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川宁生物制药废气深度脱硫项目初步设计（ID:2709321）
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| # | 文件名称 | 文件大小 |
|---|---|---|
| 1 | 17599141732162.zip | 372.71M |
| 2 | Readme.txt | 1.51K |
| 3 | 0-项目摘要.doc | 343.00K |
| 4 | 00-作品对应表.doc | 724.00K |
| 5 | 01-可行性分析说明书.doc | 1.66M |
| 6 | 02-初步设计说明书.doc | 4.32M |
| 7 | 03-创新性说明书.doc | 654.00K |
| 8 | 04-1设备设计说明书.doc | 1.29M |
| 9 | 04-2反应器设计说明书.doc | 1.96M |
| 10 | 04-3换热器设计说明书.doc | 2.51M |
| 11 | 04-4塔设备设计说明书.doc | 3.79M |
| 12 | 04-5设备选型一览表.doc | 480.50K |
| 13 | 05-分子筛深度脱硫塔设计说明书.doc | 583.50K |
| 14 | 06-能量平衡计算书.doc | 383.00K |
| 15 | 07-物料平衡计算书.doc | 438.50K |
| 16 | 08-MSDS.doc | 945.00K |
| 17 | 09-安全预评价报告.doc | 1.26M |
| 18 | 10-环境影响评价报告.doc | 2.73M |
| 19 | 11-经济分析报告.doc | 869.00K |
| 20 | 12-换热网络与节能设计.doc | 1.08M |
| 21 | 项目图册.pdf | 6.43M |
| 22 | PFD工艺流程简图.dwg | 774.32K |
| 23 | 物流表.xlsx | 40.82K |
| 24 | PID管道及仪表流程图.dwg | 918.95K |
| 25 | E0106换热器装配图.dwg | 356.97K |
| 26 | T0101脱硫吸收塔设备装配图.dwg | 276.34K |
| 27 | 列管式固定床反应器R0301.dwg | 611.77K |
| 28 | 车间平立面图.dwg | 560.98K |
| 29 | 车间设备三维图.dwg | 5.19M |
| 30 | 四五工段三维配管.dwg | 5.19M |
| 31 | 四五工段三维配管纯管道.dwg | 2.90M |
| 32 | 1中和塔进料管道.dwg | 134.12K |
| 33 | 2氧化塔进料管道.dwg | 94.38K |
| 34 | 3精馏塔管道.dwg | 194.74K |
| 35 | 总车间平面图.dwg | 102.69K |
| 36 | 1-废气深度脱硫工段.bkp | 247.33K |
| 37 | 2-沼气深度脱硫工段.bkp | 689.07K |
| 38 | 3-甲硫醚合成精制工段.bkp | 780.00K |
| 39 | 4-甲硫醚氧化工段.bkp | 387.71K |
| 40 | 5-二甲基亚砜精制工段.bkp | 479.79K |
| 41 | readme.txt | 621B |
| 42 | 全流程模拟.apw | 5.64M |
| 43 | 全流程模拟.bkp | 1.61M |
| 44 | 全流程模拟换热网络，公用工程.apw | 6.16M |
| 45 | 全流程模拟换热网络，公用工程.bkp | 1.68M |
| 46 | T-10二甲基亚砜精馏塔2.bkp | 229.16K |
| 47 | T-1脱硫塔1.bkp | 351.05K |
| 48 | T-2脱硫塔2.bkp | 350.97K |
| 49 | T-3再生解吸塔.bkp | 427.07K |
| 50 | T-4硫化氢汽提塔.bkp | 340.52K |
| 51 | T-5甲硫醇分离隔板塔.bkp | 474.92K |
| 52 | T-6萃取精馏隔板塔.bkp | 486.53K |
| 53 | T-8中和塔.bkp | 346.84K |
| 54 | T-9二甲基亚砜精馏塔1.bkp | 229.92K |
| 55 | 回流比优化.bkp | 353.36K |
| 56 | 塔釜温度优化.bkp | 354.45K |
| 57 | 进料位置优化.bkp | 351.37K |
| 58 | 进料温度优化.bkp | 351.84K |
| 59 | 塔顶压力优化.bkp | 360.96K |
| 60 | 进料温度优化.bkp | 360.36K |
| 61 | 进料量优化.bkp | 360.46K |
| 62 | 塔顶压力优化.bkp | 366.31K |
| 63 | 进料温度优化.bkp | 363.07K |
