中海壳牌年产5万吨异丙醇项目初步设计(ID:2695937)
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| # | 文件名称 | 文件大小 |
|---|---|---|
| 1 | 作品对应表.pdf | 847.21K |
| 2 | 说明.txt | 1.45K |
| 3 | 0-项目摘要.docx | 2.12M |
| 4 | 00-作品对应表.docx | 753.15K |
| 5 | 1-可行性报告.docx | 2.76M |
| 6 | 2-初步设计说明书.docx | 7.51M |
| 7 | 3-1塔设备设计说明书.docx | 1.93M |
| 8 | 3-2反应器设计说明书.docx | 3.02M |
| 9 | 3-3换热器设计说明书.docx | 3.00M |
| 10 | 3-4其他设备设计及选型说明书.docx | 3.23M |
| 11 | 4-创新性说明书.docx | 3.54M |
| 12 | 5-经济分析.docx | 1.67M |
| 13 | 6-安全评价报告.docx | 4.74M |
| 14 | 7-能量集成及换热网络设计.docx | 1.34M |
| 15 | 8-环境评价报告.docx | 2.18M |
| 16 | 附录1-物料平衡书.docx | 956.64K |
| 17 | 附录10-T0201脱轻塔优化.docx | 802.05K |
| 18 | 附录11-膜分离装置设计说明书.docx | 1.82M |
| 19 | 附录12-泄露扩散模拟.docx | 4.03M |
| 20 | 附录2-能量平衡书.docx | 816.20K |
| 21 | 附录3-设备设计及选型一览表.docx | 843.00K |
| 22 | 附录4-管道选型一览表.docx | 814.22K |
| 23 | 附录5-HAZOP分析报告书.docx | 8.58M |
| 24 | 附录6-物质MSDS一览表.docx | 854.49K |
| 25 | 附录7-公用工程供应协议及方案.docx | 729.83K |
| 26 | 附录8-绿色发展2025指标说明书.docx | 746.28K |
| 27 | 附录9-动力学说明.docx | 1.22M |
| 28 | 设计图纸集.pdf | 19.76M |
| 29 | 1-物料工艺流程图(PFD).dwg | 1.86M |
| 30 | 1-物料工艺流程图(PFD).pdf | 1.18M |
| 31 | 工艺物料流程图PFD说明.pdf | 91.71K |
| 32 | 2-管道及仪表流程图(PID).dwg | 2.59M |
| 33 | 2-管道及仪表流程图(PID).pdf | 1.97M |
| 34 | 管道及仪表流程图PID说明.pdf | 160.77K |
| 35 | 3-异丙醇精制车间平立面布置图.dwg | 795.74K |
| 36 | 3-异丙醇精制车间平立面布置图.pdf | 746.34K |
| 37 | 4-厂区总平面布置图.pdf | 1.42M |
| 38 | 4-厂区总平面布置图(2004版).dwg | 1.16M |
| 39 | 厂区总平面布置图说明.pdf | 99.19K |
| 40 | 5-典型设备工艺条件图图集.pdf | 533.52K |
| 41 | 异丙醇冷却器E0203(2004版).dwg | 340.20K |
| 42 | 异丙醇合成反应器R0101(2004版).dwg | 326.24K |
| 43 | 脱轻塔T0201(2004版).dwg | 349.33K |
| 44 | 6-车间三维布置图.pdf | 5.30M |
| 45 | 7-管道轴侧图.pdf | 294.10K |
| 46 | 1.全流程模拟(不含换热,不含节能技术).bkp | 1.43M |
| 47 | 2.全流程模拟(不含换热,含节能技术).bkp | 2.84M |
| 48 | 3.全流程模拟(含换热,含节能技术).bkp | 2.98M |
| 49 | Aspen全流程模拟运行视频.mp4 | 2.54M |
| 50 | Aspen模拟说明.docx | 382.13K |
| 51 | Aspen模拟说明.pdf | 381.50K |
| 52 | 炉火醇清厂区三维源文件.skp | 45.66M |
| 53 | 噪声分析图1.JPG | 231.04K |
| 54 | 噪声分析结果.EMF | 1.38M |
| 55 | 背景图.JPG | 140.53K |
| 56 | 背景图形文件.BIF | 113B |
| 57 | 6-车间三维配管源文件.dwg | 6.47M |
| 58 | 6-车间三维配管源文件录制视频.mp4 | 33.84M |
| 59 | 说明.txt | 930B |
| 60 | C0201.dwg | 441.24K |
| 61 | Drawing1.dwl | 44B |
| 62 | Drawing1.dwl2 | 197B |
| 63 | T0201.dwg | 679.25K |
| 64 | T0202.dwg | 675.40K |
| 65 | T0203.dwg | 655.25K |
| 66 | E0201.dwg | 121.92K |
| 67 | E0202.dwg | 475.89K |
| 68 | E0203.dwg | 506.19K |
| 69 | E0204.dwg | 105.00K |
| 70 | E0205.dwg | 426.55K |
| 71 | E0206.dwg | 483.01K |
| 72 | E0207.dwg | 426.64K |
| 73 | E0208.dwg | 477.80K |
| 74 | E0209.dwg | 61.31K |
| 75 | 1-P0209A.dwg | 457.77K |
