登录注册
微信扫码登录
18万吨年高硫天然气净化尾气脱硫及深度开发项目初步设计（ID:2709529）
0.png)
0.png)
0.png)
0.png)
0.png)
| # | 文件名称 | 文件大小 |
|---|---|---|
| 1 | 17599168056232.rar | 271.50M |
| 2 | 说明.txt | 502B |
| 3 | ECHO-PFD.dwg | 415.55K |
| 4 | ECHO-物料平衡表.dwg | 1.14M |
| 5 | ECHO-PID.dwg | 544.24K |
| 6 | ECHO-厂区平面布置图.dwg | 164.95K |
| 7 | ECHO-一级克劳斯反应器R202装配图.dwg | 110.81K |
| 8 | ECHO-MDEA再生塔T-302-装配图2004.dwg | 228.88K |
| 9 | ECHO-MDEA再生塔T-302-装配图2014.dwg | 200.53K |
| 10 | 0301.DWG | 56.08K |
| 11 | 0302.DWG | 32.02K |
| 12 | 0303.DWG | 50.42K |
| 13 | 0304.DWG | 33.97K |
| 14 | 0305.DWG | 48.10K |
| 15 | 0306.DWG | 35.59K |
| 16 | 0307.DWG | 30.75K |
| 17 | 0308.DWG | 45.66K |
| 18 | 0309.DWG | 31.75K |
| 19 | 0310.DWG | 53.57K |
| 20 | 0311.DWG | 44.60K |
| 21 | 0312.DWG | 34.21K |
| 22 | 0313.DWG | 37.03K |
| 23 | 0314.DWG | 45.10K |
| 24 | 0315.DWG | 38.63K |
| 25 | 0316.DWG | 32.12K |
| 26 | 0317.DWG | 39.44K |
| 27 | 0318.DWG | 46.47K |
| 28 | 0319.DWG | 32.00K |
| 29 | 0320.DWG | 32.00K |
| 30 | 0321.DWG | 31.78K |
| 31 | 0322.DWG | 36.84K |
| 32 | 0323.DWG | 45.19K |
| 33 | 0324.DWG | 39.75K |
| 34 | 0325.DWG | 31.72K |
| 35 | 0326.DWG | 53.04K |
| 36 | 0327.DWG | 33.65K |
| 37 | 0328.DWG | 53.04K |
| 38 | 0329.DWG | 32.09K |
| 39 | 0330.DWG | 50.32K |
| 40 | 0331.DWG | 33.84K |
| 41 | 0332.DWG | 33.06K |
| 42 | 0333.DWG | 32.22K |
| 43 | 0334.DWG | 38.57K |
| 44 | 0335.DWG | 32.21K |
| 45 | 0336.DWG | 39.50K |
| 46 | 0337.DWG | 32.37K |
| 47 | 0338.DWG | 43.32K |
| 48 | 0339.DWG | 32.43K |
| 49 | 0340.DWG | 45.82K |
| 50 | 0341.DWG | 45.60K |
| 51 | 0342.DWG | 53.82K |
| 52 | ECHO-第三车间布置图.dwg | 275.00K |
| 53 | ECHO-PFD.pdf | 434.11K |
| 54 | ECHO-物料平衡表.pdf | 484.39K |
| 55 | 物料平衡表.xlsx | 51.72K |
| 56 | ECHO-PFD-01.pdf | 157.67K |
| 57 | ECHO-PFD-02.pdf | 33.19K |
| 58 | ECHO-PFD-03.pdf | 30.26K |
| 59 | ECHO-PFD-04.pdf | 31.49K |
| 60 | ECHO-PFD-05.pdf | 31.33K |
| 61 | ECHO-PFD-06.pdf | 26.63K |
| 62 | ECHO-PFD-07.pdf | 35.83K |
| 63 | ECHO-PFD-08.pdf | 34.29K |
| 64 | ECHO-PFD-09.pdf | 33.47K |
| 65 | ECHO-PFD-10.pdf | 26.78K |
| 66 | ECHO-物料平衡表-01.pdf | 73.80K |
| 67 | ECHO-物料平衡表-02.pdf | 70.41K |
| 68 | ECHO-物料平衡表-03.pdf | 70.51K |
| 69 | ECHO-物料平衡表-04.pdf | 69.96K |
