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年产十万吨乙二醇项目初步设计
（ID:2689973）
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| # | 文件名称 | 文件大小 |
|---|---|---|
| 1 | 1-可行性研究报告.doc | 1.41M |
| 2 | 2-初步设计说明书.doc | 7.47M |
| 3 | 3-创新性说明书.doc | 717.00K |
| 4 | 4-设备选型一览表.doc | 416.50K |
| 5 | 5.1-物料衡算与能量衡算计算书.doc | 1.70M |
| 6 | 5.2-换热网络设计.doc | 666.00K |
| 7 | 5.3-设备选型与典型设备设计.doc | 8.12M |
| 8 | 5.4-经济分析.doc | 920.50K |
| 9 | 6-安全预评价报告.doc | 2.16M |
| 10 | 7-环境影响评价报告.doc | 816.50K |
| 11 | 说明.txt | 1.31K |
| 12 | 总设计图册.pdf | 3.59M |
| 13 | 说明.txt | 230B |
| 14 | PFD.dwg | 856.66K |
| 15 | PID.dwg | 708.00K |
| 16 | R0101预反应器.dwg | 145.59K |
| 17 | R0102羰化反应器.dwg | 158.93K |
| 18 | R0301加氢反应器.dwg | 154.58K |
| 19 | T0101反应精馏塔.dwg | 239.71K |
| 20 | T0403分隔壁塔.dwg | 136.62K |
| 21 | 工厂总平面布置图.dwg | 124.43K |
| 22 | 管道轴测图.dwg | 59.23K |
| 23 | 说明.txt | 509B |
| 24 | 车间布置图.dwg | 466.62K |
| 25 | PFD.pdf | 660.76K |
| 26 | 物料平衡表.pdf | 73.13K |
| 27 | PID.pdf | 551.21K |
| 28 | 工厂总平面布置图.pdf | 79.27K |
| 29 | R0101预反应器.pdf | 86.50K |
| 30 | R0102羰化反应器.pdf | 96.51K |
| 31 | R0301加氢反应器.pdf | 96.66K |
| 32 | T0101反应精馏塔.pdf | 450.79K |
| 33 | T0403分隔壁塔.pdf | 82.60K |
| 34 | 管道轴测图.pdf | 161.10K |
| 35 | 车间三维图.pdf | 625.48K |
| 36 | 车间平立面布置图.pdf | 437.04K |
| 37 | 说明.txt | 572B |
| 38 | E-ACTION.ls5 | 246.27M |
| 39 | 地基.max | 7.16M |
| 40 | 总车间.max | 342.88M |
| 41 | 说明.txt | 458B |
| 42 | E-ACTION_1.JPG | 287.78K |
| 43 | E-ACTION_2.JPG | 190.08K |
| 44 | E-ACTION_3.JPG | 266.48K |
| 45 | E-ACTION_4.JPG | 260.14K |
| 46 | E-ACTION_5.JPG | 218.49K |
| 47 | E-ACTION_6.JPG | 195.53K |
| 48 | E-ACTION_7.JPG | 205.76K |
| 49 | E-ACTION_8.JPG | 201.92K |
| 50 | NO2压力管道泄漏源文件.alo | 4.73K |
| 51 | NO2排放源文件.alo | 4.73K |
| 52 | 二氧化氮压力管道泄漏.png | 6.17K |
| 53 | 二氧化氮排放.png | 6.03K |
| 54 | 换热网络设计.hch | 9.18M |
| 55 | 说明.txt | 496B |
| 56 | 换热器性能说明书.pdf | 79.29K |
| 57 | 换热器性能说明书.xlsx | 26.50K |
| 58 | 说明.txt | 491B |
| 59 | E0101.apwz | 4.29M |
| 60 | E0101.EDR | 331.16K |
| 61 | E0101.XLS | 28.16K |
| 62 | E0101安装图.docx | 38.75K |
| 63 | E0101规格书.pdf | 14.04K |
| 64 | E0102.apwz | 4.30M |
| 65 | E0102.EDR | 503.70K |
| 66 | E0102.XLS | 27.75K |
| 67 | E0102安装图.docx | 60.40K |
| 68 | E0102规格书.pdf | 40.45K |
| 69 | E0103.apwz | 4.29M |
| 70 | E0103.EDR | 341.58K |
| 71 | E0103.XLS | 28.00K |
| 72 | E0103安装图.docx | 66.76K |
| 73 | E0103规格书.pdf | 40.03K |
| 74 | E0104.apwz | 4.29M |
| 75 | E0104.EDR | 354.59K |
