设备选型一览表

尾气深度脱硫制甲硫醇项目设备选型一览表目录1.非标设备设计一览表11.1 反应器设计一览表11.2 塔设备设计一览表11.3 换热器设计一览表21.4 气液分离器设计一览表62.标准设备选型一览表72.1 储罐选型一览表72.2 回流罐选型一览表82.3泵选型一览表82.3 压缩机选型一览表92.4管道选型10151.非标设备设计一览表1.1 反应器设计一览表位号名称类型数量直径/mm高度/mm封头形式设计温度（壳程/管程）设计压力 （壳程/管程）Kpa材料保温层保护层重量/KgR101A/BSCOT反应器固定床 板式230007300标准椭圆封头180/240200/300Q345R岩棉不锈钢薄板5785R201A/B甲硫醇合成反应器固定床列管式224008500标准椭圆封头300/400150/200Q345R岩棉不锈钢薄板36931.2 塔设备设计一览表位号名称类型数量内径/mm高度/mm设计温度设计压力 /Mpa封头形式材料保温层保护层重量kgT301深冷分离塔浮阀塔116001313618.120.19标准椭圆形封头Q345R（HIC）岩棉不锈钢薄板13967.9T302甲硫醇精馏塔浮阀塔16001450063.030.18标准椭圆形封头Q235-C岩棉不锈钢薄板7978.58T303甲醇精馏塔浮阀塔19001580097.910.28标准椭圆形封头Q235-C岩棉不锈钢薄板9370.92T304甲硫醇精制塔浮阀塔1600868553.940.17标准椭圆形封头Q235-C岩棉不锈钢薄板5088.66T102H2S吸收塔浮阀塔16001418559.160.1标准椭圆形封头Q345R（HIC）岩棉不锈钢薄板7430.5T103H2S解析塔浮阀塔1150018710106.140.1标准椭圆形封头Q345R（HIC） 岩棉不锈钢薄板23295.81.3 换热器设计一览表位号型号类型内径mm列管管数/根换热面积/m2材料壳体重量Kg管束重量/Kg管长mm列管规格/mm排列方式管程壳程E307BEM300-3/0.3-177.5-2/19-1管板式3002000192正三角形20028.316MnQ235B2212.12641.4E201BEM300-0.5/0.3-283.5-2/19-1管板式2502500192正三角形366.920Q235B224.8114.8E311BEM600-0.29/0.3-41.6-1.5/19-1管板式5001500192正三角形1006520Q235B1451.8798.2E102BEM600-0.1/0.3-157.1-2/19-1管板式5003000192正三角形654020Q235B16899.210589.9E205BEM400-0.095/0.3-47.3-1.5/19-1管板式4002000192正三角形354.220Q235B326.1403.6E310BEM900-0.5/0.3-257.9-2/19-1釜式再沸器4001500192正三角形1005820Q235B426.3160.2E202BEM900-0.5/0.3-257.9-2/19-1釜式再沸器7003000192正三角形600111.120Q235B3337.21964.4E203ABEM500-0.3/2.7-1075.9-6/19-1管板式5002000192正三角形30028.720Q345R1035.6501.4E203BBEM500-0.51/0.3-284-6/19-2管板式5002000192正三角形350056020Q235B14454.711116.9E101BBEM500-0.3-51.8-3/19-1釜式再沸器5001500192正三角形1508920Q235B1612.2894.4E101ABEM500-0.3/0.495-893.2-3/19-1管板式4002000192正三角形10012420Q235B5602.83855.1E303BEM400-0.3/0.295-21.2-2/19-1管板式4006000192正三角形728254.720Q235B8499.64263E309BKU400-2/0.105-483.9-2/19-1管板式3281500192正三角形10022.316MnQ235B380.7122.4E312BKU800-2/0.3-435.9-3/19-1管板式7003000192正三角形531188.916MnQ235B14302.57117.4E103BEM1000-3.11/1.5-386.6-6/19-1釜式再沸器10002500192正三角形50069.616MnQ245R3908.61804.9E301BBEM800-2/0.51-812.7-2/19-1管板式7007500192正三角形1521230.516MnQ235B62563830.2E306BKU500-0.5/0.08-945.8-6/19-1管板式40002500192正三角形1320151.720Q235B5446.32872.8E301ABEM1300-3.11/0.3-825.8-3/19-1管板式10003000192正三角形1576260.220Q235B14662.16456.1E305BKU800-0.3/0.505-365-2/19-1管板式7003000192正三角形61512220Q235B3375.62008.1E308BKU300-0.3/0.505-365-2/19-1管板式4504500192正三角形2002120Q235B4534.53453.5E103BEM300-3.11/0.3-825.8-3/19-1管板式2002000192正三角形383.820Q235B92.242E302BKU800-0.3/0.505-365-2/19-1管板式10002500192正三角形200151.720Q235B1446.2879.61.4 气液分离器设计一览表位号名称类型数量尺寸mm设计温度设计压力MPa材料保温防腐重量KgV101气液分离器立式120003500450.2Q245R不锈钢薄板外涂防腐层4132.90V201气液分离器立式118003200300.1Q345R不锈钢薄板外涂防腐层3116.62V202气液分离器立1Q245R不锈钢薄板外涂防腐层926.24V301气液分离器立式1300100010.50.2Q245R不锈钢薄板外涂防腐层713.5V303气液分离器立式1100500800.2Q245R不锈钢薄板外涂防腐层321.12.