| 70 | ECHO-物料平衡表-05.pdf | 69.92K |
| 71 | ECHO-物料平衡表-06.pdf | 70.02K |
| 72 | ECHO-物料平衡表-07.pdf | 67.45K |
| 73 | ECHO-PID.pdf | 600.58K |
| 74 | ECHO-PID-01.pdf | 156.80K |
| 75 | ECHO-PID-02.pdf | 54.55K |
| 76 | ECHO-PID-03.pdf | 49.22K |
| 77 | ECHO-PID-04.pdf | 51.21K |
| 78 | ECHO-PID-05.pdf | 60.56K |
| 79 | ECHO-PID-06.pdf | 47.89K |
| 80 | ECHO-PID-07.pdf | 36.80K |
| 81 | ECHO-PID-08.pdf | 56.77K |
| 82 | ECHO-PID-09.pdf | 56.16K |
| 83 | ECHO-PID-10.pdf | 37.23K |
| 84 | ECHO-厂区平面布置图.pdf | 148.84K |
| 85 | ECHO-一级克劳斯反应器R202装配图.pdf | 95.80K |
| 86 | ECHO-MDEA再生塔T-302-装配图-02.pdf | 191.94K |
| 87 | 0301.pdf | 19.91K |
| 88 | ECHO-第三车间布置图.pdf | 230.13K |
| 89 | ECHO-第三车间布置图-01.pdf | 81.93K |
| 90 | ECHO-第三车间布置图-02.pdf | 70.82K |
| 91 | ECHO-第三车间布置图-03.pdf | 44.11K |
| 92 | ECHO-第三车间布置图-04.pdf | 35.81K |
| 93 | ECHO-摘要.doc | 1.06M |
| 94 | ECHO-摘要.pdf | 1.07M |
| 95 | ECHOAbstract.doc | 999.00K |
| 96 | ECHOAbstract.pdf | 966.10K |
| 97 | ECHO-可行性报告.doc | 1.97M |
| 98 | ECHO-可行性报告.pdf | 2.33M |
| 99 | ECHO-初步设计说明书.doc | 11.35M |
| 100 | ECHO-初步设计说明书.pdf | 5.08M |
| 101 | HO-初步设计说明书.doc | 162B |
| 102 | ECHO-创新性说明书.doc | 1004.50K |
| 103 | ECHO-创新性说明书.pdf | 890.83K |
| 104 | HO-创新性说明书.doc | 162B |
| 105 | ECHO-工艺设备一览表.doc | 1.21M |
| 106 | ECHO-工艺设备一览表.pdf | 741.59K |
| 107 | ECHO-物料平衡计算书.doc | 2.26M |
| 108 | ECHO-物料平衡计算书.pdf | 1.82M |
| 109 | ECHO换热网络设计.doc | 1.31M |
| 110 | ECHO换热网络设计.pdf | 1.53M |
| 111 | ECHO-工艺设备设计.doc | 12.76M |
| 112 | ECHO-工艺设备设计.pdf | 7.54M |
| 113 | HO-工艺设备设计.doc | 162B |
| 114 | ECHO-经济分析.doc | 2.28M |
| 115 | ECHO-经济分析.pdf | 2.00M |
| 116 | ECHO安全预评价报告.doc | 4.98M |
| 117 | ECHO安全预评价报告.pdf | 2.56M |
| 118 | ECHO环境影响评价报告.doc | 2.53M |
| 119 | ECHO环境影响评价报告.pdf | 1.88M |
| 120 | 厂区.ls6 | 200.13M |
| 121 | 101.jpg | 492.02K |
| 122 | 102.jpg | 456.72K |
| 123 | 104.jpg | 601.58K |
| 124 | 105.jpg | 634.98K |
| 125 | 106.jpg | 524.86K |
| 126 | 第三车间.dwg | 3.14M |
| 127 | 第三车间有管道.dwg | 5.95M |
| 128 | CO2泄露模拟.alo | 4.73K |
| 129 | QQ截图20170706162059.png | 14.47K |
| 130 | QQ截图20170706162118.png | 33.71K |
| 131 | QQ截图20170706162129.png | 32.29K |
| 132 | MDEA泄露模拟.alo | 4.73K |
| 133 | QQ截图20170706182918.png | 15.15K |
