登录注册
微信扫码登录
21万ta己二腈项目初步设计（ID:2693560）
| # | 文件名称 | 文件大小 |
|---|---|---|
| 1 | 17592965993453.zip | 1.64G |
| 2 | 动力学验证.bkp | 488.33K |
| 3 | 反应动力学说明书.docx | 1.65M |
| 4 | 反应动力学说明书.pdf | 1.62M |
| 5 | 附件1-Ni基催化氢氰化反应动力学（文献1）.pdf | 2.02M |
| 6 | 附件2-新型螯合亚磷酸配体烯烃的合成、结构和镍催化氢氰化反应（文献2）.pdf | 293.65K |
| 7 | 附件3-丁二烯氢氰化法制备己二腈工艺的研究与优化_石广雷（文献3）.caj | 4.37M |
| 8 | 附件4-合理设计用于2-甲基-3-丁烯腈异构化的高效空间位阻催化剂2M3BN-3PN异构化动力学（文献4）.pdf | 3.47M |
| 9 | 附件5-螺双二氢茚双齿镍催化剂催化3-戊烯腈氢氰化反应研究_孙兴燊（文献5）.caj | 2.99M |
| 10 | 附件6-om701140c_si_002（文献6）.pdf | 790.98K |
| 11 | 附件7-s11144-018-1437-6（文献7）.pdf | 1.10M |
| 12 | 现代设计方法评分索引.docx | 1.45M |
| 13 | 1-原始工艺流股（不含节能技术、换热网络）.bkp | 3.82M |
| 14 | 2-改进工艺流股（含节能技术，不含换热网络）.bkp | 4.31M |
| 15 | 3-全流程模拟（含节能技术、换热网络）.bkp | 4.58M |
| 16 | _1142ibz.def | 207B |
| 17 | 全流程运行无警告无错误视频.mp4 | 11.62M |
| 18 | 1-原始工艺流股（不含节能技术、换热网络）.bmp | 418.92K |
| 19 | 2-改进工艺流股（含节能技术，不含换热网络）.bmp | 478.22K |
| 20 | 3-全流程模拟（含节能技术、换热网络）.bmp | 357.76K |
| 21 | README.txt | 640B |
| 22 | R0104反应器设计.bkp | 235.93K |
| 23 | 附录12-分离过程设计与优化.docx | 1.64M |
| 24 | 1-T0101-CH3OH.bkp | 336.09K |
| 25 | 2-T0101-最终优化结果.bkp | 322.55K |
| 26 | 1-T0201-持液量优化.bkp | 1.04M |
| 27 | 2-T0201-最终优化结果.bkp | 825.40K |
| 28 | 二氯丁烯异构化工艺研究_师宝仁.pdf | 3.60M |
| 29 | 1-T0402-PROD-STAGE.bkp | 570.25K |
| 30 | 2-T0402-PROD-FLOW.bkp | 612.62K |
| 31 | 3-T0402-最终优化结果.bkp | 549.08K |
| 32 | 1-T0403-DSTWU.bkp | 246.40K |
| 33 | 2-T0403-NSTAGE.bkp | 358.09K |
| 34 | 3-T0403-DFRR.bkp | 334.91K |
| 35 | 4-T0403-FEED-STAGE.bkp | 347.00K |
| 36 | 5-T0403-最终优化结果.bkp | 335.61K |
| 37 | 无热泵精馏.bkp | 368.73K |
| 38 | 热泵精馏.bkp | 489.68K |
| 39 | 双效精馏.bkp | 534.51K |
| 40 | 无双效精馏.bkp | 439.64K |
| 41 | 无隔壁塔.bkp | 520.48K |
| 42 | 隔壁塔.bkp | 549.08K |
| 43 | 储罐火灾爆炸.ffta | 11.27K |
| 44 | 储罐火灾爆炸.jpg | 51.38K |
| 45 | 换热器燃烧爆炸.ffta | 9.53K |
| 46 | 换热器燃烧爆炸.jpg | 35.95K |
| 47 | 氢氰酸中毒.ffta | 13.93K |
| 48 | 氢氰酸中毒.jpg | 72.57K |
| 49 | 管道泄漏.ffta | 12.42K |
| 50 | 管道泄漏.jpg | 62.93K |
| 51 | 己二腈典型泄漏事故模拟.rsm | 511B |
| 52 | 己二腈在大气中的扩散预测.rsm | 496B |
| 53 | 己二腈池火事故模型模拟.rsm | 201B |
| 54 | 己二腈沸腾液体扩展蒸汽爆炸（火球BLEVE）模型预测.rsm | 211B |
| 55 | 己二腈液体泄漏量计算.rsm | 114B |
| 56 | 己二腈蒸汽云爆炸模型预测（TNT当量法）.rsm | 165B |
| 57 | 说明.txt | 688B |
| 58 | BPnetwork.mlapp | 71.98K |
| 59 | BPnetwork.mlappinstall | 1.11M |
| 60 | BPPID.py | 614B |
| 61 | PID.py | 6.44K |
| 62 | 说明.txt | 735B |
| 63 | .gitignore | 50B |
| 64 | .name | 8B |
| 65 | misc.xml | 189B |
| 66 | modules.xml | 411B |
| 67 | PID-Control-System-Based-on-Optimized-Back-Propagation-Neural-Network-master.iml | 291B |
| 68 | workspace.xml | 2.07K |
| 69 | profiles_settings.xml | 174B |
| 70 | Project_Default.xml | 423B |
| 71 | PID.cpython-310.pyc | 4.08K |
| 72 | 程序打包测试视频.mp4 | 208.50M |
| 73 | 说明.txt | 682B |
| 74 | .dockerignore | 3.53K |
| 75 | .gitattributes | 75B |
| 76 | .gitignore | 0B |
| 77 | detect.py | 8.38K |
| 78 | Dockerfile | 1.77K |
| 79 | hubconf.py | 5.38K |
| 80 | LICENSE | 34.30K |
| 81 | main.py | 15.97K |
| 82 | project.ui | 4.25K |
| 83 | requirements.txt | 626B |
| 84 | test.py | 16.58K |
| 85 | train.py | 32.99K |
| 86 | argoverse_hd.yaml | 850B |
| 87 | coco.yaml | 1.70K |
| 88 | coco128.yaml | 1.51K |
| 89 | hyp.finetune.yaml | 847B |
| 90 | hyp.scratch.yaml | 1.53K |
