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年产22万吨煤制乙二醇项目设计==1014257=200（ID:2074939）
| # | 文件名称 | 文件大小 |
|---|---|---|
| 1 | 17458317627053.rar | 35.80M |
| 2 | PFD物料流程图.dwg | 198.79K |
| 3 | PFD物料衡算表.dwg | 483.71K |
| 4 | PID管道仪表流程图.dwg | 806.91K |
| 5 | 作品说明.txt | 629B |
| 6 | 初步设计说明书.docx | 6.52M |
| 7 | 加氢反应器R0301计算说明书.doc | 1.93M |
| 8 | 加氢反应器装配图.dwg | 274.17K |
| 9 | 加氢反应器裙座计算说明书.doc | 624.50K |
| 10 | 厂区布置图.dwg | 162.40K |
| 11 | 反应精馏塔装配图T0101.dwg | 361.50K |
| 12 | 可行性研究报告.doc | 3.46M |
| 13 | 图例.dwg | 862.81K |
| 14 | 设备一览表.docx | 35.94K |
| 15 | 车间布置图.dwg | 412.94K |
| 16 | 隔壁塔装配图T0401.dwg | 572.54K |
| 17 | T0101.doc | 740.50K |
| 18 | T0201.doc | 636.50K |
| 19 | T0202.doc | 728.50K |
| 20 | T0203.doc | 708.50K |
| 21 | T0204.doc | 660.50K |
| 22 | T0205.doc | 680.50K |
| 23 | T0301.doc | 680.50K |
| 24 | T0302.doc | 680.50K |
| 25 | T0303.doc | 672.50K |
| 26 | T0401.doc | 740.50K |
| 27 | T0402.doc | 996.50K |
| 28 | 管道温度分析.cas | 5.57M |
| 29 | 管道温度分析.cdat | 4.54M |
| 30 | 管道温度分析.cgns | 4.32M |
| 31 | 全流程模拟（不含换热网络）.bkp | 2.65M |
| 32 | 全流程模拟（含换热网络）.bkp | 2.92M |
| 33 | 隔壁塔节能对比.bkp | 1.37M |
| 34 | T0101-回流比.bkp | 411.03K |
| 35 | T0101-进料板.bkp | 411.69K |
| 36 | T0201洗涤剂用量.bkp | 301.62K |
| 37 | T0202-回流比.bkp | 361.73K |
| 38 | T0202-塔板数.bkp | 371.01K |
| 39 | T0202-进料板.bkp | 371.31K |
| 40 | T0203-回流比.bkp | 281.99K |
| 41 | T0203-塔板数.bkp | 309.78K |
| 42 | T0203进料板.bkp | 280.68K |
| 43 | T0204-回流比.bkp | 288.11K |
| 44 | T0204-塔板数.bkp | 295.55K |
| 45 | T0204-进料板.bkp | 287.09K |
| 46 | T0205-回流比.bkp | 274.16K |
| 47 | T0205-塔板数.bkp | 296.11K |
| 48 | T0205-进料板.bkp | 274.22K |
| 49 | T0301-回流比.bkp | 398.80K |
| 50 | T0301-塔板数.bkp | 466.73K |
| 51 | T0301-进料板.bkp | 406.89K |
| 52 | T0302-回流比.bkp | 644.79K |
| 53 | T0302-塔板数.bkp | 389.67K |
| 54 | T0302-进料板.bkp | 351.36K |
| 55 | T0303-回流比.bkp | 311.31K |
| 56 | T0303-塔板数.bkp | 331.10K |
| 57 | T0303-进料板.bkp | 304.15K |
| 58 | T0401-侧采板.bkp | 767.25K |
| 59 | T0401-回流比.bkp | 768.71K |
| 60 | T0401-塔板数.bkp | 910.57K |
| 61 | T0401-气相分配比.bkp | 767.69K |
| 62 | T0401-液相分配比.bkp | 768.50K |
| 63 | T0401-进料板1.bkp | 772.04K |
| 64 | T0401-进料板2.bkp | 755.17K |
| 65 | T0401-进料板3.bkp | 765.05K |
| 66 | T0501-回流比.bkp | 394.56K |
| 67 | T0501-塔板数.bkp | 385.00K |
| 68 | T0501-进料板.bkp | 382.62K |
| 69 | 乙二醇精制车间换热网络.png | 31.97K |
| 70 | 全流程模拟（含换热网络）.bkp | 2.92M |
| 71 | 前半段换热网络.hch | 1.25M |
| 72 | 后半段换热网络.hch | 1.43M |
| 73 | 对含换热网络的全流程模拟文件的补充说明.txt | 296B |
| 74 | 草酸酯生产车间换热网络.png | 33.20K |
| 75 | 神作.dynf | 2.87M |
| 76 | 神作dyn.appdf | 598.31K |
