登录注册
微信扫码登录
100万吨年对二甲苯项目初步设计（ID:2685575）
0.png)
0.png)
0.png)
0.png)
0.png)
| # | 文件名称 | 文件大小 |
|---|---|---|
| 1 | 17591189817836.zip | 204.28M |
| 2 | 7-致广大市民的一封信.docx | 19.54K |
| 3 | 致评委老师.doc | 25.00K |
| 4 | 参考文献.docx | 37.03K |
| 5 | 摘要-2003版.doc | 1.93M |
| 6 | 摘要-2007版.docx | 1.69M |
| 7 | 摘要.pdf | 1.59M |
| 8 | DesignAbstract-2003版.doc | 1.96M |
| 9 | DesignAbstract-2007版.docx | 1.74M |
| 10 | DesignAbstract.pdf | 1.57M |
| 11 | 可行性研究报告-2003版.doc | 5.43M |
| 12 | 可行性研究报告-2007版.docx | 3.43M |
| 13 | 可行性研究报告.pdf | 3.26M |
| 14 | 初步设计说明书-2003版.doc | 7.64M |
| 15 | 初步设计说明书-2007版.docx | 7.33M |
| 16 | 初步设计说明书.pdf | 7.48M |
| 17 | 设备一览表-2003版.doc | 315.50K |
| 18 | 设备一览表-2007版.docx | 67.06K |
| 19 | 设备一览表.pdf | 779.41K |
| 20 | 附录-2003版.doc | 2.81M |
| 21 | 附录-2007版.docx | 1.14M |
| 22 | 附录.pdf | 3.76M |
| 23 | 创新性说明-2003版.doc | 3.33M |
| 24 | 创新性说明-2007版.docx | 2.68M |
| 25 | 创新性说明.pdf | 1.39M |
| 26 | 安全评价报告-2003版.doc | 5.43M |
| 27 | 安全评价报告-2007版.docx | 5.04M |
| 28 | 安全评价报告.pdf | 2.83M |
| 29 | 环境影响报告-2003版.doc | 5.95M |
| 30 | 环境影响报告-2007版.docx | 4.72M |
| 31 | 环境影响报告.pdf | 2.21M |
| 32 | 03-设计图册.pdf | 28.18M |
| 33 | 首页图.dwg | 47.95K |
| 34 | PFD.bak | 995.58K |
| 35 | PFD.dwg | 995.82K |
| 36 | PID.dwg | 1.10M |
| 37 | 1-抽提工段车间布置图.dwg | 392.95K |
| 38 | 2-歧化及烷基转移工段车间布置图.dwg | 378.06K |
| 39 | 3-二甲苯分馏工段车间布置图.dwg | 390.66K |
| 40 | 4-吸附、结晶分离工段车间布置图.dwg | 579.88K |
| 41 | 5-异构化工段车间布置图.dwg | 361.50K |
| 42 | 歧化反应器R-0201装配图.dwg | 279.48K |
| 43 | 苯产品冷凝器E-0210装配图.dwg | 285.02K |
| 44 | 轻烃塔T-0502装配图.dwg | 149.60K |
| 45 | 管道轴测图.dwg | 435.60K |
| 46 | 厂区平面布置图.dwg | 160.40K |
| 47 | 首页图.dwg | 67.19K |
| 48 | PFD.dwg | 1.58M |
| 49 | PID.dwg | 1.63M |
| 50 | 1-抽提工段车间布置图.dwg | 443.41K |
| 51 | 2-歧化及烷基转移工段车间布置图.dwg | 378.91K |
| 52 | 3-二甲苯分馏工段车间布置图.dwg | 394.39K |
| 53 | 4-吸附、结晶分离工段车间布置图.dwg | 613.53K |
| 54 | 5-异构化工段车间布置图.dwg | 370.19K |
| 55 | 2010版歧化反应器R-0201装配图.dwg | 338.44K |
| 56 | 2010版轻烃塔T-0502装配图.dwg | 188.07K |
| 57 | 歧化反应器R-0201装配图.dwg | 315.00K |
| 58 | 苯产品冷凝器E-0210装配图.dwg | 336.47K |
| 59 | 轻烃塔T-0502装配图.dwg | 196.75K |
