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1.5亿Nm3a火炬气资源化脱硫项目初步设计（ID:2709526）
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| # | 文件名称 | 文件大小 |
|---|---|---|
| 1 | readme.txt | 940B |
| 2 | 0-Abstract.docx | 3.16M |
| 3 | 0-项目摘要.docx | 3.15M |
| 4 | 1-可行性研究报告.docx | 2.35M |
| 5 | 2-初步设计说明书.docx | 8.01M |
| 6 | 3-1典型设备选型计算说明书.docx | 5.36M |
| 7 | 3-2反应器设计说明书.docx | 3.54M |
| 8 | 4-创新性说明书.docx | 2.27M |
| 9 | 5-1附录一物料平衡计算书.docx | 2.02M |
| 10 | 5-2附录二能量平衡计算书.docx | 1.96M |
| 11 | 5-3附录三较大能量回用的换热网络设计.docx | 2.19M |
| 12 | 5-4附录四物质MSDS.docx | 1.86M |
| 13 | 5-5附录五设备选型一览表.docx | 1.87M |
| 14 | 5-6附录六超重力旋转填料床说明书.docx | 2.75M |
| 15 | 5-7附录七脱重烃说明书.docx | 2.28M |
| 16 | 6-经济分析.docx | 1.96M |
| 17 | 7-安全预评价.docx | 4.99M |
| 18 | 8-环境影响评价报告.docx | 4.65M |
| 19 | 9-泄漏扩散模型及其模拟计算.docx | 2.53M |
| 20 | ~$6-经济分析.docx | 162B |
| 21 | 设计图册集.pdf | 21.96M |
| 22 | 工艺流程图PFD.dwg | 7.24M |
| 23 | 工艺流程图PFD图册集.pdf | 3.72M |
| 24 | 工艺流程图说明.pdf | 342.82K |
| 25 | 管道仪表流程图说明.pdf | 343.81K |
| 26 | 管道及仪表流程图PID.dwg | 5.61M |
| 27 | 管道及仪表流程图PID图册集.pdf | 2.66M |
| 28 | 1-深度脱硫车间设备布置图.dwg | 1.73M |
| 29 | 2-甲硫醇合成车间设备布置图.dwg | 1.08M |
| 30 | 3-甲硫醇分离精制车间设备布置图.dwg | 1.68M |
| 31 | 车间布置说明.pdf | 310.90K |
| 32 | 车间设备布置图图册集.pdf | 2.33M |
| 33 | 厂区总平面布置图.dwg | 618.09K |
| 34 | 厂区总平面布置图.pdf | 418.53K |
| 35 | 厂区总平面布置图说明.pdf | 349.68K |
| 36 | 1-俯视图.jpg | 73.82K |
| 37 | 2-45°俯视图.jpg | 90.51K |
| 38 | 3-等轴图.jpg | 85.18K |
| 39 | E0204-反应气三级冷却器工艺条件图.dwg | 55.61K |
| 40 | R0201-甲醇和H2S一段催化反应器工艺条件图.dwg | 57.89K |
| 41 | T0104-解吸塔工艺条件图.dwg | 59.98K |
| 42 | 典型设备工艺条件图图册集.pdf | 361.97K |
| 43 | E0204-反应气三级冷却器总装配图.dwg | 200.49K |
| 44 | R0201-甲醇和H2S一段催化反应器总装配图.dwg | 156.81K |
| 45 | T0104-解吸塔总装配图.dwg | 195.61K |
| 46 | 典型设备总装配图图册集.pdf | 993.18K |
| 47 | 管道轴测图ISO.dwg | 1.93M |
| 48 | 管道轴测图图册集.pdf | 266.40K |
| 49 | gbcbig.shx | 881.68K |
| 50 | 字体文件存放位置.txt | 358B |
| 51 | 1-全流程（不含热泵）.bkp | 1.78M |
| 52 | 2-全流程（不含换热网络、添加设计规定）.bkp | 1.87M |
| 53 | 3-全流程（含换热网络、塔优化参数代入）.bkp | 2.32M |
| 54 | 1-MDEA脱硫动力学.pdf | 218.45K |
| 55 | 2-A.V.Mashkina硫化氢甲醇反应器动力学来源.pdf | 169.44K |
| 56 | 3-甲硫醇裂解动力学.pdf | 209.56K |
| 57 | 4-硫化氢甲硫醚反应动力学.pdf | 215.27K |
| 58 | 5-硫化氢—甲硫醚合成甲硫醇催化剂动力学的研究及其工业应用.pdf | 10.05M |
| 59 | 甲硫醇合成反应器-CATAWT.bkp | 424.98K |
| 60 | 甲硫醇合成反应器-PRESSURE.bkp | 585.45K |
| 61 | 甲硫醇合成反应器-RESIDENCETIME.bkp | 579.29K |
| 62 | 甲硫醇合成反应器-TEMP.bkp | 581.45K |
| 63 | 甲硫醇合成反应器.bkp | 550.76K |
| 64 | 转化率、选择性与停留时间关系.xlsx | 16.94K |
| 65 | 甲硫醚硫化氢反应器-CATAWT.bkp | 442.61K |
| 66 | 甲硫醚硫化氢反应器-DIAMETER.bkp | 443.32K |
| 67 | 甲硫醚硫化氢反应器-LENGTH.bkp | 443.40K |
| 68 | 甲硫醚硫化氢反应器-PRESSURE.bkp | 451.23K |
