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茂名石化年总产45万吨环氧乙烷乙二醇项目初步设计（ID:2690035）
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| # | 文件名称 | 文件大小 |
|---|---|---|
| 1 | 17592244497993.zip | 399.71M |
| 2 | 1-致评委老师.doc | 26.50K |
| 3 | 10-安全预评价.doc | 2.07M |
| 4 | 2-作品清单.doc | 158.00K |
| 5 | 3-可行性报告.doc | 5.23M |
| 6 | 4-初步设计说明书.doc | 2.68M |
| 7 | 5-设计说明书附录.doc | 7.16M |
| 8 | 6-创新性说明书.doc | 921.50K |
| 9 | 7-工艺特点及财务分析表册.doc | 2.29M |
| 10 | 8-环境影响评估报告.doc | 1.15M |
| 11 | 9-经济分析.doc | 1.51M |
| 12 | designsummary.doc | 13.35M |
| 13 | 项目设计摘要.doc | 13.35M |
| 14 | 初步设计图册.pdf | 100.06M |
| 15 | 说明.txt | 334B |
| 16 | 说明.txt | 619B |
| 17 | Drawing2.dwl | 42B |
| 18 | Drawing2.dwl2 | 195B |
| 19 | PFD.dwg | 1.40M |
| 20 | PID.dwg | 1.31M |
| 21 | 厂区平面布置总图.dwg | 213.00K |
| 22 | 车间平面布置总图.dwg | 198.24K |
| 23 | EL0.000平面.dwg | 308.47K |
| 24 | EL12.000平面.dwg | 311.38K |
| 25 | EL15.000平面.dwg | 297.78K |
| 26 | EL6.000平面.dwg | 312.13K |
| 27 | 环氧乙烷反应及分离车间A-A立面图.dwg | 301.78K |
| 28 | 环氧乙烷反应及分离车间B-B立面图.dwg | 104.63K |
| 29 | EL0.000平面.dwg | 298.18K |
| 30 | EL12.000平面.dwg | 293.56K |
| 31 | EL6.000平面.dwg | 292.49K |
| 32 | 环氧乙烷精制车间A-A立面图.dwg | 307.63K |
| 33 | EL0.000平面.dwg | 276.21K |
| 34 | EL12.000平面.dwg | 269.01K |
| 35 | EL18.000平面.dwg | 272.29K |
| 36 | EL6.000平面.dwg | 279.71K |
| 37 | 乙二醇反应及分离车间A-A立面图.dwg | 284.59K |
| 38 | EL0.000平面.dwg | 312.58K |
| 39 | EL12.000平面.dwg | 298.53K |
| 40 | EL6.000平面.dwg | 301.12K |
| 41 | 乙二醇精制车间A-A立面图.dwg | 306.66K |
| 42 | 乙二醇精制车间B-B立面图.dwg | 111.47K |
| 43 | 01.dwg | 75.23K |
| 44 | 02.dwg | 76.35K |
| 45 | 03.dwg | 76.26K |
| 46 | 04.dwg | 81.48K |
| 47 | 05.dwg | 81.73K |
| 48 | 06.dwg | 78.47K |
| 49 | 07.dwg | 76.73K |
| 50 | 08.dwg | 77.44K |
| 51 | 09.dwg | 79.32K |
| 52 | 10.dwg | 77.79K |
| 53 | 01.dwg | 79.91K |
| 54 | 02.dwg | 81.92K |
| 55 | 03.dwg | 79.16K |
| 56 | 04.dwg | 83.67K |
| 57 | 05.dwg | 81.10K |
| 58 | 06.dwg | 80.60K |
| 59 | 07.dwg | 81.41K |
| 60 | 08.dwg | 82.82K |
| 61 | 09.dwg | 82.89K |
| 62 | 10.dwg | 78.51K |
| 63 | 01.dwg | 94.77K |
| 64 | 02.dwg | 85.39K |
| 65 | 03.dwg | 80.76K |
| 66 | 04.dwg | 84.89K |
| 67 | 05.dwg | 80.50K |
| 68 | 06.dwg | 96.83K |
| 69 | 07.dwg | 80.69K |
| 70 | 08.dwg | 81.26K |
| 71 | 08_recover.dwg | 66.13K |
| 72 | 09.dwg | 85.14K |
| 73 | 10.dwg | 78.85K |
| 74 | 01.dwg | 86.54K |
| 75 | 02.dwg | 75.82K |
| 76 | 03.dwg | 82.82K |
| 77 | 04.dwg | 85.54K |
| 78 | 05.dwg | 77.00K |
| 79 | 06.dwg | 81.88K |
| 80 | 07.dwg | 80.70K |
| 81 | 08.dwg | 80.57K |