| 91 | voc.yaml | 739B |
| 92 | get_argoverse_hd.sh | 1.97K |
| 93 | get_coco.sh | 964B |
| 94 | get_voc.sh | 4.33K |
| 95 | common.py | 16.39K |
| 96 | experimental.py | 5.01K |
| 97 | export.py | 4.32K |
| 98 | yolo.py | 11.82K |
| 99 | yolov5l.yaml | 1.33K |
| 100 | yolov5m.yaml | 1.34K |
| 101 | yolov5s.yaml | 1.34K |
| 102 | yolov5x.yaml | 1.34K |
| 103 | __init__.py | 0B |
| 104 | anchors.yaml | 3.28K |
| 105 | yolov3-spp.yaml | 1.50K |
| 106 | yolov3-tiny.yaml | 1.17K |
| 107 | yolov3.yaml | 1.49K |
| 108 | yolov5-fpn.yaml | 1.22K |
| 109 | yolov5-p2.yaml | 1.70K |
| 110 | yolov5-p6.yaml | 1.77K |
| 111 | yolov5-p7.yaml | 2.18K |
| 112 | yolov5-panet.yaml | 1.43K |
| 113 | yolov5l6.yaml | 1.93K |
| 114 | yolov5m6.yaml | 1.93K |
| 115 | yolov5s-transformer.yaml | 1.37K |
| 116 | yolov5s6.yaml | 1.93K |
| 117 | yolov5x6.yaml | 1.93K |
| 118 | common.cpython-310.pyc | 17.42K |
| 119 | common.cpython-38.pyc | 18.50K |
| 120 | experimental.cpython-310.pyc | 5.56K |
| 121 | experimental.cpython-38.pyc | 5.57K |
| 122 | yolo.cpython-310.pyc | 9.81K |
| 123 | __init__.cpython-310.pyc | 161B |
| 124 | __init__.cpython-38.pyc | 159B |
| 125 | yolov5s.pt | 14.12M |
| 126 | activations.py | 2.20K |
| 127 | autoanchor.py | 6.99K |
| 128 | datasets.py | 43.51K |
| 129 | general.py | 24.54K |
| 130 | google_utils.py | 4.76K |
| 131 | loss.py | 9.24K |
| 132 | metrics.py | 8.76K |
| 133 | plots.py | 17.90K |
| 134 | torch_utils.py | 12.15K |
| 135 | __init__.py | 0B |
| 136 | mime.sh | 781B |
| 137 | resume.py | 1.09K |
| 138 | userdata.sh | 1.21K |
| 139 | __init__.py | 0B |
| 140 | additional_requirements.txt | 106B |
| 141 | app.yaml | 174B |
| 142 | Dockerfile | 822B |
| 143 | log_dataset.py | 820B |
| 144 | wandb_utils.py | 15.89K |
| 145 | __init__.py | 0B |
| 146 | autoanchor.cpython-310.pyc | 6.04K |
| 147 | datasets.cpython-310.pyc | 33.10K |
| 148 | datasets.cpython-38.pyc | 33.11K |
| 149 | general.cpython-310.pyc | 19.57K |
| 150 | general.cpython-38.pyc | 19.73K |
| 151 | google_utils.cpython-310.pyc | 3.29K |
| 152 | google_utils.cpython-38.pyc | 3.21K |
| 153 | metrics.cpython-310.pyc | 7.45K |
| 154 | metrics.cpython-38.pyc | 7.44K |
| 155 | plots.cpython-310.pyc | 15.48K |
| 156 | plots.cpython-38.pyc | 15.54K |
| 157 | torch_utils.cpython-310.pyc | 11.19K |
| 158 | torch_utils.cpython-38.pyc | 11.21K |
| 159 | __init__.cpython-310.pyc | 160B |
| 160 | __init__.cpython-38.pyc | 158B |
| 161 | download_weights.sh | 278B |
| 162 | tt.py | 1.47K |
| 163 | yolov5s.pt | 25.53M |
| 164 | 年产21万吨己二腈项目.opexxmh | 376.00K |
| 165 | 说明.txt | 669B |
| 166 | 附录7-HAZOP分析报告说明书.pdf | 937.68K |
| 167 | 腈腈耶耶耶队——变压吸附穿透曲线.ada | 132.46K |
| 168 | 附录13-PSA变压吸附提纯氢气设计说明书.docx | 1.03M |
| 169 | AM_SAI.aprpdf | 253.25K |
| 170 | PropsPlus.ads | 1.88K |
| 171 | propsplus.aprhis | 3.40K |
| 172 | propsplus.aprpdf | 253.25K |
| 173 | PropsPlus.his | 1.29K |
| 174 | PropsPlus.rep | 0B |
| 175 | snapshot.bak | 449.41K |
| 176 | snpA0000.snp | 429.72K |
| 177 | snpA0001.snp | 554.59K |
| 178 | snpA0002.snp | 404.04K |
| 179 | snpA0003.snp | 7.30K |
| 180 | snpA0004.snp | 397.02K |
| 181 | snpA0005.snp | 606.98K |
| 182 | snpA0006.snp | 449.07K |