| 64 | 进料量优化.bkp | 363.13K |
| 65 | 回流罐温度优化8.4.bkp | 781.51K |
| 66 | 回流罐进料位置优化.bkp | 444.14K |
| 67 | 塔内回流比优化.bkp | 448.75K |
| 68 | 进料温度优化.bkp | 440.08K |
| 69 | 回流比优化.bkp | 355.00K |
| 70 | 理论板数优化.bkp | 350.30K |
| 71 | 进料温度优化.bkp | 352.36K |
| 72 | 压力优化.bkp | 365.48K |
| 73 | 进料温度优化.bkp | 362.91K |
| 74 | 进料量优化.bkp | 361.09K |
| 75 | 回流比优化.bkp | 364.78K |
| 76 | 塔压力优化.bkp | 363.71K |
| 77 | 进料位置优化.bkp | 363.37K |
| 78 | 进料温度优化.bkp | 365.00K |
| 79 | 9个塔水力学数据.xls | 88.00K |
| 80 | Readme.txt | 597B |
| 81 | T-0101.plc | 196.00K |
| 82 | T-0101.xls | 179.00K |
| 83 | T-0102.plc | 196.00K |
| 84 | T-0102.xls | 179.00K |
| 85 | T-0103.plc | 196.00K |
| 86 | T-0103.xls | 179.00K |
| 87 | T0301.plc | 196.00K |
| 88 | T0301.xls | 179.00K |
| 89 | 1.kgt | 1.53K |
| 90 | 1.pdf | 16.68K |
| 91 | 2.kgt | 1.51K |
| 92 | 2.pdf | 16.69K |
| 93 | 3.kgt | 1.52K |
| 94 | 3.pdf | 16.69K |
| 95 | 1.kgt | 1.52K |
| 96 | 1.pdf | 16.69K |
| 97 | 2.kgt | 1.51K |
| 98 | 2.pdf | 16.64K |
| 99 | 3.kgt | 1.50K |
| 100 | 3.pdf | 16.65K |
| 101 | T0501工艺参数详单.doc | 244.00K |
| 102 | T0501设计源文件.CPR | 211B |
| 103 | T0501设计结果.doc | 350.50K |
| 104 | T-0502.kgt | 1.51K |
| 105 | T-0502.pdf | 16.69K |
| 106 | T-0503.kgt | 1.50K |
| 107 | t-0503.pdf | 16.63K |
| 108 | R0301列管反应器校核书.pdf | 188.44K |
| 109 | R0301反应器.fx2 | 24.27K |
| 110 | T0101校核源文件.cn2 | 30.20K |
| 111 | T0101设备设计计算书.pdf | 272.30K |
| 112 | T0102校核源文件.cn2 | 30.20K |
| 113 | T0102设备设计计算书.pdf | 225.52K |
| 114 | T0103校核源文件.cn2 | 30.20K |
| 115 | T0103设备设计计算书.pdf | 262.79K |
| 116 | T0301校核源文件.cn2 | 30.20K |
| 117 | T0301设备设计计算书.pdf | 234.38K |
| 118 | T0302校核源文件.cn2 | 30.20K |
| 119 | T0302设备设计计算书.pdf | 234.39K |
| 120 | T0501校核源文件.cn2 | 30.20K |
| 121 | T0501设备设计计算书.pdf | 234.47K |
| 122 | T0502校核源文件.cn2 | 30.20K |
| 123 | T0502设备设计计算书.pdf | 225.11K |
| 124 | T0502校核源文件.cn2 | 30.20K |
| 125 | T0502设备设计计算书.pdf | 225.11K |
| 126 | E0106-SW6校核源文件.fx2 | 24.00K |
| 127 | E0106计算说明书.pdf | 254.00K |
| 128 | E0505-SW6校核源文件.fx2 | 24.00K |
| 129 | E0505计算说明书.pdf | 244.35K |
| 130 | 111.mdb | 16.00K |
| 131 | Admin.mdb | 17.00K |
| 132 | CATA227.mdb | 438.00K |
| 133 | DESI569.mdb | 6.91M |
| 134 | PADD344.mdb | 201.00K |
| 135 | 111.mdb | 16.00K |
