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年处理10万吨C5烷烃项目初步设计（ID:2696946）
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| # | 文件名称 | 文件大小 |
|---|---|---|
| 1 | 17594012605338.zip | 448.09M |
| 2 | readme.txt | 1.69K |
| 3 | 0-项目摘要.docx | 5.20M |
| 4 | 1-可行性研究报告.docx | 5.05M |
| 5 | 10-ALOHA评估报告.docx | 3.68M |
| 6 | 2-初步设计说明书.docx | 7.31M |
| 7 | 3-设备设计及选型说明书.docx | 9.89M |
| 8 | 4-创新性说明书.docx | 5.82M |
| 9 | 5-1附录一物料平衡计算书.docx | 3.41M |
| 10 | 5-2附录二能量平衡计算书.docx | 3.10M |
| 11 | 5-3附录三设备选型一览表.docx | 3.10M |
| 12 | 5-4附录四管道选型一览表.docx | 3.03M |
| 13 | 5-5附录五能量集成及换热网络设计.docx | 3.63M |
| 14 | 5-6附录六物质MSDS一览表.docx | 3.10M |
| 15 | 5-7附录七HAZOP分析.docx | 5.15M |
| 16 | 5-8附录八中国制造2025.docx | 3.51M |
| 17 | 6-经济分析.docx | 3.23M |
| 18 | 7-安全预评价.docx | 4.04M |
| 19 | 8-环境评价.docx | 4.41M |
| 20 | 9-公用工程供应协议及方案.docx | 3.02M |
| 21 | PFD-2004版.dwg | 2.75M |
| 22 | PID-2004版.dwg | 1.66M |
| 23 | E0401-2004版.dwg | 143.82K |
| 24 | R0201-2004版.dwg | 192.34K |
| 25 | T0303-2004版.dwg | 130.61K |
| 26 | 厂区总平面布置图.dwg | 2.78M |
| 27 | 设备平立面布置图-2004版.dwg | 4.26M |
| 28 | 厂区总平面布置图.dwg | 2.77M |
| 29 | 反应工段.dwg | 3.25M |
| 30 | 废气处理工段.dwg | 5.41M |
| 31 | 异戊二烯精制工段.dwg | 5.97M |
| 32 | 拔头油分离工段.dwg | 5.03M |
| 33 | 俯视图.png | 27.59K |
| 34 | 前视图.png | 25.52K |
| 35 | 右视图.png | 21.59K |
| 36 | 后视图.png | 23.15K |
| 37 | 左视图.png | 24.85K |
| 38 | 西南等轴测图.png | 42.87K |
| 39 | 俯视图.png | 20.29K |
| 40 | 前视图.png | 19.42K |
| 41 | 右视图.png | 16.95K |
| 42 | 后视图.png | 20.40K |
| 43 | 左视图.png | 15.89K |
| 44 | 西南等轴测图.png | 40.59K |
| 45 | 1.png | 40.17K |
| 46 | 2.png | 37.13K |
| 47 | 3.png | 35.67K |
| 48 | 4.png | 69.78K |
| 49 | 5.png | 58.89K |
| 50 | 6.png | 40.51K |
| 51 | 8.png | 47.12K |
| 52 | 俯视图.png | 28.11K |
| 53 | 前视图.png | 31.82K |
| 54 | 右视图.png | 27.84K |
| 55 | 后视图.png | 28.71K |
| 56 | 左视图.png | 27.07K |
| 57 | 西南等轴测图.png | 43.06K |
| 58 | 俯视图.png | 12.54K |
| 59 | 前视图.png | 24.08K |
| 60 | 右视图.png | 14.98K |
| 61 | 后视图.png | 22.52K |
| 62 | 左视图.png | 14.82K |
| 63 | 西南等轴测图.png | 24.20K |
| 64 | 动力学来源说明.txt | 1.11K |
| 65 | 1-异戊烷脱氢动力学.pdf | 579.32K |
| 66 | 2-吉布斯平衡反应器.bkp | 130.92K |
| 67 | 3-拟合kp.xlsx | 52.98K |
| 68 | 异戊烷脱氢动力学说明.docx | 271.97K |
| 69 | 异戊烷脱氢动力学说明.pdf | 434.82K |
| 70 | 烷脱氢动力学说明.docx | 162B |
| 71 | 01-正戊烷异构化反应条件及反应动力学.pdf | 146.09K |
| 72 | 02-C5_C6烷烃异构化贵金属催化剂的研究.caj | 2.94M |
| 73 | 正戊烷异构化动力学说明.docx | 200.64K |