| 82 | 09.dwg | 80.42K |
| 83 | 10.dwg | 74.32K |
| 84 | 乙二醇反应器R-405装配图.dwg | 175.90K |
| 85 | 环氧乙烷反应器R-101装配图.dwg | 348.16K |
| 86 | T-303塔盘图.dwg | 292.83K |
| 87 | T-303装配图.dwg | 167.24K |
| 88 | T-402塔盘图.dwg | 173.72K |
| 89 | T201装配图.dwg | 256.66K |
| 90 | T402装配图.dwg | 177.71K |
| 91 | 1.png | 35.32K |
| 92 | 2.png | 48.68K |
| 93 | 3.png | 80.96K |
| 94 | 4.png | 39.81K |
| 95 | 5.png | 50.29K |
| 96 | 6.png | 69.67K |
| 97 | 7.png | 40.87K |
| 98 | 1.环氧乙烷反应及分离车间-pdmax.dwg | 6.85M |
| 99 | 2.环氧乙烷精制车间-pdmax.dwg | 6.40M |
| 100 | 3.乙二醇反应及分离车间-pdmax.dwg | 2.64M |
| 101 | 4.乙二醇精制车间-pdmax.dwg | 6.95M |
| 102 | Drawing2.dwl | 42B |
| 103 | Drawing2.dwl2 | 195B |
| 104 | PFD.dwg | 1.40M |
| 105 | PID.dwg | 1.30M |
| 106 | 厂区平面布置总图.dwg | 236.78K |
| 107 | 车间平面布置总图.dwg | 227.06K |
| 108 | EL0.000平面.dwg | 345.59K |
| 109 | EL12.000平面.dwg | 347.09K |
| 110 | EL15.000平面.dwg | 328.84K |
| 111 | EL6.000平面.dwg | 348.34K |
| 112 | 环氧乙烷反应及分离车间A-A立面图.dwg | 332.41K |
| 113 | 环氧乙烷反应及分离车间B-B立面图.dwg | 131.34K |
| 114 | EL0.000平面.dwg | 330.09K |
| 115 | EL12.000平面.dwg | 324.81K |
| 116 | EL6.000平面.dwg | 322.63K |
| 117 | 环氧乙烷精制车间A-A立面图.dwg | 338.59K |
| 118 | EL0.000平面.dwg | 308.91K |
| 119 | EL12.000平面.dwg | 298.97K |
| 120 | EL18.000平面.dwg | 302.00K |
| 121 | EL6.000平面.dwg | 309.66K |
| 122 | 乙二醇反应及分离车间A-A立面图.dwg | 314.69K |
| 123 | EL0.000平面.dwg | 347.88K |
| 124 | EL12.000平面.dwg | 328.16K |
| 125 | EL6.000平面.dwg | 331.66K |
| 126 | 乙二醇精制车间A-A立面图.dwg | 337.59K |
| 127 | 乙二醇精制车间B-B立面图.dwg | 136.97K |
| 128 | 01.dwg | 75.76K |
| 129 | 02.dwg | 76.35K |
| 130 | 03.dwg | 76.60K |
| 131 | 04.dwg | 82.76K |
| 132 | 05.dwg | 81.38K |
| 133 | 06.dwg | 78.19K |
| 134 | 07.dwg | 79.32K |
| 135 | 08.dwg | 77.85K |
| 136 | 09.dwg | 82.07K |
| 137 | 10.dwg | 77.16K |
| 138 | 01.dwg | 79.91K |
| 139 | 02.dwg | 81.92K |
| 140 | 03.dwg | 79.16K |
| 141 | 04.dwg | 83.67K |
| 142 | 05.dwg | 81.10K |
| 143 | 06.dwg | 80.60K |
| 144 | 07.dwg | 81.41K |
| 145 | 08.dwg | 82.82K |
| 146 | 09.dwg | 82.89K |
| 147 | 10.dwg | 78.51K |
| 148 | 01.dwg | 94.77K |
| 149 | 02.dwg | 85.39K |
| 150 | 03.dwg | 80.76K |
| 151 | 04.dwg | 84.89K |
| 152 | 05.dwg | 80.50K |
| 153 | 06.dwg | 96.83K |
| 154 | 07.dwg | 80.69K |
| 155 | 08.dwg | 81.26K |
| 156 | 08_recover.dwg | 66.13K |
| 157 | 09.dwg | 85.14K |
| 158 | 10.dwg | 78.85K |
| 159 | 01.dwg | 86.54K |
| 160 | 02.dwg | 75.82K |
| 161 | 03.dwg | 82.82K |
| 162 | 04.dwg | 85.54K |
| 163 | 05.dwg | 77.00K |
| 164 | 06.dwg | 81.88K |
