-1塔设备计算说明书.pdf | 9.05M |
| 9 | 3-2换热器计算说明书.pdf | 4.92M |
| 10 | 3-3反应器设计说明书.pdf | 2.55M |
| 11 | 3-4设备设计及选型一览表.pdf | 807.35K |
| 12 | 3-设备设计文档.pdf | 635.82K |
| 13 | 4-创新性说明书.pdf | 1.02M |
| 14 | 5-物料性质.pdf | 1.40M |
| 15 | 6-安全预评价报告.pdf | 1.37M |
| 16 | 7-环境影响评价报告.pdf | 1.60M |
| 17 | readme.txt | 335B |
| 18 | 五塔.ada | 1.37M |
| 19 | 单塔.ada | 138.82K |
| 20 | 双塔.ada | 489.77K |
| 21 | 床层.ada | 216.48K |
| 22 | lsprst7.dll | 236B |
| 23 | PropsPlus.ads | 791B |
| 24 | propsplus.aprhis | 6.69K |
| 25 | propsplus.aprpdf | 181.60K |
| 26 | PropsPlus.def | 315B |
| 27 | PropsPlus.his | 2.26K |
| 28 | PropsPlus.rep | 0B |
| 29 | lsprst7.dll | 243B |
| 30 | lsprst7.tgz | 257B |
| 31 | PropsPlus.ads | 791B |
| 32 | propsplus.aprhis | 6.69K |
| 33 | propsplus.aprpdf | 181.60K |
| 34 | PropsPlus.def | 315B |
| 35 | PropsPlus.his | 2.26K |
| 36 | PropsPlus.rep | 0B |
| 37 | PSA-Simulation.ada | 215.43K |
| 38 | 吸附效果随时间变化.jpg | 311.73K |
| 39 | 杂质分布随时间变化.jpg | 342.71K |
| 40 | 碳二出口浓度随时间变化.jpg | 301.01K |
| 41 | lsprst7.dll | 243B |
| 42 | lsprst7.tgz | 257B |
| 43 | PropsPlus.ads | 791B |
| 44 | propsplus.aprhis | 6.69K |
| 45 | propsplus.aprpdf | 181.58K |
| 46 | PropsPlus.def | 315B |
| 47 | PropsPlus.his | 2.26K |
| 48 | PropsPlus.rep | 0B |
| 49 | lsprst7.dll | 243B |
| 50 | lsprst7.tgz | 257B |
| 51 | PropsPlus.ads | 791B |
| 52 | propsplus.aprhis | 6.69K |
| 53 | propsplus.aprpdf | 181.57K |
| 54 | PropsPlus.def | 315B |
| 55 | PropsPlus.his | 2.26K |
| 56 | PropsPlus.rep | 0B |
| 57 | snapshot.bak | 817.86K |
| 58 | tasksnap.bak | 1.36K |
| 59 | 床层.ada.backup | 239.93K |
| 60 | readme.txt | 331B |
| 61 | 差压热耦合.bkp | 435.37K |
| 62 | 差压热耦合.dynf | 1.64M |
| 63 | 差压热耦合dyn.appdf | 368.65K |
| 64 | 流量减少10.pdf | 132.72K |
| 65 | 流量增加10.pdf | 132.05K |
| 66 | 纯度减少10.pdf | 133.22K |
| 67 | 纯度增加10.pdf | 134.04K |
| 68 | 差压热耦合dyn.his | 3.37K |
| 69 | 差压热耦合dyn.rep | 0B |
| 70 | 萃取精馏塔.bkp | 296.95K |
| 71 | 萃取精馏塔.dynf | 1.23M |
| 72 | 萃取精馏塔dyn.appdf | 316.40K |
| 73 | 萃取精馏塔dyn.his | 3.27K |
| 74 | 萃取精馏塔dyn.rep | 0B |
| 75 | HENsofPropanedehydrogen.hch | 1.72M |