| 76 | 1-P0209B.dwg | 456.77K |
| 77 | 10-P0207A.dwg | 457.34K |
| 78 | 10-P0207B.dwg | 455.24K |
| 79 | 2-P0201A.dwg | 455.11K |
| 80 | 2-P0201B.dwg | 456.68K |
| 81 | 3-P0204A.dwg | 455.23K |
| 82 | 3-P0204B.dwg | 456.65K |
| 83 | 4-P0205A.dwg | 457.59K |
| 84 | 4-P0205B.dwg | 458.18K |
| 85 | 5-P0210A.dwg | 457.56K |
| 86 | 5-P0210B.dwg | 458.00K |
| 87 | 6-P0203A.dwg | 457.81K |
| 88 | 6-P0203B.dwg | 456.11K |
| 89 | 7-P0202A.dwg | 456.40K |
| 90 | 7-P0202B.dwg | 456.39K |
| 91 | 8-P0206A.dwg | 457.09K |
| 92 | 8-P0206B.dwg | 456.40K |
| 93 | 9-P0208A.dwg | 457.68K |
| 94 | 9-P0208B.dwg | 457.93K |
| 95 | Drawing5.dwl | 44B |
| 96 | Drawing5.dwl2 | 197B |
| 97 | V0201.dwg | 470.92K |
| 98 | V0202.dwg | 475.73K |
| 99 | V0203.dwg | 478.86K |
| 100 | V0204.dwg | 105.53K |
| 101 | 管廊.dwg | 591.51K |
| 102 | 钢架.dwg | 2.02M |
| 103 | 1-全流程模拟不含节能技术.bkp | 1.43M |
| 104 | 2-原始换热网络不含节能技术).hch | 433.00K |
| 105 | 3-全流程模拟含节能技术.bkp | 2.84M |
| 106 | 4-换热网络设计含节能技术).hch | 6.56M |
| 107 | 5-全流程模拟含节能技术,含换热网络.bkp | 2.98M |
| 108 | 6-能量集成及换热网络设计.docx | 1.31M |
| 109 | 6-能量集成及换热网络设计.pdf | 1.70M |
| 110 | 换热器设计说明书.docx | 3.00M |
| 111 | 换热器设计说明书.pdf | 3.58M |
| 112 | 污垢系数来源.pdf | 149.00K |
| 113 | E0101-产品原料换热器-强度校核.docx | 280.62K |
| 114 | E0101-产品原料换热器-强度校核.pdf | 676.62K |
| 115 | E0101-产品原料换热器-强度校核.ue3 | 23.99K |
| 116 | E0101-产品原料换热器.EDR | 269.67K |
| 117 | 换热器E0101运行视频.mp4 | 3.28M |
| 118 | 说明.txt | 932B |
| 119 | E0203-异丙醇冷却器强度校核.docx | 632.28K |
| 120 | E0203-异丙醇冷却器强度校核.fx3 | 26.05K |
| 121 | E0203-异丙醇冷却器强度校核.pdf | 939.90K |
| 122 | E0203.EDR | 307.81K |
| 123 | 换热器E0203运行视频.mp4 | 2.87M |
| 124 | 说明.txt | 932B |
| 125 | 4-T0201塔.bkp | 1.97M |
| 126 | 5-塔设备设计说明书.docx | 1.93M |
| 127 | 5-塔设备设计说明书.pdf | 2.91M |
| 128 | 1-T0201脱轻塔-DSTWU-NSTAGE.bkp | 462.57K |
| 129 | 2-T0101脱轻塔-RR-DR.bkp.bkp | 1.86M |
| 130 | 3-T0201脱轻塔-FEEDSTAGE.bkp.bkp | 1.84M |
| 131 | 4-T0201脱轻塔-RESULTS.bkp | 1.81M |
| 132 | 5-T0201脱轻塔优化.docx | 802.05K |
| 133 | 5-T0201脱轻塔优化.pdf | 751.25K |
| 134 | T0201塔详细设计与水力学校核.bkp | 1.98M |
| 135 | 填料来源文献-苏尔泰公司产品(1).pdf | 4.02M |
| 136 | 填料来源文献-苏尔泰公司产品(2).pdf | 1.68M |
| 137 | T0201塔设备强度校核.cn2 | 32.58K |
| 138 | T0201塔设备强度校核.docx | 216.91K |
| 139 | T0201塔设备强度校核.pdf | 654.45K |
| 140 | R0101反应器强度校核.docx | 463.64K |
| 141 | R0101反应器强度校核.fx3 | 26.05K |
| 142 | R0101反应器强度校核.pdf | 910.37K |
| 143 | T0201塔设备强度校核.cn2 | 32.58K |
| 144 | T0201塔设备强度校核.docx | 216.91K |
| 145 | T0201塔设备强度校核.pdf | 654.45K |
| 146 | E0101-产品原料换热器-强度校核.docx | 280.62K |
| 147 | E0101-产品原料换热器-强度校核.pdf | 676.62K |
| 148 | E0101-产品原料换热器-强度校核.ue3 | 23.99K |
| 149 | E0203-异丙醇冷却器强度校核.docx | 632.28K |
