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30万吨年乙二醇联产40万吨年碳酸二甲酯项目初步设计（ID:2690115）
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| # | 文件名称 | 文件大小 |
|---|---|---|
| 1 | 17592287522020.zip | 75.54M |
| 2 | 创新性说明-2003.doc | 586.00K |
| 3 | 初步设计说明书-2003.doc | 7.19M |
| 4 | 可行性研究报告-2003.doc | 2.38M |
| 5 | 安全预评价报告-2003.doc | 1.54M |
| 6 | 清洁生产报告-2003.doc | 416.00K |
| 7 | 环境影响评价报告-2003.doc | 762.59K |
| 8 | 致评委老师.pdf | 163.86K |
| 9 | 设备设计文档-2003.doc | 2.39M |
| 10 | 附录-2003.doc | 1.08M |
| 11 | 项目摘要-2003.doc | 1.38M |
| 12 | 设计图册.pdf | 17.18M |
| 13 | EO反应器SIS系统简图.dwg | 59.47K |
| 14 | PFD.dwg | 599.08K |
| 15 | PID.dwg | 498.57K |
| 16 | 三维配管图.dwg | 3.83M |
| 17 | 乙二醇生产精制车间.dwg | 7.90M |
| 18 | 乙烯环氧化反应器R0101工艺条件图.dwg | 119.21K |
| 19 | 乙烯环氧化反应器R0101装配图.dwg | 204.25K |
| 20 | 厂区平面布置图.dwg | 228.57K |
| 21 | 反应精馏塔T0201工艺条件图.dwg | 163.37K |
| 22 | 反应精馏塔T0201装配图.dwg | 208.63K |
| 23 | 换热器E0101工艺条件图.dwg | 133.51K |
| 24 | 换热器E0101装配图.dwg | 197.58K |
| 25 | 管道轴测图.dwg | 960.43K |
| 26 | 车间布置图.dwg | 241.42K |
| 27 | RESULTS.xls | 873.50K |
| 28 | 经济衡算结果.xlsx | 75.44K |
| 29 | 软件说明.txt | 358B |
| 30 | cashflow.ics | 284.89K |
| 31 | cashflow.ict | 990.98K |
| 32 | CURRENCY.DAT | 8.20K |
| 33 | DESIGN.d01 | 52.24K |
| 34 | DESIGN.d02 | 11.65K |
| 35 | DESIGN.d03 | 72.81K |
| 36 | DESIGN.d04 | 20.74K |
| 37 | DESIGN.d05 | 36B |
| 38 | equip.ict | 38.15K |
| 39 | execsum.ics | 9.03K |
| 40 | execsum.ict | 7.36K |
| 41 | Flag.txt | 0B |
| 42 | INV.d01 | 1.24K |
| 43 | INV.d02 | 10.55K |
| 44 | INV.d03 | 5.02K |
| 45 | INV.d04 | 4.98K |
| 46 | INV.d05 | 36B |
| 47 | ipeproc.d01 | 438B |
| 48 | ipeproc.d02 | 166B |
| 49 | ipeproc.d03 | 5.02K |
| 50 | ipeproc.d04 | 4.98K |
| 51 | ipeproc.d05 | 36B |
| 52 | ipeproj.d01 | 714B |
| 53 | ipeproj.d02 | 744B |
| 54 | ipeproj.d03 | 5.02K |
| 55 | ipeproj.d04 | 4.98K |
| 56 | ipeproj.d05 | 36B |
| 57 | IPEWB.XLS | 146.00K |
| 58 | IPEWB_TRA.XLS | 22.50K |
| 59 | IPSUNTUN.d01 | 852B |
| 60 | IPSUNTUN.d02 | 337B |
| 61 | IPSUNTUN.d03 | 5.02K |
| 62 | IPSUNTUN.d04 | 4.98K |
| 63 | IPSUNTUN.d05 | 36B |
| 64 | map.d01 | 1.10K |
| 65 | map.d02 | 8.14K |
| 66 | map.d03 | 5.02K |
| 67 | map.d04 | 20.74K |
| 68 | map.d05 | 36B |
| 69 | OP.d01 | 714B |
| 70 | OP.d02 | 2.37K |
| 71 | OP.d03 | 5.02K |
| 72 | OP.d04 | 4.98K |
| 73 | OP.d05 | 36B |
| 74 | PFDDIG.d01 | 438B |
| 75 | PFDDIG.d02 | 166B |
| 76 | PFDDIG.d03 | 5.02K |