| 76 | HENsofPropeneepoxidation.hch | 1.40M |
| 77 | E0101-原料气预热.EDR | 402.32K |
| 78 | E0201-多级压缩一级冷却.EDR | 371.13K |
| 79 | E0202-多级压缩二级冷却.EDR | 387.96K |
| 80 | E0203-乙烯水冷换热器.EDR | 354.93K |
| 81 | E0204-丙烯水冷换热器.EDR | 371.68K |
| 82 | E0205-富氢气为物料预冷.EDR | 105.23K |
| 83 | E0206-釜液为物料预冷.EDR | 105.97K |
| 84 | E0207-丙烯膨胀吸热.EDR | 94.10K |
| 85 | E0208-乙烯膨胀吸热.EDR | 94.54K |
| 86 | E0209-乙烯丙烯换热.EDR | 86.46K |
| 87 | E0210-脱乙烷塔预热.EDR | 340.33K |
| 88 | E0211-脱乙烷塔再沸器.EDR | 377.55K |
| 89 | E0212-脱乙烷塔冷凝器.EDR | 419.40K |
| 90 | E0301-提馏塔辅助再沸器.EDR | 542.71K |
| 91 | E0302-耦合换热器.EDR | 510.49K |
| 92 | E0303-精馏塔辅助冷凝器.EDR | 459.21K |
| 93 | E0304-脱丁烷塔冷凝器.EDR | 468.81K |
| 94 | E0305-脱丁烷塔再沸器.EDR | 396.78K |
| 95 | E0501-耦合反应器移热器.EDR | 387.25K |
| 96 | E0502-耦合反应器移热器.EDR | 387.25K |
| 97 | E0503-耦合反应器移热器.EDR | 387.25K |
| 98 | E0601-T0601再沸器.EDR | 446.80K |
| 99 | E0602-T0601冷凝器.EDR | 388.46K |
| 100 | E0603-T0602再沸器.EDR | 446.80K |
| 101 | E0604-T0602冷凝器.EDR | 382.43K |
| 102 | E0605-T0603再沸器.EDR | 446.80K |
| 103 | E0606-T0603冷凝器.EDR | 382.43K |
| 104 | E0607-T0604再沸器.EDR | 446.80K |
| 105 | E0608-T0604冷凝器.EDR | 382.43K |
| 106 | E0701-除丙烯塔预热器.EDR | 389.16K |
| 107 | E0702-除丙烯塔再沸器.EDR | 477.20K |
| 108 | E0703-除丙烯塔冷凝器.EDR | 506.45K |
| 109 | E0704-萃取剂预冷器.EDR | 347.62K |
| 110 | E0705-萃取精馏塔再沸器.EDR | 514.28K |
| 111 | E0706-萃取精馏塔冷凝器.EDR | 465.47K |
| 112 | E0707-萃取剂回收塔再沸器.EDR | 421.62K |
| 113 | E0708-萃取剂回收塔冷凝器.EDR | 429.27K |
| 114 | E0801-蒽醌液预热.EDR | 482.33K |
| 115 | E0802-氢气预热.EDR | 482.33K |
| 116 | E0803-氢化蒽醌液冷却器.EDR | 675.43K |
| 117 | E0901-釜液冷却器.EDR | 370.15K |
| 118 | E0902-釜液辅助冷却器.EDR | 370.15K |
| 119 | E0903-渗透汽化预热器.EDR | 535.72K |
| 120 | E0904-PGME冷凝器.EDR | 430.79K |
| 121 | E0905-甲醇水冷凝器.EDR | 372.97K |
| 122 | E0906-甲醇水再沸器.EDR | 440.39K |
| 123 | E0907-甲醇水塔冷凝器.EDR | 368.57K |
| 124 | E0908-单甲醚塔冷凝器.EDR | 368.24K |
| 125 | E0909-单甲醚塔再沸器.EDR | 371.80K |
| 126 | E0101-原料气预热.pdf | 112.95K |
| 127 | E0201-多级压缩一级冷却1.pdf | 108.58K |
| 128 | E0202-多级压缩二级冷却2.pdf | 122.24K |
| 129 | E0203-乙烯水冷换热器.pdf | 104.18K |
| 130 | E0204-丙烯水冷换热器.pdf | 114.60K |
| 131 | E0205-富氢气为物料预冷.pdf | 70.00K |
