6 6-附录6-设备一览表VIP

惠州炼化年产11万吨甲基丙烯酸甲酯项目设计设备一览表惠州炼化11万吨甲基丙烯酸甲酯/年 项目设计 设备一览表广东石油化工学院烯时代2018“东华科技-陕鼓杯”第十二届全国大学生化工设计竞赛惠州炼化年产11万吨甲基丙烯酸甲酯项目设计设备一览表参赛学校： 广东石油化工学院 参赛团队： 烯时代团队 参赛队员： 黄小婵 刘洪彬 凌高业 黄健敏 林金鸿 指导老师： 陈辉、黄燕青 完成时间： 2018.3-2018.8 第一章 塔设备一览设备位号设备名称塔类型塔体内径/mm塔高/mm设计温度/设计压/Mpa封头形式材料保温层保护层重量/kg数量T0101水合反应精馏塔规整填料塔188630805650.8标准椭圆封头Q345R岩棉不锈钢22939114201400.8T0102TBA分离塔浮阀塔182030005850.1标准椭圆封头Q345R岩棉不锈钢23474113001060.1T0103脱水反应精馏塔规整填料塔13000300061500.5标准椭圆封头Q345R岩棉不锈钢333191T0104IB精制塔筛板塔190035475300.35标准椭圆封头15CrMOR岩棉不锈钢319471T0201MAL吸收塔筛板塔3700450001100.2标准椭圆封头Q345R岩棉不锈钢421251T0202MAL共沸精馏塔筛板塔5500825011100.2标准椭圆封头Q345R岩棉不锈钢2203911T0301MMA萃取塔筛板塔2980511501120.5标准椭圆封头Q345R岩棉不锈钢69013128751400.5T0302正己烷回收塔筛板塔3700301251100.2标准椭圆封头Q345R岩棉不锈钢351971T0303MMA精制塔筛板塔600318251001.2标准椭圆封头Q345R岩棉不锈钢13768110001151.5T0401甲醇高压精馏塔筛板塔650300021901.60标准椭圆封头Q345R岩棉不锈钢17330114562001.65T0402甲醇精制塔筛板塔2050300861500.13标准椭圆封头Q345R岩棉不锈钢2772411850.03第二章 反应器一览设备位号名称数量类型规格/mm封头设计温度/设计压力/MPa材质催化剂重量/kg直径高度壁厚R0101水合反应器1列管式固定床反应器3056830020标准椭圆封头702.0Q345R磺酸树脂10542R0201催化氧化反应器2列管式固定床反应器2548905010标准椭圆封头4200.2Q345R金属复合氧化物3820R0202氧化酯化反应器1列管式固定床反应器44281389010标准椭圆封头1250.2Q345R杂多酸18667第三章 换热器一览设备位号型号型式公称直径/mm管长/mm管数/根规格排列方式换热面积/m2管程数壳程数个数/台E0101BEM700-1.6/0.25-156.7-4/19-1卧式700400067019X2正三角形156.7111E0102BKU700-1/1-197.2-5.5/19-2卧式700550058019X2正三角形197.2211E0103BEM700-1.6/1.6-162.6-2.5/19-1卧式700250038519X2正三角形162.6111E0104BEM700-0.4/0.25-97.7-3.7/19-2卧式600370043019X2正三角形97.7211E0105BEM700-0.11/0.11-71.2-2.5/19-1卧式700250071019X2正三角形71.2111E0106BEM800-0.6/0.25-503.2-6/19-2卧式800600071019X2正三角形503.2211E0107BKU500-1/0.6-68.4-5/19-卧式500500023019X2正三角形68.4211E0108BEM273-1/1-17.6-4.5/19-2卧式27345007019X2正三角形17.6211E0109BKU600-0.4/0.4-907-5/19-2卧式600500023019X2正三角形90.7211E0201BEM300-0.4/0.25-3.5-0.9/19-1卧式3009007019X2正三角形3.5111E0202BEM1000-0.1/0.1-484.2-2/19-1卧式1000200054019X2正三角形484.2111E0203BEM700-0.25/0.25-349.3-2.5/19-6卧式700250032019X2正三角形349.3611E0204BEM700-0.25/0.25-2074-7/19-1/4卧式700700065019X2正三角形2074141E0205BEM500-1/0.25-198-6.1/19-1卧式500610050019X2正三角形198111E0206BEM600-2.1/0.25-129.3-5.5/19-1卧式600550040019X2正三角形129.3111E0207BEM900-0.25/0.25-1263.5-4.5/19-1卧式900450080019X2正三角形1263.5111E0208BKU1700-0.4/0.25-1605.7-4.5/19-2卧式17004500270019X2正三角形1605.7211E0209BEM700-0.4/0.25-110.8-4.6/19-1卧式700460041019X2正三角形110.8111E0301BEM700-0.25/0.25-79.4-2.5/19-1卧式700250015019X2正三角形79.4111E0302BEM700-0.25/0.25-22.7-5.5/19-1卧式20055007019X2正三角形22.7111E0303