| 136 | Admin.mdb | 17.00K |
| 137 | CATA227.mdb | 438.00K |
| 138 | DESI569.mdb | 8.78M |
| 139 | PADD344.mdb | 201.00K |
| 140 | 厂区3D建模.ls6 | 300.99M |
| 141 | 厂区模型.pdf | 208.82K |
| 142 | Readme.txt | 550B |
| 143 | 环境风险评价报告.doc | 1.00M |
| 144 | 1.png | 11.70K |
| 145 | 2.png | 11.81K |
| 146 | 氢气在大气中的扩散预测.rsm | 490B |
| 147 | 1.png | 10.81K |
| 148 | 2.png | 10.60K |
| 149 | 氢气泄露事故模拟.rsm | 504B |
| 150 | 氢气液体扩展蒸汽爆炸模型预测.rsm | 204B |
| 151 | 沸腾液体扩展蒸汽爆炸模型伤害范围.png | 18.22K |
| 152 | 氢气池火事故模型预测.rsm | 192B |
| 153 | 池火事故模型伤害范围.png | 22.75K |
| 154 | 1.png | 142.36K |
| 155 | 2.png | 13.83K |
| 156 | 3.png | 14.59K |
| 157 | 4.png | 9.88K |
| 158 | 5.png | 12.94K |
| 159 | 6.png | 22.13K |
| 160 | 蒸汽云爆炸模型预测.rsm | 166B |
| 161 | 甲醇气体泄漏量计算.rsm | 74B |
| 162 | 甲醇液体泄漏量计算.rsm | 116B |
| 163 | 甲醇质量蒸发量计算.rsm | 61B |
| 164 | 甲醇闪蒸量计算.rsm | 63B |
| 165 | 甲醇池火事故模型伤害范围.png | 21.48K |
| 166 | 甲醇池火事故模型预测.rsm | 206B |
| 167 | 甲醇沸腾液体扩展蒸汽爆炸模型.rsm | 208B |
| 168 | 甲醇沸腾液体扩展蒸汽爆炸模型伤害范围.png | 25.90K |
| 169 | 甲醇蒸汽云爆炸模型预测.rsm | 168B |
| 170 | 蒸汽云爆炸模型伤害范围.png | 23.76K |
| 171 | 1.png | 11.51K |
| 172 | 2.png | 11.87K |
| 173 | 硫化氢在大气中的扩散预测.rsm | 496B |
| 174 | 气体泄漏量计算.rsm | 76B |
| 175 | Readme.txt | 593B |
| 176 | 甲醇储罐毒性范围.png | 11.27K |
| 177 | 甲醇储罐泄露模型ALOHA分析示意.docx | 368.68K |
| 178 | 甲醇储罐源文件.alo | 4.61K |
| 179 | 甲醇储罐火球爆炸范围.png | 18.90K |
| 180 | 氢气储罐毒性范围.png | 13.67K |
| 181 | 氢气储罐气云燃烧范围.png | 12.91K |
| 182 | 氢气储罐气云爆炸范围.png | 16.77K |
| 183 | 氢气储罐源文件.alo | 4.61K |
| 184 | 硫化氢储罐毒性范围.png | 13.08K |
| 185 | 硫化氢储罐气云爆炸范围.png | 13.59K |
| 186 | 硫化氢储罐气云爆炸范围2.png | 16.31K |
| 187 | 硫化氢储罐源文件.alo | 4.61K |
| 188 | 甲硫醚储罐毒性范围.png | 19.96K |
| 189 | 甲硫醚储罐源文件.alo | 4.61K |
| 190 | 二甲基亚砜储罐.png | 22.96K |
| 191 | 二甲基亚砜储罐源文件.alo | 4.61K |
| 192 | HAZOP分析方法在DMSO精馏中的应用.doc | 1.23M |
| 193 | HAZOP分析方法在DMSO精馏中的应用.pdf | 1.03M |
| 194 | 二甲基亚砜.png | 59.31K |
| 195 | 甲硫醚.png | 55.46K |
| 196 | 硫化氢.png | 75.02K |
| 197 | 1.节点基本信息.png | 76.05K |
| 198 | 2.节点设备.png | 70.61K |
| 199 | 3.节点图纸.png | 63.36K |
| 200 | HAZOP分析工作表.png | 139.86K |
| 201 | 工艺流程.png | 9.91K |
| 202 | 1节点基本信息.png | 70.79K |
| 203 | 2节点设备.png | 68.06K |
| 204 | 3节点图纸.png | 67.87K |
| 205 | 例1.png | 124.72K |
| 206 | 例2.png | 139.00K |
| 207 | 工艺流程.png | 10.79K |