| 150 | E0203-异丙醇冷却器强度校核.fx3 | 26.05K |
| 151 | E0203-异丙醇冷却器强度校核.pdf | 939.90K |
| 152 | 具有背景的分析源文件.alo | 4.61K |
| 153 | 经济估算.xlsx | 61.24K |
| 154 | 1-物料工艺流程图(PFD).dwg | 1.86M |
| 155 | 工艺物料流程图PFD说明.pdf | 91.71K |
| 156 | 2-管道及仪表流程图(PID).dwg | 2.59M |
| 157 | 管道及仪表流程图PID说明.pdf | 160.77K |
| 158 | 3-异丙醇精制车间平立面布置图.dwg | 795.74K |
| 159 | 4-厂区总平面布置图(2004版).dwg | 1.16M |
| 160 | 厂区总平面布置图说明.pdf | 99.19K |
| 161 | 异丙醇冷却器E0203(2004版).dwg | 340.20K |
| 162 | 异丙醇合成反应器R0101(2004版).dwg | 326.24K |
| 163 | 脱轻塔T0201(2004版).dwg | 349.33K |
| 164 | 6-车间三维配管源文件.dwg | 6.47M |
| 165 | 6-车间三维配管源文件录制视频.mp4 | 33.84M |
| 166 | 说明.txt | 873B |
| 167 | C0201.dwg | 441.24K |
| 168 | Drawing1.dwl | 44B |
| 169 | Drawing1.dwl2 | 197B |
| 170 | T0201.dwg | 679.25K |
| 171 | T0202.dwg | 675.40K |
| 172 | T0203.dwg | 655.25K |
| 173 | E0201.dwg | 121.92K |
| 174 | E0202.dwg | 475.89K |
| 175 | E0203.dwg | 506.19K |
| 176 | E0204.dwg | 105.00K |
| 177 | E0205.dwg | 426.55K |
| 178 | E0206.dwg | 483.01K |
| 179 | E0207.dwg | 426.64K |
| 180 | E0208.dwg | 477.80K |
| 181 | E0209.dwg | 61.31K |
| 182 | 1-P0209A.dwg | 457.77K |
| 183 | 1-P0209B.dwg | 456.77K |
| 184 | 10-P0207A.dwg | 457.34K |
| 185 | 10-P0207B.dwg | 455.24K |
| 186 | 2-P0201A.dwg | 455.11K |
| 187 | 2-P0201B.dwg | 456.68K |
| 188 | 3-P0204A.dwg | 455.23K |
| 189 | 3-P0204B.dwg | 456.65K |
| 190 | 4-P0205A.dwg | 457.59K |
| 191 | 4-P0205B.dwg | 458.18K |
| 192 | 5-P0210A.dwg | 457.56K |
| 193 | 5-P0210B.dwg | 458.00K |
| 194 | 6-P0203A.dwg | 457.81K |
| 195 | 6-P0203B.dwg | 456.11K |
| 196 | 7-P0202A.dwg | 456.40K |
| 197 | 7-P0202B.dwg | 456.39K |
| 198 | 8-P0206A.dwg | 457.09K |
| 199 | 8-P0206B.dwg | 456.40K |
| 200 | 9-P0208A.dwg | 457.68K |
| 201 | 9-P0208B.dwg | 457.93K |
| 202 | Drawing5.dwl | 44B |
| 203 | Drawing5.dwl2 | 197B |
| 204 | V0201.dwg | 470.92K |
| 205 | V0202.dwg | 475.73K |
| 206 | V0203.dwg | 478.86K |
| 207 | V0204.dwg | 105.53K |
| 208 | 管廊.dwg | 591.51K |
| 209 | 钢架.dwg | 2.02M |
| 210 | PL-0202-40-H1B-H.dwg | 164.97K |
| 211 | PL-0203-32-H1B-H.dwg | 195.07K |
| 212 | PL-0223-65-H1B-H.dwg | 149.50K |
| 213 | PL-0231-100-H1B-H.dwg | 150.85K |
| 214 | HAZOP炉火醇清6.29导出.pdf | 605.40K |
| 215 | 动力学方程.png | 136.87K |
| 216 | 动力学来源.png | 32.25K |
| 217 | 文献-丙酮加氢法合成异丙醇反应动力学.pdf | 689.63K |
| 218 | 附录9-动力学说明.docx | 1.22M |
| 219 | 附录9-动力学说明.pdf | 1.20M |
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发布者
静
创作: 20149
粉丝: 35
加入时间:2025-05-27
模型信息
图纸ID:2695937
图纸格式:pdf,dwg,skp
文件大小:244.68M
所需金币:520
上传时间:2025-10-02 13:23:52
是否可编辑:可修改,包括参数
软件版本:AutoCAD 2004
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