| 60 | 管道轴测图.dwg | 490.13K |
| 61 | 厂区平面布置图.dwg | 188.03K |
| 62 | 厂区全貌.jpg | 674.21K |
| 63 | 厂区总览.jpg | 583.09K |
| 64 | 生产装置区1.jpg | 558.08K |
| 65 | 生产装置区2.jpg | 610.52K |
| 66 | 生产装置区3.jpg | 574.72K |
| 67 | 生产装置区4.jpg | 518.57K |
| 68 | 车间泵区.jpg | 843.61K |
| 69 | 二甲苯异构化反应器的模拟研究.pdf | 2.76M |
| 70 | 对二甲苯悬浮熔融结晶动力学.pdf | 323.31K |
| 71 | 甲苯歧化与C9芳烃烷基转移反应动力学模型和模拟分析.pdf | 525.98K |
| 72 | 高质量分数对二甲苯结晶动力学研究.pdf | 358.50K |
| 73 | CO.amd | 426.73K |
| 74 | CO.jpg | 321.21K |
| 75 | NO2.amd | 426.73K |
| 76 | NO2.jpg | 328.19K |
| 77 | PM10.amd | 428.43K |
| 78 | pm10.jpg | 324.62K |
| 79 | S02.amd | 427.31K |
| 80 | SO2.jpg | 324.84K |
| 81 | 大气评价.xls | 51.50K |
| 82 | aermod.inp | 2.89K |
| 83 | AERMOD.OUT | 99.93K |
| 84 | bp.txt | 2.19K |
| 85 | bpipprm.inp | 360B |
| 86 | bpipprm.out | 4.47K |
| 87 | bpipprm.sum | 22.35K |
| 88 | aemodProf.PFL | 2.77K |
| 89 | aemodSurf.SFC | 7.36K |
| 90 | CO_所有_POST_1h.BIN | 118.69K |
| 91 | CO_所有_POST_24h.BIN | 4.95K |
| 92 | CO_控制流文件.inp | 2.89K |
| 93 | CO_输出文件.OUT | 99.93K |
| 94 | 1.txt | 176B |
| 95 | 2.txt | 176B |
| 96 | aermod.inp | 2.92K |
| 97 | AERMOD.OUT | 100.06K |
| 98 | bp.txt | 2.19K |
| 99 | bpipprm.inp | 360B |
| 100 | bpipprm.out | 4.47K |
| 101 | bpipprm.sum | 22.35K |
| 102 | aemodProf.PFL | 2.77K |
| 103 | aemodSurf.SFC | 7.36K |
| 104 | SO2_所有_POST_1h.BIN | 118.69K |
| 105 | SO2_所有_POST_24h.BIN | 4.95K |
| 106 | SO2_控制流文件.inp | 2.92K |
| 107 | SO2_输出文件.OUT | 100.06K |
| 108 | 1.txt | 176B |
| 109 | 2.txt | 176B |
| 110 | aermod.inp | 2.96K |
| 111 | AERMOD.OUT | 101.11K |
| 112 | bp.txt | 2.19K |
| 113 | bpipprm.inp | 360B |
| 114 | bpipprm.out | 4.47K |
| 115 | bpipprm.sum | 22.35K |
| 116 | aemodProf.PFL | 2.77K |
| 117 | aemodSurf.SFC | 7.36K |
| 118 | NO2_所有_POST_1h.BIN | 118.69K |
| 119 | NO2_所有_POST_24h.BIN | 4.95K |
| 120 | NO2_控制流文件.inp | 2.96K |
| 121 | NO2_输出文件.OUT | 101.11K |
| 122 | 1.txt | 176B |
| 123 | 2.txt | 176B |
| 124 | 吸附分离简介.pdf | 218.75K |
| 125 | 模拟效果展示.avi | 9.23M |
| 126 | 模拟移动床.cra | 2.33M |
| 127 | 模拟移动床吸附分离简介.pdf | 202.42K |