| 183 | snpA0007.snp | 449.41K |
| 184 | snpA0008.snp | 449.07K |
| 185 | snpA0009.snp | 449.07K |
| 186 | snpA0010.snp | 501.71K |
| 187 | snpA0011.snp | 501.71K |
| 188 | snpA0012.snp | 449.07K |
| 189 | snpA0013.snp | 449.07K |
| 190 | snpA0014.snp | 449.07K |
| 191 | snpA0015.snp | 396.44K |
| 192 | snpA0016.snp | 606.98K |
| 193 | snpA0017.snp | 449.07K |
| 194 | snpA0018.snp | 449.07K |
| 195 | snpA0019.snp | 501.71K |
| 196 | snpA0020.snp | 449.07K |
| 197 | snpA0021.snp | 449.07K |
| 198 | snpA0022.snp | 449.07K |
| 199 | snpA0023.snp | 449.41K |
| 200 | snpA0024.snp | 449.07K |
| 201 | snpA0025.snp | 449.07K |
| 202 | snpA0026.snp | 449.07K |
| 203 | snpA0027.snp | 554.59K |
| 204 | snpA0028.snp | 764.89K |
| 205 | snpA0029.snp | 712.83K |
| 206 | snpA0030.snp | 449.07K |
| 207 | snpA0031.snp | 449.41K |
| 208 | snpA0032.snp | 396.44K |
| 209 | snpA0033.snp | 344.14K |
| 210 | snpA0034.snp | 554.68K |
| 211 | snpA0035.snp | 396.44K |
| 212 | snpA0036.snp | 344.14K |
| 213 | snpA0037.snp | 449.07K |
| 214 | snpA0038.snp | 502.05K |
| 215 | snpA0039.snp | 449.41K |
| 216 | snpA0040.snp | 449.32K |
| 217 | snpA0041.snp | 501.71K |
| 218 | snpA0042.snp | 501.71K |
| 219 | snpA0043.snp | 501.95K |
| 220 | snpA0044.snp | 501.71K |
| 221 | snpA0045.snp | 554.35K |
| 222 | tasksnap.bak | 1.11K |
| 223 | acs.jced.2c00086.pdf | 6.19M |
| 224 | AspenAdsimAdsorptionReferenceGuide.pdf | 1.97M |
| 225 | 用AspenAdsorption模拟氯化氢脱水.pdf | 257.14K |
| 226 | 厂区渲染源文件.ls10 | 385.25M |
| 227 | 厂区三维设计图.skp | 423.41M |
| 228 | 说明.txt | 477B |
| 229 | 俯视图.png | 385.39K |
| 230 | 前视图.png | 255.70K |
| 231 | 后视图.png | 205.41K |
| 232 | 轴视图.png | 367.18K |
| 233 | T04032.dynf | 981.51K |
| 234 | 附录14-动态模拟设计说明书.docx | 1.08M |
| 235 | snapshot.bak | 8.20M |
| 236 | snpA0000.snp | 2.62M |
| 237 | snpA0001.snp | 3.17M |
| 238 | snpA0002.snp | 3.42M |
| 239 | snpA0003.snp | 3.42M |
| 240 | snpA0004.snp | 2.70M |
| 241 | snpA0005.snp | 3.42M |
| 242 | t0403dyn.his | 2.97K |
| 243 | t0403dyn.rep | 0B |
| 244 | tasksnap.bak | 5.52K |
| 245 | 1-原始工艺流股（不含节能技术、换热网络）.bkp | 3.82M |
| 246 | 2-原始换热网络.hch | 1.81M |
| 247 | 3-改进工艺流股（含节能技术，不含换热网络）.bkp | 4.28M |
| 248 | 4-初步换热网络设计.hch | 17.38M |
| 249 | 4-能量集成及换热网络设计.docx | 1.67M |
| 250 | 5-全流程模拟（含节能技术、换热网络）.bkp | 4.58M |
| 251 | 6-最终换热网络.hch | 1.66M |
| 252 | 总组合曲线.png | 2.02M |
| 253 | 总费用与最小传热温差关系图.png | 1.90M |
| 254 | 温焓图.png | 2.04M |
| 255 | 总组合曲线.png | 2.04M |
| 256 | 总费用与最小传热温差关系图.png | 1.90M |
| 257 | 温焓图.png | 2.03M |
| 258 | 总组合曲线.png | 2.04M |
| 259 | 总费用与最小传热温差关系图.png | 1.91M |
| 260 | 温焓图.png | 2.04M |
| 261 | 模型-结果2-双层反向斜叶.mph | 32.07M |
| 262 | 模型-结果2-双层同向斜叶.mph | 32.03M |
| 263 | 模型-结果3-单层斜叶.mph | 20.99M |
| 264 | 雷诺数-单层搅拌桨.png | 577.59K |
| 265 | 雷诺数-双层反向搅拌桨.png | 1.49M |
| 266 | 雷诺数-双层同向搅拌桨.png | 552.17K |
| 267 | COMSOL6.0反应器流动模拟源文件.mph | 115.02M |
| 268 | 三维模型视图1.png | 466.74K |
| 269 | 三维模型视图2.png | 273.38K |
| 270 | 反应器压力分布.png | 317.15K |
| 271 | 反应器流场分布.png | 930.14K |
| 272 | 反应器速度分布.png | 618.95K |
| 273 | 模型网格划分.png | 892.48K |
| 274 | 普通折流板.gif | 4.78M |
| 275 | 普通折流板.mph | 116.87M |
| 276 | 螺旋折流板.gif | 3.48M |
| 277 | 螺旋折流板换热器.mph | 82.31M |
| 278 | E0104换热器SW6校核.docx | 1005.59K |