| 208 | 矩阵信息.png | 55.54K |
| 209 | 甲醇储罐火灾爆炸事故树分析.ftx | 3.72K |
| 210 | 甲醇储罐爆炸事故树分析.pdf | 493.88K |
| 211 | 2-噪声监测分析数据.xlsx | 12.01K |
| 212 | 3-噪声监测评估.doc | 1.02M |
| 213 | 噪声分析线图.jpg | 66.64K |
| 214 | 噪声影响.ein | 6.44K |
| 215 | 噪声评估线图.JPG | 366.05K |
| 216 | 车间位置图.jpg | 81.94K |
| 217 | 车间总图.jpg | 202.71K |
| 218 | readme.txt | 982B |
| 219 | 地表水质评价报告.doc | 2.61M |
| 220 | EIAW10.cfg | 70B |
| 221 | readme.txt | 3.18K |
| 222 | ST6UNST.LOG | 23.38K |
| 223 | BOD-DO河口耦合模式.rtf | 73.56K |
| 224 | DobbinsCamp模式估算K1K2K3BP.rtf | 43.64K |
| 225 | Ficher法测定河流纵向混合系数Mx.rtf | 175.22K |
| 226 | K1K2的温度变化修正.rtf | 34.32K |
| 227 | OConnor模式估算K1K2K3KN.rtf | 43.17K |
| 228 | S-P模型Dobbins-Camp修正式.rtf | 105.45K |
| 229 | S-P模型OConnor修正式.rtf | 123.38K |
| 230 | S-P模型Thomas修正式.rtf | 94.51K |
| 231 | S-P模型动态数值模式.rtf | 247.35K |
| 232 | S-P模型基本式.rtf | 167.23K |
| 233 | S-P模型的应用.rtf | 148.38K |
| 234 | S-P模型通用稳态平衡模式.rtf | 13.77K |
| 235 | SP模式估算K1K2.rtf | 38.16K |
| 236 | Thomas模式估算K1K2K3.rtf | 39.28K |
| 237 | 一维基本模型1.rtf | 52.35K |
| 238 | 一维基本模型2.rtf | 117.99K |
| 239 | 一维模型的显式差分.rtf | 97.35K |
| 240 | 一维模型的隐式差分.rtf | 186.46K |
| 241 | 三维基本模型1.rtf | 28.63K |
| 242 | 三维基本模型2.rtf | 47.80K |
| 243 | 二维基本模型1.rtf | 92.70K |
| 244 | 二维基本模型2.rtf | 73.77K |
| 245 | 二维平面流场的特征理论差分解法.rtf | 176.08K |
| 246 | 二维模型的全隐式差分.rtf | 90.79K |
| 247 | 二维模型的半隐式差分.rtf | 147.53K |
| 248 | 从流量计算平均流速.rtf | 23.83K |
| 249 | 公路建设项目生态环境影响评价.rtf | 382.54K |
| 250 | 各种评价方法.rtf | 176.19K |
| 251 | 地面水环境影响评价工作分级.rtf | 196.88K |
| 252 | 复氧系数K2丘吉尔经验式.rtf | 23.89K |
| 253 | 复氧系数K2欧-道经验式.rtf | 38.38K |
| 254 | 复氧系数K2欧文斯经验式.rtf | 23.59K |
| 255 | 复氧系数K2野外DO实验测定法.rtf | 143.21K |
| 256 | 欧康那河口模式.rtf | 34.40K |
| 257 | 欧康那河口衰减模式.rtf | 88.90K |
| 258 | 沃伦威得尔模型.rtf | 39.83K |
| 259 | 河口一维数值解法.rtf | 307.06K |
| 260 | 河口二维数值解法.rtf | 308.68K |
| 261 | 河口水质模拟.rtf | 288.98K |
| 262 | 河流1.rtf | 21.11K |
| 263 | 河流10.rtf | 73.38K |
| 264 | 河流11.rtf | 33.40K |
| 265 | 河流2.rtf | 24.01K |
| 266 | 河流3.rtf | 28.34K |
| 267 | 河流4.rtf | 58.46K |
| 268 | 河流5.rtf | 45.80K |
| 269 | 河流6.rtf | 51.58K |
| 270 | 河流7.rtf | 29.57K |
| 271 | 河流8.rtf | 61.22K |
| 272 | 河流9.rtf | 50.68K |
| 273 | 河流温度模型.rtf | 119.96K |
| 274 | 河流的一维模拟.rtf | 209.34K |