BEM500-0.25/0.25-13.3-2.2/19-1卧式50022003519X2正三角形13.3111E0304BEM1000-1/0.6-359.4-6.1/19-1卧式10006100100019X2正三角形359.4111E0305BKU1000-1/0.6-320.7-5/19-2卧式1000500095019X2正三角形320.7211E0306BEM500-0.6/0.25-8.4-6/19-1卧式50020008019X2正三角形8.4111E0307BEM800-0.25/0.25-540.4-3.5/19-1卧式800350066319X2正三角形540.4111E0308BKU1300-0.4/0.25-570.3-5/19-2卧式13005000180019X2正三角形570.3211E0309BEM400-0.25/0.25-53.5-2.5/19-1卧式400250037019X2正三角形53.5111E0310BEM400-0.25/0.25-11.5-2/19-1卧式400200011019X2正三角形11.5111E0311BKU500-0.4/0.25-91.8-5/19-2卧式500500030019X2正三角形91.8211E0401BKU600-4/2.1-126.8-5.5/19-2卧式600550038019X2正三角形126.8211E0402BEM700-2.1/0.25-14-2.5/19-1卧式700250010019X2正三角形14111E0403BEM800-1.6/0.25-14-2.5/19-1卧式800150073019X2正三角形120.6111E0404BKU600-4/1.6-104-5/19-2卧式600500035019X2正三角形104211第四章 泵设备一览设备编号设备名称数量连接方式型号规格介质流量/（L/s）扬程/m轴功率/kW转速/(r/min)电机总功率/kWP0101混合器进料泵1单泵GDF100-21异丁烯、正丁烷、正丁烯14.1122.89-29005.5P0102水合反应器进料泵4并联GDF100-32水、异丁烯104.0731.68-290060P0103催化反应精馏塔进料泵4并联IH65-40-250水、叔丁醇、异丁烯27.8479.9811.84290088P0104反应精馏塔塔顶回流泵2并联IH80-65-160水、叔丁醇25.8632.996.28290022P0105叔丁醇分离塔进料泵4并联IH65-50-160水、叔丁醇22.4733.343.5290030P0106叔丁醇分离塔塔顶回流泵4串联IH65-40-200水、叔丁醇5.73206.595.98290044P0107废水排出泵4并联GDF40-30水、异丁烯，叔丁醇15.2426.63-29008.8P0108反应精馏塔塔底回流泵1单泵IH50-32-250异丁烯、水1.8819.481.2514503P0109反应精馏塔塔顶回流泵1单泵IH80-65-160水、叔丁醇、异丁烯9.9735.255.55290011P0110精制塔塔顶回流泵3并联IH65-40-315水、异丁烯12.2331.743.47145022.5P0111废水排出泵2串联IH50-32-250叔丁醇，抽余C41.0842.561.2714506P0201共沸精馏塔进料泵4并联IH65-65-160水、甲基丙烯醛59.5630.846.73290044P0202精馏塔进料泵3串联GDF200-18水、甲醇、甲基丙烯醛62.4158.86-148066P0203共沸精馏塔塔顶回流泵1单泵GDF200-24水、甲醇、甲基丙烯醛67.1025.23-148030P0204废水排出泵2串联IH65-40-200水、甲醇、甲基丙烯醛6.02102.576.11290022P0301水进料泵2串联GDF100-32A水27.9554.57-290022P0302MMA反应液进料泵3串联IH80-65-125水、甲醇、甲基丙烯酸甲酯8.3669.533.16290022.5P0303正己烷进料泵2串联IH65-40-250正乙烷4.22162.49.8290044P0304萃取塔塔顶回流泵3并联IH65-50-160水、正己烷18.1532.963.61290022.5P0305甲醇回收泵5并联IS65-40-250水、甲醇35.1974.8811.92900110P0306正己烷回收塔塔顶回流泵3并联IH80-65-160水、正己烷40.02632.596.36290033P0307MMA精制泵2串联IH65-40-200水，正己烷6.02102.576.11290022P0308MMA精制塔塔顶回流泵2串联IH50-32-250水、甲基丙烯酸甲酯1.142.531.2714506P0309MMA精制塔塔底出料泵1单泵IH65-40-250水，甲基丙烯酸甲酯4.92781.1210.35290022P0401热泵精馏回流泵2串联IH65-50-160水、甲醇3.39416.070.5214503P0402热泵精馏塔循环泵2并联GDF100-32A水、甲醇37.5329.49-290022P0403闪蒸罐出料泵3并联IH80-65-125水、甲醇37.7520.943.77290022.5P0404甲醇精制塔塔顶回流泵2并联GDF80-30水、甲醇26.8426.82-290011P0405甲醇精制塔塔底出料泵2串联IH65-50-160水、甲醇5.1867.343.41290015第五章 压缩机一览设备编号型式型号数量额定排气流量/(m/min)介质进口温度/进口压力/MPa出口压力/MPa轴功率/KW冷却方式串并联方式C0301离心压缩机MCL80214306.8H2O/ N24600.1013250.1236383水冷C0401离心压缩机2MCL803212439.2H2O/甲醇165.9731.5973.313519.6水冷2台串联第六章 罐设备一览位号设备名称数量规格尺寸mm容积重量/kg材质单价/元每吨总价/万元直径总高筒体壁厚V0501抽余碳四储罐22120021200505000172913Q345R5000432.282V0502异丁烯储罐2123001230048100028888907MnMoVR85001222.778V0503甲醇储罐3107001070032650134459Q345R4500453.799V0504MMA产品储罐61800018000203000154853Q345R45001045.258V0101进料保护罐1260071006507900Q235-A.F34006.715V0102T0101回流罐1220045006203800Q345R45003.420V0103T0102回流罐1220045006203800Q345R45003.420V0104T0103回流罐1200057006203650Q345R45003.285V0105T0104回流罐1220045006203800Q345R45003.420V0201混合气缓冲罐1220058006304800Q235-A.F34004.080V0202气体缓冲罐1240080006406850Q345R45006.165V0203T0202回流罐1220045006203800Q345R45003.420V0204气体缓冲罐1240080006406850Q345R45006.165V0301气液分离罐11650500010203800Q345R45003.420V0302正己烷混合罐1260066006406850Q345R45006.165V0303T0301回流罐1220045006203800Q345R45003.420V0304T0302回流罐1220045006203650Q345R45003.285V0305T0303回流罐1220045006203650Q345R45003.285V0306T0401回流罐1220071006304800Q345R45004.320V0402热泵精馏塔回流罐1240058008304800Q235-A.F34004.080第七章 管道一览拟建项目管道分生产单元进行设计7.1原料预处理单元管道编号介质状态起止点公称直径/mm管道等级设计条件操作条件保温材料来源去向设计温度/设计压力/MPa操作温度/操作压力/MPaPL-0101-350-L1B抽余碳四L原料储罐V0101350L1B500.58450.5PL-0102-400-L1B工业用水L水输送管S0101400L1B500.58450.5PL-0103-350-L1B-H抽余碳四LV0101P0101350L1B500.58450.5复合硅酸盐PL-0104-400-M1B-H抽余碳四LP0101S0101400M1B601.9561.7复合硅酸盐PL-0105-600-M1B-H抽余碳、水LS0101P0102600M1B451.941.81.7复合硅酸盐PL-0106-600-N1B-H抽余碳、水LP0102R0101600N1B452.541.81.7复合硅酸盐PL-0107-500-M1B-HTBA和水LR0101P0103500M1B661.9601.7复合硅酸盐PL-0108-600-M1B-HTBA和水LP0103T0101600N1B661.7601.5复合硅酸盐PG-0109-800-L1B剩余碳四组分GT0101E0101800L1B631.057.50.7PGL-0110-350-L1B碳四混合组分GLE0101V0102350L1B250.8220.7PL-0111-300-L1B碳四混合组分LV0102P0104300L1B250.8220.7PL-0112-300-M1B碳四混合组分LP0104T0101300M1B251.9221.7PG-0113-500-L1B剩余碳四组分GV0102后处理500L1B200.8170.9PL-0114-400-L1B-HTBA混合液体LT0101E0102400L1B1501.0140.60.799复合硅酸盐PG-0115-600-L1B-HTBA混合气体GE0102T0101600L1B1501.0140.60.799复合硅酸盐PL-0116-300-L1B-HTBALE0102P0105300L1B1500.9140.60.799复合硅酸盐PL-0117-300-L1B-HTBALP0105T0102300L1B1500.9140.60.799复合硅酸盐PG-0118-600-L1BTBA气体GT0102E0103600L1B770.170.120.097PL-0119-350-LIBTBA液体LE0103V0103350L1B350.1300.097PL-0120-350-L1BTBA混合液体LV0103P0106350L1B350.1300.097PL-0121-150-L1BTBA液体LP0106T0102150LIB350.1300.097PL-0122-300-L1B-HTBA液体LP0106T0103300L1B770.3370.30.29复合硅酸盐PL-0123-250-L1B-H水和TBALT0102E0104250L1B1500.6137.20.52复合硅酸盐PG-0124-500-L1B-HTBA气体GE0104T0102500L1B2000.61500.52