| 77 | PFDDIG.d04 | 4.98K |
| 78 | PFDDIG.d05 | 36B |
| 79 | proc.d01 | 2.72K |
| 80 | proc.d02 | 1.58K |
| 81 | proc.d03 | 5.02K |
| 82 | proc.d04 | 4.98K |
| 83 | proc.d05 | 36B |
| 84 | procAZ.d01 | 990B |
| 85 | procAZ.d02 | 268B |
| 86 | procAZ.d03 | 5.02K |
| 87 | procAZ.d04 | 4.98K |
| 88 | procAZ.d05 | 36B |
| 89 | PROCCN.d01 | 438B |
| 90 | PROCCN.d02 | 166B |
| 91 | PROCCN.d03 | 5.02K |
| 92 | PROCCN.d04 | 4.98K |
| 93 | PROCCN.d05 | 36B |
| 94 | ProcessTemplateProject.KBW | 43B |
| 95 | PROD.d01 | 1.51K |
| 96 | PROD.d02 | 6.94K |
| 97 | PROD.d03 | 5.02K |
| 98 | PROD.d04 | 4.98K |
| 99 | PROD.d05 | 36B |
| 100 | ProdRes.txt | 127B |
| 101 | proj.d01 | 1.78K |
| 102 | proj.d02 | 2.22K |
| 103 | proj.d03 | 5.02K |
| 104 | proj.d04 | 5.02K |
| 105 | proj.d05 | 36B |
| 106 | projinfo.d01 | 714B |
| 107 | projinfo.d02 | 1.92K |
| 108 | projinfo.d03 | 5.02K |
| 109 | projinfo.d04 | 4.98K |
| 110 | projinfo.d05 | 36B |
| 111 | PROJL.d01 | 438B |
| 112 | PROJL.d02 | 166B |
| 113 | PROJL.d03 | 5.02K |
| 114 | PROJL.d04 | 4.98K |
| 115 | PROJL.d05 | 36B |
| 116 | projmap.d01 | 852B |
| 117 | projmap.d02 | 166B |
| 118 | projmap.d03 | 5.02K |
| 119 | projmap.d04 | 4.98K |
| 120 | projmap.d05 | 36B |
| 121 | PROJNAZ.d01 | 438B |
| 122 | PROJNAZ.d02 | 166B |
| 123 | PROJNAZ.d03 | 5.02K |
| 124 | PROJNAZ.d04 | 4.98K |
| 125 | PROJNAZ.d05 | 36B |
| 126 | PROJNBD.d01 | 438B |
| 127 | PROJNBD.d02 | 166B |
| 128 | PROJNBD.d03 | 5.02K |
| 129 | PROJNBD.d04 | 4.98K |
| 130 | PROJNBD.d05 | 36B |
| 131 | PROJNBG.d01 | 438B |
| 132 | PROJNBG.d02 | 166B |
| 133 | PROJNBG.d03 | 5.02K |
| 134 | PROJNBG.d04 | 4.98K |
| 135 | PROJNBG.d05 | 36B |
| 136 | PROJNBI.d01 | 438B |
| 137 | PROJNBI.d02 | 166B |
| 138 | PROJNBI.d03 | 5.02K |
| 139 | PROJNBI.d04 | 4.98K |
| 140 | PROJNBI.d05 | 36B |
| 141 | PROJNBM.d01 | 438B |
| 142 | PROJNBM.d02 | 166B |
| 143 | PROJNBM.d03 | 5.02K |
| 144 | PROJNBM.d04 | 4.98K |
| 145 | PROJNBM.d05 | 36B |
| 146 | PROJNBP.d01 | 438B |
| 147 | PROJNBP.d02 | 166B |
| 148 | PROJNBP.d03 | 5.02K |
| 149 | PROJNBP.d04 | 4.98K |
| 150 | PROJNBP.d05 | 36B |
| 151 | PROJNCN.d01 | 438B |
| 152 | PROJNCN.d02 | 166B |
| 153 | PROJNCN.d03 | 5.02K |
| 154 | PROJNCN.d04 | 4.98K |
| 155 | PROJNCN.d05 | 36B |
| 156 | PROJP.d01 | 438B |
| 157 | PROJP.d02 | 166B |
| 158 | PROJP.d03 | 5.02K |
| 159 | PROJP.d04 | 4.98K |
| 160 | PROJP.d05 | 36B |
| 161 | PROJSUM.ICS | 28.64K |