| 165 | 07.dwg | 80.70K |
| 166 | 08.dwg | 80.57K |
| 167 | 09.dwg | 80.42K |
| 168 | 10.dwg | 74.32K |
| 169 | 乙二醇反应器R-405装配图.dwg | 175.90K |
| 170 | 环氧乙烷反应器R-101装配图.dwg | 323.73K |
| 171 | T-303塔盘图.dwg | 292.83K |
| 172 | T-303装配图.dwg | 167.24K |
| 173 | T-402塔盘图.dwg | 173.72K |
| 174 | T201装配图.dwg | 256.66K |
| 175 | T402装配图.dwg | 177.71K |
| 176 | 1.png | 35.32K |
| 177 | 2.png | 48.68K |
| 178 | 3.png | 80.96K |
| 179 | 4.png | 39.81K |
| 180 | 5.png | 50.29K |
| 181 | 6.png | 69.67K |
| 182 | 7.png | 40.87K |
| 183 | 1.环氧乙烷反应及分离车间-pdmax.dwg | 6.84M |
| 184 | 2.环氧乙烷精制车间-pdmax.dwg | 6.38M |
| 185 | 3.乙二醇反应及分离车间-pdmax.dwg | 2.62M |
| 186 | 4.乙二醇精制车间-pdmax.dwg | 6.95M |
| 187 | MAXFILES.TXT | 2.59K |
| 188 | 厂区源文件.max | 504.17M |
| 189 | 背景.jpg | 2.55M |
| 190 | 说明.txt | 424B |
| 191 | 主干道.jpg | 3.87M |
| 192 | 办公楼.jpg | 7.42M |
| 193 | 厂区前视.jpg | 990.46K |
| 194 | 厂区大门.jpg | 4.00M |
| 195 | 厂区鸟瞰.jpg | 7.09M |
| 196 | 生活区.jpg | 6.71M |
| 197 | 罐区.jpg | 7.38M |
| 198 | 车间生产区1.jpg | 5.08M |
| 199 | 车间生产区2.jpg | 5.38M |
| 200 | 车间生产区3.jpg | 5.73M |
| 201 | 1242397_083945086_2.jpg | 132.24K |
| 202 | 171919llgfzofpdvwlalc0.jpg | 168.05K |
| 203 | 20110701111423984232.jpg | 5.89M |
| 204 | 20110701111423984517.jpg | 156.13K |
| 205 | 20110701111423984523.jpg | 157.90K |
| 206 | 20110701111423984598.jpg | 350.88K |
| 207 | 20110701111423984627.jpg | 938.68K |
| 208 | 20110701111423984717.jpg | 25.31K |
| 209 | 20110701111423984781.jpg | 173.25K |
| 210 | 20110701111423984816.jpg | 512.54K |
| 211 | 2011070111142398485.jpg | 32.68K |
| 212 | 20110701111423984976.jpg | 45.40K |
| 213 | 20130706041115812827.jpg | 175.88K |
| 214 | 20131024034039468102.png | 1.48M |
| 215 | 20131024034039468495.jpg | 130.58K |
| 216 | 20131024034039468861.jpg | 330.60K |
| 217 | 20131106101552906575.jpg | 115.67K |
| 218 | 20131106101552906685.jpg | 102.13K |
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| 220 | 20131227100807312137.jpg | 4.45K |
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| 222 | 20131227100807312216.jpg | 7.72K |
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| 224 | 20131227100807312270.jpg | 6.78K |
| 225 | 20131227100807312276.jpg | 48.70K |
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| 228 | 20131227100807312501.jpg | 6.78K |
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| 230 | 20131227100807312564.jpg | 15.88K |
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| 232 | 20131227100807312573.jpg | 23.11K |