| 69 | 甲硫醚硫化氢反应器-TEMP.bkp | 441.68K |
| 70 | 说明.txt | 539B |
| 71 | T0104.cn2 | 30.20K |
| 72 | T0104.doc | 616.50K |
| 73 | T0104解吸塔-design.bkp | 494.49K |
| 74 | MDEA吸收塔-DESIGN.bkp | 476.39K |
| 75 | MDEA吸收塔-DS.bkp | 136.45K |
| 76 | MDEA吸收塔-EFFIC.bkp | 149.74K |
| 77 | MDEA吸收塔-FEEDTEM.bkp | 168.47K |
| 78 | MDEA吸收塔-MDEA用量.bkp | 174.41K |
| 79 | MDEA吸收塔-NSTAGE.bkp | 167.47K |
| 80 | MDEA吸收塔-PRE.bkp | 182.64K |
| 81 | MDEA半解吸塔-DESIGN.bkp | 432.38K |
| 82 | MDEA半解吸塔-DS.bkp | 407.45K |
| 83 | MDEA半解吸塔-NSTAGE.bkp | 409.93K |
| 84 | MDEA半解吸塔-PRE.bkp | 423.71K |
| 85 | MDEA半解吸塔-再沸器产生汽量.bkp | 458.67K |
| 86 | MDEA解吸塔-DESIGN.bkp | 494.49K |
| 87 | MDEA解吸塔-EFFIC.bkp | 484.42K |
| 88 | MDEA解吸塔-NSTAGE.bkp | 503.94K |
| 89 | MDEA解吸塔-PRE.bkp | 509.16K |
| 90 | MDEA解吸塔-TEMP.bkp | 513.04K |
| 91 | MDEA解析塔-再沸器产生汽量.bkp | 531.30K |
| 92 | 低温甲醇吸收塔-DESIGN.bkp | 462.54K |
| 93 | 低温甲醇吸收塔-DS.bkp | 430.29K |
| 94 | 低温甲醇吸收塔-FEEDTEMP.bkp | 485.72K |
| 95 | 低温甲醇吸收塔-MEOHCOST.bkp | 498.78K |
| 96 | 低温甲醇吸收塔-NSTAGE.bkp | 449.40K |
| 97 | 低温甲醇吸收塔-PRESSURE.bkp | 467.27K |
| 98 | 脱硫化氢重接触塔-DESIGN.bkp | 458.65K |
| 99 | 脱硫化氢重接触塔-DSTWU.bkp | 428.20K |
| 100 | 脱硫化氢重接触塔-FEEDSTAGE1.bkp | 521.41K |
| 101 | 脱硫化氢重接触塔-FEEDSTAGE2.bkp | 521.45K |
| 102 | 脱硫化氢重接触塔-RR.bkp | 498.10K |
| 103 | 甲硫醇精制塔-DESIGN.bkp | 599.05K |
| 104 | 甲硫醇精制塔-DS.bkp | 513.20K |
| 105 | 甲硫醇精制塔-DSTWU.bkp | 407.72K |
| 106 | 甲硫醇精制塔-FEEDSTAGE.bkp | 553.49K |
| 107 | 甲硫醇精制塔-RR.bkp | 531.00K |
| 108 | 变压精馏低压塔-DESIGN.bkp | 474.25K |
| 109 | 变压精馏低压塔-DS.bkp | 445.42K |
| 110 | 变压精馏低压塔-DSTWU.bkp | 413.42K |
| 111 | 变压精馏低压塔-FEEDSTAGE.bkp | 464.70K |
| 112 | 变压精馏低压塔-RR.bkp | 461.76K |
| 113 | 变压精馏高压塔-DESIGN.bkp | 450.36K |
| 114 | 变压精馏高压塔-DS.bkp | 430.54K |
| 115 | 变压精馏高压塔-DSTWU.bkp | 406.61K |
| 116 | 变压精馏高压塔-FEEDSTAGE.bkp | 448.64K |
| 117 | 变压精馏高压塔-RR.bkp | 442.54K |
| 118 | 甲醇精馏塔-DESIGN.bkp | 505.04K |
| 119 | 甲醇精馏塔-DS.bkp | 427.86K |
| 120 | 甲醇精馏塔-DSTWU.bkp | 384.78K |
| 121 | 甲醇精馏塔-FEEDSTAGE.bkp | 458.30K |
| 122 | 甲醇精馏塔-RR.bkp | 446.78K |
| 123 | 说明.txt | 480B |
| 124 | 无双效精馏.bkp | 423.83K |
| 125 | 有双效精馏.bkp | 554.65K |
| 126 | 无热泵精馏.bkp | 484.51K |
| 127 | 有热泵精馏.bkp | 553.39K |
| 128 | 变压精馏.bkp | 702.98K |
| 129 | 萃取精馏.bkp | 583.50K |
| 130 | 方案一.bkp | 1.61M |
| 131 | 方案二.bkp | 1.05M |
| 132 | T0104.cn2 | 30.20K |
| 133 | T0104.doc | 616.50K |
| 134 | T0104解吸塔-design.bkp | 494.49K |
| 135 | MDEA半解吸塔-DESIGN.bkp | 432.38K |
| 136 | MDEA吸收塔-DESIGN.bkp | 476.39K |
| 137 | 低温甲醇吸收塔-DESIGN.bkp | 462.54K |
| 138 | 变压精馏低压塔-DESIGN.bkp | 474.25K |
| 139 | 变压精馏高压塔-DESIGN.bkp | 450.36K |
| 140 | 甲硫醇精制塔-DESIGN.bkp | 599.05K |