| 134 | QQ截图20170706182928.png | 35.70K |
| 135 | QQ截图20170706182937.png | 33.29K |
| 136 | QQ截图20170706160514.png | 14.48K |
| 137 | QQ截图20170706160524.png | 34.54K |
| 138 | QQ截图20170706160532.png | 33.50K |
| 139 | 酸性气泄露模拟.alo | 4.73K |
| 140 | file.msh | 5.89M |
| 141 | RSL.cas | 6.14M |
| 142 | RSL.cgns | 12.91M |
| 143 | RSL.dat | 19.48M |
| 144 | RSL.wbpj | 136.45K |
| 145 | 说明.txt | 394B |
| 146 | .project_cache | 447B |
| 147 | designPoint.wbdp | 41.93K |
| 148 | FFF.agdb | 3.27M |
| 149 | FFF-1-00211.dat.gz | 12.08M |
| 150 | FFF-1-00442.dat.gz | 12.10M |
| 151 | FFF-1.cas.gz | 3.52M |
| 152 | FFF-2-00504.dat.gz | 12.10M |
| 153 | FFF-2.cas.gz | 3.52M |
| 154 | FFF.set | 13.59K |
| 155 | FFF.msh | 5.89M |
| 156 | FluidFlowFluent.cst | 36.03K |
| 157 | FFF.mshdb | 1.96M |
| 158 | 说明.txt | 468B |
| 159 | 换热网络总.hch | 3.33M |
| 160 | 说明.txt | 492B |
| 161 | E101.bkp | 410.48K |
| 162 | E101.EDR | 437.85K |
| 163 | E101设计规定说明书.DOC | 420.00K |
| 164 | E101设计规定说明书.pdf | 483.69K |
| 165 | E102.bkp | 317.85K |
| 166 | E102.EDR | 461.96K |
| 167 | E102设计规定说明书.DOC | 430.00K |
| 168 | E102设计规定说明书.pdf | 522.88K |
| 169 | E103.bkp | 318.28K |
| 170 | E103.EDR | 582.89K |
| 171 | E103设计规定说明书.DOC | 428.00K |
| 172 | E103设计规定说明书.pdf | 518.62K |
| 173 | E104.bkp | 318.05K |
| 174 | E104.EDR | 538.31K |
| 175 | E104设计规定说明书.DOC | 429.50K |
| 176 | E104设计规定说明书.pdf | 519.91K |
| 177 | E201.bkp | 413.18K |
| 178 | E201.EDR | 414.87K |
| 179 | E201设计规定说明书.DOC | 421.00K |
| 180 | E201设计规定说明书.pdf | 492.34K |
| 181 | E202.bkp | 400.78K |
| 182 | E202.EDR | 450.72K |
| 183 | E202设计规定说明书.DOC | 417.50K |
| 184 | E202设计规定说明书.pdf | 483.30K |
| 185 | E203.bkp | 412.66K |
| 186 | E203.EDR | 367.87K |
| 187 | E203设计规定说明书.DOC | 418.00K |
| 188 | E203设计规定说明书.pdf | 482.87K |
| 189 | E204.bkp | 409.23K |
| 190 | E204.EDR | 397.50K |
| 191 | E204设计规定说明书.DOC | 427.00K |
| 192 | E204设计规定说明书.pdf | 517.32K |
| 193 | E205.bkp | 401.87K |
| 194 | E205.EDR | 474.49K |
| 195 | E205设计规定说明书.DOC | 428.00K |
| 196 | E205设计规定说明书.pdf | 519.18K |
| 197 | E206.bkp | 409.54K |
| 198 | E206.EDR | 400.90K |
| 199 | E206设计规定说明书.DOC | 428.00K |
| 200 | E206设计规定说明书.pdf | 517.12K |
| 201 | E207.bkp | 401.91K |