标准设备选型一览表2.1 储罐选型一览表位号名称类型数量公称容积/m技术规格设计温度/设计压力/ M Pa材料保温层保护层质量/kg标准序号V401甲醇储罐钢制立式内浮式圆筒储罐110045007850250.1Q245R无不锈钢薄板8170HG-21502-92V402甲硫醇储罐钢制立式内浮式圆筒储罐11004500785020.1Q245R岩棉不锈钢薄板8170HG-21502-92V403甲硫醚储罐卧式椭圆封头储罐118001800250.1Q245R无不锈钢薄板340HG5-1580-35V404克劳斯尾气储罐钢制球形储罐2300018000106001550.3Q345R岩棉不锈钢薄板84532GB-T17261-1998V405二甘醇胺储罐钢制立式内浮圆筒储罐1200550010260250.1Q245R无不锈钢薄板12020HG-21502-922.2 回流罐选型一览表位号名称类型数量公称容积/m尺寸/mm设计温度/设计压力/ M Pa材料保温层保护层质量/kgV302T2回流罐卧式椭圆封头储罐10.5 6001600250.1Q245R无不锈钢薄板230V304T4回流罐卧式椭圆封头储罐10.5 6001600400.28Q245R岩棉不锈钢薄板2302.3泵选型一览表编号名称类型型号数量方式是否一用一备流量L/S扬程m转速n(r/min)电机功率/kw尺寸长宽高mm重量KgP101A/B运输泵离心泵IX150-32-160B2单泵是2.7120.5429001554820034232.5P102A/B进料泵螺杆泵EH1642单泵是0.1421.272140.5573211516432.5P103A/B运输泵离心泵IX140-32-160B2单泵是1.2022.8129001.152222631032.5P104A/B运输泵离心泵IX140-32-125A2单泵是1.1619.8229000.7552222630032.5P105A/B运输泵管道泵ISG15-806串联是0.2025.029000.128511030032.5P201A/B进料泵螺杆泵EH632单泵是0.04318.722140.556421643532.5P301A/B精馏塔回流泵管道泵IS100-65-2502单泵是8.7919.7014505.5116054049032.5P302A/B运输泵螺杆泵EH636并联是0.08321.602140.556421643532.5P303A/B精馏塔回流泵离心泵IX132-25-160B2单泵是0.4721.9329000.7551231022632.5P304A/B运输泵离心泵IX132-25-160B2单泵是0.5222.3729000.7551231022632.5P305A/B运输泵螺杆泵EH632单泵是0.05920.343880.556421643532.5P306A/B精馏塔回流泵磁力泵CQB50-40-125f2单泵是0.05119.652840.556421643532.5P307A/B精馏塔回流泵磁力泵CQB50-40-125f2单泵是0.3218.479100.756761643532.5P0308A/B运输泵螺杆泵EH632单泵是0.05819.463880.556421643532.52.3 压缩机选型一览表设备位号类型型号数量介质额定排气量（m3/h）进口压力(Mpa)出口压（Mpa）功率/kW冷却方式重量/kgC201多级离心式Y355L2-21原料气2000.0980.233315水冷12000C202离心式ZW-0.1/0.4-31原料气60.040.390水冷3600C301离心式ZW-0.45/0.8-7.51载气270.080.755.5水冷750C302活塞式4M0.2-50/1-101硫化氢气体120.1170水冷80002.4管道选型管道代号物流代号气相分率质量流量Kg/h体积流量m3/h管内径mm管道尺寸mm公称直径mm厚度mmPG-101-450-L1H-H1112878.9186225.4634234334505PG-102-500-L1H-H2112878.9187389.894874975005PG-103-600-L1H3112878.9189431.8895775896005PG-104-600-L1H4112576.3828389.9225445546005PGL-101-600-L1H50.7512576.3829930.1275926026005PG-105-600-L1H7110288.6829927.7785926026005PL-101-50-L1B804232.6534.1843846504PG-106-600-L1H9110154.14510395.726076176005PL-102-50-L1B1003106.3663.2193442504PG-107-250-L1H1111126.2871520.452322422505PL-103-50-L1B1203106.3662.9343240504PL-104-25-L1B130715.780.7182331254PG-108-150-L1H141410.507538.9721261361505PL- 104-25-L1B150715.780.7182331254PG-109-600-L1H1619510.458682.185554.5645646005PL-105-25-L1B170643.6950.6462129254PL-106-50-L1E1804465.844.3053947504PL-107-50-L1E1903572.6723.4443543504PL-108-50-L1E200893.1680.8612533504PL-109-50-L1E2104098.1323.9393745504PL-110-25-L1E220525.6840.4951927254PG-110-600-L1B2319793.998843.5355595696005PL-201-25-L1B24016.5020.017814253PG-201-150-L1B251394.004494.3991201301505PG-202-100-L1B261394.004163.96369771004PG-203-50-L1B27118.65316.9652432504PL-202-15-L1H280122.5610.156713153PG-204-100-L1B291122.561116.27564721004PG-205-100-L1B301193.996171.98678861004PG-206-100-L1B311137.999130.50768761004PG-207-250-L1E3212165.5211666.9622432532505PL-203-15-L1B3300.50.001612153PG-208-250-L1B3412165.0221666.2262432532505PG-209-300-L1E3512165.0221751.9082492593005PG-210-200-L1E3612165.022976.4191581682005PG-211-200-L1E3712559.0251141.4771641742005PG-212-250-L1E3812559.0251714.8192012112505PG-213-250-L1E3912559.0252032.4282192292505 PGL-301-150-L1H400.9622559.025893.6411451551505PG-301-150-L1H4112291.949