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10万吨年1,4-丁二醇生产项目初步设计（ID:2697091）
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| # | 文件名称 | 文件大小 |
|---|---|---|
| 1 | 17594058244216.zip | 948.36M |
| 2 | readme.txt | 954B |
| 3 | 设计文档质量评分索引.pdf | 408.19K |
| 4 | 0-项目摘要.docx | 480.77K |
| 5 | 1-可行性分析.docx | 1.39M |
| 6 | 2-初步设计说明书.docx | 6.68M |
| 7 | 3-设备设计及选型说明书.docx | 5.97M |
| 8 | 4-创新性说明.docx | 2.58M |
| 9 | 5-经济分析.docx | 613.81K |
| 10 | 6-能量集成及换热网络设计.docx | 1.38M |
| 11 | 7-环境影响评价报告.docx | 3.66M |
| 12 | 8-安全评价报告.docx | 4.85M |
| 13 | 附录1-物料平衡书.docx | 529.69K |
| 14 | 附录10-反应动力学说明.docx | 903.24K |
| 15 | 附录11-重大危险源分析计算.docx | 274.32K |
| 16 | 附录12-分离过程设计与优化.docx | 481.55K |
| 17 | 附录13-浓缩工艺节能方案比选说明.docx | 395.89K |
| 18 | 附录14-T0101动态模拟说明.docx | 1.25M |
| 19 | 附录15-T0201水力学分析报告.docx | 823.57K |
| 20 | 附录16-Risksystem图集.docx | 9.06M |
| 21 | 附录2-能量平衡书.docx | 369.92K |
| 22 | 附录3-设备选型一览表.docx | 266.41K |
| 23 | 附录4-物质MSDS.docx | 295.33K |
| 24 | 附录5-HAZOP分析报告说明书.docx | 416.35K |
| 25 | 附录6-ALOHA分析报告.docx | 3.75M |
| 26 | 附录7-公用工程供应协议及方案.docx | 208.63K |
| 27 | 附录8-管道选型一览表.docx | 245.98K |
| 28 | 附录9-中国绿色低碳发展2025说明书.docx | 363.96K |
| 29 | 设计图册集.pdf | 19.35M |
| 30 | 设计图册集.pdf | 19.35M |
| 31 | 物料工艺流程图-PFD.dwg | 1.28M |
| 32 | 管道及仪表流程图PID.dwg | 1.14M |
| 33 | 车间设备平立面布置图.dwg | 984.87K |
| 34 | 厂区总平面布置图.dwg | 621.27K |
| 35 | 1-T0201-丙炔醇粗分塔工艺条件图.dwg | 355.86K |
| 36 | 2-E0305-换热器工艺条件图.dwg | 346.29K |
| 37 | 3-R0101-炔化反应器工艺条件图.dwg | 465.65K |
| 38 | 车间三维布置图.pdf | 2.75M |
| 39 | 1-厂区三维布置图.pdf | 7.88M |
| 40 | 2-厂区三维渲染图.pdf | 2.09M |
| 41 | 典型管道轴测图.dwg | 300.76K |
| 42 | readme.txt | 1.03K |
| 43 | 14-丁炔二醇加氢物性方法选择PR-BM来源.pdf | 362.14K |
| 44 | readme.txt | 1.56K |
| 45 | 【1】全流程无节能技术，无换热网络.bkp | 1.53M |
| 46 | 【2】全流程含节能技术，无换热网络.bkp | 931.67K |
| 47 | 【3】全流程含节能技术，含换热网络.bkp | 1.83M |
| 48 | 全流程运行无错误无警告.mp4 | 2.33M |
| 49 | 附录10-反应动力学说明.docx | 903.24K |
| 50 | 附录10-反应动力学说明.pdf | 1.04M |
| 51 | readme.txt | 546B |
| 52 | 【1】炔化反应动力学来源.pdf | 10.85M |
| 53 | 【2】加氢反应动力学来源.pdf | 700.89K |
| 54 | 【3】加氢反应动力学来源.pdf | 283.51K |
| 55 | 【4】加氢反应动力学来源.pdf | 159.32K |
| 56 | 1-T0201-DSTWU.bkp | 317.17K |
