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| # | 文件名称 | 文件大小 |
|---|---|---|
| 1 | 致评委老师的一封信.txt | 1.20K |
| 2 | 项目图册.pdf | 7.16M |
| 3 | Thumbs.db | 5.00K |
| 4 | 厂区平面布置图.dwg | 284.37K |
| 5 | Thumbs.db | 5.00K |
| 6 | 工艺-物料流程图—PFD.dwg | 393.93K |
| 7 | Thumbs.db | 5.00K |
| 8 | 管道-仪表流程图—PID.dwg | 746.45K |
| 9 | Thumbs.db | 5.50K |
| 10 | 管道轴测图.dwg | 724.76K |
| 11 | Thumbs.db | 6.50K |
| 12 | 丁烯冷凝器换热器.dwg | 192.81K |
| 13 | 乙烯精制塔.dwg | 257.84K |
| 14 | 烯烃反应器.dwg | 159.59K |
| 15 | 甲硫醇反应器.dwg | 86.85K |
| 16 | Thumbs.db | 5.50K |
| 17 | 车间布置图.dwg | 323.98K |
| 18 | Thumbs.db | 5.50K |
| 19 | 首页图.dwg | 66.88K |
| 20 | 1、可行性研究报告.doc | 2.65M |
| 21 | 2、初步设计说明书.doc | 9.60M |
| 22 | 3、环境预评价报告.doc | 2.45M |
| 23 | 4、安全预评价报告.doc | 2.76M |
| 24 | 5、典型设备计算说明书.doc | 23.90M |
| 25 | 6、创新性说明书.doc | 2.52M |
| 26 | 典型设备计算说明书.doc | 162B |
| 27 | 安全预评价报告.doc | 162B |
| 28 | 附录1:物料衡算.doc | 1.32M |
| 29 | 附录2:能量衡算.doc | 1.84M |
| 30 | 附录3:设备选型一览表.doc | 1.17M |
| 31 | 附录4:Risksystem.doc | 5.84M |
| 32 | 附录5:MSDS一览表.doc | 1.78M |
| 33 | 1.png | 1.18M |
| 34 | 2.png | 1.18M |
| 35 | 3.png | 1.36M |
| 36 | 4.png | 1.46M |
| 37 | 5.png | 1.02M |
| 38 | 6.png | 1.38M |
| 39 | 7.png | 1.55M |
| 40 | Thumbs.db | 19.00K |
| 41 | 模型.max | 101.28M |
| 42 | 换热网络优化前.hch | 22.94M |
| 43 | 换热网络优化后.hch | 40.28M |
| 44 | E0102A.EDR | 418.57K |
| 45 | E0102B.EDR | 418.57K |
| 46 | E0103.EDR | 358.19K |
| 47 | E0205.EDR | 470.33K |
| 48 | E0208.EDR | 422.41K |
| 49 | E0302.EDR | 379.08K |
| 50 | E0303.EDR | 366.12K |
| 51 | E0305.EDR | 427.85K |
| 52 | E0309.EDR | 362.40K |
| 53 | E0401.EDR | 446.13K |
| 54 | E0402.EDR | 341.58K |
| 55 | E0403.EDR | 501.86K |
| 56 | E0404.EDR | 442.33K |
| 57 | E0405.EDR | 381.54K |
| 58 | E0406.EDR | 456.31K |
| 59 | E0407.EDR | 364.12K |
| 60 | E0408.EDR | 327.48K |
| 61 | E0410.EDR | 360.50K |
| 62 | E0411.EDR | 353.95K |
| 63 | E0412.EDR | 398.27K |
| 64 | E0413.EDR | 440.50K |
| 65 | 工业流体污垢热阻.pdf | 60.50K |
| 66 | E0102A.docx | 54.95K |
| 67 | E0102A.XLSM | 66.25K |
| 68 | E0102B.docx | 54.95K |
