神华宁煤年产30万吨乙二醇项目初步设计
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| # | 文件名称 | 文件大小 |
|---|---|---|
| 1 | 0-项目摘要.doc | 301.50K |
| 2 | 1-可行性研究报告.doc | 6.76M |
| 3 | 2-初步设计说明书.doc | 21.29M |
| 4 | 3-创新性说明书.doc | 480.50K |
| 5 | 4-设备选型一览表.doc | 427.00K |
| 6 | 5-1附录一:物料平衡计算书.doc | 933.50K |
| 7 | 5-2附录二:能量平衡计算书.doc | 1.10M |
| 8 | 5-3附录三:能量回收的换热网络设计.doc | 679.50K |
| 9 | 5-4附录四:物质MSDS.doc | 892.50K |
| 10 | 6-经济分析.doc | 1.43M |
| 11 | 7-安全预评价报告.doc | 1.63M |
| 12 | 8-环境影响评价报告书.doc | 1.77M |
| 13 | PFD2004.dwg | 681.27K |
| 14 | PID2004.dwg | 572.96K |
| 15 | SIS2004.dwg | 70.62K |
| 16 | 厂区布置图2004.dwg | 115.05K |
| 17 | 板式反应器2004.dwg | 177.99K |
| 18 | 精馏设备2004.dwg | 233.10K |
| 19 | 车间设备布置图2004.bak | 479.34K |
| 20 | 车间设备布置图2004.dwg | 456.97K |
| 21 | 首页图2004.dwg | 118.56K |
| 22 | PFD2010.dwg | 693.01K |
| 23 | PID2010.dwg | 590.76K |
| 24 | SIS2010.dwg | 80.84K |
| 25 | 厂区布置图2010.dwg | 126.49K |
| 26 | 板式反应器2010.dwg | 190.17K |
| 27 | 精馏设备2010.dwg | 244.76K |
| 28 | 车间设备布置图2010.dwg | 472.79K |
| 29 | 首页图2010.dwg | 131.66K |
| 30 | 设计图册.pdf | 18.72M |
| 31 | readme.txt | 388B |
| 32 | 中毒.alo | 4.73K |
| 33 | 喷射火热辐射.alo | 4.73K |
| 34 | 毗邻管道的热辐射.alo | 4.73K |
| 35 | 蒸气云爆炸.alo | 4.73K |
| 36 | 闪火.alo | 4.73K |
| 37 | 中毒.jpg | 178.06K |
| 38 | 喷射火热辐射.jpg | 182.74K |
| 39 | 毗邻管道的热辐射.jpg | 154.91K |
| 40 | 蒸气云爆炸.jpg | 182.62K |
| 41 | 闪火.jpg | 163.00K |
| 42 | 1.全流程模拟(不含换热网络).bkp | 1.74M |
| 43 | 2.流股提取(不含热泵精馏).xlsx | 11.47K |
| 44 | 3.不含热泵精馏.hch | 239.78K |
| 45 | 4.流股提取(含热泵精馏).xlsx | 11.54K |
| 46 | 5.全流程模拟(含换热网络,塔优化参数代入).bkp | 2.05M |
| 47 | 5.含热泵精馏.hch | 7.35M |
| 48 | 6.全流程模拟(含换热网络,引用热流,添加设计规定).bkp | 1.84M |
| 49 | E0102.DOC | 343.00K |
| 50 | E0102.EDR | 378.03K |
| 51 | E0102.pdf | 507.49K |
| 52 | E0103.DOC | 351.00K |
| 53 | E0103.EDR | 465.88K |
| 54 | E0103.pdf | 536.62K |
| 55 | E0104.DOC | 344.50K |
| 56 | E0104.EDR | 418.90K |
| 57 | E0104.pdf | 513.17K |
| 58 | E0105.DOC | 339.00K |
| 59 | E0105.EDR | 377.66K |
| 60 | E0105.pdf | 491.03K |
| 61 | E0204.DOC | 340.00K |
| 62 | E0204.EDR | 468.23K |
| 63 | E0204.pdf | 500.15K |
| 64 | E0205.DOC | 347.00K |
| 65 | E0205.EDR | 453.79K |
| 66 | E0205.pdf | 522.93K |
| 67 | E0207.DOC | 368.50K |
| 68 | E0207.EDR | 546.34K |
| 69 | E0207.pdf | 612.41K |
| 70 | E0303.DOC | 350.50K |
| 71 | E0303.EDR | 470.83K |