| 57 | 2-T0201-灵敏度分析.bkp | 784.51K |
| 58 | 3-T0201-设计规定.bkp | 326.37K |
| 59 | readme.txt | 558B |
| 60 | 附录12-分离过程设计与优化.docx | 481.55K |
| 61 | 附录12-分离过程设计与优化.pdf | 612.21K |
| 62 | T0201初步设计.bkp | 329.06K |
| 63 | T0201校核.bkp | 483.32K |
| 64 | 附录15-T0201水力学分析报告.pdf | 910.70K |
| 65 | 反应器设计_F-RATIO.bkp | 431.00K |
| 66 | 四效蒸发.bkp | 413.39K |
| 67 | 工业普通单塔浓缩.bkp | 192.47K |
| 68 | 浓缩塔双效精馏.bkp | 486.93K |
| 69 | 浓缩塔热泵精馏.bkp | 426.70K |
| 70 | 附录13-浓缩工艺节能方案比选说明.docx | 395.89K |
| 71 | 附录13-浓缩工艺节能方案比选说明.pdf | 525.67K |
| 72 | 附录6-ALOHA分析报告.docx | 3.75M |
| 73 | 附录6-ALOHA分析报告.pdf | 2.50M |
| 74 | BLEVE分析.alo | 4.73K |
| 75 | BLEVE分析.png | 286.52K |
| 76 | 池火分析.alo | 4.73K |
| 77 | 池火分析.png | 298.78K |
| 78 | 蒸汽云中毒.alo | 4.73K |
| 79 | 蒸汽云中毒.png | 261.34K |
| 80 | 蒸汽云燃烧.alo | 4.73K |
| 81 | 蒸汽云燃烧.png | 256.59K |
| 82 | 蒸汽云爆炸.alo | 4.73K |
| 83 | 蒸汽云爆炸.png | 248.74K |
| 84 | BLEVE分析.alo | 4.73K |
| 85 | BLEVE分析.png | 313.22K |
| 86 | 池火分析.alo | 4.73K |
| 87 | 池火分析.png | 330.65K |
| 88 | 蒸汽云中毒.alo | 4.73K |
| 89 | 蒸汽云中毒.png | 303.25K |
| 90 | 蒸汽云燃烧.alo | 4.73K |
| 91 | 蒸汽云燃烧.png | 294.73K |
| 92 | 蒸汽云爆炸.alo | 4.73K |
| 93 | 蒸汽云爆炸.png | 321.09K |
| 94 | BLEVE分析.alo | 4.73K |
| 95 | BLEVE分析.png | 292.54K |
| 96 | 池火分析.alo | 4.73K |
| 97 | 池火分析.png | 297.73K |
| 98 | 蒸汽云中毒.alo | 4.73K |
| 99 | 蒸汽云中毒.png | 273.52K |
| 100 | 蒸汽云燃烧.alo | 4.73K |
| 101 | 蒸汽云燃烧.png | 264.32K |
| 102 | 蒸汽云爆炸.alo | 4.73K |
| 103 | 蒸汽云爆炸.png | 249.29K |
| 104 | 1-声源属性.png | 87.53K |
| 105 | 2-预测方案属性.png | 112.45K |
| 106 | 3-预测结果.png | 68.79K |
| 107 | 4-噪声等值线.png | 1.17M |
| 108 | 5-部分计算数据记录.png | 143.77K |
| 109 | Result.txt | 654.17K |
| 110 | ~$噪声分布数据表.xlsx | 165B |
| 111 | 厂区布置图.jpg | 300.98K |
| 112 | 噪声分布数据表.xlsx | 135.11K |
| 113 | 噪声分析图源文件.EIP | 967.06K |
| 114 | 噪声分析源文件.ein | 1.53K |
| 115 | 附录16-Risksystem图集.docx | 9.06M |
| 116 | 附录16-Risksystem图集.pdf | 6.90M |
| 117 | 1-14-丁二醇储罐液体泄漏量计算.rsm | 112B |
| 118 | 2-14-丁二醇储罐池火事故模型预测.rsm | 200B |
| 119 | 3-14-丁二醇储罐沸腾液体扩展蒸汽爆炸（火球BLEVE）模型预测.rsm | 211B |
| 120 | 4-14-丁二醇储罐蒸汽云爆炸预测（TNT当量法）.rsm | 166B |
| 121 | 5-14-丁二醇储罐有毒物质在大气中扩散预测.rsm | 494B |