| 132 | E0206-釜液为物料预冷.pdf | 69.96K |
| 133 | E0207-丙烯膨胀吸热.pdf | 69.85K |
| 134 | E0208-乙烯膨胀吸热.pdf | 69.98K |
| 135 | E0209-乙烯丙烯换热.pdf | 67.68K |
| 136 | E0210-脱乙烷塔预热器.pdf | 95.60K |
| 137 | E0211-脱乙烷塔再沸器.pdf | 104.87K |
| 138 | E0212-脱乙烷塔冷凝器.pdf | 98.00K |
| 139 | E0301-提馏塔辅助再沸器.pdf | 195.61K |
| 140 | E0302-耦合换热器.pdf | 186.29K |
| 141 | E0303-精馏塔辅助冷凝器.pdf | 108.21K |
| 142 | E0304-脱丁烷塔冷凝器.pdf | 109.12K |
| 143 | E0305-脱丁烷塔再沸器.pdf | 103.48K |
| 144 | E0501-反应外加移热器.pdf | 99.55K |
| 145 | E0502-反应外加移热器.pdf | 99.54K |
| 146 | E0503-反应外加移热器.pdf | 99.56K |
| 147 | E0601-粗分塔T0601再沸器.pdf | 123.58K |
| 148 | E0602-粗分塔T0601冷凝器.pdf | 102.13K |
| 149 | E0603-粗分塔T0602再沸器.pdf | 123.61K |
| 150 | E0604-粗分塔T0602冷凝器.pdf | 96.88K |
| 151 | E0605-粗分塔T0603再沸器.pdf | 123.59K |
| 152 | E0606-粗分塔T0603冷凝器.pdf | 96.88K |
| 153 | E0607-粗分塔T0604再沸器.pdf | 123.65K |
| 154 | E0608-粗分塔T0604冷凝器.pdf | 96.88K |
| 155 | E0701-脱丙烯塔预热器.pdf | 100.22K |
| 156 | E0702-脱丙烯塔冷凝器.pdf | 129.83K |
| 157 | E0703-脱丙烯塔再沸器.pdf | 168.78K |
| 158 | E0704-萃取剂预冷器.pdf | 100.05K |
| 159 | E0705-萃取精馏塔再沸器.pdf | 154.71K |
| 160 | E0706-萃取精馏塔冷凝器.pdf | 159.58K |
| 161 | E0707-萃取剂回收塔再沸器.pdf | 132.49K |
| 162 | E0708-萃取剂回收塔冷凝器.pdf | 123.98K |
| 163 | E0801-蒽醌液预热.pdf | 165.19K |
| 164 | E0802-氢气预热.pdf | 133.23K |
| 165 | E0803-工作液冷却器.pdf | 540.62K |
| 166 | E0901-釜液冷却器.pdf | 100.79K |
| 167 | E0902-釜液辅助冷却器.pdf | 101.34K |
| 168 | E0903-渗透汽化预热器.pdf | 130.33K |
| 169 | E0904-PGME冷凝器.pdf | 141.30K |
| 170 | E0905-甲醇水冷凝器.pdf | 98.18K |
| 171 | E0906-甲醇水塔再沸器.pdf | 150.53K |
| 172 | E0907-甲醇水塔冷凝器.pdf | 95.81K |
| 173 | E0908-单甲醚塔冷凝器.pdf | 95.35K |
| 174 | E0909-单甲醚塔再沸器.pdf | 98.94K |
| 175 | readmefirst.txt | 493B |
| 176 | readme.txt | 507B |
| 177 | 丙烯环氧化车间.bkp | 1.53M |
| 178 | 丙烷脱氢车间.bkp | 1.05M |
| 179 | 全流程模拟（带换热网络）.bkp | 2.55M |
| 180 | 复迭压缩制冷过程模拟.bkp | 84.83K |
| 181 | 差压热耦合丙烯精馏塔.bkp | 680.27K |
| 182 | T0202脱乙烷塔的优化（进料塔板总塔板回流比灵敏度分析）.bkp | 240.35K |
| 183 | T0303脱丁烷塔的优化（进料塔板总塔板回流比灵敏度分析）.bkp | 142.55K |
| 184 | T0601粗分塔的优化（进料塔板总塔板回流比灵敏度分析）.bkp | 251.25K |
| 185 | T0901甲醇水塔的优化（进料塔板总塔板回流比灵敏度分析）.bkp | 186.94K |