| 279 | E0104换热器SW6校核源文件.fx3 | 26.05K |
| 280 | E0320换热器SW6校核.docx | 887.45K |
| 281 | E0320换热器SW6校核源文件.fx3 | 26.05K |
| 282 | R0104反应器（立式容器）sw6校核.docx | 247.42K |
| 283 | R0104反应器（立式容器）sw6校核源文件.ra2 | 24.57K |
| 284 | T0403塔设备sw6校核.docx | 280.16K |
| 285 | T0403塔设备SW6校核源文件.cn2 | 32.58K |
| 286 | README.txt | 601B |
| 287 | T0403塔设备水力学校核InteractiveSizing.bkp | 571.80K |
| 288 | T0403塔设备水力学校核Rating.bkp | 408.08K |
| 289 | 污垢热阻来源.png | 419.67K |
| 290 | 说明.txt | 1.06K |
| 291 | E0104.EDR | 257.39K |
| 292 | E0320.EDR | 246.51K |
| 293 | 俯视图.png | 16.97K |
| 294 | 左视图.png | 17.38K |
| 295 | 异构化反应车间三维布置-2004.dwg | 59.80M |
| 296 | 异构化反应车间三维布置-2007.dwg | 53.30M |
| 297 | 正视图.png | 32.04K |
| 298 | 轴视图.png | 77.80K |
| 299 | 二级氢氰化反应车间.dwg | 1.07M |
| 300 | 加氢精制车间.dwg | 507.52K |
| 301 | 预处理及一级氢氰化反应车间.dwg | 1.01M |
| 302 | 俯视图.png | 47.55K |
| 303 | 左视图.png | 33.72K |
| 304 | 异构化车间三维配管-2004.dwg | 60.89M |
| 305 | 异构化车间三维配管-2007.dwg | 54.31M |
| 306 | 正视图.png | 34.17K |
| 307 | 轴视图.png | 180.93K |
| 308 | 01068-1.dwg | 102.48K |
| 309 | 01068-2.dwg | 102.45K |
| 310 | 01068-3.dwg | 101.76K |
| 311 | 02001-1.dwg | 101.17K |
| 312 | 02001-2.dwg | 108.89K |
| 313 | 02001-3.dwg | 99.79K |
| 314 | 02002-1.dwg | 98.92K |
| 315 | 02002-2.dwg | 91.20K |
| 316 | 02002-3.dwg | 101.14K |
| 317 | 02003-1.dwg | 102.01K |
| 318 | 02003-2.dwg | 111.61K |
| 319 | 02003-3.dwg | 101.71K |
| 320 | 02003-4.dwg | 118.96K |
| 321 | 02003-5.dwg | 87.45K |
| 322 | 02004-1-1.dwg | 102.42K |
| 323 | 02004-1-2.dwg | 95.32K |
| 324 | 02004-1-3.dwg | 100.33K |
| 325 | 02004-2.dwg | 58.28K |
| 326 | 02005-1.dwg | 124.34K |
| 327 | 02005-2.dwg | 97.39K |
| 328 | 02006-1.dwg | 105.86K |
| 329 | 02006-2.dwg | 97.89K |
| 330 | 02006-3.dwg | 96.17K |
| 331 | 02007-1.dwg | 109.12K |
| 332 | 02007-2.dwg | 100.02K |
| 333 | 02007-3.dwg | 89.35K |
| 334 | 02008.dwg | 80.63K |
| 335 | 02009.dwg | 78.25K |
| 336 | 02010-1.dwg | 103.30K |
| 337 | 02010-2.dwg | 130.13K |
| 338 | 02011-1.dwg | 123.47K |
| 339 | 02011-2.dwg | 103.29K |
| 340 | 02013-1.dwg | 110.93K |
| 341 | 02013-2.dwg | 92.26K |
| 342 | 02013-3.dwg | 103.99K |
| 343 | 02014-1.dwg | 110.03K |
| 344 | 02014-2.dwg | 98.33K |
| 345 | 02014-3.dwg | 91.92K |
| 346 | 02015.dwg | 81.03K |
| 347 | 02016.dwg | 79.91K |
| 348 | 02017-1.dwg | 111.74K |
| 349 | 02017-2.dwg | 109.58K |
| 350 | 02017-3.dwg | 97.10K |
| 351 | 02017-4.dwg | 105.05K |
| 352 | 02018-1.dwg | 108.09K |
| 353 | 02018-2.dwg | 107.98K |
| 354 | 02018-3.dwg | 108.52K |
| 355 | 02019-1.dwg | 107.71K |
| 356 | 02019-2.dwg | 102.23K |
| 357 | 02019-3.dwg | 127.28K |
| 358 | 02019-4.dwg | 105.89K |
| 359 | 02019-5.dwg | 109.06K |
| 360 | 02020.dwg | 98.30K |
| 361 | 02021.dwg | 96.27K |
| 362 | 02022-1.dwg | 108.15K |
| 363 | 02022-2.dwg | 112.17K |
| 364 | 02022-3.dwg | 108.28K |
| 365 | 02023-1.dwg | 62.84K |
| 366 | 02023-2-1.dwg | 93.76K |
| 367 | 02023-2-2.dwg | 128.53K |
| 368 | 02023-2-3.dwg | 112.71K |
| 369 | 02023-2-4.dwg | 108.46K |
| 370 | 02023-2-5.dwg | 106.45K |
| 371 | 02024.dwg | 88.23K |
| 372 | 02025.dwg | 78.44K |
| 373 | 02026-1.dwg | 108.02K |
| 374 | 02026-2.dwg | 104.83K |
| 375 | 02026-3.dwg | 104.14K |
| 376 | 02027-1.dwg | 106.03K |
| 377 | 02027-2.dwg | 123.97K |