| 128 | 运行说明.txt | 308B |
| 129 | E0101.EDR | 341.99K |
| 130 | E0102.EDR | 372.57K |
| 131 | E0103.EDR | 457.35K |
| 132 | E0104.EDR | 426.03K |
| 133 | E0105.EDR | 314.40K |
| 134 | E0106.EDR | 386.95K |
| 135 | E0107.EDR | 399.12K |
| 136 | E0108.EDR | 336.92K |
| 137 | E0201.EDR | 342.17K |
| 138 | E0203.EDR | 549.54K |
| 139 | E0204.EDR | 353.78K |
| 140 | E0205.EDR | 380.70K |
| 141 | E0206.EDR | 429.88K |
| 142 | E0207.EDR | 493.96K |
| 143 | E0208.EDR | 334.75K |
| 144 | E0209.EDR | 334.98K |
| 145 | E0301.EDR | 457.17K |
| 146 | E0302.EDR | 314.40K |
| 147 | E0303.EDR | 406.16K |
| 148 | E0304.EDR | 346.36K |
| 149 | E0305.EDR | 356.72K |
| 150 | E0401.EDR | 481.82K |
| 151 | E0402.EDR | 399.30K |
| 152 | E0403.EDR | 342.17K |
| 153 | E0404.EDR | 376.30K |
| 154 | E0406.EDR | 493.96K |
| 155 | E0501.EDR | 339.12K |
| 156 | E0502.EDR | 342.17K |
| 157 | E0503.EDR | 314.40K |
| 158 | E0504.EDR | 431.72K |
| 159 | E0505.EDR | 481.82K |
| 160 | 二甲苯分馏工段换热网络优化.hch | 549.00K |
| 161 | 吸附结晶分离换热网络优化.hch | 389.38K |
| 162 | 异构化换热网络优化.hch | 732.66K |
| 163 | 抽提工段换热网络优化.hch | 465.31K |
| 164 | 歧化及烷基转移换热网络优化.hch | 1.88M |
| 165 | lsprst7.dll | 228B |
| 166 | lsprst7.tgz | 242B |
| 167 | sysprs7.dll | 1.00K |
| 168 | sysprs7.tgz | 1.00K |
| 169 | 抽余液塔.appdf | 349.77K |
| 170 | 抽余液塔.apw | 1.19M |
| 171 | 抽余液塔.bkp | 238.44K |
| 172 | 抽余液塔.def | 195B |
| 173 | 抽余液塔.dynf | 521.94K |
| 174 | 抽余液塔.for | 0B |
| 175 | 抽余液塔.his | 55.03K |
| 176 | 抽余液塔2.dynf | 1.74M |
| 177 | 抽余液塔dyn.appdf | 349.58K |
| 178 | 抽余液塔dyn.his | 2.70K |
| 179 | 抽余液塔dyn.rep | 0B |
| 180 | snapshot.bak | 5.11M |
| 181 | snpA0000.snp | 5.50M |
| 182 | snpA0001.snp | 4.14M |
| 183 | snpA0002.snp | 4.88M |
| 184 | snpA0003.snp | 5.84M |
| 185 | snpA0004.snp | 7.73M |
| 186 | snpA0005.snp | 5.84M |
| 187 | snpA0006.snp | 5.84M |
| 188 | snpA0007.snp | 5.84M |
| 189 | snpA0008.snp | 7.93M |
| 190 | snpA0009.snp | 4.88M |
| 191 | snpA0010.snp | 5.83M |
| 192 | snpA0011.snp | 5.84M |
| 193 | snpA0012.snp | 5.83M |
| 194 | snpA0013.snp | 5.84M |
| 195 | snpA0014.snp | 5.84M |