| 186 | T0902PGME塔的优化（进料塔板总塔板回流比灵敏度分析）.bkp | 625.16K |
| 187 | 差压热耦合丙烯精馏塔优化.appdf | 786.69K |
| 188 | 差压热耦合丙烯精馏塔优化.apw | 1.92M |
| 189 | 差压热耦合丙烯精馏塔优化.bkp | 524.60K |
| 190 | 差压热耦合丙烯精馏塔优化.def | 296B |
| 191 | 差压热耦合丙烯精馏塔优化.for | 0B |
| 192 | 差压热耦合丙烯精馏塔优化.his | 316.40K |
| 193 | 图1.jpg | 309.41K |
| 194 | 图2.jpg | 261.24K |
| 195 | 图3.jpg | 372.92K |
| 196 | 图4.jpg | 299.15K |
| 197 | 图6.jpg | 454.51K |
| 198 | 图7.jpg | 351.76K |
| 199 | 萃取精馏优化灵敏度.bkp | 53.94K |
| 200 | readme.txt | 502B |
| 201 | 丙烯环氧化车间.bkp | 1.55M |
| 202 | 丙烷脱氢车间.bkp | 1.06M |
| 203 | 全流程模拟（带换热网络）.bkp | 2.57M |
| 204 | 复迭压缩制冷过程模拟.bkp | 84.83K |
| 205 | 差压热耦合丙烯精馏塔.bkp | 680.27K |
| 206 | T0202脱乙烷塔的优化（进料塔板总塔板回流比灵敏度分析）.bkp | 240.35K |
| 207 | T0303脱丁烷塔的优化（进料塔板总塔板回流比灵敏度分析）.bkp | 142.55K |
| 208 | T0601粗分塔的优化（进料塔板总塔板回流比灵敏度分析）.bkp | 251.25K |
| 209 | T0901甲醇水塔的优化（进料塔板总塔板回流比灵敏度分析）.bkp | 186.94K |
| 210 | T0902PGME塔的优化（进料塔板总塔板回流比灵敏度分析）.bkp | 625.16K |
| 211 | 差压热耦合丙烯精馏塔优化.bkp | 524.60K |
| 212 | 图1.jpg | 309.41K |
| 213 | 图2.jpg | 261.24K |
| 214 | 图3.jpg | 372.92K |
| 215 | 图4.jpg | 299.15K |
| 216 | 图6.jpg | 454.51K |
| 217 | 图7.jpg | 351.76K |
| 218 | 萃取精馏优化灵敏度.bkp | 53.94K |
| 219 | PFD工艺流程图.dwg | 538.74K |
| 220 | PID管道及仪表流程图.dwg | 1.66M |
| 221 | 丙烷脱氢车间平立面布置源文件.dwg | 201.56K |
| 222 | 厂区平面布置源文件.dwg | 115.81K |
| 223 | 图例.dwg | 97.21K |
| 224 | 气升式环流滤浆床装配图.dwg | 499.16K |
| 225 | readme.txt | 419B |
| 226 | 7.27-reactor-3d.cas | 16.98M |
| 227 | 7.27-reactor-3d.dat | 134.80M |
| 228 | 7.27-reactor-2d.cas | 246.98K |
| 229 | 7.27-reactor-2d.dat | 1.35M |
| 230 | 7.28-reactor-2d-2-3phases-1.cas | 292.82K |
| 231 | 7.28-reactor-2d-2-3phases-1.dat | 1.90M |
| 232 | catofin.m | 2.13K |
| 233 | PDH.m | 676B |
| 234 | PGME.m | 1.25K |
| 235 | readme.txt | 437B |
| 236 | HPPO.rvm | 4.12M |
| 237 | PDH.rvm | 9.92M |
| 238 | 第一车间主视图.PNG | 88.30K |
| 239 | 第一车间俯视图.PNG | 128.76K |
| 240 | 第一车间左视图.PNG | 56.58K |
| 241 | 第一车间管道排布图.PNG | 124.78K |
| 242 | 第一车间鸟瞰图.PNG | 290.96K |
| 243 | previewIsoStd001.pdf | 61.84K |
| 244 | previewIsoStd002.pdf | 55.31K |
| 245 | previewIsoStd003.pdf | 70.26K |