| 76 | E0104.XLS | 28.08K |
| 77 | E0104安装图.docx | 36.12K |
| 78 | E0104规格书.pdf | 39.85K |
| 79 | E0105.apwz | 4.29M |
| 80 | E0105.EDR | 310.90K |
| 81 | E0105.XLS | 27.99K |
| 82 | E0105安装图.docx | 34.23K |
| 83 | E0105规格书.pdf | 40.33K |
| 84 | E0106.apwz | 4.31M |
| 85 | E0106.EDR | 325.04K |
| 86 | E0106.XLS | 27.96K |
| 87 | E0106安装图.docx | 60.14K |
| 88 | E0106规格书.pdf | 11.82K |
| 89 | E0107.apwz | 4.31M |
| 90 | E0107.EDR | 300.06K |
| 91 | E0107.XLS | 28.13K |
| 92 | E0107安装图.docx | 43.59K |
| 93 | E0107规格书.pdf | 40.32K |
| 94 | E0108.apwz | 4.31M |
| 95 | E0108.EDR | 394.53K |
| 96 | E0108.XLS | 28.14K |
| 97 | E0108安装图.docx | 45.98K |
| 98 | E0108规格书.pdf | 40.64K |
| 99 | E0109.apwz | 4.30M |
| 100 | E0109.docx | 37.83K |
| 101 | E0109.EDR | 342.08K |
| 102 | E0109.XLS | 27.84K |
| 103 | E0109规格书.pdf | 11.74K |
| 104 | E0110.apwz | 4.30M |
| 105 | E0110.EDR | 426.45K |
| 106 | E0110.XLS | 27.31K |
| 107 | E0110安装图.docx | 36.37K |
| 108 | E0110规格书.pdf | 40.72K |
| 109 | E0111.apwz | 4.39M |
| 110 | E0111.EDR | 366.52K |
| 111 | E0111.XLS | 29.34K |
| 112 | E0111安装图.docx | 39.63K |
| 113 | E0111规格书.pdf | 11.99K |
| 114 | E0112.apwz | 4.35M |
| 115 | E0112.EDR | 438.53K |
| 116 | E0112.XLS | 27.87K |
| 117 | E0112安装图.docx | 38.22K |
| 118 | E0112规格书.pdf | 40.16K |
| 119 | E0201.apwz | 4.37M |
| 120 | E0201.EDR | 344.20K |
| 121 | E0201.XLS | 27.85K |
| 122 | E0201安装图.docx | 39.48K |
| 123 | E0201规格书.pdf | 11.78K |
| 124 | E0202.apwz | 4.44M |
| 125 | E0202.EDR | 439.40K |
| 126 | E0202.XLS | 28.69K |
| 127 | E0202安装图.docx | 39.52K |
| 128 | E0202规格书.pdf | 41.58K |
| 129 | E0203.apwz | 4.42M |
| 130 | E0203.EDR | 412.82K |
| 131 | E0203.XLS | 27.66K |
| 132 | E0203规格书.docx | 48.03K |
| 133 | E0203规格书.pdf | 40.10K |
| 134 | E0204.apwz | 4.45M |
| 135 | E0204.EDR | 372.13K |
| 136 | E0204.XLS | 27.99K |
| 137 | E0204安装图.docx | 40.41K |
| 138 | E0204规格书.pdf | 40.56K |
| 139 | E0205.apwz | 4.45M |
| 140 | E0205.EDR | 503.60K |
| 141 | E0205.XLS | 28.66K |
| 142 | E0205安装图.docx | 60.39K |
| 143 | E0205规格书.pdf | 41.11K |
| 144 | E0301.apwz | 4.48M |
| 145 | E0301.EDR | 438.41K |
| 146 | E0301.XLS | 28.38K |
| 147 | E0301安装图.docx | 47.40K |
| 148 | E0301规格书.pdf | 41.85K |
| 149 | E0302.apwz | 4.46M |
| 150 | E0302.EDR | 353.93K |
| 151 | E0302.XLS | 27.85K |
| 152 | E0302安装图.docx | 43.09K |
| 153 | E0302规格书.pdf | 40.33K |
| 154 | E0303.apwz | 4.47M |
| 155 | E0303.EDR | 397.95K |