| 77 | 神作dyn.def | 215B |
| 78 | 神作dyn.for | 0B |
| 79 | 神作dyn.his | 188.79K |
| 80 | snapshot.bak | 8.83M |
| 81 | snpA0000.snp | 12.15M |
| 82 | snpA0001.snp | 12.15M |
| 83 | snpA0002.snp | 7.57M |
| 84 | tasksnap.bak | 2.87K |
| 85 | 神作.dynf.backup | 2.87M |
| 86 | 神作dyn.his | 3.34K |
| 87 | 神作dyn.rep | 0B |
| 88 | jiaqingchejian.rvm | 3.24M |
| 89 | tanghuachejian.rvm | 3.55M |
| 90 | 1.JPG | 88.08K |
| 91 | 10.JPG | 61.15K |
| 92 | 11.JPG | 55.66K |
| 93 | 12.JPG | 37.62K |
| 94 | 13.JPG | 37.76K |
| 95 | 14.JPG | 50.50K |
| 96 | 15.JPG | 104.46K |
| 97 | 2.JPG | 59.27K |
| 98 | 3.JPG | 74.85K |
| 99 | 4.JPG | 66.73K |
| 100 | 5.JPG | 54.26K |
| 101 | 6.JPG | 51.44K |
| 102 | 7.JPG | 49.85K |
| 103 | 8.JPG | 61.83K |
| 104 | 9.JPG | 50.81K |
| 105 | Thumbs.db | 276.00K |
| 106 | 泵阀.JPG | 55.29K |
| 107 | 车间一角.JPG | 85.75K |
| 108 | 配管一角.JPG | 80.31K |
| 109 | T0101.rtf | 137.88K |
| 110 | T0101.sulcol | 108.93K |
| 111 | T0201.rtf | 82.12K |
| 112 | T0201.sulcol | 56.72K |
| 113 | T0202.rtf | 165.89K |
| 114 | T0202.sulcol | 135.06K |
| 115 | T0203.rtf | 82.10K |
| 116 | T0203.sulcol | 56.71K |
| 117 | T0204.rtf | 82.13K |
| 118 | T0204.sulcol | 56.71K |
| 119 | T0205.rtf | 82.05K |
| 120 | T0205.sulcol | 56.71K |
| 121 | T0301.rtf | 165.91K |
| 122 | T0301.sulcol | 135.09K |
| 123 | T0302.rtf | 110.06K |
| 124 | T0302.sulcol | 82.86K |
| 125 | T0303.rtf | 137.68K |
| 126 | T0303.sulcol | 108.99K |
| 127 | 侧线精馏段.rtf | 138.29K |
| 128 | 侧线精馏段.sulcol | 108.95K |
| 129 | 公共提馏段.rtf | 110.30K |
| 130 | 公共提馏段.sulcol | 82.83K |
| 131 | 公共精馏段.rtf | 54.09K |
| 132 | 公共精馏段.sulcol | 30.60K |
| 133 | 预分离段.rtf | 138.23K |
| 134 | 预分离段.sulcol | 108.95K |
| 135 | T0402.rtf | 165.60K |
| 136 | T0402.sulcol | 135.06K |
| 137 | T0101.xls | 33.50K |
| 138 | T0201.xls | 30.00K |
| 139 | T0202.xls | 37.00K |
| 140 | T0203.xls | 30.00K |
| 141 | T0204.xls | 32.50K |
| 142 | T0205.xls | 30.00K |
| 143 | T0301.xls | 42.50K |
| 144 | T0302.xls | 34.50K |
| 145 | T0303.xls | 35.50K |
| 146 | T0501.xls | 42.50K |
| 147 | 侧线精馏段.xls | 35.00K |
| 148 | 提留段.xls | 35.50K |
| 149 | 精馏段.xls | 25.50K |
| 150 | 预分离段.xls | 35.00K |
| 151 | T0201.cn2 | 30.20K |
| 152 | T0201.doc | 636.50K |
| 153 | T0202.cn2 | 30.20K |
| 154 | T0202.doc | 728.50K |
| 155 | T0203.cn2 | 30.20K |
| 156 | T0203.doc | 708.50K |
| 157 | T0204.cn2 | 30.20K |
| 158 | T0204.doc | 660.50K |
| 159 | T0205.cn2 | 30.20K |
| 160 | T0205.doc | 680.50K |
| 161 | T0301.cn2 | 30.20K |
| 162 | T0301.doc | 680.50K |
| 163 | T0302.cn2 | 30.20K |