| 122 | 6-14-丁二醇储罐典型泄露事故模拟.rsm | 500B |
| 123 | 1-丙炔醇液体泄漏量计算.rsm | 109B |
| 124 | 2-丙炔醇储罐池火事故模型预测.rsm | 210B |
| 125 | 3-丙炔醇储罐沸腾液体扩展蒸汽爆炸模型预测.rsm | 213B |
| 126 | 4-丙炔醇储罐蒸汽云爆炸模型预测.rsm | 167B |
| 127 | 5-丙炔醇储罐大气扩散预测.rsm | 496B |
| 128 | 6-丙炔醇储罐典型泄露事故模拟.rsm | 513B |
| 129 | 1-乙酸正丙酯储罐液体泄漏量计算.rsm | 113B |
| 130 | 2-乙酸正丙酯储罐池火事故模型预测.rsm | 207B |
| 131 | 3-乙酸正丙酯储罐沸腾液体扩展蒸汽爆炸模型预测.rsm | 213B |
| 132 | 4-乙酸正丙酯储罐蒸汽云爆炸模型预测.rsm | 168B |
| 133 | 5-乙酸正丙酯储罐在大气中的扩散预测.rsm | 508B |
| 134 | 6-乙酸正丙酯储罐典型泄露事故模拟.rsm | 526B |
| 135 | 1-甲醛储罐液体泄漏量计算.rsm | 105B |
| 136 | 2-甲醛储罐池火事故模型预测.rsm | 199B |
| 137 | 3-甲醛储罐沸腾液体扩散蒸汽爆炸模型.rsm | 204B |
| 138 | 4-甲醛储罐蒸汽爆炸模型预测.rsm | 159B |
| 139 | 5-甲醛储罐有毒有害物质在大气中的扩散模型预测.rsm | 490B |
| 140 | 6-甲醛储罐典型泄露事故模拟.rsm | 498B |
| 141 | 1-厂区三维布置图.pdf | 7.88M |
| 142 | 2-厂区三维渲染图.pdf | 2.09M |
| 143 | 3-厂区三维渲染源文件.ls9 | 369.96M |
| 144 | 4-创新性说明.docx | 2.58M |
| 145 | 无液体分布器.png | 183.65K |
| 146 | 无液体分布器动图.gif | 33.22M |
| 147 | 有液体分布器.png | 158.91K |
| 148 | 有液体分布器动图1.gif | 30.42M |
| 149 | 有液体分布器动图2.gif | 41.02M |
| 150 | 1-无分布器.mph | 68.84M |
| 151 | 2-有分布器.mph | 395.56M |
| 152 | 6-能量集成及换热网络设计.docx | 1.38M |
| 153 | 6-能量集成及换热网络设计.pdf | 1.58M |
| 154 | 【1】全流程无节能技术原始流股.hch | 559.47K |
| 155 | 【2】全流程无节能技术删除部分流股.hch | 455.71K |
| 156 | 【3】全流程含节能技术原始流股.hch | 666.91K |
| 157 | 【4】全流程含节能技术优化过程与优化结果.hch | 5.01M |
| 158 | 【5】全流程含换热网络aspen导出.hch | 594.43K |
| 159 | 图4-1总费用-最小传热温差曲线（不含节能技术）.tif | 75.29K |
| 160 | 图4-2组合曲线（不含节能技术）.tif | 91.34K |
| 161 | 图4-3总费用-最小传热温差曲线（含热泵技术、双效精馏、隔壁塔）.tif | 77.04K |
| 162 | 图4-4组合曲线（含热泵技术、双效精馏、隔壁塔）.tif | 73.34K |
| 163 | 图4-5能量集成目标（含热泵技术、双效精馏、隔壁塔）.tif | 23.13K |
| 164 | 图4-6过程总组合曲线（含热泵技术、双效精馏、隔壁塔）.tif | 70.25K |
| 165 | 图5-1系统推荐的10个方案.tif | 51.53K |
| 166 | 图5-2（1）系统推荐的方案7.tif | 147.09K |
| 167 | 图5-2（2）删除换热面积较小的换热器（例E-137换热面积为0.98m^2）.tif | 141.49K |
| 168 | 图5-2（3）loops回路展示1.tif | 154.05K |
| 169 | 图5-2（4）loops回路展示2.tif | 155.75K |
| 170 | 图5-2（5）loops回路展示3.tif | 156.92K |
| 171 | 图5-2（6）loops回路展示4.tif | 156.39K |
| 172 | 图5-2（8）打破loops回路，删除换热面积小的换热器.tif | 134.11K |
| 173 | 图5-3最终调整优化的设计方案.tif | 131.91K |
| 174 | 图5-4流股间换热示意图.png | 15.21K |
| 175 | 图5-4流股间换热示意图.tif | 39.20K |