| 141 | 甲醇精馏塔-DESIGN.bkp | 505.04K |
| 142 | 脱硫化氢重接触塔-DESIGN.bkp | 458.65K |
| 143 | 1-3D厂区模拟设计.skp | 50.81M |
| 144 | 2-俯视图.jpg | 73.82K |
| 145 | 3-45°俯视图.jpg | 90.51K |
| 146 | 4-等轴图.jpg | 85.18K |
| 147 | 5-说明.txt | 384B |
| 148 | 1-厂区三维.nwf | 411.14K |
| 149 | 2-车间三维.nwf | 333.65K |
| 150 | 3-俯视图.jpg | 63.64K |
| 151 | 4-45°俯视图.jpg | 57.01K |
| 152 | 5-等轴图.jpg | 53.37K |
| 153 | 6-说明.txt | 448B |
| 154 | 1.jpg | 618.92K |
| 155 | 2.jpg | 584.38K |
| 156 | 3.jpg | 611.50K |
| 157 | 4.jpg | 466.22K |
| 158 | 5.jpg | 540.34K |
| 159 | 6.jpg | 610.18K |
| 160 | 7.jpg | 611.19K |
| 161 | 8.jpg | 619.15K |
| 162 | Sense8.ls4 | 212.12M |
| 163 | 说明.txt | 398B |
| 164 | 3-Risksystem图集.docx | 7.57M |
| 165 | 4-Risksystem图集.pdf | 1.66M |
| 166 | 典型泄漏事故模拟.rsm | 507B |
| 167 | 甲硫蒸汽云爆炸预测.rsm | 166B |
| 168 | 甲硫醇在大气中的扩散预测.rsm | 497B |
| 169 | 甲硫醇气体泄露量计算.rsm | 73B |
| 170 | 甲硫醇池火事故-事故源.rsm | 198B |
| 171 | 甲硫醇沸腾液体扩展蒸汽爆炸.rsm | 211B |
| 172 | 甲醇典型泄漏事故模拟.rsm | 504B |
| 173 | 甲醇在大气扩散.rsm | 490B |
| 174 | 甲醇池火.rsm | 196B |
| 175 | 甲醇沸腾液体.rsm | 208B |
| 176 | 甲醇泄漏量计算气.rsm | 73B |
| 177 | 甲醇泄漏量计算液.rsm | 106B |
| 178 | 甲醇蒸汽云.rsm | 163B |
| 179 | 10敏感点.png | 183.61K |
| 180 | 10毒性.png | 159.28K |
| 181 | 10毒性敏感点.alo | 4.61K |
| 182 | 10池火.alo | 4.61K |
| 183 | 10池火.png | 177.82K |
| 184 | 10蒸汽云.alo | 4.61K |
| 185 | 10蒸汽云.png | 178.85K |
| 186 | 10闪火.alo | 4.61K |
| 187 | 10闪火.png | 169.82K |
| 188 | 5敏感点.png | 150.47K |
| 189 | 5毒性.png | 154.54K |
| 190 | 5毒性敏感点.alo | 4.61K |
| 191 | 5池火.alo | 4.61K |
| 192 | 5池火.png | 178.49K |
| 193 | 5蒸汽云.alo | 4.61K |
| 194 | 5蒸汽云.png | 160.28K |
| 195 | 5闪火.alo | 4.61K |
| 196 | 5闪火.png | 178.23K |
| 197 | B30.alo | 4.61K |
| 198 | B30.png | 174.40K |
| 199 | B40.alo | 4.61K |
| 200 | B40.png | 168.75K |
| 201 | B10.png | 164.08K |
| 202 | B20.png | 167.16K |
| 203 | B30.png | 163.90K |
| 204 | B40.png | 164.26K |
| 205 | 敏1.png | 159.64K |
| 206 | 敏10.png | 162.69K |
| 207 | 敏2.png | 171.22K |
| 208 | 敏3.png | 160.72K |
| 209 | 敏4.png | 162.82K |
| 210 | 敏5.png | 163.73K |
| 211 | 敏6.png | 161.92K |
| 212 | 敏7.png | 163.88K |
| 213 | 敏8.png | 183.65K |
| 214 | 敏9.png | 162.25K |
| 215 | 毒性1.png | 192.06K |
| 216 | 毒性10.png | 163.57K |
| 217 | 毒性2.png | 164.59K |
| 218 | 毒性3.png | 170.55K |
| 219 | 毒性4.png | 162.14K |
| 220 | 毒性5.png | 161.79K |
| 221 | 毒性6.png | 164.94K |
| 222 | 毒性7.png | 163.48K |
| 223 | 毒性8.png | 164.70K |
| 224 | 毒性9.png | 163.54K |
| 225 | 池火1.png | 161.15K |
| 226 | 池火10.png | 175.07K |
| 227 | 池火2.png | 166.94K |
| 228 | 池火3.png | 160.08K |
| 229 | 池火4.png | 168.75K |
| 230 | 池火5.png | 170.82K |
| 231 | 池火6.png | 176.81K |