| 69 | E0102B.XLSM | 66.25K |
| 70 | E0103.docx | 43.00K |
| 71 | E0103.XLSM | 66.10K |
| 72 | E0205.docx | 75.87K |
| 73 | E0205.XLSM | 65.97K |
| 74 | E0208.docx | 51.42K |
| 75 | E0208.XLSM | 65.78K |
| 76 | E0302.docx | 41.76K |
| 77 | E0302.XLSM | 66.04K |
| 78 | E0303.docx | 44.54K |
| 79 | E0303.XLSM | 65.72K |
| 80 | E0305.docx | 46.42K |
| 81 | E0305.XLSM | 66.73K |
| 82 | E0309.docx | 40.65K |
| 83 | E0309.XLSM | 66.09K |
| 84 | E0401.docx | 71.31K |
| 85 | E0401.XLSM | 66.10K |
| 86 | E0402.docx | 40.85K |
| 87 | E0402.XLSM | 65.96K |
| 88 | E0403.docx | 73.73K |
| 89 | E0403.XLSM | 66.05K |
| 90 | E0404.docx | 63.93K |
| 91 | E0404.XLSM | 66.27K |
| 92 | E0405.docx | 48.50K |
| 93 | E0405.XLSM | 65.95K |
| 94 | E0406.docx | 55.43K |
| 95 | E0406.XLSM | 66.03K |
| 96 | E0407.docx | 43.49K |
| 97 | E0407.XLSM | 66.13K |
| 98 | E0408.docx | 39.13K |
| 99 | E0408.XLSM | 65.76K |
| 100 | E0410.docx | 45.30K |
| 101 | E0410.XLSM | 65.97K |
| 102 | E0411.docx | 40.91K |
| 103 | E0411.XLSM | 66.06K |
| 104 | E0412.docx | 44.99K |
| 105 | E0412.XLSM | 65.68K |
| 106 | E0413.docx | 65.12K |
| 107 | E0413.XLSM | 66.17K |
| 108 | 优化前全流程模拟.apw | 5.61M |
| 109 | 优化前全流程模拟.bkp | 974.78K |
| 110 | 优化后不含热泵精馏全流程模拟.apw | 6.18M |
| 111 | 优化后不含热泵精馏全流程模拟.bkp | 1.61M |
| 112 | 优化后含热泵精馏全流程模拟.apw | 6.31M |
| 113 | 优化后含热泵精馏全流程模拟.bkp | 1.69M |
| 114 | 热泵精馏模拟.apw | 2.73M |
| 115 | 热泵精馏模拟.bkp | 163.32K |
| 116 | 烯烃合成精制工段.apw | 2.38M |
| 117 | 烯烃合成精制工段.bkp | 441.72K |
| 118 | 甲硫醇工段.apw | 5.68M |
| 119 | 甲硫醇工段.bkp | 336.05K |
| 120 | 甲醇合成工段.apw | 843.00K |
| 121 | 甲醇合成工段.bkp | 128.19K |
| 122 | 甲醇精制工段.apw | 1.21M |
| 123 | 甲醇精制工段.bkp | 221.18K |
| 124 | 预处理工段.apw | 1.47M |
| 125 | 预处理工段.bkp | 289.34K |
| 126 | Thumbs.db | 5.00K |
| 127 | 厂区平面布置图.bak | 310.03K |
| 128 | 厂区平面布置图.dwg | 304.78K |
| 129 | acad.fas | 2.27K |
| 130 | Thumbs.db | 5.00K |
| 131 | 工艺-物料流程图—PFD.bak | 603.16K |
| 132 | 工艺-物料流程图—PFD.dwg | 603.16K |
| 133 | acad.fas | 2.27K |
| 134 | Thumbs.db | 5.00K |
| 135 | 管道-仪表流程图—PID.bak | 1.51M |
| 136 | 管道-仪表流程图—PID.dwg | 1.51M |