| 164 | T0302.doc | 680.50K |
| 165 | T0303.cn2 | 30.20K |
| 166 | T0303.doc | 672.50K |
| 167 | T0402.cn2 | 30.20K |
| 168 | T0402.doc | 996.50K |
| 169 | 加氢反应器.doc | 1.93M |
| 170 | 加氢反应器.fx2 | 24.00K |
| 171 | 加氢反应器裙座.cn2 | 30.20K |
| 172 | 加氢反应器裙座.doc | 624.50K |
| 173 | 反应精馏塔T0101.cn2 | 30.20K |
| 174 | 反应精馏塔T0101.doc | 740.50K |
| 175 | 隔壁塔T0401.cn2 | 30.20K |
| 176 | 隔壁塔T0401.doc | 740.50K |
| 177 | E-0101.EDR | 1.09M |
| 178 | E-0102.EDR | 464.17K |
| 179 | E-0103.EDR | 513.50K |
| 180 | E-0201.EDR | 611.57K |
| 181 | E-0202.EDR | 499.71K |
| 182 | E-0203.EDR | 582.48K |
| 183 | E-0204.EDR | 538.02K |
| 184 | E-0205.EDR | 460.18K |
| 185 | E-0206.EDR | 666.45K |
| 186 | E-0207.EDR | 448.10K |
| 187 | E-0209.EDR | 553.23K |
| 188 | E-0210.EDR | 491.80K |
| 189 | E-0211.EDR | 494.11K |
| 190 | E-0212.EDR | 465.78K |
| 191 | E-0213.EDR | 480.96K |
| 192 | E-0214.EDR | 445.91K |
| 193 | E-0215.EDR | 682.53K |
| 194 | E-0216.EDR | 442.03K |
| 195 | E-0301.EDR | 509.34K |
| 196 | E-0302.EDR | 532.14K |
| 197 | E-0303.EDR | 641.59K |
| 198 | E-0304.EDR | 487.85K |
| 199 | E-0305.EDR | 571.67K |
| 200 | E-0306.EDR | 678.24K |
| 201 | E-0307.EDR | 510.44K |
| 202 | E-0308.EDR | 1.19M |
| 203 | E-0309.EDR | 461.38K |
| 204 | E-0310.EDR | 434.75K |
| 205 | E-0311.EDR | 575.24K |
| 206 | E-0312.EDR | 1.16M |
| 207 | E-0313.EDR | 429.83K |
| 208 | E-0314.EDR | 430.88K |
| 209 | E-0401.EDR | 1.05M |
| 210 | E-0402.EDR | 505.58K |
| 211 | E-0403.EDR | 451.73K |
| 212 | E-0404.EDR | 530.43K |
| 213 | E-0405.EDR | 453.82K |
| 214 | E-0406.EDR | 632.32K |
| 215 | E-0407.EDR | 472.77K |
| 216 | E-0408.EDR | 428.54K |
| 217 | E-120.EDR | 459.29K |
| 218 | E-121.EDR | 639.75K |
| 219 | E-122.EDR | 569.42K |
| 220 | E-124.EDR | 513.42K |
| 221 | E-125.EDR | 585.67K |
| 222 | E-126.EDR | 452.70K |
| 223 | E-127.EDR | 635.19K |
| 224 | E-128.EDR | 491.72K |
| 225 | E-129.EDR | 460.07K |
| 226 | E-130.EDR | 494.85K |
| 227 | E-131.EDR | 548.46K |
| 228 | E-132.EDR | 492.34K |
| 229 | E-133.EDR | 664.26K |
| 230 | E-135.EDR | 683.22K |
| 231 | E-136.EDR | 530.33K |
| 232 | E-138.EDR | 622.05K |
| 233 | E-141.EDR | 429.61K |
| 234 | E-143.EDR | 582.59K |
| 235 | E-144.EDR | 516.37K |
| 236 | E-148.EDR | 680.26K |
| 237 | E-149.EDR | 479.98K |
| 238 | E-152.EDR | 465.70K |
| 239 | E-153.EDR | 457.94K |
| 240 | E-154.EDR | 504.03K |
| 241 | E-155.EDR | 646.40K |
| 242 | HOUE-125.EDR | 453.94K |
| 243 | HOUE-126.EDR | 431.01K |
| 244 | HOUE-127.EDR | 502.72K |
| 245 | HOUE-128.EDR | 693.67K |
| 246 | HOUE-129.EDR | 567.60K |