| 156 | E0303.XLS | 28.18K |
| 157 | E0303安装图.docx | 45.04K |
| 158 | E0303规格书.pdf | 40.74K |
| 159 | E0401.apwz | 4.48M |
| 160 | E0401.EDR | 385.98K |
| 161 | E0401.XLS | 27.91K |
| 162 | E0401安装图.docx | 50.21K |
| 163 | E0401规格书.pdf | 11.78K |
| 164 | E0402.apwz | 4.45M |
| 165 | E0402.EDR | 355.99K |
| 166 | E0402.XLS | 28.05K |
| 167 | E0402安装图.docx | 40.09K |
| 168 | E0402规格书.pdf | 40.87K |
| 169 | E0403.apwz | 4.51M |
| 170 | E0403.EDR | 395.85K |
| 171 | E0403.XLS | 28.12K |
| 172 | E0403规格书.docx | 46.11K |
| 173 | E0403规格书.pdf | 40.94K |
| 174 | E0404.apwz | 4.52M |
| 175 | E0404.EDR | 416.65K |
| 176 | E0404.XLS | 28.25K |
| 177 | E0404安装图.docx | 48.01K |
| 178 | E0404规格书.pdf | 41.46K |
| 179 | E0405.apwz | 4.51M |
| 180 | E0405.EDR | 380.87K |
| 181 | E0405.XLS | 28.54K |
| 182 | E0405安装图.docx | 40.85K |
| 183 | E0405规格书.pdf | 40.75K |
| 184 | E0406.apwz | 4.51M |
| 185 | E0406.EDR | 387.61K |
| 186 | E0406.XLS | 28.19K |
| 187 | E0406安装图.docx | 42.56K |
| 188 | E0406规格书.pdf | 40.16K |
| 189 | E0407.apwz | 4.52M |
| 190 | E0407.EDR | 380.73K |
| 191 | E0407.XLS | 28.09K |
| 192 | E0407安装图.docx | 43.58K |
| 193 | E0407规格书.pdf | 40.03K |
| 194 | E0408.apwz | 4.52M |
| 195 | E0408.EDR | 375.34K |
| 196 | E0408.XLS | 28.16K |
| 197 | E0408安装图.docx | 40.76K |
| 198 | E0408规格书.pdf | 11.93K |
| 199 | E0409.apwz | 4.53M |
| 200 | E0409.EDR | 286.63K |
| 201 | E0409.XLS | 27.69K |
| 202 | E0409安装图.docx | 43.02K |
| 203 | E0409规格书.pdf | 11.54K |
| 204 | E0410.apwz | 4.59M |
| 205 | E0410.EDR | 311.84K |
| 206 | E0410.XLS | 27.18K |
| 207 | E0410安装图.docx | 49.03K |
| 208 | E0410规格书.pdf | 11.68K |
| 209 | 全流程模拟.bkp | 1.41M |
| 210 | 说明.txt | 585B |
| 211 | SDMO路线合成乙二醇的模拟研究.pdf | 3.29M |
| 212 | Vapor–liquidequilibriafortheternarysystemmethanoldimethyl.pdf | 260.44K |
| 213 | 乙二醇_1_2_丁二醇汽液相平衡及分离的研究.caj | 1.72M |
| 214 | 亚硝酸甲酯再生反应的动力学研究.pdf | 423.23K |
| 215 | 亚硝酸甲酯在甲醇溶剂中的亨利常数测定.pdf | 391.76K |
| 216 | 亚硝酸酯合成工艺及反应器选型_吴良泉.caj | 113.84K |
| 217 | 全热耦合精馏塔的动态模拟_赵然然.caj | 1.74M |
| 218 | 真空下1_2_丁二醇_乙二醇二元体系气液平衡数据的测定及关联_陈军航.caj | 470.60K |
| 219 | 真空下1_2_丙二醇_乙二醇二元体系汽液平衡研究_陈卫航.caj | 206.34K |
| 220 | 碳酸酯合成体系中汽液相平衡的测定与关联.pdf | 2.14M |
| 221 | 隔壁热耦合精馏塔的综合与设计_王鹏.caj | 5.92M |
| 222 | R0101预反应器优化.bkp | 319.79K |
| 223 | R0102羰化反应器优化.bkp | 326.52K |
| 224 | R0301反应器优化.bkp | 331.71K |
| 225 | T0102塔板数优化—灵敏度分析.bkp | 447.17K |
| 226 | T0102甲醇量优化—设计规定.bkp | 420.37K |
| 227 | T0103回流比优化—设计规定.bkp | 365.46K |