复合硅酸盐PL-0125-300-L1B-H废液LE0104P0107300L1B1500.6137.20.52复合硅酸盐PL-0126-300-L1B-H废液LP0107E0105300L1B1500.6137.20.52复合硅酸盐PL-0127-300-L1B-H废液LE0105后处理300L1B1500.6137.20.52复合硅酸盐PL-0132-250-L1B-HIBLP0109T0104250L1B500.642.30.50复合硅酸盐PL-0136-250-LIB-H循环液LP0108T0102250L1B1500.6137.20.52复合硅酸盐PL-0137-300-MIB-H废液LE0105T0102300L1B1800.61500.52复合硅酸盐PG-0142-300-LIB-H循环液LV0105E0201300L1B50.22.950.15复合硅酸盐PL-0146-150-L1B废液LP0111后处理150L1B50.22.950.15复合硅酸盐7.2异丁烯反应单元管道编号介质状态起止点公称直径/mm管道等级设计条件操作条件保温材料来源去向设计温度/设计压力/MPa操作温度/操作压力/MPaPG-0201-350-L1B氧气G氧气管道V0201350L1B300.1250.1PG-0202-800-L1B氮气G氮气管道V0201800L1B300.1250.1PG-0203-350-L1B-H水蒸气G水蒸气管道V0201350L1B1100.11000.1复合硅酸盐PG-0204-300-L1B-HIBGE0201V0201300L1B300.2250.15复合硅酸盐PG-0205-700-LIB-H混合原料气GV0201R0201700L1B500.242.40.1复合硅酸盐PG-0206-700-LIB-H混合原料气GV0201R0201A700L1B500.242.40.1复合硅酸盐PG-0207-700-LIB-H混合原料气GV0201R0201B700L1B500.242.40.1复合硅酸盐PG-0208-350-L1B-H反应气GR0201C0201350L1B5000.24600.1复合硅酸盐PG-0209-350-L1B-H反应气GR0201AC0201350L1B5000.24600.1复合硅酸盐PG-0210-350-L1B-H反应气GR0201BC0201350L1B5000.24600.1复合硅酸盐PG-0211-300-L1B-H反应气GC0201E0203300L1B5500.25010.12复合硅酸盐PL-0212-150-L1B-CMAL混合液体LE0203T0201150L1B1200.21100.12复合硅酸盐PL-0213-500-L1B水L水输送管E0202500L1B300.2250.1PL-0214-500-L1B-C水LE0202T0201500L1B100.250.1复合硅酸盐PG-0215-400-L1B废气GT0201后处理400L1B250.1200.1PL-0218-250-L1B-CMAL吸收液LE0204P0202250L1B300.15250.12复合硅酸盐PL-0219-250-L1B甲醇L甲醇储罐V0202250L1B300.15250.12PL-0220-250-L1B-C精制甲醇LE0205V0202250L1B300.15250.12复合硅酸盐PL-0221-300-L1B-CMAL甲醇混合物LE0206V0202300L1B300.15250.12复合硅酸盐PL-0223-350-L1B-C混合液LP0202T0202350L1B300.1526.40.12复合硅酸盐PL-0228-200-L1B-H共沸精馏液LP0220E0209200L1B300.225.40.1复合硅酸盐PG-0229-150-L1B甲醇废气GV0203后处理150L1B300.225.40.1PL-0233-100-L1B废水LP0204后处理100L1B1100.25103.90.17PG-0234-350-L1B-H共沸物GE0209V0204350L1B770.15700.1复合硅酸盐PG-0235-350-L1B空气G大气V0204350L1B300.15250.1PG-0237-500-L1B-H混合气GV0204R0203500L1B550.1550.20.1复合硅酸盐PG-0238-500-L1B反应气GR0203C0202500L1B1200.151100.17.3MMA精制单元管道编号介质状态起止点公称直径/mm管道等级设计条件操作条件保温材料来源去向设计温度/设计压力/MPa操作温度/操作压力/MPaPGL-0301-400-L1B-C产物GLE0301V0301400L1B600.15500.1复合硅酸盐PG-0306-150-L1B废气GE0303后处理150L1B500.15400.1PL-0309-350-L1B-H产物LP0302T0301350L1B550.15450.1复合硅酸盐PL-0310-350-L1B水L水输送管道P0301350L1B300.15250.1PL-0311-350-L1B水LP0301T0301350L1B300.5250.4PL-0314-400-L1B-H正己烷LV0302P0303400L1B300.15250.1复合硅酸盐PL-0315-400-L1B-H正己烷LP0303T0301400L1B300.55250.43复合硅酸盐PL-0320-200-L1B-HMMA反应液LP0304T0302200L1B1070.45980.4复合硅酸盐PL-0323-300-L1B甲醇回收液LE0305E0306300L1B1