| 162 | projsum.ict | 232.10K |
| 163 | RAW.d01 | 1.51K |
| 164 | RAW.d02 | 6.87K |
| 165 | RAW.d03 | 5.02K |
| 166 | RAW.d04 | 4.98K |
| 167 | RAW.d05 | 36B |
| 168 | RawRes.txt | 132B |
| 169 | REP_GEN.d01 | 438B |
| 170 | REP_GEN.d02 | 166B |
| 171 | REP_GEN.d03 | 5.02K |
| 172 | REP_GEN.d04 | 4.98K |
| 173 | REP_GEN.d05 | 36B |
| 174 | RESULTS.xls | 873.50K |
| 175 | Scenario1.izp | 1.02M |
| 176 | Scenario1.szp | 798.19K |
| 177 | SCHD.d01 | 162B |
| 178 | SCHD.d02 | 77B |
| 179 | SCHD.d03 | 5.02K |
| 180 | SCHD.d04 | 4.98K |
| 181 | SCHD.d05 | 36B |
| 182 | SPECS.xls | 3.25M |
| 183 | STD.d01 | 9.59K |
| 184 | STD.d02 | 19.96K |
| 185 | STD.d03 | 20.97K |
| 186 | STD.d04 | 20.74K |
| 187 | STD.d05 | 36B |
| 188 | US_IP.KBW | 45B |
| 189 | UTILITY.d01 | 3.26K |
| 190 | UTILITY.d02 | 16.90K |
| 191 | UTILITY.d03 | 5.02K |
| 192 | UTILITY.d04 | 28.62K |
| 193 | UTILITY.d05 | 36B |
| 194 | E0101ADesign.EDR | 475.51K |
| 195 | E0101ARating.EDR | 460.91K |
| 196 | E0101BDesign.EDR | 475.51K |
| 197 | E0101BRating.EDR | 460.91K |
| 198 | E0101CDesign.EDR | 475.51K |
| 199 | E0101CRating.EDR | 460.91K |
| 200 | E0102ADesign.EDR | 338.72K |
| 201 | E0102ARating.EDR | 408.56K |
| 202 | E0102BDesign.EDR | 338.72K |
| 203 | E0102BRating.EDR | 408.56K |
| 204 | E0102CDesign.EDR | 338.72K |
| 205 | E0102CRating.EDR | 408.56K |
| 206 | E0103ADesign.EDR | 419.83K |
| 207 | E0103ARating.EDR | 462.84K |
| 208 | E0103BDesign.EDR | 419.83K |
| 209 | E0103BRating.EDR | 462.84K |
| 210 | E0103CDesign.EDR | 419.83K |
| 211 | E0103CRating.EDR | 462.84K |
| 212 | E0104Design.EDR | 383.77K |
| 213 | E0104Rating.EDR | 435.01K |
| 214 | E0105Design.EDR | 616.17K |
| 215 | E0105Rating.EDR | 409.16K |
| 216 | E0106Desig.EDR | 354.64K |
| 217 | E0106Rating.EDR | 381.30K |
| 218 | E0107Design.EDR | 407.40K |
| 219 | E0107Rating.EDR | 369.69K |
| 220 | E0108ADesign.EDR | 408.95K |
| 221 | E0108ARating.EDR | 546.45K |
| 222 | E0108BDesign.EDR | 408.95K |
| 223 | E0108BRating.EDR | 546.45K |
| 224 | E0108CDesign.EDR | 408.95K |
| 225 | E0108CRating.EDR | 546.45K |
| 226 | E0109Design.EDR | 372.27K |
| 227 | E0109Rating.EDR | 382.37K |
| 228 | E0110Design.EDR | 337.98K |
| 229 | E0110Rating.EDR | 350.91K |
| 230 | E0301Design.EDR | 440.46K |
| 231 | E0301Rating.EDR | 451.13K |
| 232 | E0302Design.EDR | 379.06K |
| 233 | E0302Rating.EDR | 372.06K |
| 234 | E0303ADesign.EDR | 444.07K |