| 228 | T0103塔板数优化—捷算法.bkp | 270.79K |
| 229 | T0103进料板优化—灵敏度分析.bkp | 364.94K |
| 230 | T0104回流比优化—设计规定.bkp | 320.74K |
| 231 | T0104塔板数优化—灵敏度分析.bkp | 336.08K |
| 232 | T0104进料板优化—灵敏度分析.bkp | 319.31K |
| 233 | T0201侧线采出位置优化—灵敏度分析.bkp | 373.91K |
| 234 | T0201侧线采出量优化—灵敏度分析.bkp | 374.63K |
| 235 | T0201回流比优化—设计规定.bkp | 374.94K |
| 236 | T0201塔板数优化—捷算法.bkp | 269.73K |
| 237 | T0201进料板优化—灵敏度分析.bkp | 374.23K |
| 238 | T0202回流比优化—设计规定.bkp | 327.25K |
| 239 | T0202塔板数优化—捷算法.bkp | 270.34K |
| 240 | T0202进料板优化—灵敏度分析.bkp | 326.53K |
| 241 | T0401侧线采出位置优化—灵敏度分析.bkp | 379.54K |
| 242 | T0401侧线采出量优化—灵敏度分析.bkp | 377.61K |
| 243 | T0401回流比优化—设计规定.bkp | 378.62K |
| 244 | T0401塔板数优化—灵敏度分析.bkp | 396.10K |
| 245 | T0401进料板优化—灵敏度分析.bkp | 380.81K |
| 246 | T0402回流比优化—设计规定.bkp | 374.06K |
| 247 | T0402塔板数优化—捷算法.bkp | 271.02K |
| 248 | T0402进料板优化—灵敏度分析.bkp | 375.17K |
| 249 | T0403侧线采出位置—灵敏度分析.bkp | 333.29K |
| 250 | T0403侧线采出量—灵敏度分析.bkp | 330.17K |
| 251 | T0403回流比优化—灵敏度分析.bkp | 334.62K |
| 252 | T0403塔板数优化——三塔模拟捷算法.bkp | 123.28K |
| 253 | T0403进料板优化—灵敏度分析.bkp | 330.17K |
| 254 | T0101塔结构设计.bkp | 361.24K |
| 255 | T0102塔结构设计.bkp | 435.29K |
| 256 | T0103塔结构设计.bkp | 384.25K |
| 257 | T0104塔结构设计.bkp | 359.95K |
| 258 | T0201塔结构设计.bkp | 389.55K |
| 259 | T0202塔结构设计.bkp | 371.25K |
| 260 | T0401塔结构设计.bkp | 445.46K |
| 261 | T0402塔结构设计.bkp | 451.75K |
| 262 | T0403塔结构设计.bkp | 395.93K |
| 263 | PFD.dwg | 856.66K |
| 264 | PID.dwg | 708.00K |
| 265 | R0101预反应器.dwg | 145.59K |
| 266 | R0102羰化反应器.dwg | 158.93K |
| 267 | R0301加氢反应器.dwg | 154.58K |
| 268 | T0101反应精馏塔.dwg | 239.71K |
| 269 | T0403分隔壁塔.dwg | 136.62K |
| 270 | 工厂总平面布置图.dwg | 124.43K |
| 271 | 管道轴测图.dwg | 59.23K |
| 272 | 说明.txt | 509B |
| 273 | 车间布置图.dwg | 466.62K |
| 274 | 说明.txt | 553B |
| 275 | T0101提馏段校核源文件.plc | 204.00K |
| 276 | T0101提馏段输出报告.doc | 296.50K |
| 277 | T0101水力学数据.xls | 21.00K |
| 278 | T0101精馏段源文件.pak | 688B |
| 279 | T0101精馏段示意图.pdf | 57.41K |
| 280 | T0101精馏段设计数据.pdf | 68.91K |
| 281 | T0101精馏段负荷性能图.pdf | 112.96K |
| 282 | T0103提馏段输出报告.doc | 297.00K |
| 283 | T0103校核源文件.plc | 212.00K |
| 284 | T0103水力学数据.xls | 35.50K |
| 285 | T0103精馏段输出报告.doc | 297.00K |
| 286 | T0104提馏段输出报告.doc | 298.00K |
| 287 | T0104校核源文件.plc | 212.00K |
| 288 | T0104水力学数据.xls | 32.50K |
| 289 | T0104精馏段输出报告.doc | 297.00K |
| 290 | T0201校核源文件.plc | 204.00K |
| 291 | T0201水力学数据.xls | 39.00K |
| 292 | T0201输出报告.doc | 296.50K |
| 293 | T0202提馏段输出报告.doc | 298.50K |