| 232 | 池火7.png | 182.65K |
| 233 | 池火8.png | 175.92K |
| 234 | 池火9.png | 168.36K |
| 235 | 蒸汽云1.png | 162.42K |
| 236 | 蒸汽云10.png | 162.27K |
| 237 | 蒸汽云2.png | 160.39K |
| 238 | 蒸汽云3.png | 158.38K |
| 239 | 蒸汽云4.png | 162.15K |
| 240 | 蒸汽云5.png | 158.79K |
| 241 | 蒸汽云6.png | 162.44K |
| 242 | 蒸汽云7.png | 160.97K |
| 243 | 蒸汽云8.png | 161.86K |
| 244 | 蒸汽云9.png | 369.85K |
| 245 | 闪火1.png | 160.13K |
| 246 | 闪火10.png | 158.79K |
| 247 | 闪火2.png | 156.43K |
| 248 | 闪火3.png | 175.91K |
| 249 | 闪火4.png | 156.71K |
| 250 | 闪火5.png | 155.49K |
| 251 | 闪火6.png | 156.68K |
| 252 | 闪火7.png | 174.17K |
| 253 | 闪火8.png | 156.70K |
| 254 | 闪火9.png | 156.65K |
| 255 | 10敏感点.png | 160.15K |
| 256 | 10毒性.png | 174.10K |
| 257 | 10毒性敏感点.alo | 4.61K |
| 258 | 10池火.alo | 4.61K |
| 259 | 10池火.png | 185.48K |
| 260 | 10蒸汽云.alo | 4.61K |
| 261 | 10蒸汽云.png | 176.21K |
| 262 | 10闪火.alo | 4.61K |
| 263 | 10闪火.png | 163.05K |
| 264 | 5敏感点.png | 175.76K |
| 265 | 5毒性.png | 162.19K |
| 266 | 5毒性敏感点.alo | 4.61K |
| 267 | 5池火.alo | 4.61K |
| 268 | 5池火.png | 180.39K |
| 269 | 5蒸汽云.alo | 4.61K |
| 270 | 5蒸汽云.png | 182.13K |
| 271 | 5闪火.alo | 4.61K |
| 272 | 5闪火.png | 165.06K |
| 273 | B30.alo | 4.61K |
| 274 | B30.png | 175.68K |
| 275 | B40.alo | 4.61K |
| 276 | B40.png | 177.12K |
| 277 | B10.png | 161.76K |
| 278 | B20.png | 151.92K |
| 279 | B30.png | 155.73K |
| 280 | B40.png | 159.35K |
| 281 | 敏1.png | 158.29K |
| 282 | 敏10.png | 349.62K |
| 283 | 敏2.png | 150.89K |
| 284 | 敏3.png | 150.36K |
| 285 | 敏4.png | 152.02K |
| 286 | 敏5.png | 351.80K |
| 287 | 敏6.png | 154.01K |
| 288 | 敏7.png | 158.31K |
| 289 | 敏8.png | 155.86K |
| 290 | 敏9.png | 156.54K |
| 291 | 毒性1.png | 157.16K |
| 292 | 毒性10.png | 158.58K |
| 293 | 毒性2.png | 160.85K |
| 294 | 毒性3.png | 161.20K |
| 295 | 毒性4.png | 158.49K |
| 296 | 毒性5.png | 161.12K |
| 297 | 毒性6.png | 158.62K |
| 298 | 毒性7.png | 160.39K |
| 299 | 毒性8.png | 162.51K |
| 300 | 毒性9.png | 160.95K |
| 301 | 池火1.png | 301.62K |
| 302 | 池火10.png | 178.91K |
| 303 | 池火2.png | 179.39K |
| 304 | 池火3.png | 175.38K |
| 305 | 池火4.png | 183.36K |
| 306 | 池火5.png | 185.73K |
| 307 | 池火6.png | 176.55K |
| 308 | 池火7.png | 177.08K |
| 309 | 池火8.png | 183.86K |
| 310 | 池火9.png | 175.61K |
| 311 | 蒸汽云1.png | 162.77K |
| 312 | 蒸汽云10.png | 168.46K |
| 313 | 蒸汽云2.png | 165.17K |
| 314 | 蒸汽云3.png | 173.04K |
| 315 | 蒸汽云4.png | 168.41K |
| 316 | 蒸汽云5.png | 170.42K |
| 317 | 蒸汽云6.png | 172.50K |
| 318 | 蒸汽云7.png | 160.33K |
| 319 | 蒸汽云8.png | 169.14K |
| 320 | 蒸汽云9.png | 169.61K |
| 321 | 闪火1.png | 187.59K |
| 322 | 闪火10.png | 152.26K |
| 323 | 闪火2.png | 209.70K |