| 72 | E0303.pdf | 537.33K |
| 73 | E0304.DOC | 357.00K |
| 74 | E0304.EDR | 499.73K |
| 75 | E0304.pdf | 566.48K |
| 76 | E0308.DOC | 351.50K |
| 77 | E0308.EDR | 476.64K |
| 78 | E0308.pdf | 541.98K |
| 79 | E0309.DOC | 347.50K |
| 80 | E0309.EDR | 446.42K |
| 81 | E0309.pdf | 523.22K |
| 82 | E0101.DOC | 342.00K |
| 83 | E0101.EDR | 346.51K |
| 84 | E0101.pdf | 503.28K |
| 85 | E0201.DOC | 340.00K |
| 86 | E0201.EDR | 411.56K |
| 87 | E0201.pdf | 493.05K |
| 88 | E0202.DOC | 343.50K |
| 89 | E0202.EDR | 378.20K |
| 90 | E0202.pdf | 508.52K |
| 91 | E0203.DOC | 339.50K |
| 92 | E0203.EDR | 355.85K |
| 93 | E0203.pdf | 491.54K |
| 94 | E0206.DOC | 350.00K |
| 95 | E0206.EDR | 456.73K |
| 96 | E0206.pdf | 531.47K |
| 97 | E0208.DOC | 342.50K |
| 98 | E0208.EDR | 362.07K |
| 99 | E0208.pdf | 502.50K |
| 100 | E0301.DOC | 340.00K |
| 101 | E0301.EDR | 381.87K |
| 102 | E0301.pdf | 493.02K |
| 103 | E0302.DOC | 341.00K |
| 104 | E0302.EDR | 406.55K |
| 105 | E0302.pdf | 498.33K |
| 106 | E0305.DOC | 339.00K |
| 107 | E0305.EDR | 375.90K |
| 108 | E0305.pdf | 492.43K |
| 109 | E0306.DOC | 343.00K |
| 110 | E0306.EDR | 409.97K |
| 111 | E0306.pdf | 505.12K |
| 112 | E0307.DOC | 342.00K |
| 113 | E0307.EDR | 353.67K |
| 114 | E0307.pdf | 503.75K |
| 115 | E0310.DOC | 349.50K |
| 116 | E0310.EDR | 528.16K |
| 117 | E0310.pdf | 521.38K |
| 118 | E0311.DOC | 356.50K |
| 119 | E0311.EDR | 479.77K |
| 120 | E0311.pdf | 558.91K |
| 121 | E0312.DOC | 342.50K |
| 122 | E0312.EDR | 424.74K |
| 123 | E0312.pdf | 503.43K |
| 124 | E0313.DOC | 348.00K |
| 125 | E0313.EDR | 438.29K |
| 126 | E0313.pdf | 523.99K |
| 127 | E0314.DOC | 347.00K |
| 128 | E0314.EDR | 393.62K |
| 129 | E0314.pdf | 519.52K |
| 130 | 1.全流程模拟(不含换热网络,添加设计规定).bkp | 1.74M |
| 131 | 2.全流程模拟(含换热网络,引用热流,添加设计规定).bkp | 1.84M |
| 132 | 3.全流程模拟(含换热网络,塔优化参数代入).bkp | 2.05M |
| 133 | R0101-压力.bkp | 413.86K |
| 134 | R0101-温度.bkp | 423.98K |
| 135 | 催化剂装填率.xlsx | 9.12K |
| 136 | T0102-反应压力.bkp | 341.71K |
| 137 | T0102-反应器体积.bkp | 348.97K |
| 138 | T0102-反应温度.bkp | 347.08K |
| 139 | T0102-氢气量.bkp | 353.41K |
| 140 | 不同压力下醇类沸点差异.xlsx | 165B |
| 141 | T0101-Design.bkp | 371.51K |
| 142 | T0101-Efficiency.bkp | 331.28K |
| 143 | T0101-RR.bkp | 327.54K |
| 144 | T0101-VFEEDSTAGE-REBDUTY.bkp | 325.01K |