| 74 | 正戊烷异构化动力学说明.pdf | 306.86K |
| 75 | 1-全流程模拟（不含热泵、换热网络）.bkp | 3.50M |
| 76 | 2-全流程模拟（含热泵，不含换热网络）.bkp | 3.90M |
| 77 | 3-全流程模拟（含热泵，换热网络.bkp | 4.03M |
| 78 | PDMSPS中空纤维复合膜分离氢气的性能研究.pdf | 193.64K |
| 79 | 压缩冷凝富集氢气.png | 67.76K |
| 80 | 综合回收炼厂气中氢气及轻烃工艺的设计研究_彭琳.caj | 3.73M |
| 81 | 膜分离技术.png | 44.78K |
| 82 | 原料分离工段.bkp | 886.65K |
| 83 | 反应工段.bkp | 815.09K |
| 84 | 废气处理工段.bkp | 1.21M |
| 85 | 异戊二烯精制工段.bkp | 1.37M |
| 86 | 燃烧尾气产低压蒸汽及碳化处理.bkp | 687.43K |
| 87 | 药用针剂小苏打的开发生产.pdf | 139.19K |
| 88 | 1-DSTWU-NSTAGE.bkp | 192.55K |
| 89 | 2-RR-MOLD.bkp | 222.53K |
| 90 | 3-FEEDSTAGE.bkp | 543.84K |
| 91 | 4-已优化.bkp | 217.64K |
| 92 | 塔参数优化说明.docx | 259.58K |
| 93 | 塔参数优化说明.pdf | 400.90K |
| 94 | DSTWU-NSTAGE.bkp | 138.42K |
| 95 | NTFEEDRD.bkp | 420.11K |
| 96 | RR-MOLD.bkp | 200.21K |
| 97 | 已优化.bkp | 193.34K |
| 98 | FEEDSTAGERD.bkp | 351.39K |
| 99 | NSTAGERR.bkp | 340.69K |
| 100 | RR-MOLD.bkp | 346.20K |
| 101 | 优化后.bkp | 267.96K |
| 102 | DSTWU-NSTAGE.bkp | 165.39K |
| 103 | FEEDNTRD.bkp | 540.35K |
| 104 | RR-MOLD.bkp | 352.60K |
| 105 | 已优化.bkp | 255.81K |
| 106 | DSTWU-NSTAGE.bkp | 135.96K |
| 107 | FSTAGENSTAGERD.bkp | 452.81K |
| 108 | RR-MOLD.bkp | 190.60K |
| 109 | 已优化.bkp | 184.47K |
| 110 | DSTWU-NSTAGE.bkp | 136.02K |
| 111 | FSTAGENSTAGERD.bkp | 284.16K |
| 112 | RR-MOLD.bkp | 156.20K |
| 113 | 已优化.bkp | 154.76K |
| 114 | FEEDSTAGERD.bkp | 382.53K |
| 115 | NSTAGERR.bkp | 456.44K |
| 116 | RR-MOLD.bkp | 306.12K |
| 117 | 已优化.bkp | 293.75K |
| 118 | FEEDSTAGE.bkp | 325.84K |
| 119 | NSTAGE.bkp | 338.49K |
| 120 | RR-MOLD.bkp | 387.23K |
| 121 | 已优化.bkp | 259.33K |
| 122 | 萃取剂用量.bkp | 362.22K |
| 123 | DSTWU-NSTAGE.bkp | 163.69K |
| 124 | FEEDSTAGERD.bkp | 186.05K |
| 125 | RR-MOLD.bkp | 158.43K |
| 126 | 已优化.bkp | 148.62K |
| 127 | DSTWU-NSTAGE.bkp | 118.98K |
| 128 | FEEDSTAGENSTAGERD.bkp | 250.79K |
| 129 | RR-MOLD.bkp | 149.73K |
| 130 | 已优化.bkp | 143.06K |
| 131 | DSTWU-NSTAGE.bkp | 146.23K |
| 132 | FEEDSTAGE.bkp | 252.29K |
| 133 | RR-MOLD.bkp | 223.84K |
| 134 | 已优化.bkp | 221.89K |
| 135 | 吸收剂用量.bkp | 265.52K |
| 136 | 塔板数.bkp | 315.25K |
| 137 | 已优化.bkp | 193.23K |
| 138 | DSTWU-NSTAGE.bkp | 121.01K |
| 139 | FSTAGERD.bkp | 228.31K |
| 140 | RR-MOLD.bkp | 203.00K |
| 141 | 已优化.bkp | 194.98K |
| 142 | FEEDSTAGERD.bkp | 251.61K |
| 143 | NSTAGERR.bkp | 285.38K |
| 144 | RR-MOLD.bkp | 227.61K |
| 145 | 已优化.bkp | 225.20K |