| 324 | 闪火3.png | 157.92K |
| 325 | 闪火4.png | 149.97K |
| 326 | 闪火5.png | 163.07K |
| 327 | 闪火6.png | 153.08K |
| 328 | 闪火7.png | 159.30K |
| 329 | 闪火8.png | 163.73K |
| 330 | 闪火9.png | 158.99K |
| 331 | LHF1.CATPart | 105.85M |
| 332 | LHF1.igs | 255.01M |
| 333 | 侧视图.png | 129.43K |
| 334 | 俯视图.png | 175.62K |
| 335 | 建模界面.png | 507.52K |
| 336 | 模型图.png | 235.49K |
| 337 | 1-全流程（不含换热网络、不含热泵）.bkp | 1.78M |
| 338 | 2-流股提取（不含热泵）.xls | 28.00K |
| 339 | 3-全流程（不含热泵）.hch | 537.72K |
| 340 | 4-全流程（含换热网络、塔优化参数代入）.bkp | 2.32M |
| 341 | 5-流股提取（含热泵）.xls | 28.00K |
| 342 | 6-全流程（含热泵）.hch | 18.34M |
| 343 | 7-全流程（不含换热网络、含热泵、添加设计规定）.bkp | 1.87M |
| 344 | 4-本项目污垢热阻系数经验值来源.doc | 45.00K |
| 345 | 说明.txt | 321B |
| 346 | E0204.EDR | 321.09K |
| 347 | E0204.pdf | 89.61K |
| 348 | E0204.doc | 1.50M |
| 349 | E0204.fx2 | 24.00K |
| 350 | E0311.EDR | 403.54K |
| 351 | E0311.pdf | 111.21K |
| 352 | E0311.doc | 1.61M |
| 353 | E0311.fx2 | 24.00K |
| 354 | E0102.EDR | 353.85K |
| 355 | E0102.pdf | 94.54K |
| 356 | E0103.EDR | 347.93K |
| 357 | E0103.pdf | 99.33K |
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| 364 | E0107.EDR | 352.05K |
| 365 | E0107.pdf | 115.76K |
| 366 | E0108.EDR | 423.89K |
| 367 | E0108.pdf | 83.54K |
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| 369 | E0110.pdf | 83.20K |
| 370 | E0111.EDR | 333.84K |
| 371 | E0111.pdf | 87.48K |
| 372 | E0112.EDR | 580.64K |
| 373 | E0112.pdf | 178.66K |
| 374 | E0113.EDR | 487.46K |
| 375 | E0113.pdf | 185.58K |
| 376 | E0114.EDR | 483.43K |
| 377 | E0114.pdf | 163.17K |
| 378 | E0115.EDR | 414.08K |
| 379 | E0115.pdf | 96.43K |
| 380 | E0201.EDR | 327.18K |
| 381 | E0201.pdf | 90.51K |
| 382 | E0202.EDR | 341.21K |
| 383 | E0202.pdf | 97.10K |
| 384 | E0203.EDR | 322.31K |
| 385 | E0203.pdf | 89.06K |
| 386 | E0204.EDR | 321.09K |
| 387 | E0204.pdf | 89.61K |
| 388 | E0205.EDR | 307.58K |
| 389 | E0205.pdf | 87.20K |
| 390 | E0301.EDR | 413.31K |
| 391 | E0301.pdf | 113.84K |
| 392 | E0302.EDR | 400.14K |
| 393 | E0302.pdf | 95.66K |
| 394 | E0303.EDR | 435.95K |
| 395 | E0303.pdf | 104.41K |
| 396 | E0304.EDR | 344.24K |
| 397 | E0304.pdf | 102.19K |
| 398 | E0307.EDR | 369.29K |
| 399 | E0307.pdf | 92.59K |
| 400 | E0310.EDR | 424.43K |
| 401 | E0310.pdf | 113.86K |
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| 404 | E0318.EDR | 322.51K |
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| 407 | E0319.pdf | 139.47K |
| 408 | E0109.EDR | 371.99K |
| 409 | E0109.pdf | 97.39K |
| 410 | E0305.EDR | 425.70K |
| 411 | E0305.pdf | 115.29K |
| 412 | E0306.EDR | 376.68K |