| 145 | T0101-VFEEDSTAGE-分离效果.bkp | 330.18K |
| 146 | T0101-持液量.bkp | 358.71K |
| 147 | T0101-气液分别进料.bkp | 314.82K |
| 148 | T0101-氧气三股进料.bkp | 325.56K |
| 149 | 反应器塔.bkp | 377.22K |
| 150 | 塔设备优化(DSTWU简捷计算).bkp | 379.97K |
| 151 | 塔设备优化(回流比).bkp | 405.37K |
| 152 | 塔设备优化(设计规定).bkp | 397.17K |
| 153 | 塔设备优化(进料板位置).bkp | 405.80K |
| 154 | T0102-Design.bkp | 352.11K |
| 155 | T0102-DS.bkp | 237.03K |
| 156 | T0102-DSTWU.bkp | 236.18K |
| 157 | T0102-FEEDSTAGE.bkp | 320.20K |
| 158 | T0102-RR.bkp | 248.15K |
| 159 | T0201-Design.bkp | 434.75K |
| 160 | T0201-EFFIC.bkp | 408.98K |
| 161 | T0201-ME用量.bkp | 418.75K |
| 162 | T0201-NSTAGE.bkp | 429.12K |
| 163 | T0201-PRE.bkp | 409.80K |
| 164 | T0202-Design.bkp | 387.33K |
| 165 | T0202-DS.bkp | 237.39K |
| 166 | T0202-DSTWU.bkp | 289.25K |
| 167 | T0202-FEEDSTAGE.bkp | 339.95K |
| 168 | T0202-RR.bkp | 333.33K |
| 169 | T0202-气相出口.bkp | 328.84K |
| 170 | T0203-Design.bkp | 465.47K |
| 171 | T0203-DS.bkp | 380.83K |
| 172 | T0203-DSTWU.bkp | 289.60K |
| 173 | T0203-FEEDSTAGE.bkp | 380.90K |
| 174 | T0203-RR.bkp | 392.44K |
| 175 | T0301-Design.bkp | 356.73K |
| 176 | T0301-DS.bkp | 333.88K |
| 177 | T0301-DSTWU.bkp | 304.54K |
| 178 | T0301-FEEDSTAGE.bkp | 250.26K |
| 179 | T0301-RR.bkp | 350.63K |
| 180 | T0302-Design.bkp | 628.72K |
| 181 | T0302-DS.bkp | 460.27K |
| 182 | T0302-DSTWU.bkp | 320.07K |
| 183 | T0302-FEEDSTAGE.bkp | 467.13K |
| 184 | T0302-RR.bkp | 469.06K |
| 185 | T0303-Design.bkp | 445.94K |
| 186 | T0303-DSTWU-BPRE.bkp | 281.82K |
| 187 | T0303-DSTWU.bkp | 308.55K |
| 188 | T0303-FEEDSTAGE.bkp | 247.46K |
| 189 | T0303-RR.bkp | 348.88K |
| 190 | T0304-Design.bkp | 601.96K |
| 191 | T0304-DS.bkp | 270.81K |
| 192 | T0304-DSTWU.bkp | 333.79K |
| 193 | T0304-FEEDSTAGE.bkp | 507.14K |
| 194 | T0304-RR.bkp | 501.21K |
| 195 | T0305-Design.bkp | 548.60K |
| 196 | T0305-DSTWU.bkp | 283.28K |
| 197 | T0305-FEEDSTAGE.bkp | 415.23K |
| 198 | T0305-RE-RR.bkp | 414.75K |
| 199 | T0305-RR.bkp | 368.77K |
| 200 | V0201-PRE.bkp | 343.79K |
| 201 | V0201-TEM.bkp | 338.80K |
| 202 | V0301-PRE.bkp | 303.84K |
| 203 | V0301-TEM.bkp | 316.23K |
| 204 | EconomicAnalysis.izp | 1.97M |
| 205 | EconomicAnalysis.szp | 1.41M |
| 206 | Results.xls | 286.50K |
| 207 | Risksystem甲醇储罐泄漏模拟.pdf | 881.34K |
| 208 | 两相流泄漏.rsm | 95B |