| 196 | snpA0015.snp | 5.84M |
| 197 | snpA0016.snp | 5.84M |
| 198 | snpA0017.snp | 5.83M |
| 199 | snpA0018.snp | 5.83M |
| 200 | snpA0019.snp | 5.84M |
| 201 | snpA0020.snp | 5.85M |
| 202 | snpA0021.snp | 5.85M |
| 203 | snpA0022.snp | 5.96M |
| 204 | snpA0023.snp | 7.74M |
| 205 | snpA0024.snp | 6.70M |
| 206 | snpA0025.snp | 11.53M |
| 207 | snpA0026.snp | 8.59M |
| 208 | snpA0027.snp | 9.64M |
| 209 | snpA0028.snp | 6.70M |
| 210 | snpA0029.snp | 7.65M |
| 211 | tasksnap.bak | 856B |
| 212 | 抽余液塔dyn.his | 3.17K |
| 213 | 抽余液塔dyn.rep | 0B |
| 214 | 二甲苯分馏工段.bkp | 603.81K |
| 215 | 全流程.bkp | 2.28M |
| 216 | 吸附、结晶工段.bkp | 458.46K |
| 217 | 异构化工段.bkp | 449.19K |
| 218 | 抽提工段.bkp | 598.72K |
| 219 | 歧化及烷基转移工段.bkp | 519.39K |
| 220 | T0101优化.bkp | 213.23K |
| 221 | T0102优化.bkp | 405.57K |
| 222 | T0103优化.bkp | 93.61K |
| 223 | T0104优化.bkp | 165.29K |
| 224 | T0201优化.bkp | 201.88K |
| 225 | T0301优化.bkp | 412.09K |
| 226 | T0302优化.bkp | 339.71K |
| 227 | T0303优化.bkp | 207.92K |
| 228 | T0402优化.bkp | 240.29K |
| 229 | T0403优化.bkp | 169.19K |
| 230 | T0501-T0502优化.bkp | 451.50K |
| 231 | 分隔壁精馏塔优化.bkp | 271.63K |
| 232 | 抽提蒸馏塔带回流.bkp | 82.79K |
| 233 | 中间冷凝.bkp | 441.82K |
| 234 | 分隔壁精馏塔.bkp | 367.76K |
| 235 | 异构化热高分技术.bkp | 145.94K |
| 236 | 歧化热高分技术.bkp | 149.97K |
| 237 | 高品位热量的利用.bkp | 174.47K |
| 238 | Scenario1.izp | 2.67M |
| 239 | Scenario1.szp | 3.35M |
| 240 | 123_Xref_01.doc | 37.54M |
| 241 | Default.doc | 12.19M |
| 242 | Default2.doc | 11.43M |
| 243 | Default_Xref_012.doc | 38.56M |
| 244 | 首页图.dwg | 47.95K |
| 245 | PFD.bak | 995.58K |
| 246 | PFD.dwg | 995.89K |
| 247 | PID.dwg | 1.10M |
| 248 | 1-抽提工段车间布置图.dwg | 392.95K |
| 249 | 2-歧化及烷基转移工段车间布置图.dwg | 378.06K |
| 250 | 3-二甲苯分馏工段车间布置图.dwg | 390.66K |
| 251 | 4-吸附、结晶分离工段车间布置图.dwg | 579.88K |
| 252 | 5-异构化工段车间布置图.dwg | 361.50K |
| 253 | 歧化反应器R-0201装配图.dwg | 315.00K |
| 254 | 苯产品冷凝器E-0210装配图.dwg | 285.02K |
| 255 | 轻烃塔T-0502装配图.dwg | 149.60K |
| 256 | 管道轴测图.dwg | 435.60K |
| 257 | 厂区平面布置图.dwg | 160.40K |
| 258 | 首页图.dwg | 67.19K |
| 259 | PFD.dwg | 1.58M |