| 275 | 河流的二维模拟.rtf | 459.32K |
| 276 | 混合系数M.rtf | 31.55K |
| 277 | 混合过程.rtf | 75.21K |
| 278 | 湖库1.rtf | 29.05K |
| 279 | 湖库10.rtf | 24.69K |
| 280 | 湖库2.rtf | 24.81K |
| 281 | 湖库3.rtf | 43.22K |
| 282 | 湖库4.rtf | 35.47K |
| 283 | 湖库5.rtf | 47.02K |
| 284 | 湖库6.rtf | 23.56K |
| 285 | 湖库7.rtf | 47.67K |
| 286 | 湖库8.rtf | 112.66K |
| 287 | 湖库9.rtf | 23.07K |
| 288 | 湖库营养负荷与富营养化.rtf | 98.67K |
| 289 | 特征理论混合模式.rtf | 109.30K |
| 290 | 特征理论温度模式.rtf | 131.20K |
| 291 | 相关系数.rtf | 70.48K |
| 292 | 相对误差.rtf | 53.03K |
| 293 | 硝化动力学方程.rtf | 101.78K |
| 294 | 示踪试验法测定河流横向混合系数My.rtf | 156.25K |
| 295 | 示踪试验法测定河流纵向混合系数Mx.rtf | 151.50K |
| 296 | 约-新模式.rtf | 54.82K |
| 297 | 经验公式法估算混合系数M.rtf | 114.53K |
| 298 | 耗氧系数K1四点DO测定法.rtf | 50.18K |
| 299 | 耗氧系数K1实验室测定法.rtf | 216.68K |
| 300 | 耗氧系数K1野外两点测定法.rtf | 78.26K |
| 301 | 耗氧系数K1野外多点测定法.rtf | 88.80K |
| 302 | 计算平均流速的曼宁公式.rtf | 20.54K |
| 303 | 计算摩阻流速的公式.rtf | 20.12K |
| 304 | 计算流量的公式.rtf | 20.70K |
| 305 | 计算谢才系数的曼宁公式.rtf | 31.92K |
| 306 | 迪龙模型.rtf | 54.35K |
| 307 | 零维基本模型.rtf | 41.29K |
| 308 | 面源源强的确定方法.rtf | 403.08K |
| 309 | 饱和溶解氧.rtf | 22.57K |
| 310 | Drawer2.0.cnt | 914B |
| 311 | DRAWER2.0.HLP | 894.82K |
| 312 | EIAW10.cnt | 636B |
| 313 | EIAW10.HLP | 457.28K |
| 314 | EIAW10基本操作方法.cnt | 494B |
| 315 | EIAW10基本操作方法.HLP | 107.34K |
| 316 | EIAW10模块使用详解.cnt | 2.13K |
| 317 | EIAW10模块使用详解.HLP | 157.26K |
| 318 | EIAW10综述.cnt | 285B |
| 319 | HJT2.1-1993导则-大纲.doc | 58.00K |
| 320 | HJT2.2-1993导则-大气环境.doc | 714.50K |
| 321 | HJT2.3-1993导则-地面水.doc | 526.00K |
| 322 | HJT2.4-1995导则-声环境.doc | 203.00K |
| 323 | JTJ005-96公路建设项目环评规范.doc | 422.50K |
| 324 | 参数估值方法.cnt | 1.53K |
| 325 | 参数估值方法.HLP | 110.42K |
| 326 | 导则中的地面水模式.cnt | 1.13K |
| 327 | 导则中的地面水模式.HLP | 78.39K |
| 328 | 河口海湾水流水质模型.cnt | 1.10K |
| 329 | 河口海湾水流水质模型.HLP | 141.57K |
| 330 | 河流水质模型.cnt | 1.86K |
| 331 | 河流水质模型.HLP | 221.35K |
| 332 | 湖泊水库水质模型.cnt | 323B |
| 333 | 湖泊水库水质模型.HLP | 25.69K |
| 334 | 表格的使用.cnt | 210B |
| 335 | 表格的使用.HLP | 28.39K |
| 336 | GB9661-88图C1.bmp | 13.81K |
| 337 | HJT2.2-93图4.bmp | 12.44K |
| 338 | HJT2.4-1995图2.bmp | 4.91K |
| 339 | HJT2.4-1995图3.bmp | 6.51K |
| 340 | HJT2.4-1995图4.bmp | 3.62K |
| 341 | HJT2.4-1995图5.bmp | 7.87K |