| 209 | 典型泄漏事故.rsm | 526B |
| 210 | 气体泄漏.rsm | 73B |
| 211 | 池火事故.rsm | 204B |
| 212 | 池火事故伤害范围.rsp | 444.00K |
| 213 | 泄漏扩散.rsm | 491B |
| 214 | 液体泄漏.rsm | 108B |
| 215 | 火球BLEVE.rsm | 211B |
| 216 | 火球BLEVE伤害范围.rsp | 444.00K |
| 217 | 热量蒸发.rsm | 56B |
| 218 | 蒸汽云爆炸.rsm | 174B |
| 219 | 蒸汽云爆炸伤害范围.rsp | 444.00K |
| 220 | 质量蒸发.rsm | 56B |
| 221 | 闪蒸.rsm | 54B |
| 222 | designnew.ses | 6.58M |
| 223 | SP3D布置图-1.pdf | 65.96K |
| 224 | SP3D布置图-10.pdf | 29.51K |
| 225 | SP3D布置图-11.pdf | 34.12K |
| 226 | SP3D布置图-12.pdf | 18.72K |
| 227 | SP3D布置图-2.pdf | 65.11K |
| 228 | SP3D布置图-3.pdf | 57.65K |
| 229 | SP3D布置图-4.pdf | 57.67K |
| 230 | SP3D布置图-5.pdf | 24.33K |
| 231 | SP3D布置图-6.pdf | 32.20K |
| 232 | SP3D布置图-7.pdf | 37.47K |
| 233 | SP3D布置图-8.pdf | 29.47K |
| 234 | SP3D布置图-9.pdf | 51.06K |
| 235 | 管道轴测图-1.dwg | 46.41K |
| 236 | 管道轴测图-10.dwg | 46.57K |
| 237 | 管道轴测图-101.tif | 58.01K |
| 238 | 管道轴测图-11.dwg | 44.96K |
| 239 | 管道轴测图-11.tif | 58.59K |
| 240 | 管道轴测图-111.tif | 58.13K |
| 241 | 管道轴测图-12.dwg | 44.76K |
| 242 | 管道轴测图-121.tif | 58.04K |
| 243 | 管道轴测图-13.dwg | 45.86K |
| 244 | 管道轴测图-131.tif | 57.94K |
| 245 | 管道轴测图-14.dwg | 50.11K |
| 246 | 管道轴测图-141.tif | 57.94K |
| 247 | 管道轴测图-15.dwg | 46.04K |
| 248 | 管道轴测图-151.tif | 57.88K |
| 249 | 管道轴测图-2.dwg | 47.28K |
| 250 | 管道轴测图-21.tif | 58.04K |
| 251 | 管道轴测图-3.dwg | 41.33K |
| 252 | 管道轴测图-31.tif | 58.38K |
| 253 | 管道轴测图-4.dwg | 45.82K |
| 254 | 管道轴测图-41.tif | 58.13K |
| 255 | 管道轴测图-5.dwg | 40.21K |
| 256 | 管道轴测图-51.tif | 58.09K |
| 257 | 管道轴测图-6.dwg | 51.64K |
| 258 | 管道轴测图-61.tif | 58.00K |
| 259 | 管道轴测图-7.dwg | 40.28K |
| 260 | 管道轴测图-71.tif | 58.03K |
| 261 | 管道轴测图-8.dwg | 57.92K |
| 262 | 管道轴测图-81.tif | 58.10K |
| 263 | 管道轴测图-9.dwg | 43.24K |
| 264 | 管道轴测图-91.tif | 58.15K |
| 265 | 管道轴测图-1.pdf | 65.39K |
| 266 | 管道轴测图-10.pdf | 60.52K |
| 267 | 管道轴测图-11.pdf | 65.76K |
| 268 | 管道轴测图-12.pdf | 64.89K |
| 269 | 管道轴测图-13.pdf | 61.22K |
| 270 | 管道轴测图-15.pdf | 65.74K |
| 271 | 管道轴测图-2.pdf | 66.17K |
| 272 | 管道轴测图-3.pdf | 58.55K |
| 273 | 管道轴测图-4.pdf | 65.69K |
| 274 | 管道轴测图-5.pdf | 58.42K |
| 275 | 管道轴测图-6.pdf | 66.44K |
| 276 | 管道轴测图-7.pdf | 58.69K |
| 277 | 管道轴测图-8.pdf | 61.78K |
| 278 | 管道轴测图-9.pdf | 59.85K |
| 279 | R0201.docx | 157.53K |
| 280 | R0301.docx | 157.65K |
| 281 | T0101.docx | 267.49K |