| 233 | 20131227100807312595.jpg | 5.26K |
| 234 | 2013122710080731261.jpg | 44.79K |
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| 239 | 20131227100807312827.jpg | 30.53K |
| 240 | 20131227100807312848.jpg | 11.48K |
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| 245 | 20131227100807312948.jpg | 40.93K |
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| 249 | 20131227100807328348.jpg | 41.35K |
| 250 | 20131227100807328422.jpg | 35.62K |
| 251 | 20140103060551586359.jpg | 679.79K |
| 252 | 20140103060551586361.jpg | 104.93K |
| 253 | 20140103060551586499.jpg | 564.02K |
| 254 | 20140104061115390727.jpg | 6.98K |
| 255 | 20140104093952333198.jpg | 907.43K |
| 256 | 20140104093952333362.jpg | 128.74K |
| 257 | 20140104093952333608.jpg | 53.57K |
| 258 | 20140116031243014248.jpg | 19.81K |
| 259 | 20140116031243014370.jpg | 37.96K |
| 260 | 20140118042319843783.JPG | 137.06K |
| 261 | 20140118042319843998.JPG | 117.27K |
| 262 | 52141e98b1a62副本.jpg | 2.55M |
| 263 | 9D0DNEZN`XFX66319LAX.png | 19.78K |
| 264 | eaaeefe4-aff1-41fe-8bf1-ffb821766c55.jpg | 58.74K |
| 265 | LAKEREF.JPG | 127.79K |
| 266 | REJILLA1.JPG | 5.20K |
| 267 | RFY`CPG5MUBX3ZP}0WLTYQ.png | 7.24K |
| 268 | t01ad417a20c7439a08.jpg | 13.64K |
| 269 | t01e80dd39be8eaa947.jpg | 35.67K |
| 270 | 广砖77.jpg | 156.08K |
| 271 | 草皮.jpg | 1.06M |
| 272 | 说明.txt | 654B |
| 273 | E-204.EDR | 456.71K |
| 274 | E-210.EDR | 780.93K |
| 275 | E-306.EDR | 370.82K |
| 276 | E-410.EDR | 497.73K |
| 277 | E-505.EDR | 358.13K |
| 278 | E-208.EDR | 104.09K |
| 279 | E-209.EDR | 96.43K |
| 280 | E-211.EDR | 81.76K |
| 281 | E-213.EDR | 112.78K |
| 282 | E-214.EDR | 78.52K |
| 283 | E-404.EDR | 103.94K |
| 284 | E-405.EDR | 82.71K |
| 285 | E-415.EDR | 93.15K |
| 286 | E-205.EDR | 188.21K |
| 287 | E-215.EDR | 204.50K |
| 288 | E-216.EDR | 241.43K |
| 289 | E-403.EDR | 188.20K |
| 290 | E-407.EDR | 330.08K |
| 291 | E-408.EDR | 197.29K |
| 292 | E-409.EDR | 226.89K |
| 293 | E-412.EDR | 196.60K |
| 294 | E-413.EDR | 196.51K |
| 295 | E-414.EDR | 298.00K |
| 296 | E-503.EDR | 218.87K |
| 297 | E-507.EDR | 296.37K |
| 298 | E-101.EDR | 686.35K |
| 299 | E-102.EDR | 484.35K |
| 300 | E-201.EDR | 418.93K |
| 301 | E-202.EDR | 366.73K |
| 302 | E-203.EDR | 362.41K |
| 303 | E-206.EDR | 559.41K |
| 304 | E-207.EDR | 407.06K |
| 305 | E-212.EDR | 288.68K |
| 306 | E-217.EDR | 376.36K |
| 307 | E-218.EDR | 413.16K |
| 308 | E-219.EDR | 403.86K |
| 309 | E-301.EDR | 357.15K |
| 310 | E-302.EDR | 361.91K |