| 294 | T0202校核源文件.plc | 212.00K |
| 295 | T0202水力学数据.xls | 37.00K |
| 296 | T0202精馏段输出报告.doc | 295.00K |
| 297 | 说明.txt | 478B |
| 298 | 10minNO储罐泄漏.jpg | 107.56K |
| 299 | 5minNO储罐泄漏.jpg | 45.97K |
| 300 | NO储罐泄漏源文件.rsm | 495B |
| 301 | CO10min泄漏.jpg | 111.55K |
| 302 | CO5min泄漏.jpg | 113.75K |
| 303 | CO储罐泄漏源文件.rsm | 499B |
| 304 | 1.jpg | 75.70K |
| 305 | 2.jpg | 48.60K |
| 306 | 3.jpg | 57.05K |
| 307 | 4.jpg | 44.27K |
| 308 | 一氧化碳储罐爆炸源文件.rsm | 198B |
| 309 | 模拟结果.jpg | 105.32K |
| 310 | 1.jpg | 48.86K |
| 311 | 2.jpg | 75.69K |
| 312 | 3.jpg | 55.72K |
| 313 | 4.jpg | 45.56K |
| 314 | 乙二醇储罐爆炸源文件.rsm | 197B |
| 315 | 模拟结果.jpg | 108.02K |
| 316 | 1.jpg | 74.57K |
| 317 | 2.jpg | 47.06K |
| 318 | 3.jpg | 57.14K |
| 319 | 4.jpg | 44.31K |
| 320 | 模拟结果.jpg | 100.91K |
| 321 | 氢气储罐爆炸源文件.rsm | 193B |
| 322 | 1.jpg | 48.39K |
| 323 | 2.jpg | 76.02K |
| 324 | 3.jpg | 58.21K |
| 325 | 4.jpg | 44.42K |
| 326 | 模拟结果.jpg | 103.61K |
| 327 | 甲醇储罐爆炸源文件.rsm | 169B |
| 328 | MN再生车间.max | 423.63M |
| 329 | MN再生车间.ses | 8.55M |
| 330 | 说明.txt | 570B |
| 331 | 1.jpg | 287.76K |
| 332 | 2.jpg | 160.45K |
| 333 | 3.jpg | 194.30K |
| 334 | 4.jpg | 243.79K |
| 335 | 0103_Sheet1.dwg | 33.47K |
| 336 | 0103_Sheet11.tif | 49.48K |
| 337 | 0104_Sheet1.dwg | 31.72K |
| 338 | 0104_Sheet11.tif | 50.18K |
| 339 | 0105_Sheet1.dwg | 37.69K |
| 340 | 0105_Sheet11.tif | 50.34K |
| 341 | 0106_Sheet1.dwg | 30.28K |
| 342 | 0106_Sheet11.tif | 50.18K |
| 343 | 0108_Sheet1.dwg | 31.84K |
| 344 | 0108_Sheet11.tif | 50.32K |
| 345 | 0109_Sheet1.dwg | 41.44K |
| 346 | 0109_Sheet11.tif | 75.16K |
| 347 | 0110_Sheet1.dwg | 40.47K |
| 348 | 0110_Sheet11.tif | 74.99K |
| 349 | 0111_Sheet1.dwg | 28.68K |
| 350 | 0111_Sheet11.tif | 50.00K |
| 351 | 0404_Sheet1.dwg | 32.16K |
| 352 | 0404_Sheet11.tif | 50.18K |
| 353 | 0408_Sheet1.dwg | 38.53K |
| 354 | 0408_Sheet11.tif | 75.16K |
| 355 | 0409_Sheet1.dwg | 40.35K |
| 356 | 0409_Sheet11.tif | 74.99K |
| 357 | 0410_Sheet1.dwg | 34.19K |
| 358 | 0410_Sheet11.tif | 49.29K |
| 359 | lengshuichu_Sheet1.dwg | 40.60K |
| 360 | lengshuichu_Sheet11.tif | 76.21K |
| 361 | lengshuijin_Sheet1.dwg | 37.81K |
| 362 | lengshuijin_Sheet11.tif | 76.21K |
| 363 | t0101hl01_Sheet1.dwg | 33.69K |
| 364 | t0101hl01_Sheet11.tif | 50.44K |
| 365 | t0101hl02_Sheet1.dwg | 32.63K |
| 366 | t0101hl02_Sheet11.tif | 50.24K |
| 367 | t0101hl03_Sheet1.dwg | 40.97K |
| 368 | t0101hl03_Sheet11.tif | 74.99K |