| 282 | T0102.docx | 267.27K |
| 283 | T0201.docx | 172.93K |
| 284 | T0202.docx | 305.93K |
| 285 | T0203.docx | 267.17K |
| 286 | T0301.docx | 172.10K |
| 287 | T0302.docx | 284.19K |
| 288 | T0303.docx | 189.31K |
| 289 | T0304.docx | 188.20K |
| 290 | T0305.docx | 283.19K |
| 291 | E0101.docx | 478.42K |
| 292 | E0102.docx | 477.90K |
| 293 | E0103.docx | 478.56K |
| 294 | E0104.docx | 478.17K |
| 295 | E0105.docx | 477.50K |
| 296 | E0201.docx | 479.14K |
| 297 | E0202.docx | 478.45K |
| 298 | E0203.docx | 478.36K |
| 299 | E0204.docx | 477.90K |
| 300 | E0205.docx | 478.58K |
| 301 | E0206.docx | 477.79K |
| 302 | E0207.docx | 477.88K |
| 303 | E0208.docx | 478.09K |
| 304 | E0301.docx | 477.99K |
| 305 | E0302.docx | 477.81K |
| 306 | E0303.docx | 478.29K |
| 307 | E0304.docx | 477.92K |
| 308 | E0305.docx | 477.81K |
| 309 | E0306.docx | 432.72K |
| 310 | E0307.docx | 209.87K |
| 311 | E0308.docx | 208.58K |
| 312 | E0309.docx | 208.33K |
| 313 | E0310.docx | 208.52K |
| 314 | E0311.docx | 207.78K |
| 315 | E0312.docx | 225.55K |
| 316 | E0313.docx | 209.41K |
| 317 | E0314.docx | 208.98K |
| 318 | R0201.ra2 | 23.24K |
| 319 | R0301.ra2 | 23.24K |
| 320 | T0101.cn2 | 30.20K |
| 321 | T0102.cn2 | 30.20K |
| 322 | T0201.cn2 | 30.20K |
| 323 | T0202.cn2 | 30.20K |
| 324 | T0203.cn2 | 30.20K |
| 325 | T0301.cn2 | 30.20K |
| 326 | T0302.cn2 | 30.20K |
| 327 | T0303.cn2 | 30.20K |
| 328 | T0304.cn2 | 30.20K |
| 329 | T0305.cn2 | 30.20K |
| 330 | E0101.fx2 | 24.00K |
| 331 | E0102.fx2 | 24.00K |
| 332 | E0103.fx2 | 24.00K |
| 333 | E0104.fx2 | 24.00K |
| 334 | E0105.fx2 | 24.00K |
| 335 | E0201.fx2 | 24.00K |
| 336 | E0202.fx2 | 24.00K |
| 337 | E0203.fx2 | 24.00K |
| 338 | E0204.fx2 | 24.00K |
| 339 | E0205.fx2 | 24.00K |
| 340 | E0206.fx2 | 24.00K |
| 341 | E0207.fx2 | 24.00K |
| 342 | E0208.fx2 | 24.00K |
| 343 | E0301.fx2 | 24.00K |
| 344 | E0302.fx2 | 24.00K |
| 345 | E0303.fx2 | 24.00K |
| 346 | E0304.fx2 | 24.00K |
| 347 | E0305.fx2 | 24.00K |
| 348 | E0306.fx2 | 24.00K |
| 349 | E0307.fx2 | 24.00K |
| 350 | E0308.fx2 | 24.00K |
| 351 | E0309.fx2 | 24.00K |
| 352 | E0310.fx2 | 24.00K |
| 353 | E0311.fx2 | 24.00K |
| 354 | E0312.fx2 | 24.00K |
| 355 | E0313.fx2 | 24.00K |
| 356 | E0314.fx2 | 24.00K |
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