| 202 | E207.EDR | 466.33K |
| 203 | E207设计规定说明书.DOC | 423.00K |
| 204 | E207设计规定说明书.pdf | 504.98K |
| 205 | E208.bkp | 400.87K |
| 206 | E208.EDR | 473.57K |
| 207 | E208设计规定说明书.DOC | 427.50K |
| 208 | E208设计规定说明书.pdf | 519.00K |
| 209 | E209.bkp | 401.45K |
| 210 | E209.EDR | 414.62K |
| 211 | E209设计规定说明书.DOC | 421.50K |
| 212 | E209设计规定说明书.pdf | 504.25K |
| 213 | E210.bkp | 401.33K |
| 214 | E210.EDR | 429.67K |
| 215 | E210设计规定说明书.DOC | 423.50K |
| 216 | E210设计规定说明书.pdf | 500.04K |
| 217 | E211.bkp | 352.24K |
| 218 | E211.EDR | 389.28K |
| 219 | E211设计规定说明书.DOC | 412.50K |
| 220 | E211设计规定说明书.pdf | 455.97K |
| 221 | E301.bkp | 337.41K |
| 222 | E301.EDR | 535.07K |
| 223 | E301设计规定说明书.DOC | 418.50K |
| 224 | E301设计规定说明书.pdf | 482.66K |
| 225 | E302.bkp | 330.98K |
| 226 | E302.EDR | 406.77K |
| 227 | E302设计规定说明书.DOC | 412.00K |
| 228 | E302设计规定说明书.pdf | 455.72K |
| 229 | E303.bkp | 334.05K |
| 230 | E303.EDR | 371.98K |
| 231 | E303设计规定说明书.DOC | 409.00K |
| 232 | E303设计规定说明书.pdf | 447.23K |
| 233 | E304.bkp | 329.31K |
| 234 | E304.EDR | 369.77K |
| 235 | E304设计规定说明书.DOC | 407.50K |
| 236 | E304设计规定说明书.pdf | 447.75K |
| 237 | E305.bkp | 331.50K |
| 238 | E305.EDR | 390.96K |
| 239 | E305设计规定说明书.DOC | 410.50K |
| 240 | E305设计规定说明书.pdf | 446.53K |
| 241 | E401.bkp | 401.61K |
| 242 | E401.EDR | 294.89K |
| 243 | E401设计规定说明书.DOC | 408.00K |
| 244 | E401设计规定说明书.pdf | 443.55K |
| 245 | E402.bkp | 384.88K |
| 246 | E402.EDR | 328.34K |
| 247 | E402设计规定说明书.DOC | 409.00K |
| 248 | E402设计规定说明书.pdf | 441.08K |
| 249 | E403.bkp | 384.91K |
| 250 | E403.EDR | 348.24K |
| 251 | E403设计规定说明书.DOC | 409.00K |
| 252 | E403设计规定说明书.pdf | 442.88K |
| 253 | E404.bkp | 385.26K |
| 254 | E404.EDR | 394.56K |
| 255 | E404设计规定说明书.DOC | 408.50K |
| 256 | E404设计规定说明书.pdf | 442.22K |
| 257 | E501.bkp | 401.53K |
| 258 | E501.EDR | 327.23K |
| 259 | E501设计规定说明书.DOC | 411.50K |
| 260 | E501设计规定说明书.pdf | 455.21K |
| 261 | condenserA.xls | 165.50K |
| 262 | condenserE.xls | 186.50K |
| 263 | 原始全流程（带换热热泵.bkp | 2.00M |
| 264 | 说明.txt | 695B |
| 265 | condenserA.xls | 166.00K |
| 266 | condenserE.xls | 181.00K |
| 267 | 克劳斯.bkp | 1.08M |
| 268 | condenserA.xls | 166.00K |
| 269 | condenserE.xls | 181.00K |