| 137 | Thumbs.db | 5.50K |
| 138 | 管道轴测图.dwg | 750.00K |
| 139 | acad.fas | 2.27K |
| 140 | Thumbs.db | 6.50K |
| 141 | 丁烯冷凝器换热器.bak | 208.81K |
| 142 | 丁烯冷凝器换热器.dwg | 207.28K |
| 143 | 乙烯精制塔.bak | 235.69K |
| 144 | 乙烯精制塔.dwg | 233.44K |
| 145 | 烯烃反应器.bak | 178.53K |
| 146 | 烯烃反应器.dwg | 171.88K |
| 147 | 甲硫醇反应器.bak | 97.13K |
| 148 | 甲硫醇反应器.dwg | 97.38K |
| 149 | acad.fas | 2.27K |
| 150 | Thumbs.db | 5.50K |
| 151 | 车间布置图.bak | 342.28K |
| 152 | 车间布置图.dwg | 354.00K |
| 153 | acad.fas | 2.27K |
| 154 | Thumbs.db | 5.50K |
| 155 | 首页图.bak | 76.34K |
| 156 | 首页图.dwg | 76.84K |
| 157 | 噪声分析.docx | 950.53K |
| 158 | HAZOP分析表.docx | 23.61K |
| 159 | 甲醇常压精制塔HAZOP分析.hzip | 779.85K |
| 160 | 甲醇常压精制塔分析1.png | 98.83K |
| 161 | 甲醇常压精制塔分析2.png | 202.28K |
| 162 | 甲醇常压精制塔分析3.png | 73.05K |
| 163 | matlab膜分离.mat | 3.03M |
| 164 | matlab膜分离.txt | 1.23K |
| 165 | 预处理车间布置图.dwg | 15.64M |
| 166 | Risksystem源文件.docx | 5.64M |
| 167 | 烃反应器校核.docx | 162B |
| 168 | 浮阀塔校核.docx | 48.56K |
| 169 | 浮阀校核.plc | 200.00K |
| 170 | 浮阀校核.xls | 179.00K |
| 171 | 浮阀设计.docx | 49.28K |
| 172 | 浮阀设计校核.plc | 196.00K |
| 173 | T0404乙烯精制塔校核1.cn2 | 30.20K |
| 174 | 乙烯精制塔SW-6校核.docx | 173.82K |
| 175 | 乙烯精制塔校核.pdf | 420.05K |
| 176 | 硫化氢吸收塔校核.cn2 | 30.20K |
| 177 | 硫化氢吸收塔校核.docx | 173.89K |
| 178 | 硫化氢吸收塔校核.pdf | 419.77K |
| 179 | 硫化氢浓缩塔校核.cn2 | 30.20K |
| 180 | 硫化氢浓缩塔校核.docx | 173.52K |
| 181 | 硫化氢浓缩塔校核.pdf | 420.19K |
| 182 | 硫化氢解析塔校核.cn2 | 30.20K |
| 183 | 硫化氢解析塔校核.docx | 174.92K |
| 184 | 硫化氢解析塔校核.pdf | 419.86K |
| 185 | 甲醇预分离塔校核.cn2 | 30.20K |
| 186 | 甲醇预分离塔校核.docx | 172.83K |
| 187 | 甲醇预分离塔校核.pdf | 419.93K |
| 188 | 甲醇加压精制塔校核.cn2 | 30.20K |
| 189 | 甲醇加压精制塔校核.docx | 173.70K |
| 190 | 甲醇加压精制塔校核.pdf | 419.68K |
| 191 | 甲醇常压精制塔校核.cn2 | 30.20K |
| 192 | 甲醇常压精制塔校核.docx | 173.85K |
| 193 | 甲醇常压精制塔校核.pdf | 419.81K |
| 194 | 甲硫醇预分离塔校核.cn2 | 30.20K |
| 195 | 甲硫醇预分离塔校核.docx | 173.74K |
| 196 | 甲硫醇预分离塔校核.pdf | 420.06K |
| 197 | 甲硫醇精制塔校核.cn2 | 30.20K |
| 198 | 甲硫醇精制塔校核.docx | 173.54K |
| 199 | 甲硫醇精制塔校核.pdf | 419.60K |
| 200 | 烯烃预分离塔校核.cn2 | 30.20K |