| 176 | 图5.2（7）loops回路展示5.tif | 155.26K |
| 177 | 图8-1优化前的总组合曲线图.tif | 91.34K |
| 178 | 图8-2优化后的总组合曲线图.tif | 77.62K |
| 179 | E0301氢气进料第一换热器.EDR | 251.28K |
| 180 | E0305-Design.EDR | 235.46K |
| 181 | E0305-Rating.EDR | 253.84K |
| 182 | T0101-动态模拟-TC整定.dynf | 560.43K |
| 183 | T0101-动态模拟-进料减少10.dynf | 564.47K |
| 184 | T0101-动态模拟-进料增加10.dynf | 563.65K |
| 185 | T0101-动态模拟.bkp | 566.35K |
| 186 | T0101-动态模拟.dynf | 193.00K |
| 187 | T0101-动态模拟dyn.appdf | 445.04K |
| 188 | 附录14-T0101动态模拟说明.docx | 1.25M |
| 189 | 附录14-T0101动态模拟说明.pdf | 657.70K |
| 190 | snpA0000.snp | 1.65M |
| 191 | snpA0001.snp | 1.67M |
| 192 | snpA0002.snp | 1.66M |
| 193 | t0101-动态模拟dyn.his | 1.25K |
| 194 | t0101-动态模拟dyn.rep | 0B |
| 195 | tasksnap.bak | 856B |
| 196 | tasksnap.tsnp | 1.11K |
| 197 | snapshot.bak | 2.46M |
| 198 | snpA0000.snp | 1.65M |
| 199 | snpA0001.snp | 1.67M |
| 200 | snpA0002.snp | 1.66M |
| 201 | t0101-动态模拟dyn.his | 1.06K |
| 202 | t0101-动态模拟dyn.rep | 0B |
| 203 | tasksnap.bak | 1.63K |
| 204 | tasksnap.tsnp | 1.63K |
| 205 | AM_SAI.appdf | 445.04K |
| 206 | snapshot.bak | 2.42M |
| 207 | snpA0000.snp | 1.65M |
| 208 | snpA0001.snp | 1.67M |
| 209 | snpA0002.snp | 1.66M |
| 210 | t0101-动态模拟dyn.his | 1.06K |
| 211 | t0101-动态模拟dyn.rep | 0B |
| 212 | tasksnap.bak | 1.63K |
| 213 | AM_SAI.appdf | 445.04K |
| 214 | snapshot.bak | 2.42M |
| 215 | snpA0000.snp | 1.65M |
| 216 | snpA0001.snp | 1.67M |
| 217 | snpA0002.snp | 1.66M |
| 218 | t0101-动态模拟dyn.his | 1.06K |
| 219 | t0101-动态模拟dyn.rep | 0B |
| 220 | tasksnap.bak | 1.11K |
| 221 | 设计图册集.pdf | 19.35M |
| 222 | 物料工艺流程图-PFD.dwg | 1.28M |
| 223 | 管道及仪表流程图PID.dwg | 1.14M |
| 224 | 车间设备平立面布置图.dwg | 984.87K |
| 225 | 厂区总平面布置图.dwg | 621.27K |
| 226 | 1-T0201-丙炔醇粗分塔工艺条件图.dwg | 355.86K |
| 227 | 2-E0305-换热器工艺条件图.dwg | 346.29K |
| 228 | 3-R0101-炔化反应器工艺条件图.dwg | 474.51K |
| 229 | 车间三维布置图.pdf | 2.75M |
| 230 | 1-厂区三维布置图.pdf | 7.88M |
| 231 | 2-厂区三维渲染图.pdf | 2.09M |
| 232 | 典型管道轴测图.dwg | 300.76K |
| 233 | T0201-强度校核.cn2 | 32.58K |
| 234 | 塔设备强度校核.doc | 808.00K |
| 235 | E0301强度校核.fx3 | 26.05K |
| 236 | E0301氢气进料第一换热器-强度校核.doc | 2.42M |