| 342 | HJT2.4-1995图6.bmp | 7.09K |
| 343 | HJT2.4-1995图7.bmp | 5.33K |
| 344 | HJT2.4-1995附图B1.bmp | 3.81K |
| 345 | HJT2.4-1995附图B2.bmp | 12.56K |
| 346 | 全流程模拟.hch | 10.08M |
| 347 | E0101.EDR | 421.32K |
| 348 | E0102.EDR | 452.09K |
| 349 | E0103.EDR | 376.01K |
| 350 | E0104A.EDR | 476.93K |
| 351 | E0104B.EDR | 446.06K |
| 352 | E0105.edr | 467.44K |
| 353 | E0106.EDR | 342.60K |
| 354 | E0201.EDR | 414.04K |
| 355 | E0202.EDR | 533.51K |
| 356 | E0301.EDR | 354.16K |
| 357 | E0303A.EDR | 358.08K |
| 358 | E0303B.EDR | 404.68K |
| 359 | E0304A.EDR | 355.25K |
| 360 | E0304B.EDR | 333.80K |
| 361 | E0305.EDR | 598.16K |
| 362 | E0306.EDR | 341.54K |
| 363 | E0308.EDR | 354.55K |
| 364 | E0310.EDR | 401.34K |
| 365 | E0311.EDR | 409.24K |
| 366 | E0501.EDR | 395.08K |
| 367 | E0503.EDR | 364.43K |
| 368 | E0505.EDR | 276.01K |
| 369 | 二甲基亚砜精馏塔.bkp | 175.77K |
| 370 | 二甲基亚砜精馏塔.dynf | 275.72K |
| 371 | 动态模拟.pdf | 321.82K |
| 372 | AM_SAI.appdf | 260.76K |
| 373 | snapshot.bak | 3.04M |
| 374 | snpA0000.snp | 920.55K |
| 375 | snpA0001.snp | 946.80K |
| 376 | snpA0002.snp | 946.80K |
| 377 | snpA0003.snp | 1.26M |
| 378 | snpA0004.snp | 2.57M |
| 379 | snpA0005.snp | 1.26M |
| 380 | snpA0006.snp | 2.08M |
| 381 | snpA0007.snp | 1.27M |
| 382 | snpA0008.snp | 2.41M |
| 383 | snpA0009.snp | 2.26M |
| 384 | snpA0010.snp | 1.27M |
| 385 | snpA0011.snp | 1.93M |
| 386 | snpA0012.snp | 1.93M |
| 387 | snpA0013.snp | 1.43M |
| 388 | snpA0014.snp | 1.99M |
| 389 | snpA0015.snp | 1.43M |
| 390 | snpA0016.snp | 2.16M |
| 391 | snpA0017.snp | 1.83M |
| 392 | snpA0018.snp | 1.27M |
| 393 | snpA0019.snp | 3.90M |
| 394 | snpA0020.snp | 3.95M |
| 395 | snpA0021.snp | 3.07M |
| 396 | snpA0022.snp | 1.60M |
| 397 | snpA0023.snp | 1.42M |
| 398 | snpA0024.snp | 1.27M |
| 399 | snpA0025.snp | 1.09M |
| 400 | snpA0026.snp | 4.56M |
| 401 | snpA0027.snp | 2.10M |
| 402 | snpA0028.snp | 1.61M |
| 403 | snpA0029.snp | 2.25M |
| 404 | snpA0030.snp | 1.43M |
| 405 | snpA0031.snp | 1.43M |
| 406 | snpA0032.snp | 1.83M |
| 407 | snpA0033.snp | 2.61M |
| 408 | snpA0034.snp | 2.81M |
| 409 | snpA0035.snp | 2.25M |
| 410 | snpA0036.snp | 1.43M |
| 411 | snpA0037.snp | 1.44M |
| 412 | snpA0038.snp | 2.66M |