| 369 | t0101hl04_Sheet1.dwg | 41.84K |
| 370 | t0101hl04_Sheet11.tif | 74.99K |
| 371 | t0104hl01_Sheet1.dwg | 34.06K |
| 372 | t0104hl01_Sheet11.tif | 50.27K |
| 373 | t0104hl02_Sheet1.dwg | 28.43K |
| 374 | t0104hl02_Sheet11.tif | 49.51K |
| 375 | t0104hl03_Sheet1.dwg | 40.44K |
| 376 | t0104hl03_Sheet11.tif | 74.99K |
| 377 | t0104hl04_Sheet1.dwg | 42.25K |
| 378 | t0104hl04_Sheet11.tif | 74.99K |
| 379 | zfq1_Sheet1.dwg | 20.87K |
| 380 | zfq1_Sheet11.tif | 75.51K |
| 381 | zfq2_Sheet1.dwg | 20.55K |
| 382 | zfq2_Sheet11.tif | 75.77K |
| 383 | zhengqichu_Sheet1.dwg | 45.12K |
| 384 | zhengqichu_Sheet11.tif | 76.01K |
| 385 | zhengqijin_Sheet1.dwg | 43.66K |
| 386 | zhengqijin_Sheet11.tif | 76.21K |
| 387 | 说明.txt | 570B |
| 388 | T0101提馏段校核源文件.plc | 204.00K |
| 389 | T0101提馏段输出报告.doc | 296.50K |
| 390 | T0101水力学数据.xls | 21.00K |
| 391 | T0101精馏段源文件.pak | 688B |
| 392 | T0101精馏段示意图.pdf | 57.41K |
| 393 | T0101精馏段设计数据.pdf | 68.91K |
| 394 | T0101精馏段负荷性能图.pdf | 112.96K |
| 395 | T0102水力学数据.xls | 42.00K |
| 396 | T0102源文件.pak | 1.05K |
| 397 | T0102示意图.pdf | 59.28K |
| 398 | T0102设计数据.pdf | 76.29K |
| 399 | T0102负荷性能图.pdf | 222.87K |
| 400 | T0401水力学数据.xls | 42.00K |
| 401 | T0401源文件.pak | 1.05K |
| 402 | T0401示意图.pdf | 58.35K |
| 403 | T0401设计数据.pdf | 76.29K |
| 404 | T0401负荷性能图.pdf | 222.67K |
| 405 | T0402水力学数据.xls | 48.50K |
| 406 | T0402源文件.pak | 1.19K |
| 407 | T0402示意图.pdf | 58.45K |
| 408 | T0402设计数据.pdf | 83.89K |
| 409 | T0402负荷性能图.pdf | 278.31K |
| 410 | T0403主塔水力学数据.xls | 46.50K |
| 411 | T0403主塔源文件.pak | 1.40K |
| 412 | T0403主塔示意图.pdf | 58.98K |
| 413 | T0403主塔设计数据.pdf | 84.87K |
| 414 | T0403主塔负荷性能图.pdf | 335.78K |
| 415 | T0403副塔水力学数据.xls | 30.50K |
| 416 | T0403副塔源文件.pak | 726B |
| 417 | T0403副塔示意图.pdf | 60.87K |
| 418 | T0403副塔设计数据.pdf | 70.05K |
| 419 | T0403副塔负荷性能图.pdf | 145.45K |
| 420 | 说明.txt | 459B |
| 421 | T0101.cn2 | 30.20K |
| 422 | T0101.doc | 798.50K |
| 423 | T0102.cn2 | 30.20K |
| 424 | T0102.doc | 764.50K |
| 425 | T0103.cn2 | 30.20K |
| 426 | T0103.doc | 817.00K |
| 427 | T0104.cn2 | 30.20K |
| 428 | T0104.doc | 950.50K |
| 429 | T0201.cn2 | 30.20K |
| 430 | T0201.doc | 807.00K |
| 431 | T0202.cn2 | 30.20K |
| 432 | T0202.doc | 817.00K |
| 433 | T0401.cn2 | 30.20K |
| 434 | T0401.doc | 928.00K |
| 435 | T0402.cn2 | 30.20K |
| 436 | T0402.doc | 764.50K |
| 437 | T0403.cn2 | 30.20K |
| 438 | T0403.doc | 779.00K |
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