| 237 | E0305强度校核.docx | 739.79K |
| 238 | E0305强度校核.fx3 | 26.05K |
| 239 | R0101强度校核.doc | 2.72M |
| 240 | R0101强度校核.fx3 | 26.05K |
| 241 | 气液分离器V0104强度校核.doc | 304.50K |
| 242 | 气液分离罐V0104强度校核.ra2 | 24.57K |
| 243 | readme.txt | 899B |
| 244 | 主视图.png | 100.68K |
| 245 | 俯视图.png | 81.45K |
| 246 | 右视图.png | 78.67K |
| 247 | 后视图.png | 115.09K |
| 248 | 左视图.png | 88.27K |
| 249 | 管道图.png | 288.88K |
| 250 | 设备布置图.png | 200.68K |
| 251 | 车间三维布置图.pdf | 2.75M |
| 252 | 轴测图1.png | 328.20K |
| 253 | 轴测图2.png | 283.81K |
| 254 | 轴测图3.png | 417.79K |
| 255 | 轴测图4.png | 332.21K |
| 256 | 钢结构图.png | 217.85K |
| 257 | DefaultConnectorsConfig.xml | 31.77K |
| 258 | Iso.dcf | 156.00K |
| 259 | IsoPart.xml | 2.11K |
| 260 | Metric_OrthoPart.xml | 2.66K |
| 261 | Metric_PipeBendDefaultValues.txt | 1.05K |
| 262 | Metric_PipingPart.xml | 16.13K |
| 263 | Misc.dcf | 100.00K |
| 264 | MiscPart.xml | 1.81K |
| 265 | Ortho.dcf | 168.00K |
| 266 | PIDTo3dClassMapping.xml | 920.75K |
| 267 | PIDToSpecClassMapping.xml | 926.56K |
| 268 | Piping.dcf | 3.61M |
| 269 | PIP_Metric_PnIdPart.xml | 133.03K |
| 270 | ProcessPower.dcf | 1.01M |
| 271 | Project.xml | 1.95K |
| 272 | Project.xml.lock | 0B |
| 273 | projSymbolStyle.dwg | 352.13K |
| 274 | SubstitutionPalettes.xml | 84.17K |
| 275 | BoltSizeMappings.xml | 1.71K |
| 276 | IsoSkeyAcadBlockMap.xml | 14.65K |
| 277 | IsoSymbolStyles.dwg | 249.04K |
| 278 | Plant3dIsoSymbols.dwg | 39.15K |
| 279 | PropertyTranslationMapping.xml | 462B |
| 280 | Iso.atr | 436B |
| 281 | Iso.dwt | 39.58K |
| 282 | IsoConfig.xml | 210.24K |
| 283 | Iso.atr | 436B |
| 284 | Iso.dwt | 90.97K |
| 285 | IsoConfig.xml | 210.06K |
| 286 | Iso.atr | 436B |
| 287 | Iso.dwt | 58.13K |
| 288 | IsoConfig.xml | 210.67K |
| 289 | Iso.atr | 436B |
| 290 | Iso.dwt | 97.47K |
| 291 | IsoConfig.xml | 210.25K |
| 292 | SampleIsoPreview.pcf | 11.22K |
| 293 | Iso.atr | 436B |
| 294 | Iso.dwt | 97.79K |
| 295 | IsoConfig.xml | 210.47K |
| 296 | Iso.atr | 382B |
| 297 | Iso.dwt | 122.67K |
| 298 | IsoConfig.xml | 219.73K |
| 299 | OrthoSymbolStyles.dwg | 36.55K |
| 300 | orthoTemp.dwt | 32.99K |