| 378 | 02028-1.dwg | 128.59K |
| 379 | 02028-2.dwg | 91.63K |
| 380 | 02028-3.dwg | 87.60K |
| 381 | 02029.dwg | 100.11K |
| 382 | 02030.dwg | 100.99K |
| 383 | 02031-1.dwg | 128.16K |
| 384 | 02031-2.dwg | 93.98K |
| 385 | 02031-3.dwg | 95.98K |
| 386 | 02032.dwg | 92.91K |
| 387 | 02033.dwg | 77.35K |
| 388 | 02034-1.dwg | 107.99K |
| 389 | 02034-2.dwg | 131.90K |
| 390 | 02035-1.dwg | 105.34K |
| 391 | 02035-2.dwg | 97.29K |
| 392 | 02035-3.dwg | 106.34K |
| 393 | 02036-1.dwg | 127.06K |
| 394 | 02036-2.dwg | 87.32K |
| 395 | 02036-3.dwg | 94.85K |
| 396 | 02037.dwg | 98.92K |
| 397 | 02038.dwg | 105.20K |
| 398 | 02039-1.dwg | 98.45K |
| 399 | 02039-2.dwg | 109.37K |
| 400 | 02039-3.dwg | 99.64K |
| 401 | 02040-1.dwg | 98.58K |
| 402 | 02040-2.dwg | 106.27K |
| 403 | 02040-3.dwg | 101.52K |
| 404 | 02041-1.dwg | 101.95K |
| 405 | 02041-2.dwg | 121.72K |
| 406 | 07001-1.dwg | 94.67K |
| 407 | 07001-10.dwg | 102.11K |
| 408 | 07001-11.dwg | 104.42K |
| 409 | 07001-2.dwg | 95.76K |
| 410 | 07001-3.dwg | 106.99K |
| 411 | 07001-4.dwg | 108.58K |
| 412 | 07001-5.dwg | 105.27K |
| 413 | 07001-6.dwg | 91.45K |
| 414 | 07001-7.dwg | 89.95K |
| 415 | 07001-8.dwg | 114.53K |
| 416 | 07001-9.dwg | 103.55K |
| 417 | 07002-1.dwg | 114.49K |
| 418 | 07002-10.dwg | 104.54K |
| 419 | 07002-11.dwg | 101.33K |
| 420 | 07002-2.dwg | 106.17K |
| 421 | 07002-3.dwg | 103.27K |
| 422 | 07002-4.dwg | 93.51K |
| 423 | 07002-5.dwg | 109.11K |
| 424 | 07002-6.dwg | 94.67K |
| 425 | 07002-7.dwg | 117.02K |
| 426 | 07002-8.dwg | 95.92K |
| 427 | 07002-9.dwg | 91.82K |
| 428 | 07003-1.dwg | 114.65K |
| 429 | 07003-10.dwg | 104.52K |
| 430 | 07003-11.dwg | 103.74K |
| 431 | 07003-2.dwg | 108.64K |
| 432 | 07003-3.dwg | 112.30K |
| 433 | 07003-4.dwg | 94.92K |
| 434 | 07003-5.dwg | 105.36K |
| 435 | 07003-6.dwg | 94.39K |
| 436 | 07003-7.dwg | 117.37K |
| 437 | 07003-8.dwg | 95.57K |
| 438 | 07003-9.dwg | 96.20K |
| 439 | 08001.dwg | 87.82K |
| 440 | 08002-1-1.dwg | 113.77K |
| 441 | 08002-1-2.dwg | 105.67K |
| 442 | 08002-1-3.dwg | 112.02K |
| 443 | 08002-2.dwg | 71.03K |
| 444 | 08003.dwg | 93.98K |
| 445 | 08004-1.dwg | 112.93K |
| 446 | 08004-2.dwg | 90.48K |
| 447 | 08004-3.dwg | 73.62K |
| 448 | 08004-4.dwg | 109.96K |
| 449 | 08005.dwg | 85.23K |
| 450 | 08006-1.dwg | 112.40K |
| 451 | 08006-2.dwg | 91.07K |
| 452 | 08006-3.dwg | 67.15K |
| 453 | 08006-4.dwg | 111.46K |
| 454 | 08007-1.dwg | 127.52K |
| 455 | 08007-2.dwg | 77.35K |
| 456 | 08007-3.dwg | 92.63K |
| 457 | 08008-1.dwg | 114.33K |
| 458 | 08008-2.dwg | 95.51K |
| 459 | 08008-3.dwg | 108.52K |
| 460 | 08009.dwg | 99.83K |
| 461 | 08010.dwg | 106.52K |
| 462 | 08011-1.dwg | 73.40K |
| 463 | 08011-2.dwg | 89.10K |
| 464 | 08012.dwg | 101.55K |
| 465 | 08013.dwg | 105.54K |
| 466 | 08014.dwg | 106.05K |
| 467 | 说明.txt | 686B |
| 468 | 13-丁二烯储罐泄漏BLEVE模拟.alo | 4.73K |
| 469 | 13-丁二烯储罐泄漏BLEVE模拟.png | 268.68K |
| 470 | 13-丁二烯储罐泄漏喷射火模拟.alo | 4.73K |
| 471 | 13-丁二烯储罐泄漏喷射火模拟.png | 295.97K |
| 472 | 13-丁二烯储罐泄漏易燃区模拟.alo | 4.73K |
| 473 | 13-丁二烯储罐泄漏易燃区模拟.png | 270.24K |
| 474 | 13-丁二烯储罐泄漏毒性模拟.alo | 4.73K |
| 475 | 13-丁二烯储罐泄漏毒性模拟.png | 279.25K |
| 476 | 13-丁二烯储罐泄漏蒸汽云爆炸模拟.alo | 4.73K |