| 247 | HOUE-130.EDR | 532.26K |
| 248 | HOUE-131.EDR | 577.75K |
| 249 | HOUE-148.EDR | 507.32K |
| 250 | HOUE-149.EDR | 434.88K |
| 251 | HOUE-153.EDR | 507.96K |
| 252 | lsprst7.dll | 227B |
| 253 | lsprst7.tgz | 241B |
| 254 | sysprs7.dll | 1.00K |
| 255 | sysprs7.tgz | 1.00K |
| 256 | X-0301.EDR | 313.65K |
| 257 | X-0401.EDR | 314.23K |
| 258 | 1.JPG | 91.77K |
| 259 | 2.JPG | 76.16K |
| 260 | 1.JPG | 120.23K |
| 261 | 2.JPG | 98.04K |
| 262 | 3.JPG | 61.91K |
| 263 | 1.JPG | 56.66K |
| 264 | 2.JPG | 97.89K |
| 265 | 3.JPG | 115.81K |
| 266 | 1.JPG | 57.06K |
| 267 | 2.JPG | 97.42K |
| 268 | 3.JPG | 99.33K |
| 269 | 1.JPG | 55.26K |
| 270 | 2.JPG | 100.93K |
| 271 | 3.JPG | 100.59K |
| 272 | 1.JPG | 104.56K |
| 273 | 2.JPG | 112.45K |
| 274 | 3.JPG | 64.89K |
| 275 | 1.JPG | 63.79K |
| 276 | 2.JPG | 115.95K |
| 277 | 3.JPG | 107.81K |
| 278 | 1.JPG | 62.26K |
| 279 | 2.JPG | 103.12K |
| 280 | 3.JPG | 100.98K |
| 281 | 1.JPG | 64.41K |
| 282 | 2.JPG | 109.55K |
| 283 | 3.JPG | 102.05K |
| 284 | 1.JPG | 54.38K |
| 285 | 2.JPG | 99.71K |
| 286 | 3.JPG | 98.14K |
| 287 | 1.JPG | 60.38K |
| 288 | 2.JPG | 91.76K |
| 289 | 3.JPG | 112.34K |
| 290 | 1.JPG | 59.50K |
| 291 | 2.JPG | 101.32K |
| 292 | 3.JPG | 95.83K |
| 293 | 1.JPG | 91.77K |
| 294 | 2.JPG | 76.16K |
| 295 | 1.JPG | 79.91K |
| 296 | 2.JPG | 98.59K |
| 297 | 1.JPG | 63.58K |
| 298 | 2.JPG | 111.40K |
| 299 | 3.JPG | 101.88K |
| 300 | 1.JPG | 62.48K |
| 301 | 2.JPG | 91.30K |
| 302 | 3.JPG | 114.21K |
| 303 | 1.JPG | 59.36K |
| 304 | 2.JPG | 99.90K |
| 305 | 3.JPG | 97.02K |
| 306 | 1.JPG | 77.13K |
| 307 | 2.JPG | 100.52K |
| 308 | 1.JPG | 52.82K |
| 309 | 2.JPG | 96.46K |
| 310 | 3.JPG | 98.64K |
| 311 | 1.JPG | 91.61K |
| 312 | 2.JPG | 111.55K |
| 313 | 1.JPG | 92.03K |
| 314 | 2.JPG | 109.38K |
| 315 | 1.JPG | 60.96K |
| 316 | 2.JPG | 87.99K |
| 317 | 3.JPG | 100.11K |
| 318 | 1.JPG | 62.52K |
| 319 | 2.JPG | 110.11K |
| 320 | 3.JPG | 105.04K |
| 321 | 1.JPG | 95.60K |
| 322 | 2.JPG | 107.27K |
| 323 | 1.JPG | 61.97K |
| 324 | 2.JPG | 114.34K |
| 325 | 3.JPG | 102.71K |
| 326 | RISKSYSTEM文档.docx | 354.74K |
| 327 | 反应精馏塔-一氧化氮泄露-有毒气体扩散预测.rsm | 542B |
| 328 | 反应精馏塔-一氧化碳泄露-有毒气体扩散预测.rsm | 552B |
| 329 | 反应精馏塔-亚硝酸甲酯泄露-有毒气体扩散预测.rsm | 537B |
| 330 | 反应精馏塔-亚硝酸甲酯泄露-蒸汽云爆炸模型.rsm | 176B |
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发布者
大胆的石头
创作: 505
粉丝: 182
加入时间：2023-04-15
模型信息
图纸格式：dwg
文件大小：36.66M
所需金币：1000
上传时间：2025-04-28 17:16:16
是否可编辑：可修改，包括参数
版本：AutoCAD 2004
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