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| 417 | E0309.pdf | 88.82K |
| 418 | E0311.EDR | 403.54K |
| 419 | E0311.pdf | 111.21K |
| 420 | E0312.EDR | 361.40K |
| 421 | E0312.pdf | 97.94K |
| 422 | E0313.EDR | 394.31K |
| 423 | E0313.pdf | 98.00K |
| 424 | E0314.EDR | 345.74K |
| 425 | E0314.pdf | 86.86K |
| 426 | E0316.EDR | 368.55K |
| 427 | E0316.pdf | 97.66K |
| 428 | E0317.EDR | 405.38K |
| 429 | E0317.pdf | 115.79K |
| 430 | 6-说明.txt | 456B |
| 431 | 2-Result.xlsm | 125.36K |
| 432 | 3-全流程（经济分析）.bkp | 2.34M |
| 433 | Scenario1.izp | 1.03M |
| 434 | Scenario1.szp | 798.02K |
| 435 | 1-有双效精馏（经济分析）.bkp | 577.80K |
| 436 | 2-有双效精馏.xlsm | 115.51K |
| 437 | 3-Scenario1.izp | 1.03M |
| 438 | 4-Scenario1.szp | 798.02K |
| 439 | 1-无双效精馏（经济分析）.bkp | 445.07K |
| 440 | 2-无双效精馏.xlsm | 115.22K |
| 441 | 3-Scenario1.izp | 1.03M |
| 442 | 4-Scenario1.szp | 798.02K |
| 443 | 1-有热泵再生（经济分析）.bkp | 588.83K |
| 444 | 2-有热泵再生.xlsm | 116.62K |
| 445 | 3-Scenario1.izp | 1.03M |
| 446 | 4--Scenario1.szp | 798.02K |
| 447 | 1-无热泵精馏（经济分析）.bkp | 522.81K |
| 448 | 2-有热泵再生.xlsm | 116.62K |
| 449 | 3-Scenario1.izp | 1.03M |
| 450 | 4-Scenario1.szp | 798.02K |
| 451 | 1-萃取精馏经济分析.bkp | 707.56K |
| 452 | 2-萃取精馏.xlsm | 117.55K |
| 453 | 3-Scenario1.izp | 1.03M |
| 454 | 4-Scenario1.szp | 798.02K |
| 455 | 1-变压精馏（经济分析）.bkp | 745.41K |
| 456 | 2-变压精馏.xlsm | 118.11K |
| 457 | 3-Scenario1.izp | 1.03M |
| 458 | 4-Scenario1.szp | 798.02K |
| 459 | 1-方案一经济分析.bkp | 1.63M |
| 460 | 2-方案一.xlsm | 121.76K |
| 461 | 3-Scenario1.szp | 798.02K |
| 462 | 4-Scenario1.izp | 1.03M |
| 463 | 1-方案二经济分析.bkp | 1.06M |
| 464 | 2-方案二.xlsm | 117.87K |
| 465 | 3-Scenario1.izp | 1.03M |
| 466 | 4-Scenario1.szp | 798.02K |
| 467 | sulpakDIN材料对应表.doc | 22.50K |
| 468 | T0301低温甲醇洗塔.pak | 512B |
| 469 | T0301低温甲醇洗塔.XLS | 10.59K |
| 470 | T0302脱硫化氢重接触塔.pak | 512B |
| 471 | T0302脱硫化氢重接触塔.XLS | 10.58K |
| 472 | T0303甲硫醇精制塔.pak | 688B |
| 473 | T0303甲硫醇精制塔.XLS | 10.87K |
| 474 | T0304变压精馏低压塔.pak | 688B |
| 475 | T0304变压精馏低压塔.XLS | 10.87K |
| 476 | T0305变压精馏塔高压塔.pak | 688B |
| 477 | T0305变压精馏塔高压塔.xls | 10.88K |
| 478 | T0306双效精馏高压塔.pak | 864B |
| 479 | T0306双效精馏高压塔.xls | 11.11K |
| 480 | T0307双效精馏低压塔.pak | 688B |
| 481 | T0307双效精馏低压塔.XLS | 10.85K |
| 482 | T0103.cn2 | 30.20K |
| 483 | T0103.doc | 598.00K |
| 484 | T0104.cn2 | 30.20K |
| 485 | T0104.doc | 616.50K |
| 486 | T0103.cn2 | 30.20K |
| 487 | T0301.doc | 597.50K |
| 488 | E0203.doc | 597.50K |
| 489 | T0302.cn2 | 30.20K |
| 490 | T0303.cn2 | 30.20K |
| 491 | T0303甲硫醇精制塔.doc | 693.50K |
| 492 | T0304.cn2 | 30.20K |
| 493 | T0304.doc | 642.50K |