| 301 | Ortho-A1-ColorDependentPlotStyles.dwt | 66.68K |
| 302 | Ortho-A1-NamedPlotStyles.dwt | 67.33K |
| 303 | OrthoConfig.xml | 2.86K |
| 304 | 管道布置图.bak | 17.22M |
| 305 | 管道布置图.dwg | 14.54M |
| 306 | 设备布置图.bak | 11.90M |
| 307 | 设备布置图.dwg | 11.92M |
| 308 | ControlValveList.xml | 2.88K |
| 309 | DocumentList.xml | 681B |
| 310 | EquipmentList.xml | 1.74K |
| 311 | InstrumentationIndex.xml | 2.85K |
| 312 | LineList.xml | 2.60K |
| 313 | LineSummaryList.xml | 2.19K |
| 314 | NozzleList.xml | 3.20K |
| 315 | SpecialtyItemsList.xml | 2.87K |
| 316 | ValveList.xml | 2.89K |
| 317 | 100HC01.pspc | 1.51M |
| 318 | 100HC01.pspx | 9.39K |
| 319 | 100HS01.pspc | 1.51M |
| 320 | 100HS01.pspx | 9.42K |
| 321 | 10HC01.pspc | 1.94M |
| 322 | 10HC01.pspx | 9.99K |
| 323 | 10HS01.pspc | 1.95M |
| 324 | 10HS01.pspx | 10.01K |
| 325 | 160HC01.pspc | 1.50M |
| 326 | 160HC01.pspx | 9.39K |
| 327 | 160HS01.pspc | 1.50M |
| 328 | 160HS01.pspx | 9.42K |
| 329 | 16HC01.pspc | 1.84M |
| 330 | 16HC01.pspx | 9.77K |
| 331 | 16HS01.pspc | 1.83M |
| 332 | 16HS01.pspx | 9.80K |
| 333 | 1HC01.pspc | 1.53M |
| 334 | 1HC01.pspx | 9.41K |
| 335 | 1HS01.pspc | 1.53M |
| 336 | 1HS01.pspx | 9.42K |
| 337 | 250HC01.pspc | 1.50M |
| 338 | 250HC01.pspx | 9.39K |
| 339 | 250HS01.pspc | 1.50M |
| 340 | 250HS01.pspx | 9.42K |
| 341 | 25HC01.pspc | 1.54M |
| 342 | 25HC01.pspx | 9.63K |
| 343 | 25HS01.pspc | 1.54M |
| 344 | 25HS01.pspx | 9.65K |
| 345 | 2HC01.pspc | 1.53M |
| 346 | 2HC01.pspx | 9.39K |
| 347 | 2HS01.pspc | 1.53M |
| 348 | 2HS01.pspx | 9.42K |
| 349 | 320HC01.pspc | 1.50M |
| 350 | 320HC01.pspx | 9.39K |
| 351 | 320HS01.pspc | 1.50M |
| 352 | 320HS01.pspx | 9.42K |
| 353 | 400HC01.pspc | 1.50M |
| 354 | 400HC01.pspx | 9.39K |
| 355 | 400HS01.pspc | 1.50M |
| 356 | 400HS01.pspx | 9.42K |
| 357 | 40HC01.pspc | 1.81M |
| 358 | 40HC01.pspx | 9.64K |
| 359 | 40HS01.pspc | 1.82M |
| 360 | 40HS01.pspx | 9.66K |
| 361 | 64HC01.pspc | 1.51M |
| 362 | 64HC01.pspx | 9.39K |
| 363 | 64HS01.pspc | 1.51M |
| 364 | 64HS01.pspx | 9.42K |
| 365 | 6HC01.pspc | 1.57M |
| 366 | 6HC01.pspx | 7.30K |
| 367 | 6HS01.pspc | 1.57M |