| 477 | 13-丁二烯储罐泄漏蒸汽云爆炸模拟.png | 306.81K |
| 478 | 2-氨基-3-甲基吡啶储罐泄漏BLEVE模拟.alo | 4.73K |
| 479 | 2-氨基-3-甲基吡啶储罐泄漏BLEVE模拟.png | 257.98K |
| 480 | 2-氨基-3-甲基吡啶储罐泄漏易燃区模拟.alo | 4.73K |
| 481 | 2-氨基-3-甲基吡啶储罐泄漏易燃区模拟.png | 360.41K |
| 482 | 2-氨基-3-甲基吡啶储罐泄漏毒性模拟.alo | 4.73K |
| 483 | 2-氨基-3-甲基吡啶储罐泄漏毒性模拟.png | 345.56K |
| 484 | 2-氨基-3-甲基吡啶储罐泄漏池火模拟.alo | 4.73K |
| 485 | 2-氨基-3-甲基吡啶储罐泄漏池火模拟.png | 305.74K |
| 486 | 2-氨基-3-甲基吡啶储罐泄漏蒸汽云爆炸模拟.alo | 4.73K |
| 487 | 2-氨基-3-甲基吡啶储罐泄漏蒸汽云爆炸模拟.png | 299.75K |
| 488 | 3-甲基吡啶储罐泄漏BLEVE模拟.alo | 4.73K |
| 489 | 3-甲基吡啶储罐泄漏BLEVE模拟.png | 277.32K |
| 490 | 3-甲基吡啶储罐泄漏易燃区模拟.alo | 4.73K |
| 491 | 3-甲基吡啶储罐泄漏易燃区模拟.png | 333.65K |
| 492 | 3-甲基吡啶储罐泄漏毒性模拟.alo | 4.73K |
| 493 | 3-甲基吡啶储罐泄漏毒性模拟.png | 298.48K |
| 494 | 3-甲基吡啶储罐泄漏池火模拟.alo | 4.73K |
| 495 | 3-甲基吡啶储罐泄漏池火模拟.png | 311.66K |
| 496 | 3-甲基吡啶储罐泄漏蒸汽云爆炸模拟.alo | 4.73K |
| 497 | 3-甲基吡啶储罐泄漏蒸汽云爆炸模拟.png | 300.16K |
| 498 | 3-甲基哌啶储罐泄漏BLEVE分析.alo | 4.73K |
| 499 | 3-甲基哌啶储罐泄漏BLEVE分析.png | 276.59K |
| 500 | 3-甲基哌啶储罐泄漏易燃区分析.alo | 4.73K |
| 501 | 3-甲基哌啶储罐泄漏易燃区分析.png | 359.51K |
| 502 | 3-甲基哌啶储罐泄漏毒性分析.alo | 4.73K |
| 503 | 3-甲基哌啶储罐泄漏毒性分析.png | 347.92K |
| 504 | 3-甲基哌啶储罐泄漏池火分析.alo | 4.73K |
| 505 | 3-甲基哌啶储罐泄漏池火分析.png | 308.28K |
| 506 | 3-甲基哌啶储罐泄漏蒸汽云爆炸分析.alo | 4.73K |
| 507 | 3-甲基哌啶储罐泄漏蒸汽云爆炸分析.png | 295.95K |
| 508 | 氢氰酸储罐泄漏BLEVE模拟.alo | 4.73K |
| 509 | 氢氰酸储罐泄漏BLEVE模拟.png | 281.58K |
| 510 | 氢氰酸储罐泄漏喷射火模拟.alo | 4.73K |
| 511 | 氢氰酸储罐泄漏喷射火模拟.png | 299.11K |
| 512 | 氢氰酸储罐泄漏易燃区模拟.alo | 4.73K |
| 513 | 氢氰酸储罐泄漏易燃区模拟.png | 278.92K |
| 514 | 氢氰酸储罐泄漏毒性模拟.alo | 4.73K |
| 515 | 氢氰酸储罐泄漏毒性模拟.png | 296.58K |
| 516 | 氢氰酸储罐泄漏蒸汽云爆炸模拟.alo | 4.73K |
| 517 | 氢氰酸储罐泄漏蒸汽云爆炸模拟.png | 310.01K |
| 518 | 厂区总平面布置图.pdf | 365.98K |
| 519 | 噪声预测.ein | 14.95K |
| 520 | 噪声预测数据.xlsx | 20.48K |
| 521 | 噪声预测结果.png | 967.10K |
| 522 | 背景图.BIF | 137B |
| 523 | 背景图.jpg | 132.05K |
| 524 | 说明.txt | 673B |
| 525 | PFD工艺物料流程图.pdf | 4.70M |
| 526 | PFD工艺物料流程图2004.dwg | 2.95M |
| 527 | PFD工艺物料流程图2007.dwg | 2.69M |
| 528 | PID管道及仪表流程图.pdf | 14.14M |
| 529 | PID管道及仪表流程图（2004）.dwg | 3.30M |
| 530 | PID管道及仪表流程图（2007）.dwg | 3.28M |
| 531 | 厂区总平面布置图-2004.dwg | 445.00K |
| 532 | 厂区总平面布置图-2007.dwg | 454.75K |
| 533 | 厂区总平面布置图.pdf | 377.18K |
| 534 | R0104反应器工艺条件图.pdf | 136.99K |
| 535 | R0104反应器工艺条件图（2004）.dwg | 253.87K |
| 536 | R0104反应器工艺条件图（2007）.dwg | 274.25K |
| 537 | T0403塔设备工艺条件图.pdf | 127.35K |
| 538 | T0403塔设备工艺条件图2004.dwg | 167.65K |
| 539 | T0403塔设备工艺条件图2007.dwg | 191.94K |
| 540 | E0320换热器工艺条件图.pdf | 123.92K |
| 541 | E0320换热器工艺条件图（2004）.dwg | 138.45K |
| 542 | E0320换热器工艺条件图（2007）.dwg | 163.06K |
| 543 | 异构化反应车间平立面布置图-2004.dwg | 833.89K |
| 544 | 异构化反应车间平立面布置图-2007.dwg | 828.38K |
| 545 | 异构化反应车间平立面布置图.pdf | 1017.98K |
| 546 | 异构化反应车间三维布置-2004.dwg | 59.80M |
| 547 | 二级氢氰化反应车间.dwg | 1.53M |
| 548 | 加氢精制车间.dwg | 952.21K |
| 549 | 预处理及一级氢氰化反应车间.dwg | 1.46M |
| 550 | 异构化反应车间三维布置-2007.dwg | 53.30M |
| 551 | 二级氢氰化反应车间.dwg | 1.33M |
| 552 | 加氢精制车间.dwg | 906.50K |
| 553 | 预处理及一级氢氰化反应车间.dwg | 1.27M |
| 554 | 异构化车间三维配管-2004.dwg | 60.89M |
| 555 | 异构化车间三维配管-2007.dwg | 54.31M |
| 556 | 01068-1.dwg | 102.48K |
| 557 | 01068-2.dwg | 102.45K |
| 558 | 01068-3.dwg | 101.76K |
| 559 | 02001-1.dwg | 101.17K |
| 560 | 02001-2.dwg | 108.89K |
| 561 | 02001-3.dwg | 99.79K |