| 201 | 烯烃预分离塔校核.docx | 173.82K |
| 202 | 烯烃预分离塔校核.pdf | 419.71K |
| 203 | 烯烃反应器R0401校核.docx | 561.80K |
| 204 | 烯烃反应器校核R0401.fx2 | 24.00K |
| 205 | 甲硫醇反应器R0301校核.docx | 561.56K |
| 206 | 甲硫醇反应器校核R0301.fx2 | 24.00K |
| 207 | 丁烯塔冷凝器校核.fx2 | 24.00K |
| 208 | 丁烯精制塔塔顶冷凝器E04012校核.docx | 479.57K |
| 209 | 丙烯精制塔塔顶冷凝器E0406校核.docx | 478.77K |
| 210 | 丙烯精制塔塔顶冷凝器校核.fx2 | 24.00K |
| 211 | 乙烯精制塔.apw | 934.00K |
| 212 | 乙烯精制塔.bkp | 105.49K |
| 213 | 乙烯精制塔.dynf | 445.19K |
| 214 | 进料流量改变.xlsx | 196.91K |
| 215 | 进料组成改变.xlsx | 200.97K |
| 216 | snpA0000.snp | 1.60M |
| 217 | snpA0001.snp | 1.82M |
| 218 | snpA0002.snp | 1.53M |
| 219 | snpA0003.snp | 2.60M |
| 220 | 乙烯精制塔dyn.his | 2.70K |
| 221 | 乙烯精制塔dyn.rep | 0B |
| 222 | ADVR浮阀塔盘在气体分馏装置中的应用.pdf | 352.55K |
| 223 | 一种氢气和二氧化碳合成甲醇的工艺方法.pdf | 404.29K |
| 224 | 三井化学公司寻求二氧化碳制甲醇项目合作伙伴.pdf | 1.65M |
| 225 | 三井化学计划新建以二氧化碳为原料的大型甲醇装置.pdf | 322.47K |
| 226 | 二氧化碳膜分离技术_曹映玉.pdf | 488.19K |
| 227 | 净化天然气的膜分离技术_曹卫平.pdf | 34.68K |
| 228 | 国内甲醇制烯烃技术最新进展.pdf | 981.24K |
| 229 | 天然气膜法脱水净化技术及应用.pdf | 333.80K |
| 230 | 日本三井化学公司二氧化碳制甲醇中试装置获成功.pdf | 203.76K |
| 231 | 煤制烯烃工艺及下游项目的发展前景.pdf | 269.00K |
| 232 | 硫化氢下游产品开发与应用.pdf | 1.04M |
| 233 | 硫化氢甲醇法合成甲硫醇工艺研究进展.pdf | 557.95K |
| 234 | 膜分离技术在环保中的应用研究和进展.pdf | 239.76K |
| 235 | KineticModeloftheReactionofMethanolwithHydrogenSulfide.pdf | 1.34M |
| 236 | 甲醇制烯烃反应动力学.pdf | 154.63K |
| 237 | 回流比参数优化.apw | 3.50M |
| 238 | 回流比参数优化.bkp | 68.57K |
| 239 | 塔板数优化.apw | 3.30M |
| 240 | 塔板数优化.bkp | 17.22K |
| 241 | 进料位置优化.apw | 3.37M |
| 242 | 进料位置优化.bkp | 66.19K |
| 243 | 回流比参数优化.apw | 3.76M |
| 244 | 回流比参数优化.bkp | 89.26K |
| 245 | 塔板数优化.apw | 3.72M |
| 246 | 塔板数优化.bkp | 103.95K |
| 247 | 进料位置优化.apw | 3.62M |
| 248 | 进料位置优化.bkp | 89.59K |
| 249 | 回流比参数优化.apw | 3.80M |
| 250 | 回流比参数优化.bkp | 73.15K |
| 251 | 塔板数优化.apw | 3.81M |
| 252 | 塔板数优化.bkp | 82.55K |
| 253 | 进料位置优化.apw | 3.54M |
| 254 | 进料位置优化.bkp | 72.52K |
| 255 | 回流比参数优化.apw | 4.17M |
| 256 | 回流比参数优化.bkp | 77.31K |
| 257 | 塔板数优化.apw | 3.97M |
| 258 | 塔板数优化.bkp | 83.89K |
| 259 | 进料位置优化.apw | 3.70M |