| 413 | snpA0039.snp | 1.83M |
| 414 | snpA0040.snp | 1.28M |
| 415 | snpA0041.snp | 2.81M |
| 416 | snpA0042.snp | 1.61M |
| 417 | snpA0043.snp | 1.28M |
| 418 | snpA0044.snp | 1.83M |
| 419 | snpA0045.snp | 1.94M |
| 420 | snpA0046.snp | 2.16M |
| 421 | snpA0047.snp | 1.61M |
| 422 | snpA0048.snp | 1.61M |
| 423 | snpA0049.snp | 2.43M |
| 424 | snpA0050.snp | 1.28M |
| 425 | snpA0051.snp | 1.27M |
| 426 | snpA0052.snp | 1.83M |
| 427 | snpA0053.snp | 1.27M |
| 428 | snpA0054.snp | 1.60M |
| 429 | snpA0055.snp | 1.83M |
| 430 | snpA0056.snp | 986.09K |
| 431 | snpA0057.snp | 1.11M |
| 432 | snpA0058.snp | 2.81M |
| 433 | snpA0059.snp | 1.28M |
| 434 | snpA0060.snp | 1.61M |
| 435 | snpA0061.snp | 1.28M |
| 436 | snpA0062.snp | 2.27M |
| 437 | snpA0063.snp | 1.28M |
| 438 | snpA0064.snp | 1.28M |
| 439 | snpA0065.snp | 986.11K |
| 440 | snpA0066.snp | 1.14M |
| 441 | snpA0067.snp | 3.14M |
| 442 | snpA0068.snp | 1.83M |
| 443 | snpA0069.snp | 962.29K |
| 444 | snpA0070.snp | 1.91M |
| 445 | snpA0071.snp | 1.60M |
| 446 | snpA0072.snp | 1.60M |
| 447 | snpA0073.snp | 1.60M |
| 448 | snpA0074.snp | 2.08M |
| 449 | snpA0075.snp | 1.42M |
| 450 | snpA0076.snp | 1.42M |
| 451 | snpA0077.snp | 3.24M |
| 452 | snpA0078.snp | 2.08M |
| 453 | snpA0079.snp | 2.08M |
| 454 | snpA0080.snp | 1.42M |
| 455 | snpA0081.snp | 1.41M |
| 456 | tasksnap.bak | 2.50K |
| 457 | 亚砜精馏塔dyn.his | 2.62K |
| 458 | 亚砜精馏塔dyn.rep | 0B |
| 459 | AspenEconomic.ads | 221.31K |
| 460 | AspenEconomic.appdf | 2.13M |
| 461 | AspenEconomic.apw | 5.53M |
| 462 | AspenEconomic.bkp | 373.96K |
| 463 | AspenEconomic.def | 257B |
| 464 | AspenEconomic.for | 0B |
| 465 | AspenEconomic.his | 553.47K |
| 466 | readme.txt | 551B |
| 467 | Scenario1.izp | 1.64M |
| 468 | Scenario1.szp | 1.32M |
| 469 | 分析结果.xls | 264.50K |
| 470 | readme.txt | 545B |
| 471 | 隔板塔优化.docx | 960.36K |
| 472 | 隔板塔优化1.dxp | 12.04K |
| 473 | 隔板塔优化1.xlsx | 16.27K |
| 474 | 隔板塔优化2.dxp | 21.58K |
| 475 | 隔板塔优化2.xlsx | 18.94K |
| 476 | ADOBEPS4.DRV | 1.24M |
| 477 | Custdata.ini | 284B |
| 478 | dex_mkl.dll | 2.30M |
| 479 | DX8helpfile.chm | 5.05M |
| 480 | DX8logo.bmp | 52.62K |
| 481 | DX8splash.bmp | 900.05K |
| 482 | HHActiveX.dll | 460.00K |