| 260 | PID.dwg | 1.63M |
| 261 | 1-抽提工段车间布置图.dwg | 443.41K |
| 262 | 2-歧化及烷基转移工段车间布置图.dwg | 378.91K |
| 263 | 3-二甲苯分馏工段车间布置图.dwg | 394.39K |
| 264 | 4-吸附、结晶分离工段车间布置图.dwg | 600.63K |
| 265 | 5-异构化工段车间布置图.dwg | 370.19K |
| 266 | 2010版歧化反应器R-0201装配图.dwg | 338.44K |
| 267 | 2010版轻烃塔T-0502装配图.dwg | 188.07K |
| 268 | 歧化反应器R-0201装配图.dwg | 473.72K |
| 269 | 苯产品冷凝器E-0210装配图.dwg | 336.47K |
| 270 | 轻烃塔T-0502装配图.dwg | 196.75K |
| 271 | 管道轴测图.dwg | 490.13K |
| 272 | 厂区平面布置图.dwg | 188.03K |
| 273 | T0101.plc | 200.00K |
| 274 | T0101.xlsx | 20.95K |
| 275 | T0101校核.xlsx | 100.69K |
| 276 | T0102.plc | 200.00K |
| 277 | T0102.xlsx | 25.70K |
| 278 | T0102校核.xlsx | 99.45K |
| 279 | T0103.plc | 200.00K |
| 280 | T0103.xlsx | 12.22K |
| 281 | T0103校核.xlsx | 167.25K |
| 282 | T0104.plc | 200.00K |
| 283 | T0104.xlsx | 15.59K |
| 284 | T0104校核.xlsx | 156.81K |
| 285 | T0201-1.plc | 200.00K |
| 286 | T0201-1校核.xlsx | 168.48K |
| 287 | T0201-2.plc | 200.00K |
| 288 | T0201-2校核.xlsx | 165.26K |
| 289 | T0201.xlsx | 17.95K |
| 290 | T0301.plc | 200.00K |
| 291 | T0301.xlsx | 31.83K |
| 292 | T0301校核.xlsx | 175.13K |
| 293 | T0302.plc | 200.00K |
| 294 | T0302.xlsx | 28.71K |
| 295 | T0302校核.xlsx | 175.17K |
| 296 | T0303.plc | 200.00K |
| 297 | T0303.xlsx | 20.67K |
| 298 | T0303校核.xlsx | 197.98K |
| 299 | T0402.plc | 200.00K |
| 300 | T0402.xlsx | 22.89K |
| 301 | T0402校核.xlsx | 191.00K |
| 302 | T0403.plc | 200.00K |
| 303 | T0403.xlsx | 18.60K |
| 304 | T0403校核.xlsx | 168.82K |
| 305 | T0501.plc | 200.00K |
| 306 | T0501.xlsx | 18.74K |
| 307 | T0501校核.xlsx | 174.18K |
| 308 | T0502.plc | 200.00K |
| 309 | T0502.xlsx | 15.40K |
| 310 | T0502校核.xlsx | 185.92K |
| 311 | 分割壁塔.plc | 200.00K |
| 312 | 分割壁塔.xlsx | 19.09K |
| 313 | 分割壁塔校核.xlsx | 185.92K |
| 314 | 噪音评价.xls | 44.00K |
| 315 | 夜间叠加值.jpg | 258.96K |
| 316 | 夜间垂向线接受点.jpg | 61.34K |
| 317 | 徐圩区.nosm | 824B |
| 318 | 昼间叠加值.jpg | 285.97K |
| 319 | 昼间垂向线接受点.jpg | 52.17K |
| 320 | 对二甲苯储罐爆炸模拟.jpg | 208.94K |
| 321 | 对二甲苯储罐爆炸模拟.rsm | 176B |
| 322 | 对二甲苯储罐爆炸模拟预测结果.jpg | 70.22K |
| 323 | 对二甲苯储罐爆炸模拟预测范围.jpg | 207.49K |
