附录3设备选型一览表-catalyst

5 | 哈尔滨理工大学Catalyst团队年产6万吨叔丁胺项目 | 设备选型一览表目录概述1表1-1 塔设备选型设计参数一览表2表1-2 反应器设计一览表2表1-3 换热器设计一览表2表1-4 气液分离器设计结果一览表3表1-5 压缩机选型一览表3表1-6 泵选型结果一览表4表1-7 储罐选型一览表5表1-8 透平机选型一览表6概述本项目总工艺设备的组成包括7个塔器，8个反应器，37台泵，2个压缩机，1台透平机，36个储罐，4个气液分离器和25个换热器。标准设备：换热器，压缩机，泵，透平机非标设备：反应器，气液分离器，塔，储罐表1-1 塔设备选型设计参数一览表设备位号设备名称类型塔体内径，mm塔高，mm设计温度，设计压力，MPa封头形式材料重量，kg数量T0101反应精馏塔浮阀塔4200587201000.88标准椭圆封头Q245R1740831T0102萃取精馏塔浮阀塔1400/2600531161400.88标准椭圆封头Q245R62166.21T0103溶剂回收塔浮阀塔1200/1400219642200.9标准椭圆封头S3040813428.81T0301脱氨塔浮阀塔4200/4600229301203.3标准椭圆封头Q345R2623201T0302脱异丁烯塔浮阀塔3600/2400193201300.88标准椭圆封头Q245R38368.11T0303隔壁塔浮阀塔1400555701200.825标准椭圆封头Q245R50596.21T0401热泵精馏塔浮阀塔3200/2800519161000.8标准椭圆封头Q245R82560.61表1-2 反应器设计一览表设备位号T0201材料Q345R/18MnMoNbR设备名称异丁烯胺化反应器内径，mm4400数量8筒体长度，mm20000设计温度，250设计压力，MPa5.08管数5688管径452.5型式列管式固定床反应器封头标准椭圆封头表1-3 换热器设计一览表换热器位号换热器型号数量换热器面积，m2型式材料E0101BEU1000-0.9/0.4-349.9-4.5/19-2I1349.9卧式Q235BE0102BEU1100-0.8/0.3-315.5-2/19-2I1315.5卧式Q235BE0103BEM500-0.4/0.9-77.8-4.5/19-2I177.8卧式Q235BE0104BEM-400-0.4/0.9-15.8-1.5/19-2I115.8卧式Q235BE0105BEU1000-0.4/1.0-175.9-2/19-2I175.9卧式Q235BE0106BEU800-0.9/1.1-281.4-6/19-2I1281.4卧式Q235BE0107BEU500-0.4/0.9-28.3-1.5/19-2I128.3卧式Q235BE0108BEU1000-0.4/0.9-159.1-2/19-2I1159.1卧式Q235BE0109BEU800-0.4/1.1-151.6-3/19-2I1151.6卧式Q235BE0110BEU800-0.4/1.1-151.6-3/19-2I1151.6卧式Q235BE0111BEM500-0.4/0.9-50.7-3/19-2I150.7卧式Q235BE0201BEU1100-5.7/0.4-391.6-4.5/19-2I1391.6卧式Q235BE0301BEU900-3.5/0.4-83.7-2/19-2I183.7卧式Q235BE0302BEU1100-5.7/0.4-391.6-4.5/19-2I1391.6卧式Q235BE0303BEU900-3.4/0.4-103.9-2.5/19-2I1103.9卧式Q235BE0304BEU700-0.4/0.9-70-2/19-2I170卧式Q235BE0305BEM700-0.9/0.4-73.6-2.5/19-2I173.6卧式Q235BE0306BEU500-0.4/0.9-27.9-1.5/19-2I127.9卧式Q235BE0307BEM500-0.4/0.9-32.5-2/19-2I132.5卧式Q235BE0308BEU200-0.4/0.9-1.5-2/19-2I11.5卧式Q235BE0309BEU500-0.4/0.9-35.5-2/19-2I135.5卧式Q235BE0401BEU500-0.9/0.4-27.1-1.5/19-2I127.1卧式Q235BE0402BEM100-1.3/0.9-453.2-6/19-2I1453.2卧式Q235BE0403BEU500-1.3/0.4-22.4-1.5/19-2I122.4卧式Q235BE0404BEU500-0.9/0.4-24.9-1.5/19-2I124.9卧式Q235B表1-4 