| 483 | KEYLIB32.dll | 486.00K |
| 484 | libiomp5md.dll | 522.18K |
| 485 | machnm32.sys | 2.25K |
| 486 | PS5UI.DLL | 129.50K |
| 487 | PSCRIPT.DLL | 220.02K |
| 488 | PSCRIPT5.DLL | 453.50K |
| 489 | PSCRPTUI.DLL | 175.27K |
| 490 | Read_Me.htm | 37.21K |
| 491 | SEPS.PPD | 1.79K |
| 492 | SKCA32.dll | 111.50K |
| 493 | user.lf | 3.05K |
| 494 | 隔板塔优化1.dxp | 12.04K |
| 495 | 隔板塔优化2.dxp | 21.58K |
| 496 | Anova.dtd | 3.92K |
| 497 | BuildPower.dtd | 409B |
| 498 | CoefTable.dtd | 582B |
| 499 | ColumnInfo.dtd | 528B |
| 500 | CommandList.dtd | 99B |
| 501 | Constraints.dtd | 374B |
| 502 | CriteriaGraphic.dtd | 714B |
| 503 | CriteriaNumeric.dtd | 1.09K |
| 504 | DesignLayout.dtd | 633B |
| 505 | DEXXMLDoc.dtd | 8.01K |
| 506 | DEXXMLScript.dtd | 2.28K |
| 507 | Diagnostics.dtd | 1.10K |
| 508 | Effects.dtd | 488B |
| 509 | Evaluation.dtd | 3.48K |
| 510 | FitSummary.dtd | 2.30K |
| 511 | PointPrediction.dtd | 1.28K |
| 512 | Preferences.dtd | 145B |
| 513 | SolutionsNumeric.dtd | 1.71K |
| 514 | Summary.dtd | 1.30K |
| 515 | Battery.sim | 863B |
| 516 | Biker.dxp | 14.58K |
| 517 | DEX.log | 0B |
| 518 | Filtrate.dxp | 7.33K |
| 519 | Filtrate.sim | 887B |
| 520 | FishPatties.sim | 1.69K |
| 521 | Longley.dxp | 35.26K |
| 522 | Mix-a.dxp | 7.99K |
| 523 | Mix.dxp | 7.22K |
| 524 | Paper-a.dxp | 10.81K |
| 525 | Paper.dxp | 10.24K |
| 526 | Peel.dxp | 15.02K |
| 527 | Plasma.dxp | 12.79K |
| 528 | Purity.dxp | 7.73K |
| 529 | RSM-a.dxp | 13.28K |
| 530 | RSM.dxp | 11.28K |
| 531 | Taguchi-L16.dxp | 158.38K |
| 532 | fluentr0301.cas | 590.05M |
| 533 | fluent源文件截图.jpg | 10.89K |
| 534 | readme.txt | 917B |
| 535 | 反应器模拟温度图.jpg | 50.92K |
| 536 | readme.txt | 733B |
| 537 | 列管反应器模拟.mph | 69.76K |
| 538 | lieguanjifen.m | 365B |
| 539 | Readme.txt | 678B |
| 540 | Ahighlyefficientprocessfortransformingmethylmercaptanintohydrocarbons.pdf | 485.98K |
| 541 | Conversionofmethylmercaptanandmethanoltohydrocarbonsover.pdf | 662.06K |
| 542 | ZSM-5负载金属新型液化气脱硫剂的吸附与再生性能研究_刘新宇.pdf | 1.04M |
| 543 | KineticModeloftheReactionofMethanolwithHydrogenSulfide.pdf | 123.58K |
| 544 | NO_2氧化二甲基硫醚动力学研究_任海伦.pdf | 287.91K |
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