| 494 | T0305.cn2 | 30.20K |
| 495 | T0305.doc | 596.50K |
| 496 | T0306.cn2 | 30.20K |
| 497 | T0306.doc | 681.50K |
| 498 | T0307.cn2 | 30.20K |
| 499 | T0307.doc | 640.50K |
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| 501 | E0102.fx2 | 24.00K |
| 502 | E0103.doc | 1.61M |
| 503 | E0103.fx2 | 24.00K |
| 504 | E0104.doc | 1.61M |
| 505 | E0104.fx2 | 24.00K |
| 506 | E0105.doc | 1.61M |
| 507 | E0105.fx2 | 24.00K |
| 508 | E0106.doc | 1.61M |
| 509 | E0106.fx2 | 24.00K |
| 510 | E0107.doc | 1.62M |
| 511 | E0107.fx2 | 24.00K |
| 512 | E0108.doc | 1.62M |
| 513 | E0108.fx2 | 24.00K |
| 514 | E0110.doc | 1.62M |
| 515 | E0110.fx2 | 24.00K |
| 516 | E0111.doc | 1.62M |
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| 518 | E0112.doc | 1.62M |
| 519 | E0112.fx2 | 24.00K |
| 520 | E0113.doc | 1.62M |
| 521 | E0113.fx2 | 24.00K |
| 522 | E0114.doc | 1.62M |
| 523 | E0114.fx2 | 24.00K |
| 524 | E0115.doc | 1.60M |
| 525 | E0115.fx2 | 24.00K |
| 526 | E0201.doc | 1.62M |
| 527 | E0201.fx2 | 24.00K |
| 528 | E0202.doc | 1.50M |
| 529 | E0202.fx2 | 24.00K |
| 530 | E0203.doc | 1.50M |
| 531 | E0203.fx2 | 24.00K |
| 532 | E0204.doc | 1.50M |
| 533 | E0204.fx2 | 24.00K |
| 534 | E0205.doc | 1.53M |
| 535 | E0205.fx2 | 24.00K |
| 536 | E0301.doc | 1.62M |
| 537 | E0301.fx2 | 24.00K |
| 538 | E0302.doc | 1.62M |
| 539 | E0302.fx2 | 24.00K |
| 540 | E0303.doc | 1.62M |
| 541 | E0303.fx2 | 24.00K |
| 542 | E0304.doc | 1.62M |
| 543 | E0304.fx2 | 24.00K |
| 544 | E0307.doc | 1.62M |
| 545 | E0307.fx2 | 24.00K |
| 546 | E0310.doc | 1.62M |
| 547 | E0310.fx2 | 24.00K |
| 548 | E0315.doc | 1.62M |
| 549 | E0315.fx2 | 24.00K |
| 550 | E0318.doc | 1.62M |
| 551 | E0318.fx2 | 24.00K |
| 552 | E0319.doc | 1.61M |
| 553 | E0319.fx2 | 24.00K |
| 554 | E0109.doc | 1.50M |
| 555 | E0109.ue2 | 22.70K |
| 556 | E0305.doc | 1.62M |
| 557 | E0305.fx2 | 24.00K |
| 558 | E0306.doc | 1.50M |
| 559 | E0306.ue2 | 22.70K |
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| 573 | E0316.ue2 | 22.70K |
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| 577 | 精制反应器校核.fx2 | 24.00K |
| 578 | 反应器校核.doc | 451.00K |
| 579 | 反应器校核.ra2 | 23.24K |
| 580 | 2-储罐区火灾爆炸.jpg | 65.56K |
| 581 | 3-反应器内易燃物料.jpg | 49.38K |
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| 583 | 5-硫化氢中毒.jpg | 83.58K |
| 584 | 6-气液分离罐爆炸.jpg | 36.42K |
| 585 | 7-说明.txt | 693B |
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| 587 | 反应器内易燃物料.ffta | 11.60K |
| 588 | 气液分离罐爆炸.ffta | 9.62K |
| 589 | 甲醇中毒.ffta | 7.94K |
| 590 | 硫化氢中毒.ffta | 12.87K |
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| 592 | 6-Sense8（全车间）.txt | 3.70M |