| 311 | E-303.EDR | 371.48K |
| 312 | E-304.EDR | 361.99K |
| 313 | E-305.EDR | 338.11K |
| 314 | E-307.EDR | 655.10K |
| 315 | E-308.EDR | 478.86K |
| 316 | E-401.EDR | 350.82K |
| 317 | E-402.EDR | 379.20K |
| 318 | E-406.EDR | 338.37K |
| 319 | E-411.EDR | 332.61K |
| 320 | E-501.EDR | 342.63K |
| 321 | E-502.EDR | 375.07K |
| 322 | E-504.EDR | 394.54K |
| 323 | E-506.EDR | 336.42K |
| 324 | E-508.EDR | 391.51K |
| 325 | E-509.EDR | 382.71K |
| 326 | 全流程换热网络优化.hch | 1.51M |
| 327 | 说明.txt | 690B |
| 328 | 全流程模拟-企业数据库.bkp | 2.17M |
| 329 | 全流程模拟-本地数据库.bkp | 2.17M |
| 330 | 说明.txt | 794B |
| 331 | YS_7型银催化剂上乙烯环氧化宏观动力学_梁汝军.pdf | 467.24K |
| 332 | 固载化离子液体催化环氧乙烷和二氧化碳合成碳酸乙烯酯_吴青海.pdf | 1.60M |
| 333 | 均相催化碳酸乙烯酯水解反应动力学.pdf | 177.17K |
| 334 | 乙二醇脱水塔T401回流比的优化.bkp | 223.74K |
| 335 | 乙二醇脱水塔T401塔板数优化.bkp | 159.73K |
| 336 | 乙二醇脱水塔T401进料位置的优化.bkp | 229.69K |
| 337 | 二氧化碳吸收塔T201吸收剂用量优化.bkp | 176.56K |
| 338 | 二氧化碳吸收塔T201塔板数优化.bkp | 180.43K |
| 339 | 说明.txt | 649B |
| 340 | T-303设计源文件.plc | 204.00K |
| 341 | T303导入水力学数据.xls | 37.00K |
| 342 | T303设计结果.docx | 49.26K |
| 343 | T303设计结果.xls | 179.50K |
| 344 | T402导入水力学数据.xlsx | 13.11K |
| 345 | T402设计源文件.plc | 200.00K |
| 346 | T402设计结果.docx | 48.93K |
| 347 | T402设计结果.xls | 179.50K |
| 348 | 投资估算和财务分析.xls | 80.00K |
| 349 | 说明.txt | 508B |
| 350 | Admin.mdb | 16.00K |
| 351 | CATA228.mdb | 16.00K |
| 352 | DESI344.mdb | 4.09M |
| 353 | PADD404.mdb | 16.00K |
| 354 | Admin.mdb | 16.00K |
| 355 | CATA299.mdb | 16.00K |
| 356 | DESI415.mdb | 3.53M |
| 357 | PADD335.mdb | 16.00K |
| 358 | Admin.mdb | 16.00K |
| 359 | CATA685.mdb | 16.00K |
| 360 | DESI519.mdb | 1.58M |
| 361 | PADD527.mdb | 16.00K |
| 362 | Admin.mdb | 16.00K |
| 363 | CATA609.mdb | 16.00K |
| 364 | DESI461.mdb | 3.42M |
| 365 | PADD533.mdb | 16.00K |
| 366 | 说明.txt | 351B |
| 367 | 1.png | 55.95K |
| 368 | 2.png | 38.28K |
| 369 | 3.png | 34.11K |
| 370 | 4.png | 34.01K |
| 371 | 5.png | 50.07K |
| 372 | 6.png | 39.03K |
| 373 | 典型泄漏事故模拟.rsm | 504B |
| 374 | 1.png | 29.59K |
| 375 | 2.png | 24.30K |
| 376 | 3.png | 17.58K |
| 377 | 4.png | 28.93K |
| 378 | 5.png | 18.03K |
| 379 | 池火事故模型预测.rsm | 197B |
| 380 | 1.png | 28.40K |
| 381 | 2.png | 27.71K |
| 382 | 3.png | 24.92K |
| 383 | 4.png | 26.57K |
| 384 | 5.png | 51.45K |
| 385 | 沸腾液体扩展蒸汽爆炸模型伤害范围.rsm | 211B |
| 386 | 1.png | 24.40K |
| 387 | 2.png | 25.50K |
| 388 | 3.png | 15.60K |
| 389 | 4.png | 22.22K |
| 390 | 5.png | 47.07K |
| 391 | 蒸汽云爆炸模型预测.rsm | 173B |
| 392 | 大气稳定度计算.png | 21.10K |
| 393 | 气体泄漏量计算.png | 27.58K |