| 146 | DSTWU-NSTAGE.bkp | 121.57K |
| 147 | FEEDSTAGE.bkp | 222.97K |
| 148 | RR-MOLD.bkp | 345.86K |
| 149 | 已优化.bkp | 163.84K |
| 150 | DIAMETER.bkp | 386.65K |
| 151 | LENGTH.bkp | 273.95K |
| 152 | PRESURE.bkp | 283.26K |
| 153 | T0104环戊烷精馏塔热泵改造.bkp | 428.92K |
| 154 | T0302异戊烷粗分塔热泵改造.bkp | 650.65K |
| 155 | 双效精馏.bkp | 669.55K |
| 156 | 渲染.ls8 | 392.20M |
| 157 | 动力学来源说明.txt | 1.11K |
| 158 | 1-异戊烷脱氢动力学.pdf | 579.32K |
| 159 | 2-吉布斯平衡反应器.bkp | 130.92K |
| 160 | 3-拟合kp.xlsx | 52.98K |
| 161 | 异戊烷脱氢动力学说明.docx | 271.97K |
| 162 | 异戊烷脱氢动力学说明.pdf | 434.82K |
| 163 | 烷脱氢动力学说明.docx | 162B |
| 164 | 01-正戊烷异构化反应条件及反应动力学.pdf | 146.09K |
| 165 | 02-C5_C6烷烃异构化贵金属催化剂的研究.caj | 2.94M |
| 166 | 正戊烷异构化动力学说明.docx | 200.64K |
| 167 | 正戊烷异构化动力学说明.pdf | 306.86K |
| 168 | 1-全流程模拟（不含热泵、换热网络）.bkp | 3.50M |
| 169 | 2-全流程模拟（含热泵，不含换热网络）.bkp | 3.90M |
| 170 | 3-全流程模拟（含热泵，换热网络.bkp | 4.03M |
| 171 | PDMSPS中空纤维复合膜分离氢气的性能研究.pdf | 193.64K |
| 172 | 压缩冷凝富集氢气.png | 67.76K |
| 173 | 综合回收炼厂气中氢气及轻烃工艺的设计研究_彭琳.caj | 3.73M |
| 174 | 膜分离技术.png | 44.78K |
| 175 | 原料分离工段.bkp | 886.65K |
| 176 | 反应工段.bkp | 815.09K |
| 177 | 废气处理工段.bkp | 1.21M |
| 178 | 异戊二烯精制工段.bkp | 1.37M |
| 179 | 燃烧尾气产低压蒸汽及碳化处理.bkp | 687.43K |
| 180 | 药用针剂小苏打的开发生产.pdf | 139.19K |
| 181 | 1-DSTWU-NSTAGE.bkp | 192.55K |
| 182 | 2-RR-MOLD.bkp | 222.53K |
| 183 | 3-FEEDSTAGE.bkp | 543.84K |
| 184 | 4-已优化.bkp | 217.64K |
| 185 | 塔参数优化说明.docx | 259.58K |
| 186 | 塔参数优化说明.pdf | 400.90K |
| 187 | DSTWU-NSTAGE.bkp | 138.42K |
| 188 | NTFEEDRD.bkp | 420.11K |
| 189 | RR-MOLD.bkp | 200.21K |
| 190 | 已优化.bkp | 193.34K |
| 191 | FEEDSTAGERD.bkp | 351.39K |
| 192 | NSTAGERR.bkp | 340.69K |
| 193 | RR-MOLD.bkp | 346.20K |
| 194 | 优化后.bkp | 267.96K |
| 195 | DSTWU-NSTAGE.bkp | 165.39K |
| 196 | FEEDNTRD.bkp | 540.35K |
| 197 | RR-MOLD.bkp | 352.60K |
| 198 | 已优化.bkp | 255.81K |
| 199 | DSTWU-NSTAGE.bkp | 135.96K |
| 200 | FSTAGENSTAGERD.bkp | 452.81K |
| 201 | RR-MOLD.bkp | 190.60K |
| 202 | 已优化.bkp | 184.47K |
| 203 | DSTWU-NSTAGE.bkp | 136.02K |
| 204 | FSTAGENSTAGERD.bkp | 284.16K |
| 205 | RR-MOLD.bkp | 156.20K |
| 206 | 已优化.bkp | 154.76K |
| 207 | FEEDSTAGERD.bkp | 382.53K |
| 208 | NSTAGERR.bkp | 456.44K |
| 209 | RR-MOLD.bkp | 306.12K |
| 210 | 已优化.bkp | 293.75K |
| 211 | FEEDSTAGE.bkp | 325.84K |
| 212 | NSTAGE.bkp | 338.49K |
| 213 | RR-MOLD.bkp | 387.23K |
| 214 | 已优化.bkp | 259.33K |
| 215 | 萃取剂用量.bkp | 362.22K |