| 270 | 尾气处理.bkp | 817.49K |
| 271 | condenserA.xls | 161.00K |
| 272 | condenserE.xls | 181.00K |
| 273 | 硫精制及聚合.bkp | 643.43K |
| 274 | 预处理.bkp | 704.13K |
| 275 | AdetailedreactionmechanismforhydrogenproductionviahydrogensulphideH2Sthermolysisandoxidation.pdf | 1.58M |
| 276 | Ahigh-temperatureexperimentalandmodelingstudyof.pdf | 202.71K |
| 277 | ASPEN_PLUS_102623463B0_物性方法和模型.pdf | 1.62M |
| 278 | CS2FormationintheClausReactionFurnaceAKineticStudyof.pdf | 193.26K |
| 279 | HydrodynamicandkineticmodellingofcirculatingfluidizedbedreactorsappliedtoamodifiedClausplant.pdf | 904.28K |
| 280 | Kineticmodelfornaturalgasreburning.pdf | 845.64K |
| 281 | KineticmodelingandoptimizationofClausreactionfurnace.pdf | 881.60K |
| 282 | Kineticmodelingofthehydrolysisofcarbonylsulfidecatalyzedbyeithertitaniaoralumina.pdf | 836.02K |
| 283 | Kineticmodelingofthethermaldecompositionofammonia.pdf | 6.04M |
| 284 | KineticmodellingofacommercialsulfurrecoveryunitbasedonClausstraightthroughprocess_Comparisonwithequilibriummodel.pdf | 2.76M |
| 285 | Kineticmodellingofafluidizedbedclausplant.pdf | 650.03K |
| 286 | Kineticsofthermalnoncatalyticdecompositionofhydrogensulphide.pdf | 680.20K |
| 287 | LS_941H_2S选择性氧化制硫催化剂的研制_唐昭峥.pdf | 131.68K |
| 288 | LS_941硫化氢选择性氧化超级克劳斯催化剂的研究_殷树青.pdf | 304.71K |
| 289 | LS_951Q尾气加氢催化剂在镇海炼化的工业应用_师彦俊.pdf | 523.73K |
| 290 | LS_951T新型Claus尾气加氢催化剂的工业应用_刘爱华.pdf | 121.24K |
| 291 | LS_951T硫磺回收尾气加氢催化剂的工业应用_路蒙蒙.pdf | 234.21K |
| 292 | LS_951T硫磺尾气加氢催化剂在辽河石化公司的工业应用_刘龙军.pdf | 255.10K |
| 293 | LS_951催化剂Claus反应尾气加氢转化动力学研究_张孔远.pdf | 327.49K |
| 294 | LS_951催化剂在Claus尾气加氢装置上的应用_刘爱华.pdf | 103.79K |
| 295 | Modelingandmulti-optimizationofthermalsectionofClausprocess.pdf | 1.40M |
| 296 | NewexperimentaldataandkineticrateexpressionfortheClausreaction.pdf | 249.59K |
| 297 | NewMicrosoftWordDocument.docx | 11.73K |
| 298 | RecoveryofSulfwrfromSourAcid.pdf | 1.78M |
| 299 | RigorousKineticModelingandOptimizationStudyofaModified.pdf | 2.24M |
| 300 | SafetyassessmentapproachofhazardandoperabilityHAZOPfor.pdf | 773.76K |
| 301 | SimulationofFlowandChemicalReactionsinaClausSulfur.pdf | 457.01K |
| 302 | SulfurRecoveryUnits_AdaptiveSimulationandModelValidationonan.pdf | 1.26M |