气液分离器设计结果一览表设备位号类型内径，mm高度，mm材料用途V0101立式重力分离器120018500Q235B异丁烯气液分离器V0102立式重力分离器8007420Q235B异丁烯气液分离器V0103立式重力分离器4001280Q235B异丁烯气液分离器V0401立式重力分离器4001600Q235B叔丁胺气液分离器表1-5 压缩机选型一览表位号类型型号入口压力，MPa出口压力,MPa排出流量，m3/min总功率,kW台数C0101喷油螺杆式DA-3722.62.29151C0401喷油螺杆式DAH-600-200.581.1243.15001表1-6 泵选型结果一览表位号用途型号流量，L/S扬程，m方式台数电机总功率，kWP0101C4原料进料泵GDF65-507.0855395串联215P0102T0101塔底出液泵GDF50-404.4291180串联28P0103T0101塔顶回流泵GDF150-204560串联355.5P0104T0102溶剂进料泵GDF50-173.4640串联23P0105T0102塔底出料泵GDF100-5036.350并联345P0106T0102塔顶回流泵ISG25-1250.840串联21.5P0107T0103塔底出料泵GDF100-32A33.190串联444P0108T0103塔顶回流泵GDF65-50940单泵17.5P0201液氨进料泵25FYS-160.9150串联31.65P0202换热器进料泵XBD(HW)20/3032.9429380串联2264P0301T0301进料泵GDF100-32A32.157550串联222P0302T0302进料泵GDF100-5038.425550并联345P0303T0301塔顶回流泵GDF100-5011.864250单泵115P0304T0303进料泵GDF50-504.4559651.13单泵15.5P0305T0302塔顶回流泵GDF150-204643.21串联237P0306T0303塔顶回流泵GDF50-17631.12串联23P0401T0401塔顶回流泵GDF100-32A32.722752.28串联222表1-7 储罐选型一览表名称数量类型尺寸，mm公称容积，m3材料标准序列号叔丁胺产品储罐4混合式球形储罐D=123001000Q345RGBT17261-2011混合C4原料储罐4混合式球形储罐D=123001000Q345RGBT17261-20112-丁烯产品储罐3混合式球形储罐D=123001000Q345RGBT17261-2011液氨原料储罐3混合式球形储罐D=7100200Q345RGBT17261-2011异丁烷产品储罐1混合式球形储罐D=7100200Q345RGBT17261-2011软水储罐1卧式圆筒形储罐D=1200L=32004Q345RHG5-1580-85氢气储罐1卧式圆筒形储罐D=3000L=800063Q345RHG5-1580-85异丁烯、液氨预混合罐1卧式圆筒形储罐D=2400L=480025Q345RHG5-1580-85水、NMP预混合罐1卧式圆筒形储罐D=2400L=480025Q345RHG5-1580-85罐区缓冲罐10立式圆筒形储罐D=2600H=660040Q345RHG5-1579-85T0101回流罐1卧式圆筒形储罐D=1400L=34006Q345RHG5-1580-85T0102回流罐1卧式圆筒形储罐D=1600L=36008Q345RHG5-1580-85T0103回流罐1卧式圆筒形储罐D=2600L=660040Q345RHG5-1580-85T0301回流罐1卧式圆筒形储罐D=2200L=460020Q345RHG5-1580-85T0302回流罐1卧式圆筒形储罐D=2600L=660040Q345RHG5-1580-85T0