| 246 | previewIsoStd004.pdf | 72.38K |
| 247 | previewIsoStd005.pdf | 82.03K |
| 248 | previewIsoStd006.pdf | 44.19K |
| 249 | 环境风险评价报告.docx | 1.31M |
| 250 | 说明.txt | 255B |
| 251 | 丙烯典型泄露事故模拟.rsm | 508B |
| 252 | 丙烯两相流泄漏量计算.rsm | 99B |
| 253 | 丙烯气体泄漏量计算.rsm | 78B |
| 254 | 丙烯液体泄漏量计算.rsm | 115B |
| 255 | 丙烯热量蒸发量计算.rsm | 53B |
| 256 | 丙烯质量蒸发量计算.rsm | 62B |
| 257 | 丙烯闪蒸量计算.rsm | 61B |
| 258 | 丙烯池火事故模型预测.rsm | 196B |
| 259 | 丙烯火球BLEVE模型预测.rsm | 205B |
| 260 | 丙烯蒸汽云爆炸模型预测.rsm | 160B |
| 261 | 丙烷典型泄露事故模拟.rsm | 510B |
| 262 | 丙烷两相流泄漏量计算.rsm | 99B |
| 263 | 丙烷气体泄漏量计算.rsm | 77B |
| 264 | 丙烷液体泄漏量计算.rsm | 114B |
| 265 | 丙烷热量蒸发量计算.rsm | 53B |
| 266 | 丙烷质量蒸发量计算.rsm | 62B |
| 267 | 丙烷闪蒸量计算.rsm | 61B |
| 268 | 丙烷池火事故模型预测.rsm | 200B |
| 269 | 丙烷火球BLEVE模型预测.rsm | 209B |
| 270 | 丙烷蒸汽云爆炸模型预测.rsm | 164B |
| 271 | 环氧丙烷典型泄露事故模拟.rsm | 526B |
| 272 | 环氧丙烷气体泄漏量计算.rsm | 78B |
| 273 | 环氧丙烷液体泄漏量计算.rsm | 118B |
| 274 | 环氧丙烷质量蒸发量计算.rsm | 65B |
| 275 | 环氧丙烷闪蒸量计算.rsm | 66B |
| 276 | 环氧丙烷池火事故模型预测.rsm | 209B |
| 277 | 环氧丙烷沸腾液体扩展蒸汽爆炸模型预测.rsm | 217B |
| 278 | 环氧丙烷蒸汽云爆炸模型预测.rsm | 172B |
| 279 | 甲醇气体泄漏量计算.rsm | 74B |
| 280 | 甲醇液体泄漏量计算.rsm | 112B |
| 281 | 甲醇质量蒸发量计算.rsm | 61B |
| 282 | 甲醇闪蒸量计算.rsm | 63B |
| 283 | 甲醇池火事故模型预测.rsm | 201B |
| 284 | 甲醇沸腾液体扩散蒸汽爆炸模型.rsm | 208B |
| 285 | 甲醇蒸汽云爆炸模型预测.rsm | 163B |
| 286 | 塔设备选型一览表.docx | 21.04K |
| 287 | 脱乙烷塔.xls | 16.00K |
| 288 | 脱乙烷塔.rtf | 82.45K |
| 289 | 脱乙烷塔.sulcol | 117.90K |
| 290 | 脱乙烷塔.cn2 | 30.20K |
| 291 | 脱乙烷塔.doc | 783.50K |
| 292 | 丙烯提馏塔.plc | 208.00K |
| 293 | 丙烯提馏塔.xlsx | 20.30K |
| 294 | 丙烯提馏塔.cn2 | 30.20K |
| 295 | 丙烯提馏塔.doc | 819.50K |
| 296 | T0302-1丙烯精馏塔.plc | 208.00K |
| 297 | 丙烯精馏塔.xlsx | 23.23K |
| 298 | 丙烯精馏塔.cn2 | 30.20K |
| 299 | 丙烯精馏塔.doc | 117.50K |
| 300 | 脱丁烷塔.xls | 16.50K |
| 301 | 脱丁烷塔.rtf | 54.43K |
| 302 | 脱丁烷塔.sulcol | 30.74K |
| 303 | 脱丁烷塔.cn2 | 30.20K |
| 304 | 脱丁烷塔.doc | 721.50K |
| 305 | 粗分塔.xls | 20.50K |
| 306 | 粗分塔.rtf | 82.42K |
| 307 | 粗分塔.sulcol | 117.90K |
| 308 | 粗分塔.cn2 | 30.20K |
| 309 | 粗分塔.doc | 770.00K |
| 310 | 除丙烯塔.xls | 16.50K |
| 311 | 除丙烯塔.rtf | 82.45K |
| 312 | 除丙烯塔.sulcol | 117.90K |
| 313 | 除丙烯塔.cn2 | 30.20K |