| 303 | SulphurcondensationinfluenceinClauscatalyst.pdf | 171.57K |
| 304 | ThermalConvectioninanOscillatingCubeatVariousFrequenciesandAmplitudes.pdf | 1.09M |
| 305 | Thermo-kineticmodelingandoptimizationofthesulfurrecoveryunitthermalstage.pdf | 2.57M |
| 306 | Three-dimensionalCFDsimulationofindustrialClausreactors.pdf | 1.49M |
| 307 | TYTS_2000脱硫剂用于天然气脱硫可行性的探讨_李正西.pdf | 300.94K |
| 308 | variationsofexperimentalconditionsandfortheinfluence.pdf | 163.93K |
| 309 | 【书】克劳斯法硫磺回收工艺技术.pdf | 17.10M |
| 310 | 不溶性硫磺制备过程的机理研究.pdf | 1.92M |
| 311 | 不溶性硫黄的制备技术_欧阳福生.pdf | 382.15K |
| 312 | 低温克劳斯硫磺回收的改良工艺_曾彬洋.pdf | 273.98K |
| 313 | 低温法制备不溶性硫磺技术研究_焦安喆.caj | 4.00M |
| 314 | 含氨煤气再燃脱硝反应的化学动力学模拟_卢志民.pdf | 847.85K |
| 315 | 含硫天然气净化厂硫化氢泄漏分析及对策_高少华.pdf | 815.64K |
| 316 | 国产超级克劳斯催化剂的工业应用_陈昌介.pdf | 1.72M |
| 317 | 基于AspenPlus的超级Claus硫磺回收SSR尾气处理工艺模拟.pdf | 1.40M |
| 318 | 基于ASPEN的PTFE聚合流程模拟与分析_曹琴.caj | 9.12M |
| 319 | 基于密度泛函的硫黄S8开环裂解机理.pdf | 327.79K |
| 320 | 如何使用ASPENTM软件模拟完成精馏的设计和控制[全本][马后炮化工][水印].pdf | 26.31M |
| 321 | 川东北某酸性气成分.jpg | 126.46K |
| 322 | 川东北罗家寨飞仙关组气藏成藏过程及聚集效率.pdf | 217.15K |
| 323 | 炼厂气MDEA脱硫系统模拟与优化.pdf | 2.65M |
| 324 | 环型硫分子的从头算及其应用.pdf | 406.33K |
| 325 | 硫回收装置主燃烧炉设计中的几个问题_张小康.pdf | 296.35K |
| 326 | 硫磺制酸装置液硫精制采用两次过滤的实践_余琴花.pdf | 471.69K |
| 327 | 硫磺回收装置主燃烧炉运行问题探讨及燃烧器改造技术总结_张有军.pdf | 241.27K |
| 328 | 硫磺回收装置酸性气燃烧炉分析_韩桂兰.pdf | 110.03K |
| 329 | 超级克劳斯工艺的五年操作经验.pdf | 184.32K |
| 330 | 超级克劳斯硫磺回收技术及选择性氧化催化剂_罗守坤.pdf | 294.44K |
| 331 | 酸性气回收工艺过程研究_邢海燕.caj | 2.61M |
| 332 | 采用催化聚合法制取不溶性硫的研究_童仕唐.pdf | 215.71K |
| 333 | 高含硫天然气净化厂总硫回收率的主要影响因素探讨_马永波.pdf | 221.77K |
| 334 | 高含硫天然气净化厂设计特点.pdf | 301.95K |
| 335 | 高酸性天然气净化厂设计基本要求.pdf | 303.44K |
| 336 | 一级克劳斯反应器优化.bkp | 391.73K |
| 337 | 二级克劳斯超优克劳斯反应器优化.bkp | 439.63K |
| 338 | 加氢反应器优化.bkp | 386.98K |
| 339 | 超级克劳斯反应器优化.bkp | 374.41K |
| 340 | 回流比优化.bkp | 412.17K |
| 341 | 塔板数优化.bkp | 343.43K |
| 342 | 进料板优化.bkp | 401.58K |
| 343 | T302-rr-nstage.py | 2.93K |
| 344 | T302-rr-nstage.txt | 2.96K |
| 345 | T302-rr-nstage.xlsx | 21.73K |
| 346 | 回流比塔板数优化.bkp | 414.64K |
| 347 | 进料板优化.bkp | 416.56K |
| 348 | T101塔设计.bkp | 439.89K |
| 349 | T301塔设计.bkp | 535.11K |
| 350 | T302塔设计.bkp | 424.80K |
| 351 | 说明.txt | 516B |