| 562 | 02002-1.dwg | 98.92K |
| 563 | 02002-2.dwg | 91.20K |
| 564 | 02002-3.dwg | 101.14K |
| 565 | 02003-1.dwg | 102.01K |
| 566 | 02003-2.dwg | 111.61K |
| 567 | 02003-3.dwg | 101.71K |
| 568 | 02003-4.dwg | 118.96K |
| 569 | 02003-5.dwg | 87.45K |
| 570 | 02004-1-1.dwg | 102.42K |
| 571 | 02004-1-2.dwg | 95.32K |
| 572 | 02004-1-3.dwg | 100.33K |
| 573 | 02004-2.dwg | 58.28K |
| 574 | 02005-1.dwg | 124.34K |
| 575 | 02005-2.dwg | 97.39K |
| 576 | 02006-1.dwg | 105.86K |
| 577 | 02006-2.dwg | 97.89K |
| 578 | 02006-3.dwg | 96.17K |
| 579 | 02007-1.dwg | 109.12K |
| 580 | 02007-2.dwg | 100.02K |
| 581 | 02007-3.dwg | 89.35K |
| 582 | 02008.dwg | 80.63K |
| 583 | 02009.dwg | 78.25K |
| 584 | 02010-1.dwg | 103.30K |
| 585 | 02010-2.dwg | 130.13K |
| 586 | 02011-1.dwg | 123.47K |
| 587 | 02011-2.dwg | 103.29K |
| 588 | 02013-1.dwg | 110.93K |
| 589 | 02013-2.dwg | 92.26K |
| 590 | 02013-3.dwg | 103.99K |
| 591 | 02014-1.dwg | 110.03K |
| 592 | 02014-2.dwg | 98.33K |
| 593 | 02014-3.dwg | 91.92K |
| 594 | 02015.dwg | 81.03K |
| 595 | 02016.dwg | 79.91K |
| 596 | 02017-1.dwg | 111.74K |
| 597 | 02017-2.dwg | 109.58K |
| 598 | 02017-3.dwg | 97.10K |
| 599 | 02017-4.dwg | 105.05K |
| 600 | 02018-1.dwg | 108.09K |
| 601 | 02018-2.dwg | 107.98K |
| 602 | 02018-3.dwg | 108.52K |
| 603 | 02019-1.dwg | 107.71K |
| 604 | 02019-2.dwg | 102.23K |
| 605 | 02019-3.dwg | 127.28K |
| 606 | 02019-4.dwg | 105.89K |
| 607 | 02019-5.dwg | 109.06K |
| 608 | 02020.dwg | 98.30K |
| 609 | 02021.dwg | 96.27K |
| 610 | 02022-1.dwg | 108.15K |
| 611 | 02022-2.dwg | 112.17K |
| 612 | 02022-3.dwg | 108.28K |
| 613 | 02023-1.dwg | 62.84K |
| 614 | 02023-2-1.dwg | 93.76K |
| 615 | 02023-2-2.dwg | 128.53K |
| 616 | 02023-2-3.dwg | 112.71K |
| 617 | 02023-2-4.dwg | 108.46K |
| 618 | 02023-2-5.dwg | 106.45K |
| 619 | 02024.dwg | 88.23K |
| 620 | 02025.dwg | 78.44K |
| 621 | 02026-1.dwg | 108.02K |
| 622 | 02026-2.dwg | 104.83K |
| 623 | 02026-3.dwg | 104.14K |
| 624 | 02027-1.dwg | 106.03K |
| 625 | 02027-2.dwg | 123.97K |
| 626 | 02028-1.dwg | 128.59K |
| 627 | 02028-2.dwg | 91.63K |
| 628 | 02028-3.dwg | 87.60K |
| 629 | 02029.dwg | 100.11K |
| 630 | 02030.dwg | 100.99K |
| 631 | 02031-1.dwg | 128.16K |
| 632 | 02031-2.dwg | 93.98K |
| 633 | 02031-3.dwg | 95.98K |
| 634 | 02032.dwg | 92.91K |
| 635 | 02033.dwg | 77.35K |
| 636 | 02034-1.dwg | 107.99K |
| 637 | 02034-2.dwg | 131.90K |
| 638 | 02035-1.dwg | 105.34K |
| 639 | 02035-2.dwg | 97.29K |
| 640 | 02035-3.dwg | 106.34K |
| 641 | 02036-1.dwg | 127.06K |
| 642 | 02036-2.dwg | 87.32K |
| 643 | 02036-3.dwg | 94.85K |
| 644 | 02037.dwg | 98.92K |
| 645 | 02038.dwg | 105.20K |
| 646 | 02039-1.dwg | 98.45K |
| 647 | 02039-2.dwg | 109.37K |
| 648 | 02039-3.dwg | 99.64K |
| 649 | 02040-1.dwg | 98.58K |
| 650 | 02040-2.dwg | 106.27K |
| 651 | 02040-3.dwg | 101.52K |
| 652 | 02041-1.dwg | 101.95K |
| 653 | 02041-2.dwg | 121.72K |
| 654 | 07001-1.dwg | 94.67K |
| 655 | 07001-10.dwg | 102.11K |
| 656 | 07001-11.dwg | 104.42K |
| 657 | 07001-2.dwg | 95.76K |
| 658 | 07001-3.dwg | 106.99K |
| 659 | 07001-4.dwg | 108.58K |
| 660 | 07001-5.dwg | 105.27K |
| 661 | 07001-6.dwg | 91.45K |
| 662 | 07001-7.dwg | 89.95K |