| 394 | 气体泄漏量计算.rsm | 75B |
| 395 | 热量蒸发量计算.png | 25.45K |
| 396 | 热量蒸发量计算.rsm | 56B |
| 397 | 闪蒸量计算.png | 30.41K |
| 398 | 闪蒸量计算.rsm | 62B |
| 399 | 1.png | 55.38K |
| 400 | 2.png | 38.19K |
| 401 | 3.png | 33.55K |
| 402 | 4.png | 33.57K |
| 403 | 典型泄漏事故模拟.rsm | 511B |
| 404 | 1.png | 30.16K |
| 405 | 2.png | 23.77K |
| 406 | 3.png | 17.73K |
| 407 | 4.png | 29.40K |
| 408 | 5.png | 18.40K |
| 409 | 池火事故模型预测.rsm | 201B |
| 410 | 1.png | 30.20K |
| 411 | 2.png | 28.47K |
| 412 | 3.png | 23.30K |
| 413 | 4.png | 26.86K |
| 414 | 5.png | 51.50K |
| 415 | 沸腾液体扩展蒸汽爆炸模型预测.rsm | 215B |
| 416 | 1.png | 25.52K |
| 417 | 2.png | 24.92K |
| 418 | 3.png | 15.80K |
| 419 | 4.png | 21.60K |
| 420 | 5.png | 48.94K |
| 421 | 蒸汽云爆炸模型预测.rsm | 192B |
| 422 | Sulpak免安装包.rar | 5.55M |
| 423 | 说明.txt | 627B |
| 424 | Asycfilt.dll | 144.27K |
| 425 | COMCAT.DLL | 21.77K |
| 426 | COMDLG32.OCX | 137.00K |
| 427 | Msflxgrd.ocx | 238.51K |
| 428 | msvbvm60.dll | 1.32M |
| 429 | ntsm1.bmp | 95.17K |
| 430 | ntsm10.bmp | 64.99K |
| 431 | ntsm13.bmp | 73.62K |
| 432 | ntsm14.bmp | 67.19K |
| 433 | ntsm15.bmp | 39.26K |
| 434 | ntsm16.bmp | 128.01K |
| 435 | ntsm17.bmp | 64.36K |
| 436 | ntsm18.bmp | 63.79K |
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| 440 | ntsm4.bmp | 51.89K |
| 441 | ntsm5.bmp | 57.16K |
| 442 | ntsm6.bmp | 51.68K |
| 443 | ntsm7.bmp | 53.26K |
| 444 | ntsm8.bmp | 73.90K |
| 445 | ntsm9.bmp | 71.08K |
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| 447 | OLEPRO32.DLL | 160.27K |
| 448 | STDOLE2.TLB | 17.50K |
| 449 | SULPAK1.GID | 8.43K |
| 450 | SULPAK1.HLP | 805.80K |
| 451 | TABCTL32.OCX | 204.50K |
| 452 | VB6STKIT.DLL | 99.50K |
| 453 | 填料塔设计软件Sulpak.rar | 2.78M |
| 454 | Asycfilt.dll | 144.27K |
| 455 | COMCAT.DLL | 21.77K |
| 456 | COMDLG32.OCX | 137.00K |
| 457 | Msflxgrd.ocx | 238.51K |
| 458 | msvbvm60.dll | 1.32M |
| 459 | ntsm1.bmp | 95.17K |
| 460 | ntsm10.bmp | 64.99K |
| 461 | ntsm13.bmp | 73.62K |
| 462 | ntsm14.bmp | 67.19K |
| 463 | ntsm15.bmp | 39.26K |
| 464 | ntsm16.bmp | 128.01K |
| 465 | ntsm17.bmp | 64.36K |
| 466 | ntsm18.bmp | 63.79K |
| 467 | ntsm19.bmp | 42.93K |
| 468 | ntsm2.bmp | 55.16K |
| 469 | ntsm3.bmp | 54.04K |
| 470 | ntsm4.bmp | 51.89K |
| 471 | ntsm5.bmp | 57.16K |
| 472 | ntsm6.bmp | 51.68K |
| 473 | ntsm7.bmp | 53.26K |
| 474 | ntsm8.bmp | 73.90K |
| 475 | ntsm9.bmp | 71.08K |
| 476 | OLEAUT32.DLL | 584.27K |
| 477 | OLEPRO32.DLL | 160.27K |
| 478 | STDOLE2.TLB | 17.50K |
| 479 | sulpak1.GID | 8.43K |