| 593 | 7-说明.txt | 871B |
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| 595 | 车间全貌俯视图（含屋顶）.png | 25.86K |
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| 597 | 车间全貌轴测图（不封闭视角）02.png | 190.15K |
| 598 | 车间全貌轴测图（半封闭视角）.png | 138.21K |
| 599 | 车间全貌轴测图（密闭车间视角）01.png | 136.34K |
| 600 | 车间全貌轴测图（密闭车间视角）02.png | 116.15K |
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| 602 | 深度脱硫车间侧视图（含配管）01.png | 64.62K |
| 603 | 深度脱硫车间侧视图（含配管）02.png | 71.91K |
| 604 | 深度脱硫车间俯视图（含配管）.png | 65.69K |
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| 606 | 深度脱硫车间背视图（含配管）.png | 68.02K |
| 607 | 深度脱硫车间轴侧图（含配管）01.png | 136.36K |
| 608 | 深度脱硫车间轴侧图（含配管）02.png | 141.85K |
| 609 | 甲硫醇合成车间不封闭轴测图（含配管）.png | 78.52K |
| 610 | 甲硫醇合成车间主视图（含配管）.png | 10.63K |
| 611 | 甲硫醇合成车间侧视图（含配管）01.png | 14.93K |
| 612 | 甲硫醇合成车间侧视图（含配管）02.png | 13.97K |
| 613 | 甲硫醇合成车间俯视图（含配管）.png | 15.53K |
| 614 | 甲硫醇合成车间半封闭轴测图（含配管）.png | 55.16K |
| 615 | 甲硫醇合成车间封闭轴测图（含配管）.png | 19.61K |
| 616 | 甲硫醇合成车间管道全貌.png | 47.55K |
| 617 | 甲硫醇合成车间背视图（含配管）.png | 24.26K |
| 618 | 甲硫醇分离精制车间不封闭轴侧图（含配管）.png | 66.39K |
| 619 | 甲硫醇分离精制车间主图（含配管）.png | 45.19K |
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| 621 | 甲硫醇分离精制车间侧视图（含配管）02.png | 31.63K |
| 622 | 甲硫醇分离精制车间俯视图（含配管）.png | 15.39K |
| 623 | 甲硫醇分离精制车间半封闭轴侧图（含配管）.png | 76.72K |
| 624 | 甲硫醇分离精制车间封闭轴侧图（含配管）.png | 6.12K |
| 625 | 甲硫醇分离精制车间管道全貌.png | 71.93K |
| 626 | 甲硫醇分离精制车间背视图（含配管）.png | 46.73K |
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| 628 | 工艺流程图PFD图册集.pdf | 3.72M |
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| 630 | 管道仪表流程图说明.pdf | 343.81K |
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| 632 | 管道及仪表流程图PID图册集.pdf | 2.66M |
| 633 | 1-深度脱硫车间设备布置图.dwg | 1.73M |
| 634 | 2-甲硫醇合成车间设备布置图.dwg | 1.08M |
| 635 | 3-甲硫醇分离精制车间设备布置图.dwg | 1.68M |
| 636 | 车间布置说明.pdf | 310.90K |
| 637 | 车间设备布置图图册集.pdf | 2.33M |
| 638 | 厂区总平面布置图.dwg | 618.09K |
| 639 | 厂区总平面布置图.pdf | 418.53K |
| 640 | 厂区总平面布置图说明.pdf | 349.68K |
| 641 | 1-俯视图.jpg | 73.82K |
| 642 | 2-45°俯视图.jpg | 90.51K |
| 643 | 3-等轴图.jpg | 85.18K |
| 644 | E0204-反应气三级冷却器工艺条件图.dwg | 55.61K |
| 645 | R0201-甲醇和H2S一段催化反应器工艺条件图.dwg | 57.89K |
| 646 | T0104-解吸塔工艺条件图.dwg | 59.98K |
| 647 | 典型设备工艺条件图图册集.pdf | 361.97K |
| 648 | E0204-反应气三级冷却器总装配图.dwg | 200.49K |
| 649 | R0201-甲醇和H2S一段催化反应器总装配图.dwg | 156.81K |
| 650 | T0104-解吸塔总装配图.dwg | 195.61K |
| 651 | 典型设备总装配图图册集.pdf | 993.18K |
| 652 | 管道轴测图ISO.dwg | 1.93M |
| 653 | 管道轴测图图册集.pdf | 266.40K |
| 654 | gbcbig.shx | 881.68K |
| 655 | 字体文件存放位置.txt | 358B |
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