| 216 | DSTWU-NSTAGE.bkp | 163.69K |
| 217 | FEEDSTAGERD.bkp | 186.05K |
| 218 | RR-MOLD.bkp | 158.43K |
| 219 | 已优化.bkp | 148.62K |
| 220 | DSTWU-NSTAGE.bkp | 118.98K |
| 221 | FEEDSTAGENSTAGERD.bkp | 250.79K |
| 222 | RR-MOLD.bkp | 149.73K |
| 223 | 已优化.bkp | 143.06K |
| 224 | DSTWU-NSTAGE.bkp | 146.23K |
| 225 | FEEDSTAGE.bkp | 252.29K |
| 226 | RR-MOLD.bkp | 223.84K |
| 227 | 已优化.bkp | 221.89K |
| 228 | 吸收剂用量.bkp | 265.52K |
| 229 | 塔板数.bkp | 315.25K |
| 230 | 已优化.bkp | 193.23K |
| 231 | DSTWU-NSTAGE.bkp | 121.01K |
| 232 | FSTAGERD.bkp | 228.31K |
| 233 | RR-MOLD.bkp | 203.00K |
| 234 | 已优化.bkp | 194.98K |
| 235 | FEEDSTAGERD.bkp | 251.61K |
| 236 | NSTAGERR.bkp | 285.38K |
| 237 | RR-MOLD.bkp | 227.61K |
| 238 | 已优化.bkp | 225.20K |
| 239 | DSTWU-NSTAGE.bkp | 121.57K |
| 240 | FEEDSTAGE.bkp | 222.97K |
| 241 | RR-MOLD.bkp | 345.86K |
| 242 | 已优化.bkp | 163.84K |
| 243 | DIAMETER.bkp | 386.65K |
| 244 | LENGTH.bkp | 273.95K |
| 245 | PRESURE.bkp | 283.26K |
| 246 | T0104环戊烷精馏塔热泵改造.bkp | 428.92K |
| 247 | T0302异戊烷粗分塔热泵改造.bkp | 650.65K |
| 248 | 双效精馏.bkp | 669.55K |
| 249 | 能量集成及换热网络设计.docx | 3.62M |
| 250 | 能量集成及换热网络设计.pdf | 2.08M |
| 251 | 1-原始工艺流股.hch | 1.10M |
| 252 | 1-原始工艺流股全流程模拟.bkp.bkp | 3.53M |
| 253 | 总组合曲线图.png | 23.20K |
| 254 | 总费用与最小传热温差关系图.png | 26.81K |
| 255 | 温焓图.png | 21.20K |
| 256 | 总组合曲线图.png | 21.01K |
| 257 | 总费用与最小传热温差关系图.png | 43.77K |
| 258 | 改进工艺流股.hch | 18.40M |
| 259 | 改进工艺流股全流程模拟.bkp | 3.90M |
| 260 | 温焓图.png | 22.28K |
| 261 | 优化后换热网络.hch | 23.94M |
| 262 | 全流程模拟（含热泵，换热网络.bkp | 4.16M |
| 263 | 总组合曲线图.png | 22.92K |
| 264 | 总费用与最小传热温差关系图.png | 26.30K |
| 265 | 温焓图.png | 39.58K |
| 266 | 污垢热阻来源于《化工工艺设计手册》第四版.pdf | 365.35K |
| 267 | E0201.EDR | 275.30K |
| 268 | E0201.fx2 | 24.00K |
| 269 | E0201.htm | 627.51K |
| 270 | colorschememapping.xml | 314B |
| 271 | filelist.xml | 1.64K |
| 272 | header.htm | 6.18K |
| 273 | image001.wmz | 286B |
| 274 | image002.png | 397B |
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| 317 | oledata.mso | 41.50K |
| 318 | themedata.thmx | 3.02K |
| 319 | E0401.EDR | 291.97K |
| 320 | E0401.fx2 | 24.00K |
| 321 | E0401.htm | 1.22M |
| 322 | colorschememapping.xml | 314B |
| 323 | filelist.xml | 11.61K |
| 324 | header.htm | 6.18K |
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| 904 | 优化后换热网络.hch | 23.94M |
| 905 | 全流程模拟（含热泵，换热网络.bkp | 4.16M |
| 906 | 总组合曲线图.png | 22.92K |