| 663 | 07001-8.dwg | 114.53K |
| 664 | 07001-9.dwg | 103.55K |
| 665 | 07002-1.dwg | 114.49K |
| 666 | 07002-10.dwg | 104.54K |
| 667 | 07002-11.dwg | 101.33K |
| 668 | 07002-2.dwg | 106.17K |
| 669 | 07002-3.dwg | 103.27K |
| 670 | 07002-4.dwg | 93.51K |
| 671 | 07002-5.dwg | 109.11K |
| 672 | 07002-6.dwg | 94.67K |
| 673 | 07002-7.dwg | 117.02K |
| 674 | 07002-8.dwg | 95.92K |
| 675 | 07002-9.dwg | 91.82K |
| 676 | 07003-1.dwg | 114.65K |
| 677 | 07003-10.dwg | 104.52K |
| 678 | 07003-11.dwg | 103.74K |
| 679 | 07003-2.dwg | 108.64K |
| 680 | 07003-3.dwg | 112.30K |
| 681 | 07003-4.dwg | 94.92K |
| 682 | 07003-5.dwg | 105.36K |
| 683 | 07003-6.dwg | 94.39K |
| 684 | 07003-7.dwg | 117.37K |
| 685 | 07003-8.dwg | 95.57K |
| 686 | 07003-9.dwg | 96.20K |
| 687 | 08001.dwg | 87.82K |
| 688 | 08002-1-1.dwg | 113.77K |
| 689 | 08002-1-2.dwg | 105.67K |
| 690 | 08002-1-3.dwg | 112.02K |
| 691 | 08002-2.dwg | 71.03K |
| 692 | 08003.dwg | 93.98K |
| 693 | 08004-1.dwg | 112.93K |
| 694 | 08004-2.dwg | 90.48K |
| 695 | 08004-3.dwg | 73.62K |
| 696 | 08004-4.dwg | 109.96K |
| 697 | 08005.dwg | 85.23K |
| 698 | 08006-1.dwg | 112.40K |
| 699 | 08006-2.dwg | 91.07K |
| 700 | 08006-3.dwg | 67.15K |
| 701 | 08006-4.dwg | 111.46K |
| 702 | 08007-1.dwg | 127.52K |
| 703 | 08007-2.dwg | 77.35K |
| 704 | 08007-3.dwg | 92.63K |
| 705 | 08008-1.dwg | 114.33K |
| 706 | 08008-2.dwg | 95.51K |
| 707 | 08008-3.dwg | 108.52K |
| 708 | 08009.dwg | 99.83K |
| 709 | 08010.dwg | 106.52K |
| 710 | 08011-1.dwg | 73.40K |
| 711 | 08011-2.dwg | 89.10K |
| 712 | 08012.dwg | 101.55K |
| 713 | 08013.dwg | 105.54K |
| 714 | 08014.dwg | 106.05K |
| 715 | 俯视图.png | 385.39K |
| 716 | 前视图.png | 255.70K |
| 717 | 后视图.png | 205.41K |
| 718 | 轴视图.png | 367.18K |
| 719 | 文档质量评分索引.docx | 746.34K |
| 720 | 1-可行性研究报告.docx | 1.52M |
| 721 | 1典型设备选型及设计说明书.docx | 162B |
| 722 | 1反应器设计说明书.docx | 162B |
| 723 | 2-初步设计说明书.docx | 11.30M |
| 724 | 3-1反应器设计说明书.docx | 5.49M |
| 725 | 3-2塔设备选型及设计说明书.docx | 2.51M |
| 726 | 3-3换热器选型及设计说明书.docx | 3.03M |
| 727 | 3-设备设计及选型一览表（ok）.docx | 162B |
| 728 | 3换热器选型及设计说明书（ok）.docx | 162B |
| 729 | 4-能量集成及换热网络设计.docx | 1.67M |
| 730 | 5-安全预评价报告.docx | 9.24M |
| 731 | 6-环境影响评价报告.docx | 1.19M |
| 732 | 7-经济分析.docx | 944.98K |
| 733 | 8-创新性说明书.docx | 3.57M |
| 734 | ~$7-经济分析.docx | 162B |
| 735 | 初步设计说明书.docx | 162B |
| 736 | 可行性研究报告.docx | 162B |
| 737 | 环境影响评价报告.docx | 162B |
| 738 | 附录1-物料平衡书.docx | 1.11M |
| 739 | 附录10-基于YOLOv5和PyQt5的行为检测识别UI说明.docx | 1.84M |
| 740 | 附录11-基于MATLABAPP的BP神经网络PID自整定系统开发.docx | 26.77M |
| 741 | 附录12-分离过程设计与优化.docx | 1.64M |
| 742 | 附录13-PSA变压吸附提纯氢气设计说明书.docx | 1.03M |
| 743 | 附录14-动态模拟设计说明书.docx | 1.08M |
| 744 | 附录2-能量平衡书.docx | 1004.79K |
| 745 | 附录3-设备设计及选型一览表.docx | 803.71K |
| 746 | 附录4-中国绿色低碳发展要求评估报告.docx | 784.78K |
| 747 | 附录5-MSDS一览表.docx | 922.13K |
| 748 | 附录6-公用工程供应协议及方案.docx | 773.05K |
| 749 | 附录8-ALOHA评估报告.docx | 8.06M |
| 750 | 附录9-Risksystem环境风险评价.docx | 2.56M |
此图纸下载需要520金币
立即下载
发布者
静
创作: 10046
粉丝: 6
加入时间：2025-05-27
模型信息
图纸格式：pdf,skp,dwg
文件大小：1721.94M
所需金币：520
上传时间：2025-10-01 13:42:06
是否可编辑：可修改，包括参数
版本：AutoCAD 2004
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)
猜你喜欢
0.png)
0.png)
0.png)
0.png)
0.png)
QQ在线客服
官方QQ群