| 235 | E0303ARating.EDR | 434.84K |
| 236 | E0303BDesign.EDR | 444.07K |
| 237 | E0303BRating.EDR | 434.84K |
| 238 | E0303CDesign.EDR | 444.07K |
| 239 | E0303CRating.EDR | 434.84K |
| 240 | E0304Design.EDR | 412.30K |
| 241 | E0304Rating.EDR | 373.30K |
| 242 | E0305Design.EDR | 329.46K |
| 243 | E0305Rating.EDR | 341.93K |
| 244 | E0306Design.EDR | 418.43K |
| 245 | E0306Rating.EDR | 406.47K |
| 246 | E0307Design.EDR | 460.46K |
| 247 | E0307Rating.EDR | 408.17K |
| 248 | E0308Design.EDR | 420.56K |
| 249 | E0308Rating.EDR | 406.47K |
| 250 | E0309Design.EDR | 459.66K |
| 251 | E0309Rating.EDR | 408.17K |
| 252 | E0310Design.EDR | 365.90K |
| 253 | E0310Rating.EDR | 349.26K |
| 254 | E0311Design.EDR | 381.16K |
| 255 | E0311Rating.EDR | 427.79K |
| 256 | E0312Design.EDR | 525.81K |
| 257 | E0312Rating.EDR | 425.99K |
| 258 | E0313Design.EDR | 381.17K |
| 259 | E0313Rating.EDR | 427.80K |
| 260 | E0314Design.EDR | 525.82K |
| 261 | E0314Rating.EDR | 426.02K |
| 262 | E0315Design.EDR | 405.19K |
| 263 | E0315Rating.EDR | 362.69K |
| 264 | E0201Design.EDR | 349.19K |
| 265 | E0201Rating.EDR | 348.02K |
| 266 | E0202Design.EDR | 399.88K |
| 267 | E0202Rating.EDR | 412.93K |
| 268 | E0203Design.EDR | 390.60K |
| 269 | E0203Rating.EDR | 361.73K |
| 270 | E0204Design.EDR | 349.34K |
| 271 | E0204Rating.EDR | 359.21K |
| 272 | E0205Design.EDR | 352.57K |
| 273 | E0205Rating.EDR | 392.44K |
| 274 | E0206Design.EDR | 407.82K |
| 275 | E0206Rating.EDR | 449.10K |
| 276 | E0207Design.EDR | 458.13K |
| 277 | E0207Rating.EDR | 406.78K |
| 278 | E0208Design.EDR | 405.70K |
| 279 | E0208Rating.EDR | 446.97K |
| 280 | E0209Design.EDR | 458.94K |
| 281 | E0209Rating.EDR | 406.78K |
| 282 | E0210Design.EDR | 395.80K |
| 283 | E0210Rating.EDR | 395.47K |
| 284 | E0211Design.EDR | 412.70K |
| 285 | E0211Rating.EDR | 419.30K |
| 286 | E0212Design.EDR | 488.16K |
| 287 | E0212Rating.EDR | 430.10K |
| 288 | 总换热网络.hch | 1.24M |
| 289 | CondPC曲线.png | 10.76K |
| 290 | DrumLC曲线.png | 10.89K |
| 291 | MassFrac曲线.png | 8.51K |
| 292 | SumpLC曲线.png | 10.38K |
| 293 | T202_EG精制塔.bkp | 68.12K |
| 294 | t202_eg精制塔.def | 227B |
| 295 | T202_EG精制塔.dynf | 280.62K |
| 296 | t202_eg精制塔.for | 0B |
| 297 | T202_EG精制塔dyn.appdf | 198.76K |
| 298 | snapshot.bak | 2.01M |
| 299 | snpA0000.snp | 850.29K |
| 300 | t202_eg精制塔dyn.his | 2.70K |
| 301 | t202_eg精制塔dyn.rep | 0B |
| 302 | tasksnap.bak | 3.61K |