| 368 | 6HS01.pspx | 9.87K |
| 369 | AWWAC110.pspc | 1.31M |
| 370 | AWWAC110.pspx | 6.55K |
| 371 | CS150.pspc | 831.00K |
| 372 | CS150.pspx | 6.54K |
| 373 | CS1500.pspc | 859.00K |
| 374 | CS1500.pspx | 6.68K |
| 375 | CS150Flanged.pspc | 385.00K |
| 376 | CS150Flanged.pspx | 3.96K |
| 377 | CS2500.pspc | 757.00K |
| 378 | CS2500.pspx | 6.63K |
| 379 | CS300.pspc | 846.00K |
| 380 | CS300.pspx | 6.63K |
| 381 | CS600.pspc | 903.00K |
| 382 | CS600.pspx | 6.51K |
| 383 | CS900.pspc | 766.00K |
| 384 | CS900.pspx | 6.22K |
| 385 | CustomPartsImperial.pspc | 1.68M |
| 386 | CustomPartsImperial.pspx | 8.80K |
| 387 | CustomPartsMetric.pspc | 1.32M |
| 388 | CustomPartsMetric.pspx | 8.83K |
| 389 | DIClass150.pspc | 307.00K |
| 390 | DIClass150.pspx | 2.86K |
| 391 | DIClass250.pspc | 485.00K |
| 392 | DIClass250.pspx | 3.71K |
| 393 | GroovedClass150.pspc | 578.00K |
| 394 | GroovedClass150.pspx | 4.40K |
| 395 | GroovedClass300.pspc | 327.00K |
| 396 | GroovedClass300.pspx | 3.79K |
| 397 | InstrumentationImperial.pspc | 155.00K |
| 398 | InstrumentationImperial.pspx | 2.73K |
| 399 | InstrumentationMetric.pspc | 188.00K |
| 400 | InstrumentationMetric.pspx | 2.73K |
| 401 | PipeSupportsSpec.pspc | 1.09M |
| 402 | PipeSupportsSpec.pspx | 3.07K |
| 403 | PlaceHolderImperial.pspc | 1.70M |
| 404 | PlaceHolderImperial.pspx | 8.80K |
| 405 | PlaceHolderMetric.pspc | 1.34M |
| 406 | PlaceHolderMetric.pspx | 8.83K |
| 407 | PN01CA1S01.pspc | 1.96M |
| 408 | PN01CA1S01.pspx | 4.69K |
| 409 | PN01CB2S01.pspc | 1.98M |
| 410 | PN01CB2S01.pspx | 4.72K |
| 411 | PN01CJ1S01.pspc | 1.61M |
| 412 | PN01CJ1S01.pspx | 3.74K |
| 413 | PN01CK1S01.pspc | 1.62M |
| 414 | PN01CK1S01.pspx | 3.74K |
| 415 | PN01CL1S01.pspc | 1.54M |
| 416 | PN01CL1S01.pspx | 3.83K |
| 417 | PN01CM1S01.pspc | 1.54M |
| 418 | PN01CM1S01.pspx | 3.83K |
| 419 | PN01CS1B01.pspc | 1.25M |
| 420 | PN01CS1B01.pspx | 3.17K |
| 421 | PN01CS1S01.pspc | 2.01M |
| 422 | PN01CS1S01.pspx | 4.49K |
| 423 | PN01SA0B01.pspc | 1.49M |
| 424 | PN01SA0B01.pspx | 3.65K |
| 425 | PN01SA0B02.pspc | 2.04M |
| 426 | PN01SA0B02.pspx | 4.54K |