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| 909 | 污垢热阻来源于《化工工艺设计手册》第四版.pdf | 365.35K |
| 910 | E0201.EDR | 275.30K |
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| 1330 | image363.png | 2.52K |
| 1331 | oledata.mso | 260.50K |
| 1332 | themedata.thmx | 3.02K |
| 1333 | T0303异戊烷精制塔.bkp | 1016.16K |
| 1334 | T0303.cn2 | 30.20K |
| 1335 | T0303.docx | 225.84K |
| 1336 | T0303动态模拟.bkp | 453.64K |
| 1337 | T0303动态模拟.dynf | 1.30M |
| 1338 | snapshot.bak | 3.00M |
| 1339 | snpA0000.snp | 4.93M |
| 1340 | t0303动态模拟dyn.his | 1.54K |
| 1341 | t0303动态模拟dyn.rep | 0B |
| 1342 | tasksnap.bak | 572B |
| 1343 | R0201.docx | 457.87K |
| 1344 | R0201.fx2 | 24.00K |
| 1345 | T0303.cn2 | 30.20K |
| 1346 | T0303.docx | 201.90K |
| 1347 | E0201.docx | 121.53K |
| 1348 | E0201.fx2 | 24.00K |
| 1349 | E0401.docx | 436.16K |
| 1350 | E0401.fx2 | 24.00K |
| 1351 | readme.txt | 636B |
| 1352 | reactionvolume.mph | 924.05K |
| 1353 | 反应体积与反应速度的关系.png | 26.10K |
| 1354 | 反应体积与摩尔流速的关系.png | 38.21K |
| 1355 | 反应体积与转化率的关系.png | 24.95K |
| 1356 | reactiontime.mph | 674.73K |
| 1357 | 反应时间与浓度的关系.png | 39.31K |
| 1358 | 反应时间与转化率的关系.png | 27.23K |
| 1359 | 厂区三维建模.skp | 368.01M |
| 1360 | 俯视图.png | 367.00K |
| 1361 | 右视图.png | 88.93K |
| 1362 | 后视图.png | 94.31K |
| 1363 | 左视图.png | 108.55K |
| 1364 | 西南侧等轴图.png | 199.29K |
| 1365 | VAC合成工段设备布置三维图.dwl | 42B |
| 1366 | VAC合成工段设备布置三维图.dwl2 | 195B |
| 1367 | 反应工段.dwg | 4.79M |
| 1368 | 废气处理工段.dwg | 8.82M |
| 1369 | 异戊二烯精制工段.dwg | 8.61M |
| 1370 | 拔头油分离工段.dwg | 6.10M |
| 1371 | 配管.max | 20.39M |
| 1372 | T0303动态模拟.bkp | 453.64K |
| 1373 | T0303动态模拟.dynf | 1.30M |
| 1374 | snapshot.bak | 3.00M |
| 1375 | snpA0000.snp | 4.93M |
| 1376 | t0303动态模拟dyn.his | 1.54K |
| 1377 | t0303动态模拟dyn.rep | 0B |
| 1378 | tasksnap.bak | 572B |
| 1379 | 动力学来源说明.txt | 1.11K |
| 1380 | 1-异戊烷脱氢动力学.pdf | 579.32K |
| 1381 | 2-吉布斯平衡反应器.bkp | 130.92K |
| 1382 | 3-拟合kp.xlsx | 52.98K |
| 1383 | 异戊烷脱氢动力学说明.docx | 271.97K |
| 1384 | 异戊烷脱氢动力学说明.pdf | 434.82K |
| 1385 | 烷脱氢动力学说明.docx | 162B |
| 1386 | 01-正戊烷异构化反应条件及反应动力学.pdf | 146.09K |
| 1387 | 02-C5_C6烷烃异构化贵金属催化剂的研究.caj | 2.94M |
| 1388 | 正戊烷异构化动力学说明.docx | 200.64K |
| 1389 | 正戊烷异构化动力学说明.pdf | 306.86K |
此图纸下载需要520金币
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发布者
静
创作: 14267
粉丝: 6
加入时间：2025-05-27
模型信息
图纸格式：dwg,pdf,skp
文件大小：458.84M
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