| 314 | 除丙烯塔.doc | 770.00K |
| 315 | 萃取精馏塔.xls | 28.50K |
| 316 | 萃取精馏塔.rtf | 166.35K |
| 317 | 萃取精馏塔.sulcol | 135.18K |
| 318 | 萃取精馏塔.cn2 | 30.20K |
| 319 | 萃取精馏塔.doc | 758.50K |
| 320 | 萃取剂回收塔.xls | 16.50K |
| 321 | 萃取剂回收塔.rtf | 82.35K |
| 322 | 萃取剂回收塔.sulcol | 56.86K |
| 323 | 萃取剂回收塔.cn2 | 30.20K |
| 324 | 萃取剂回收塔.doc | 768.50K |
| 325 | 甲醇水塔.xls | 16.50K |
| 326 | 甲醇水塔.rtf | 54.51K |
| 327 | 甲醇水塔.sulcol | 30.75K |
| 328 | 甲醇水塔.cn2 | 30.20K |
| 329 | 甲醇水塔.doc | 783.00K |
| 330 | PGSE精制塔.xls | 16.50K |
| 331 | PGSE精制塔.rtf | 82.34K |
| 332 | PGSE精制塔.sulcol | 56.86K |
| 333 | PGSE精制塔.cn2 | 30.20K |
| 334 | PGSE精制塔.doc | 770.50K |
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| 336 | E0201.fx2 | 24.00K |
| 337 | E0202.fx2 | 24.00K |
| 338 | E0203.fx2 | 24.00K |
| 339 | E0204.fx2 | 24.00K |
| 340 | E0210.fx2 | 24.00K |
| 341 | E0211.fx2 | 24.00K |
| 342 | E0212.fx2 | 24.00K |
| 343 | E0301.fx2 | 24.00K |
| 344 | E0302.fx2 | 24.00K |
| 345 | E0303.fx2 | 24.00K |
| 346 | E0304.fx2 | 24.00K |
| 347 | E0305.fx2 | 24.00K |
| 348 | E0501.fx2 | 24.00K |
| 349 | E0502.fx2 | 24.00K |
| 350 | E0503.fx2 | 24.00K |
| 351 | E0601.fx2 | 24.00K |
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| 380 | E0201.doc | 1.35M |
| 381 | E0202.doc | 1.35M |
| 382 | E0203.doc | 1.35M |
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| 385 | E0211.doc | 1.35M |
| 386 | E0212.doc | 1.35M |
| 387 | E0301.doc | 1.35M |
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| 393 | E0502.doc | 1.35M |
| 394 | E0503.doc | 1.35M |
| 395 | E0601.doc | 1.91M |
| 396 | E0602.doc | 1.35M |
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| 398 | E0604.doc | 1.35M |
| 399 | E0605.doc | 1.35M |
| 400 | E0606.doc | 1.35M |
| 401 | E0607.doc | 1.35M |
| 402 | E0608.doc | 1.35M |
| 403 | E0701.doc | 1.35M |
| 404 | E0702.doc | 1.35M |
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| 409 | E0707.doc | 1.35M |
| 410 | E0708.doc | 1.17M |
| 411 | E0801.doc | 1.35M |
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| 413 | E0803.doc | 1.35M |
| 414 | E0901.doc | 1.35M |