| 427 | PN01SA0B03.pspc | 2.06M |
| 428 | PN01SA0B03.pspx | 4.54K |
| 429 | PN01SA0B05.pspc | 1.39M |
| 430 | PN01SA0B05.pspx | 3.55K |
| 431 | PN03CA1S01.pspc | 1.87M |
| 432 | PN03CA1S01.pspx | 4.49K |
| 433 | PN03CJ1S01.pspc | 1.58M |
| 434 | PN03CJ1S01.pspx | 3.81K |
| 435 | PN06CA1S01.pspc | 1.84M |
| 436 | PN06CA1S01.pspx | 4.59K |
| 437 | PN06CB2S01.pspc | 1.82M |
| 438 | PN06CB2S01.pspx | 4.54K |
| 439 | PN09CB1S01.pspc | 1.57M |
| 440 | PN09CB1S01.pspx | 3.83K |
| 441 | PN09SP1S01.pspc | 1.52M |
| 442 | PN09SP1S01.pspx | 4.06K |
| 443 | PN15CL1S01.pspc | 1.48M |
| 444 | PN15CL1S01.pspx | 3.81K |
| 445 | PN15CM1S01.pspc | 1.48M |
| 446 | PN15CM1S01.pspx | 3.81K |
| 447 | Sch40PVC.pspc | 214.00K |
| 448 | Sch40PVC.pspx | 3.77K |
| 449 | Sch80CPVC.pspc | 215.00K |
| 450 | Sch80CPVC.pspx | 3.68K |
| 451 | Sch80PVC.pspc | 218.00K |
| 452 | Sch80PVC.pspx | 3.73K |
| 453 | SS150.pspc | 819.00K |
| 454 | SS150.pspx | 6.43K |
| 455 | SS1500.pspc | 854.00K |
| 456 | SS1500.pspx | 6.85K |
| 457 | SS2500.pspc | 752.00K |
| 458 | SS2500.pspx | 6.74K |
| 459 | SS300.pspc | 787.00K |
| 460 | SS300.pspx | 6.49K |
| 461 | SS600.pspc | 829.00K |
| 462 | SS600.pspx | 6.67K |
| 463 | SS900.pspc | 691.00K |
| 464 | SS900.pspx | 6.16K |
| 465 | 1-厂区三维布置图.pdf | 7.88M |
| 466 | 2-厂区三维渲染图.pdf | 2.09M |
| 467 | 厂区三维布置图.skp | 280.43M |
| 468 | 中石化重庆川维年产10万吨14-丁二醇项目.opexxmh | 416.00K |
| 469 | 附录5-HAZOP分析报告说明书.pdf | 1.37M |
| 470 | 附录10-反应动力学说明.docx | 903.24K |
| 471 | 附录10-反应动力学说明.pdf | 1.04M |
| 472 | readme.txt | 546B |
| 473 | 【1】炔化反应动力学来源.pdf | 10.85M |
| 474 | 【2】加氢反应动力学来源.pdf | 700.89K |
| 475 | 【3】加氢反应动力学来源.pdf | 283.51K |
| 476 | 【4】加氢反应动力学来源.pdf | 159.32K |
| 477 | 4-创新性说明.docx | 2.57M |
| 478 | 一种喷射式水环真空泵.pdf | 274.19K |
| 479 | 一种新型液体分布器.pdf | 342.57K |
| 480 | 一种新型的气液分离器.pdf | 168.17K |
| 481 | 一种自吸式气液搅拌器.pdf | 455.70K |
| 482 | 列管式固定床滴流反应器.pdf | 289.01K |
| 483 | 滴流床反应器的气液分布器.pdf | 338.18K |
| 484 | 竖管降膜新型液体分布器设计及性能研究.pdf | 2.57M |
| 485 | 鱼骨形的新型板式换热器板片.pdf | 288.72K |
| 486 | 一种气、液、固三相加氢反应系统.pdf | 372.92K |
| 487 | 气—液相管壳式滴流床固相催化反应器.pdf | 565.55K |
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