| 303 | T0101吸收剂用量.bkp | 115.04K |
| 304 | T0102吸收剂用量）.bkp | 124.18K |
| 305 | T0203回流比.bkp | 56.04K |
| 306 | T0203塔板数.bkp | 69.07K |
| 307 | T0203进料板位置.bkp | 68.70K |
| 308 | T0303再沸器负荷.bkp | 113.88K |
| 309 | T0303回流比.bkp | 112.03K |
| 310 | T0303塔板数.bkp | 144.42K |
| 311 | T0303进料板位置.bkp | 114.18K |
| 312 | DMC精制工段.bkp | 238.06K |
| 313 | 乙二醇生产精制工段.bkp | 263.85K |
| 314 | 全流程模拟.bkp | 943.77K |
| 315 | 环氧乙烷工段.bkp | 500.84K |
| 316 | EO反应器SIS系统简图.dwg | 59.47K |
| 317 | PFD.dwg | 599.08K |
| 318 | PID.dwg | 498.57K |
| 319 | 三维配管图.dwg | 3.83M |
| 320 | 乙二醇生产精制车间.dwg | 7.90M |
| 321 | 乙烯环氧化反应器R0101工艺条件图.dwg | 119.21K |
| 322 | 乙烯环氧化反应器R0101装配图.dwg | 204.25K |
| 323 | 厂区平面布置图.dwg | 228.57K |
| 324 | 反应精馏塔T0201工艺条件图.dwg | 163.37K |
| 325 | 反应精馏塔T0201装配图.dwg | 208.63K |
| 326 | 换热器E0101工艺条件图.dwg | 133.51K |
| 327 | 换热器E0101装配图.dwg | 197.58K |
| 328 | 管道轴测图.dwg | 960.43K |
| 329 | 车间布置图.dwg | 241.42K |
| 330 | EO反应器SIS系统简图.dwg | 76.82K |
| 331 | PFD.dwg | 686.42K |
| 332 | PID.dwg | 543.26K |
| 333 | 三维配管图.dwg | 3.84M |
| 334 | 乙二醇生产精制车间.dwg | 7.92M |
| 335 | 乙烯环氧化反应器R0101工艺条件图.dwg | 163.61K |
| 336 | 乙烯环氧化反应器R0101装配图.dwg | 255.98K |
| 337 | 厂区平面布置图.dwg | 319.48K |
| 338 | 反应精馏塔T0201工艺条件图.dwg | 195.54K |
| 339 | 反应精馏塔T0201装配图.dwg | 218.59K |
| 340 | 换热器E0101工艺条件图.dwg | 191.73K |
| 341 | 换热器E0101装配图.dwg | 213.58K |
| 342 | 管道轴测图.dwg | 992.10K |
| 343 | 车间布置图.dwg | 254.08K |
| 344 | T0101-EO吸收塔.doc | 312.50K |
| 345 | T0102-CO2吸收塔.doc | 303.00K |
| 346 | T0103-EO解吸塔.doc | 302.00K |
| 347 | T0104-CO2解吸塔.doc | 303.50K |
| 348 | T0105-EO吸收塔.doc | 551.00K |
| 349 | T0106-EO尾气塔.doc | 139.50K |
| 350 | T0201-EC精制塔.xls | 182.50K |
| 351 | T0202-反应精馏塔.doc | 330.50K |
| 352 | T0203-EG精制塔.doc | 272.50K |
| 353 | T0301-DMC一级精制塔.doc | 292.50K |
| 354 | T0302-DMC二级精制塔.doc | 291.50K |
| 355 | T0303-DMC三级精制塔.doc | 291.50K |
| 356 | T0101-EO吸收塔.plc | 200.00K |
| 357 | T0102-CO2吸收塔.plc | 200.00K |
| 358 | T0103-EO解吸塔.plc | 200.00K |
| 359 | T0104-CO2解吸塔.plc | 200.00K |
| 360 | T0105-EO精制塔提馏段.plc | 200.00K |
| 361 | T0105-EO精制塔精馏段.plc | 200.00K |
| 362 | T0106-EO尾气塔.CPS | 279B |
| 363 | T0201-EC精制塔.plc | 200.00K |
| 364 | T0202-反应段.CPS | 295B |
| 365 | T0202-精馏段.plc | 200.00K |
| 366 | T0203-cup-Tower源文件.plc | 200.00K |
| 367 | T0301-DMC一级精制塔.plc | 200.00K |
| 368 | T0302-DMC二级精制塔.plc | 200.00K |
| 369 | T303-DMC三级精制塔.plc | 200.00K |
| 370 | 典型泄漏事故模拟.rsm | 502B |
| 371 | 泄漏源参数.png | 24.40K |