| 480 | SULPAK1.HLP | 805.80K |
| 481 | TABCTL32.OCX | 204.50K |
| 482 | VB6STKIT.DLL | 99.50K |
| 483 | 导入水力学数据.xlsx | 12.50K |
| 484 | 示意图.png | 26.55K |
| 485 | 设计数据.xls | 11.80K |
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| 487 | 负荷性能图.png | 27.71K |
| 488 | 导入水力学数据.xlsx | 11.91K |
| 489 | 示意图.png | 26.04K |
| 490 | 设计数据.xls | 11.51K |
| 491 | 设计源文件.pak | 688B |
| 492 | 负荷性能图.png | 28.82K |
| 493 | 导入水力学数据.xlsx | 14.87K |
| 494 | 示意图.png | 23.74K |
| 495 | 设计数据.xls | 12.11K |
| 496 | 设计源文件.pak | 1.02K |
| 497 | 负荷性能图.png | 23.32K |
| 498 | 导入水力学数据.xlsx | 15.73K |
| 499 | 示意图.png | 26.47K |
| 500 | 设计数据.xls | 12.11K |
| 501 | 设计源文件.pak | 1.19K |
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| 503 | 导入水力学源文件.xlsx | 10.21K |
| 504 | 示意图.png | 19.04K |
| 505 | 设计数据.xls | 11.16K |
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| 508 | 导入水力学数据.xlsx | 10.35K |
| 509 | 示意图.png | 20.93K |
| 510 | 设计数据.xls | 11.15K |
| 511 | 设计源文件.pak | 512B |
| 512 | 负荷性能图.png | 29.05K |
| 513 | 导入水力学数据.xlsx | 12.10K |
| 514 | 示意图.png | 26.07K |
| 515 | 设计数据.xls | 11.78K |
| 516 | 设计源文件.pak | 864B |
| 517 | 负荷性能图.png | 28.92K |
| 518 | 导入水力学数据.xlsx | 18.11K |
| 519 | 示意图.png | 26.85K |
| 520 | 设计数据.xls | 12.15K |
| 521 | 设计源文件.pak | 1.02K |
| 522 | 负荷性能图.png | 28.07K |
| 523 | 导入水力学数据.xlsx | 14.63K |
| 524 | 示意图.png | 25.92K |
| 525 | 设计数据.xls | 11.80K |
| 526 | 设计源文件.pak | 864B |
| 527 | 负荷性能图.png | 26.65K |
| 528 | 说明.txt | 721B |
| 529 | T203上封头.doc | 34.79K |
| 530 | T203下封头.doc | 34.51K |
| 531 | T203强度校核源文件.cn2 | 30.20K |
| 532 | T203筒体强度校核结果.doc | 145.12K |
| 533 | T303上封头.doc | 66.50K |
| 534 | T303下封头.doc | 66.00K |
| 535 | T303强度校核源文件.cn2 | 30.20K |
| 536 | T303筒体强度校核结果.doc | 444.00K |
| 537 | 说明.txt | 371B |
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| 539 | P-203.docx | 288.06K |
| 540 | P-205.docx | 342.03K |
| 541 | P-206.docx | 312.60K |
| 542 | P-207.docx | 353.93K |
| 543 | P-301.docx | 329.73K |
| 544 | P-303.docx | 286.71K |
| 545 | P-304.docx | 316.20K |
| 546 | P-305.docx | 326.94K |
| 547 | P-306.docx | 342.15K |
| 548 | P-307.docx | 320.92K |
| 549 | P-401.docx | 319.33K |
| 550 | P-402.docx | 335.54K |
| 551 | P-403.docx | 331.31K |
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| 554 | P-406.docx | 331.10K |
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| 556 | P-502.docx | 332.53K |
| 557 | P-503.docx | 288.57K |
| 558 | P-504.docx | 290.95K |
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