| 260 | 进料位置优化.bkp | 76.84K |
| 261 | 回流比参数优化.apw | 2.69M |
| 262 | 回流比参数优化.bkp | 75.81K |
| 263 | 塔板数优化.apw | 2.50M |
| 264 | 塔板数优化.bkp | 89.55K |
| 265 | 进料位置优化.apw | 2.48M |
| 266 | 进料位置优化.bkp | 74.43K |
| 267 | 回流比参数优化.appdf | 254.28K |
| 268 | 回流比参数优化.apw | 3.21M |
| 269 | 回流比参数优化.bkp | 89.97K |
| 270 | 回流比参数优化.def | 250B |
| 271 | 回流比参数优化.for | 0B |
| 272 | 回流比参数优化.his | 43.20K |
| 273 | 塔板数优化.apw | 2.70M |
| 274 | 塔板数优化.bkp | 93.35K |
| 275 | 进料位置优化.appdf | 282.16K |
| 276 | 进料位置优化.apw | 3.19M |
| 277 | 进料位置优化.bkp | 88.12K |
| 278 | 进料位置优化.def | 240B |
| 279 | 进料位置优化.for | 0B |
| 280 | 进料位置优化.his | 50.24K |
| 281 | 回流比参数优化.apw | 4.10M |
| 282 | 回流比参数优化.bkp | 93.67K |
| 283 | 塔板数优化.apw | 3.79M |
| 284 | 塔板数优化.bkp | 103.90K |
| 285 | 进料位置优化.apw | 3.83M |
| 286 | 进料位置优化.bkp | 91.51K |
| 287 | 回流比参数优化.apw | 3.91M |
| 288 | 回流比参数优化.bkp | 72.20K |
| 289 | 塔板数优化.apw | 3.74M |
| 290 | 塔板数优化.bkp | 82.98K |
| 291 | 进料位置优化.apw | 3.83M |
| 292 | 进料位置优化.bkp | 71.97K |
| 293 | 回流比参数优化.apw | 4.11M |
| 294 | 回流比参数优化.bkp | 98.75K |
| 295 | 塔板数优化.apw | 4.01M |
| 296 | 塔板数优化.bkp | 109.67K |
| 297 | 进料位置优化.apw | 4.00M |
| 298 | 进料位置优化.bkp | 97.78K |
| 299 | 回流比参数优化.apw | 3.10M |
| 300 | 回流比参数优化.bkp | 72.91K |
| 301 | 塔板数优化.apw | 3.14M |
| 302 | 塔板数优化.bkp | 79.87K |
| 303 | 进料位置优化.apw | 3.21M |
| 304 | 进料位置优化.bkp | 71.56K |
| 305 | 回流比参数优化.apw | 3.29M |
| 306 | 回流比参数优化.bkp | 81.29K |
| 307 | 塔板数优化.apw | 2.56M |
| 308 | 塔板数优化.bkp | 73.23K |
| 309 | 进料位置优化.apw | 2.68M |
| 310 | 进料位置优化.bkp | 66.20K |
| 311 | T0101吸收液最小用量设计规定.apw | 2.59M |
| 312 | T0101吸收液最小用量设计规定.bkp | 89.60K |
| 313 | T0103塔底再沸比优化.apw | 2.48M |
| 314 | T0103塔底再沸比优化.bkp | 74.27K |
| 315 | T0101.bkp | 116.95K |
| 316 | T0103.bkp | 90.95K |
| 317 | T0201.bkp | 90.19K |
| 318 | T0202.bkp | 129.37K |
| 319 | T0203.bkp | 104.87K |
| 320 | T0302.bkp | 124.25K |
| 321 | T0401.bkp | 133.54K |
| 322 | T0403.bkp | 189.27K |
| 323 | T0404.bkp | 87.64K |
| 324 | T0405.bkp | 82.40K |
| 325 | 泵选型文件.docx | 7.94M |
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