| 324 | 混合芳烃储罐爆炸模拟.rsm | 179B |
| 325 | 混合芳烃储罐爆炸蒸汽云爆炸预测.jpg | 72.17K |
| 326 | 混合芳烃储罐爆炸蒸汽云爆炸预测模型伤害范围.jpg | 208.60K |
| 327 | 苯储罐爆炸模拟.rsm | 167B |
| 328 | 苯储罐爆炸模拟预测结果.jpg | 70.48K |
| 329 | 苯储罐爆炸模拟预测范围.jpg | 207.47K |
| 330 | 邻二甲苯储罐爆炸模拟.rsm | 177B |
| 331 | 邻二甲苯储罐爆炸模拟预测结果.jpg | 70.45K |
| 332 | 邻二甲苯储罐爆炸模拟预测范围.jpg | 208.17K |
| 333 | 苯储罐泄漏模拟.rsm | 484B |
| 334 | 苯储罐泄露模拟-10min.jpg | 75.02K |
| 335 | 苯储罐泄露模拟-5min.jpg | 75.00K |
| 336 | RUNNERS车间三维布置.ses | 39.72M |
| 337 | 主视图.jpg | 348.18K |
| 338 | 全貌.jpg | 383.39K |
| 339 | 右视.jpg | 306.58K |
| 340 | 后视图.jpg | 424.05K |
| 341 | 管子主视图.jpg | 158.31K |
| 342 | 管子全貌.jpg | 174.46K |
| 343 | 管子右视图.jpg | 145.01K |
| 344 | 管子顶视图.jpg | 169.06K |
| 345 | 设备主视.jpg | 162.94K |
| 346 | 设备全貌.jpg | 231.44K |
| 347 | 设备右视.jpg | 185.40K |
| 348 | 设备顶视.jpg | 241.79K |
| 349 | 钢结构全貌.jpg | 370.64K |
| 350 | 钢结构前视图.jpg | 184.27K |
| 351 | 钢结构右视图.jpg | 149.84K |
| 352 | 钢结构顶视图.jpg | 193.50K |
| 353 | 顶视.jpg | 373.79K |
| 354 | V0101.ht2 | 22.62K |
| 355 | V0101右封头.doc | 70.00K |
| 356 | V0101左封头.doc | 72.00K |
| 357 | V0101筒体.doc | 67.50K |
| 358 | V0102.ht2 | 22.62K |
| 359 | V0102右封头.doc | 70.00K |
| 360 | V0102左封头.doc | 70.00K |
| 361 | V0102筒体.doc | 67.50K |
| 362 | V0103.ht2 | 22.62K |
| 363 | V0103右封头.doc | 70.00K |
| 364 | V0103左封头.doc | 70.00K |
| 365 | V0103筒体.doc | 67.50K |
| 366 | V0104.ht2 | 22.62K |
| 367 | V0104右封头.doc | 70.00K |
| 368 | V0104左封头.doc | 70.00K |
| 369 | V0104筒体.doc | 67.50K |
| 370 | V0105.ht2 | 22.62K |
| 371 | V0105右封头.doc | 70.00K |
| 372 | V0105左封头.doc | 70.00K |
| 373 | V0105筒体.doc | 67.50K |
| 374 | V0201.ht2 | 22.62K |
| 375 | V0201右封头.doc | 70.00K |
| 376 | V0201左封头.doc | 70.00K |
| 377 | V0201筒体.doc | 67.50K |
| 378 | V0203.ht2 | 22.62K |
| 379 | V0203右封头.doc | 70.00K |
| 380 | V0203左封头.doc | 67.50K |
| 381 | V0203筒体.doc | 70.00K |
| 382 | V0204.ht2 | 22.62K |
| 383 | V0204右封头.doc | 70.00K |
| 384 | V0204左封头.doc | 70.00K |
| 385 | V0204筒体.doc | 67.50K |
| 386 | V0205.ht2 | 22.62K |
| 387 | V0205右封头.doc | 70.00K |
| 388 | V0205左封头.doc | 67.50K |