| 352 | ECHO-PFD.dwg | 415.55K |
| 353 | ECHO-物料平衡表.dwg | 1.14M |
| 354 | ECHO-PID.dwg | 544.24K |
| 355 | ECHO-厂区平面布置图.dwg | 164.95K |
| 356 | ECHO-一级克劳斯反应器R202装配图.dwg | 110.81K |
| 357 | ECHO-MDEA再生塔T-302-装配图2004.dwg | 228.88K |
| 358 | ECHO-MDEA再生塔T-302-装配图2014.dwg | 200.53K |
| 359 | 0301.DWG | 56.08K |
| 360 | 0302.DWG | 32.02K |
| 361 | 0303.DWG | 50.42K |
| 362 | 0304.DWG | 33.97K |
| 363 | 0305.DWG | 48.10K |
| 364 | 0306.DWG | 35.59K |
| 365 | 0307.DWG | 30.75K |
| 366 | 0308.DWG | 45.66K |
| 367 | 0309.DWG | 31.75K |
| 368 | 0310.DWG | 53.57K |
| 369 | 0311.DWG | 44.60K |
| 370 | 0312.DWG | 34.21K |
| 371 | 0313.DWG | 37.03K |
| 372 | 0314.DWG | 45.10K |
| 373 | 0315.DWG | 38.63K |
| 374 | 0316.DWG | 32.12K |
| 375 | 0317.DWG | 39.44K |
| 376 | 0318.DWG | 46.47K |
| 377 | 0319.DWG | 32.00K |
| 378 | 0320.DWG | 32.00K |
| 379 | 0321.DWG | 31.78K |
| 380 | 0322.DWG | 36.84K |
| 381 | 0323.DWG | 45.19K |
| 382 | 0324.DWG | 39.75K |
| 383 | 0325.DWG | 31.72K |
| 384 | 0326.DWG | 53.04K |
| 385 | 0327.DWG | 33.65K |
| 386 | 0328.DWG | 53.04K |
| 387 | 0329.DWG | 32.09K |
| 388 | 0330.DWG | 50.32K |
| 389 | 0331.DWG | 33.84K |
| 390 | 0332.DWG | 33.06K |
| 391 | 0333.DWG | 32.22K |
| 392 | 0334.DWG | 38.57K |
| 393 | 0335.DWG | 32.21K |
| 394 | 0336.DWG | 39.50K |
| 395 | 0337.DWG | 32.37K |
| 396 | 0338.DWG | 43.32K |
| 397 | 0339.DWG | 32.43K |
| 398 | 0340.DWG | 45.82K |
| 399 | 0341.DWG | 45.60K |
| 400 | 0342.DWG | 53.82K |
| 401 | ECHO-第三车间布置图.dwg | 275.00K |
| 402 | 噪音模拟.ein | 27.26K |
| 403 | 捕获.JPG | 118.97K |
| 404 | 捕获.PNG | 455.35K |
| 405 | 捕获1.PNG | 24.69K |
| 406 | 捕获2.PNG | 27.33K |
| 407 | 捕获3.PNG | 20.84K |
| 408 | 说明.txt | 443B |
| 409 | T101提馏段.kgt | 1.34K |
| 410 | t101提馏段.pdf | 19.31K |
| 411 | T101精馏段.kgt | 1.44K |
| 412 | t101精馏段.pdf | 19.36K |
| 413 | T302提馏段.kgt | 1.35K |
| 414 | t302提馏段.pdf | 20.75K |
| 415 | T302精馏段.kgt | 1.43K |
| 416 | t302精馏段.pdf | 20.75K |
| 417 | 说明.txt | 477B |
| 418 | mdea.rsm | 183B |
| 419 | mdea1.jpg | 30.09K |
| 420 | mdea2.jpg | 34.26K |
| 421 | mdea3.jpg | 28.44K |
| 422 | mdea4.jpg | 39.75K |
| 423 | h2s.rsm | 181B |
| 424 | h2s1.jpg | 29.46K |
| 425 | h2s2.jpg | 34.35K |
| 426 | h2s3.jpg | 27.16K |
