长岭焦化大表

1、 9表2-11 焦化装置电机机泵效率汇总表中国石化长炼分公司焦化装置能量平衡报告 序机泵名称型 号介温度流量压力(mpa)有效功率 电流电压功率因数消耗功率电机功率电机效率机组效率运行时间实际消耗号质m3/h入口出口kwavcosfkwkwkwhrkw1汽油出装置泵3y-10汽油3926.110.11.016.6034.01224.30.8511.2316.800.6680.5872411.232对流泵50y2-50a 柴油 272880.261.4529.09139.22250.88447.9682.390.5760.6122447.963中段回流泵100y2-120蜡油3061580.17

2、1.245.30133.92250.86645.1877.830.5720.9852445.184汽油回流泵6dr-6汽油10382.80.161.121.6271.12250.85523.6933.920.6980.9122423.695柴油泵6dr-6柴油227890.161.2627.1974.63224.70.88425.7143.170.5750.9952425.716蜡油泵5dr-6蜡油368100.161.1511.4060.6224.10.81819.4333.370.5760.1422419.437轻蜡油泵5dr-6蜡油342380.171.252.7567.2224.50.

3、7620.334.050.5830.5722420.38冲洗油泵50y1-42*10柴油661.890.7562.7650.4223.80.8516.8528.630.5800.1652416.859污水泵40f-652水394.510.151.251.3817.8225.50.8546.0710.190.5820.232246.0710高压水泵dy55-170b*9水381800.0915.6775.5128.861200.8441152.312500.9210.6722.512011冷焦水泵8sh-9水381800.110.939.50117.2225.10.87940.869.650.5

4、760.9837.512.7512封油泵40y1-40*2蜡油722.870.010.90.7110.4224.60.8423.517.800.4360.208243.5113除焦送水泵8sh-9水382400.8154.0079.5222.20.8927.5846.880.5800.9643.54.0214辐射进料泵hdrb-125/4渣油3771640.183.6155.827.961200.863255.22480.000.5310.34724255.2215炉-1风机空气3052.6224.70.76615.6827.190.5760.4372415.6816炉-2风机空气3050.2

5、224.10.75614.7326.340.5590.4342414.7317空冷风机pg*3空气10337.2224.50.5878.4914.810.5732425.4718180润滑油泵gap2-16-e-20r353.0224.10.7680.781.350.662240.78191250润滑油泵fj-7359.118.0224.20.7652.717.260.32750.5720泵-701柴油3034.82250.79310.8818.620.5570.8472410.88表2-12 焦化装置蒸汽驱动机泵效率汇总表序压 力密流量有效功透平蒸 汽进 汽排 汽能 耗机组设备名称规格型号m

6、pa度量温度压力温度压力效率备 注号入口出口kg/m3m3/hkw型式t/hmpampakw%1富气压缩机2mcl457-260.070.990.8356750297.66背压150003903.42781.2812.50.37多变指数取0.9合 计中国石化长炼分公司焦化装置能量平衡报告 10表2-13 焦化装置冷换设备能量平衡表序工 艺程介流入出焓 热热传热传热温差换热备规 格 型 号量口口差流量损失系数温差修正面积号编 号别质 t/h kw/kg kw kw w/m2.k 系数m2注1h-102$2000-240-16/25-2-1壳除氧水92561351902200.505657.733

7、3.56118.86104.60.948480管蜡油105070306240195.005691.292h-103$2000-240-16/25-2-1壳除氧水13501351902200.50825.1812.1636.6650.040.937480管柴油5993022720950.50837.363h-104t-900-240-16/25-2-1壳除氧水1060680135235.00692.3348.4417.9381.070.991480管柴油3380020918078.90740.784h-105fb700-135-25-4壳软化水3280053133330.764075.4437.

8、8203.6120.080.91810管柴油3380018066318.004114.295h-106fb700-135-25-4壳软化水4580053132320.003013.5938.85327.6616.80.914810管汽油5197015374285.003051.397l-101p9*3*4*3020*1562/70壳风66管油气.水2685610366786.005863.568l-102fh-900-240-16-壳循环水20425304251.20290.4824.6745.7614.220.93480管油气.水2685667355.60315.169l-301-202壳循

9、环水1155304385225.007220管油气、水2810348570925.00722010l-701/1.2壳20204.8111.7449.0517.950.6749325管富气5973.810239130.50216.5511l-702壳20214.6310.39165.1819.280.681325管富气5973.810839135.60225.01表2-14 焦化装置管线散热损失汇总表中国石化长炼分公司焦化装置能量平衡报告 11序管线名称公称直径管线长度保温厚度保温材料表面温度表面积热流散热系数散热量备注号mmmmmm2kw/

10、m2mw/m2kw2对流出口-分馏塔管线21880222.130.23637.393对流入口管线23980262.990.1528.664辐射入口线2548083.30.25865.75辐射出口-焦炭塔线7080273.780.24854.626重蜡油线19080169.120.28733.667轻蜡油线1008091.860.31523.868柴油线15580149.60.15322.929中段回流线23580213.410.15523.2710分馏塔顶循环线908090.150.09312.7811平衡线158034.410.0390.5712二层回流线508043.020.1275.48

11、13挥发线13580234.690.3176.2814饱和蒸汽线15080147.170.13250.5515过热蒸汽线60080638.680.1892.2216除氧水线658044.690.1818.1217换-105软化水线808080.130.0120.9618换-106软化水线808080.130.0241.99193.5mpa蒸汽线30080476.020.435151.6220换热器外表面10078.3521焦炭塔外表面(201.203)540026.5100508.68405.6822容-101外表面320015.19100178.0272.7623分馏塔外表面560027.5

12、100341.26146.2524炉-301外表面200553.4525炉-302外表面583.2626合 计2530.4 12中国石化长炼分公司焦化装置能量平衡报告 表2-16 焦化装置回收输出物流能量(热出料、介质)汇总表序物流名称流量相对压出装置物流规定参数焓差能流量热损失净能流量备号t/h密度力mpa温度焓kj/kg温度焓kj/kgkj/kgkwkwkwmj/t注 回收输出(热出料)1热蜡油去催化26042.000.91310.2326810.9480182.25628.694547.874547.87176.212富 气5063.000.88500.13939.656077.81-3

13、8.16-53.67-53.67-2.083汽 油10833.000.73350.139111.2060159.10-47.90-144.14-144.14-5.584柴 油20833.000.83120.1566161.3080192.30-31.0-179.40-179.40-6.945蜡 油7000.000.91310.1572164.4080181.20-16.80-32.67-32.67-1.26小 计160.14 回收输出(能量)1自产蒸汽出7000.00-1.2252.02973.88150063.222910.665659.62132.775526.85213.892柴油软化水45800.001.000.4133.0552.6653221.90330.764075.444075.44157.723汽油软化水32800.001.000.4132.0541.9053221.90320.003013.593013.59116.63小 计12748.6512615.88488.23表2-17 焦化装置回收循环物流、能量汇总表序物流名称流 量相对压力初始温度焓基准焓能流量热损失净能流量单位能