| 389 | V0205筒体.doc | 70.00K |
| 390 | V0301.ht2 | 22.62K |
| 391 | V0301右封头.doc | 70.00K |
| 392 | V0301左封头.doc | 70.00K |
| 393 | V0301筒体.doc | 67.50K |
| 394 | V0302.ht2 | 22.62K |
| 395 | V0302右封头.doc | 70.00K |
| 396 | V0302左封头.doc | 70.00K |
| 397 | V0302筒体.doc | 67.50K |
| 398 | V0303.ht2 | 22.62K |
| 399 | V0303右封头.doc | 70.00K |
| 400 | V0303左封头.doc | 70.00K |
| 401 | V0303筒体.doc | 67.50K |
| 402 | V0304.ht2 | 22.62K |
| 403 | V0304右封头.doc | 70.00K |
| 404 | V0304左封头.doc | 70.00K |
| 405 | V0304筒体.doc | 67.50K |
| 406 | V0402.ht2 | 22.62K |
| 407 | V0402右封头.doc | 70.00K |
| 408 | V0402左封头.doc | 70.00K |
| 409 | V0402筒体.doc | 67.50K |
| 410 | V0403.ht2 | 22.62K |
| 411 | V0403右封头.doc | 70.00K |
| 412 | V0403左封头.doc | 70.00K |
| 413 | V0403筒体.doc | 67.50K |
| 414 | V0404.ht2 | 22.62K |
| 415 | V0404右封头.doc | 70.00K |
| 416 | V0404左封头.doc | 70.00K |
| 417 | V0404筒体.doc | 67.50K |
| 418 | V0501.ht2 | 22.62K |
| 419 | V0501右封头.doc | 70.00K |
| 420 | V0501左封头.doc | 70.00K |
| 421 | V0501筒体.doc | 67.50K |
| 422 | V0503.ht2 | 22.62K |
| 423 | V0503右封头.doc | 70.00K |
| 424 | V0503左封头.doc | 70.00K |
| 425 | V0503筒体.doc | 67.50K |
| 426 | V0504.ht2 | 22.62K |
| 427 | V0504右封头.doc | 70.00K |
| 428 | V0504左封头.doc | 70.00K |
| 429 | V0504筒体.doc | 67.50K |
| 430 | V0601.dot | 62.00K |
| 431 | V0601.ra2 | 23.24K |
| 432 | V0601上封头.dot | 62.50K |
| 433 | R0201.hp2 | 21.67K |
| 434 | R0201上封头.doc | 62.50K |
| 435 | R0201下封头.doc | 62.50K |
| 436 | R0201筒体.doc | 167.00K |
| 437 | T0101.cn2 | 30.20K |
| 438 | T0101上封头.doc | 70.00K |
| 439 | T0101下封头.doc | 70.00K |
| 440 | T0102.cn2 | 30.20K |
| 441 | T0102上封头.doc | 70.00K |
| 442 | T0102下封头.doc | 70.00K |
| 443 | T0103.cn2 | 30.20K |
| 444 | T0103上封头.doc | 70.00K |
| 445 | T0103下封头.doc | 70.00K |
| 446 | T0104.cn2 | 30.20K |
| 447 | T0104上封头.doc | 70.00K |
| 448 | T0104下封头.doc | 70.00K |
| 449 | T0201-1.cn2 | 30.20K |
| 450 | T0201-1上封头.doc | 70.00K |
| 451 | T0201-1下封头.doc | 70.00K |
| 452 | T0201-2.cn2 | 30.20K |
| 453 | T0201-2上封头.doc | 70.00K |
| 454 | T0201-2下封头.doc | 70.00K |