| 415 | E0902.doc | 1.35M |
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| 417 | E0904.docx | 56.13K |
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| 419 | E0906.docx | 85.09K |
| 420 | E0907.docx | 589.50K |
| 421 | E0908.docx | 502.42K |
| 422 | E0909.docx | 201.37K |
| 423 | 0-现代设计方法评阅索引.doc | 1.22M |
| 424 | 0-项目摘要.doc | 1.55M |
| 425 | 1-可行性研究报告.doc | 7.44M |
| 426 | 2-初步设计说明书.doc | 18.07M |
| 427 | 3-3反应器设计说明书.doc | 10.06M |
| 428 | 3-4设备设计及选型一览表.doc | 1.54M |
| 429 | 3-设备设计文档.doc | 1.36M |
| 430 | 4-创新性说明书.doc | 1.71M |
| 431 | 5-物料性质表.doc | 1.47M |
| 432 | 6-安全预评价报告.doc | 1.73M |
| 433 | 7-环境影响评价报告.doc | 2.13M |
| 434 | 1.jpg | 510.85K |
| 435 | 2.jpg | 653.37K |
| 436 | 3.jpg | 614.93K |
| 437 | 4.jpg | 627.94K |
| 438 | 5.jpg | 492.53K |
| 439 | 6.jpg | 479.81K |
| 440 | 7.jpg | 468.87K |
| 441 | lumion厂区3D建模加车间.ls5 | 120.91M |
| 442 | readme.txt | 415B |
| 443 | SketchUp厂区3D建模.skp | 140.07M |
| 444 | 泵选型一览表.xls | 28.00K |
| 445 | 风机选型一览表.xls | 19.50K |
| 446 | P0201A_B.pdf | 99.57K |
| 447 | P0202A_B.pdf | 99.57K |
| 448 | P0203A_B.pdf | 109.74K |
| 449 | P0204A_B.pdf | 91.68K |
| 450 | P0301A_B.pdf | 91.68K |
| 451 | P0302A_B.pdf | 99.57K |
| 452 | P0303A_B.pdf | 98.88K |
| 453 | P0501A_B---P0506A_B.pdf | 91.68K |
| 454 | P0507A_B---P0509A_B.pdf | 99.92K |
| 455 | P0510A_B.pdf | 91.68K |
| 456 | P0511A_B.pdf | 99.92K |
| 457 | P0601A_BP0603A_BP0605A_BP0607A_B.pdf | 104.31K |
| 458 | P0602A_BP0604A_BP0606A_BP0608A_B.pdf | 103.79K |
| 459 | P0701A_B.pdf | 104.41K |
| 460 | P0702A_B.pdf | 92.55K |
| 461 | P0703A_B.pdf | 87.39K |
| 462 | P0704A_B.pdf | 87.39K |
| 463 | P0705A_B.pdf | 87.39K |
| 464 | P0706A_B.pdf | 87.39K |
| 465 | P0801A_B.pdf | 92.10K |
| 466 | P0802A_B.pdf | 92.10K |
| 467 | P0803A_B.pdf | 92.10K |
| 468 | P0901A_B.pdf | 89.53K |
| 469 | P0902A_B.pdf | 89.53K |
| 470 | P0903A_B.pdf | 92.10K |
| 471 | P0904A_B.pdf | 89.77K |
| 472 | P0906A_B.pdf | 103.94K |
| 473 | P0907A_B.pdf | 89.77K |
| 474 | P0908A_B.pdf | 109.43K |
| 475 | P0909A_B.pdf | 109.30K |
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