| 427 | h2s4.jpg | 38.97K |
| 428 | 1.pdf | 203.75K |
| 429 | BOTTOM1.pdf | 182.74K |
| 430 | BOTTOM2.pdf | 181.96K |
| 431 | T301.pak | 688B |
| 432 | T301SULPAK.zip | 918.51K |
| 433 | T301示意图.pdf | 183.06K |
| 434 | T301装配图.dxf | 15.31K |
| 435 | TOP1.pdf | 182.74K |
| 436 | TOP2.pdf | 181.96K |
| 437 | 1.pdf | 203.75K |
| 438 | BOTTOM1.pdf | 182.74K |
| 439 | BOTTOM2.pdf | 181.96K |
| 440 | T301.pak | 688B |
| 441 | T301装配图.dxf | 15.31K |
| 442 | TOP1.pdf | 182.74K |
| 443 | TOP2.pdf | 181.96K |
| 444 | T101.cn2 | 30.20K |
| 445 | T101设备校核20170811.doc | 654.50K |
| 446 | T301.cn2 | 30.20K |
| 447 | T301设备校核20170811.doc | 669.50K |
| 448 | T302.cn2 | 30.20K |
| 449 | T302设备校核.doc | 701.50K |
| 450 | R202.ht2 | 22.62K |
| 451 | R202设备设计.doc | 406.00K |
| 452 | 右封头报告.doc | 66.00K |
| 453 | 左封头报告.doc | 66.50K |
| 454 | 筒体报告.doc | 62.50K |
| 455 | R203.ht2 | 22.62K |
| 456 | R203设备设计.doc | 406.00K |
| 457 | 右封头报告.doc | 66.00K |
| 458 | 左封头报告.doc | 66.00K |
| 459 | 筒体报告.doc | 62.50K |
| 460 | R204.ht2 | 22.62K |
| 461 | R204设备设计.doc | 406.00K |
| 462 | 右封头报告.doc | 66.00K |
| 463 | 左封头报告.doc | 66.00K |
| 464 | 筒体报告.doc | 62.50K |
| 465 | R205.ht2 | 22.62K |
| 466 | R205设备设计.doc | 406.00K |
| 467 | 右封头.doc | 66.00K |
| 468 | 左封头.doc | 66.00K |
| 469 | 筒体报告.doc | 62.50K |
| 470 | R501.ra2 | 23.24K |
| 471 | R501设备设计.doc | 396.00K |
| 472 | 夹套封头报告.doc | 66.00K |
| 473 | 夹套筒体报告.doc | 62.50K |
| 474 | 封头报告.doc | 57.50K |
| 475 | 筒体报告.doc | 103.00K |
| 476 | 设备法兰报告.doc | 241.50K |
| 477 | 01换热器校核.doc | 162B |
| 478 | E301.fx2 | 24.00K |
| 479 | E301换热器校核.doc | 2.01M |
| 480 | E302.fx2 | 24.00K |
| 481 | E302设备校核.doc | 1.44M |
| 482 | 气包.doc | 166.50K |
| 483 | 气包.ra2 | 23.24K |
| 484 | 气包.rar | 28.78K |
| 485 | 气包.doc | 166.50K |
| 486 | 气包.ra2 | 23.24K |
此图纸下载需要520金币
立即下载
发布者
静
创作: 12900
粉丝: 6
加入时间：2025-05-27
模型信息
图纸格式：dwg,pdf,dxf
文件大小：278.01M
所需金币：520
上传时间：2025-10-08 17:51:51
是否可编辑：可修改，包括参数
版本：AutoCAD 2013
标签
图纸简介
版权说明
用户在本站上传的作品如侵犯到您的权益，请与本站管理员联系删除。用户在本站下载的原创作品，只拥有作品的使用权，著作权归原作者所有，未经合法授权，用户不得以任何形式发布、传播、复制、转售该作品。
作者其它图纸 查看更多
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
猜你喜欢
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
0.png)
QQ在线客服
官方QQ群