| 372 | 预测方案.png | 20.91K |
| 373 | 预测结果概述.png | 18.02K |
| 374 | 事故源.png | 13.57K |
| 375 | 池火事故模型预测.rsm | 197B |
| 376 | 结果输出.png | 14.70K |
| 377 | 事故源.png | 11.62K |
| 378 | 结果图.png | 23.87K |
| 379 | 结果输出.png | 11.00K |
| 380 | 蒸汽云爆炸模型预测.rsm | 173B |
| 381 | 事故源.png | 13.95K |
| 382 | 火球BLEVE模型预测.rsm | 211B |
| 383 | 结果图.png | 24.73K |
| 384 | 结果输出.png | 13.19K |
| 385 | 下风向结果.png | 24.57K |
| 386 | 典型泄漏事故模拟.rsm | 497B |
| 387 | 模拟结果图.png | 12.31K |
| 388 | 泄漏源参数.png | 24.62K |
| 389 | 泄漏量结果.png | 28.46K |
| 390 | 网格点结果.png | 25.83K |
| 391 | 计算模型.png | 17.18K |
| 392 | 预测方案.png | 21.16K |
| 393 | 事故源.png | 13.88K |
| 394 | 伤害范围图.png | 24.89K |
| 395 | 火球BLEVE模型预测.rsm | 207B |
| 396 | 结果输出.png | 13.54K |
| 397 | 预测方案.png | 12.82K |
| 398 | 事故源.png | 11.79K |
| 399 | 结果图.png | 21.38K |
| 400 | 结果输出.png | 10.97K |
| 401 | 蒸汽云爆炸模型预测.rsm | 168B |
| 402 | 预测方案.png | 12.33K |
| 403 | 大气稳定度计算.png | 10.29K |
| 404 | 事故源.png | 12.00K |
| 405 | 爆炸伤害范围.png | 23.80K |
| 406 | 结果输出.png | 10.90K |
| 407 | 蒸汽云爆炸模型预测.rsm | 179B |
| 408 | 事故源.png | 14.85K |
| 409 | 沸腾液体扩展蒸汽爆炸模型预测.rsm | 219B |
| 410 | 结果图.png | 25.31K |
| 411 | 结果输出.png | 13.56K |
| 412 | 环氧化反应器.doc | 209.00K |
| 413 | 环氧化反应器.ra2 | 23.24K |
| 414 | T0101.cn2 | 30.20K |
| 415 | T0101.doc | 623.00K |
| 416 | T0102.cn2 | 30.20K |
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| 436 | T0303.cn2 | 30.20K |
| 437 | T0303.doc | 621.50K |
| 438 | E0203.doc | 329.50K |
| 439 | 换热器.fx2 | 24.00K |
| 440 | 环氧乙烷尾气塔.bkp | 121.84K |
| 441 | 环氧乙烷尾气塔中间冷凝器.bkp | 116.33K |
| 442 | 双效精馏.bkp | 239.86K |
| 443 | DMC三级精制塔气相压缩式热泵精馏.bkp | 117.99K |
| 444 | DMC三级精制塔液相闪蒸式热泵精馏.bkp | 154.42K |
| 445 | 乙烯环氧化反应器动力学模拟.bkp | 58.76K |
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| 447 | cashflow.ict | 990.98K |
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| 449 | DESIGN.d01 | 52.24K |
| 450 | DESIGN.d02 | 11.65K |
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| 576 | PROJP.d05 | 36B |
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| 580 | RAW.d02 | 6.87K |
| 581 | RAW.d03 | 5.02K |
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| 588 | REP_GEN.d04 | 4.98K |
| 589 | REP_GEN.d05 | 36B |
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| 591 | Scenario1.izp | 1.02M |
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| 602 | STD.d04 | 20.74K |
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