| 455 | T0201.cn2 | 30.20K |
| 456 | T0201上封头.doc | 70.00K |
| 457 | T0201下封头.doc | 70.00K |
| 458 | T0203上封头（主）.doc | 70.00K |
| 459 | T0203上封头（副）.doc | 72.00K |
| 460 | T0203下封头（主）.doc | 70.00K |
| 461 | T0203下封头（副）.doc | 70.00K |
| 462 | T0203主）.cn2 | 30.20K |
| 463 | T0203副）.cn2 | 30.20K |
| 464 | T0302.cn2 | 30.20K |
| 465 | T0302上封头.doc | 70.00K |
| 466 | T0302下封头.doc | 70.00K |
| 467 | T0303.cn2 | 30.20K |
| 468 | T0303上封头.doc | 70.00K |
| 469 | T0303下封头.doc | 70.00K |
| 470 | T0304.cn2 | 30.20K |
| 471 | T0304上封头.doc | 70.00K |
| 472 | T0304下封头.doc | 70.00K |
| 473 | T0402.cn2 | 30.20K |
| 474 | T0402上封头.doc | 70.00K |
| 475 | T0402下封头.doc | 70.00K |
| 476 | T0403.cn2 | 30.20K |
| 477 | T0403上封头.doc | 70.00K |
| 478 | T0403下封头.doc | 70.00K |
| 479 | T0404.cn2 | 30.20K |
| 480 | T0404上封头.doc | 70.00K |
| 481 | T0404下封头.doc | 70.00K |
| 482 | T0501.cn2 | 30.20K |
| 483 | T0501上封头.doc | 70.00K |
| 484 | T0501下封头.doc | 70.00K |
| 485 | T0502.cn2 | 30.20K |
| 486 | T0502上封头.doc | 70.00K |
| 487 | T0502下封头.doc | 70.00K |
| 488 | E0101.fx2 | 24.00K |
| 489 | 前端管箱筒体.dot | 112.00K |
| 490 | 后端管箱筒体.dot | 62.00K |
| 491 | 开孔补强.dot | 59.00K |
| 492 | 换热管内压.dot | 73.00K |
| 493 | V0202.ra2 | 23.24K |
| 494 | V0202上封头.doc | 70.00K |
| 495 | V0202下封头.doc | 70.00K |
| 496 | V0202筒体.doc | 67.50K |
| 497 | V0401.ra2 | 23.24K |
| 498 | V0401上封头.doc | 72.00K |
| 499 | V0401下封头.doc | 70.00K |
| 500 | V0401筒体.doc | 69.50K |
| 501 | V0502.ra2 | 23.24K |
| 502 | V0502上封头.doc | 70.00K |
| 503 | V0502下封头.doc | 70.00K |
| 504 | V0502筒体.doc | 67.50K |
| 505 | 反应器.mph | 722.39K |
| 506 | 反应器截面浓度.jpg | 23.86K |
| 507 | 反应时间.JPG | 54.26K |
| 508 | 反应时间.mph | 57.96K |
此图纸下载需要520金币
立即下载
发布者
静
创作: 8886
粉丝: 6
加入时间：2025-05-27
模型信息
图纸格式：pdf,dwg
文件大小：209.18M
所需金币：520
上传时间：2025-09-29 12:12:31
是否可编辑：可修改，包括参数
版本：AutoCAD 2007
标签
图纸简介
版权说明
用户在本站上传的作品如侵犯到您的权益，请与本站管理员联系删除。用户在本站下载的原创作品，只拥有作品的使用权，著作权归原作者所有，未经合法授权，用户不得以任何形式发布、传播、复制、转售该作品。
作者其它图纸 查看更多
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
猜你喜欢
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
QQ在线客服
官方QQ群
