長(zhǎng)嶺焦化大表.doc

此文檔收集于網(wǎng)絡(luò)，如有侵權(quán)，請(qǐng)聯(lián)系網(wǎng)站刪除 9表2-11 焦化裝置電機(jī)機(jī)泵效率匯總表中國石化長(zhǎng)煉分公司焦化裝置能量平衡報(bào)告 序機(jī)泵名稱型 號(hào)介溫度流量壓力(MPa)有效功率 電流電壓功率因數(shù)消耗功率電機(jī)功率電機(jī)效率機(jī)組效率運(yùn)行時(shí)間實(shí)際消耗號(hào)質(zhì)m3/h入口出口kWAVcosFkWkWkWhrkW1汽油出裝置泵3Y-10汽油3926.110.11.016.6034.01224.30.8511.2316.800.6680.5872411.232對(duì)流泵50Y2-50A 柴油 272880.261.4529.09139.22250.88447.9682.390.5760.6122447.963中段回流泵100Y2-120蠟油3061580.171.245.30133.92250.86645.1877.830.5720.9852445.184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蠟油泵5DR-6蠟油368100.161.1511.4060.6224.10.81819.4333.370.5760.1422419.437輕蠟油泵5DR-6蠟油342380.171.252.7567.2224.50.7620.334.050.5830.5722420.38沖洗油泵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高壓水泵DY55-170B*9水381800.0915.6775.5128.861200.8441152.312500.9210.6722.512011冷焦水泵8SH-9水381800.110.939.50117.2225.10.87940.869.650.5760.9837.512.7512封油泵40Y1-40*2蠟油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輻射進(jìn)料泵HDRB-125/4渣油3771640.183.6155.827.961200.863255.22480.000.5310.34724255.2215爐-1風(fēng)機(jī)空氣3052.6224.70.76615.6827.190.5760.4372415.6816爐-2風(fēng)機(jī)空氣3050.2224.10.75614.7326.340.5590.4342414.7317空冷風(fēng)機(jī)PG*3空氣10337.2224.50.5878.4914.810.5732425.4718180潤滑油泵GAP2-16-E-20R353.0224.10.7680.781.350.662240.78191250潤滑油泵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 焦化裝置蒸汽驅(qū)動(dòng)機(jī)泵效率匯總表序壓 力密流量有效功透平蒸 汽進(jìn) 汽排 汽能 耗機(jī)組設(shè)備名稱規(guī)格型號(hào)MPa度量溫度壓力溫度壓力效率備 注號(hào)入口出口kg/m3m3/hkW型式t/hMPaMPakW%1富氣壓縮機(jī)2MCL457-260.070.990.8356750297.66背壓150003903.42781.2812.50.37多變指數(shù)取0.9合 計(jì)中國石化長(zhǎng)煉分公司焦化裝置能量平衡報(bào)告 10表2-13 焦化裝置冷換設(shè)備能量平衡表序工 藝程介流入出焓 熱熱傳熱傳熱溫差換熱備規(guī) 格 型 號(hào)量口口差流量損失系數(shù)溫差修正面積號(hào)編 號(hào)別質(zhì) t/h kW/kg kW kW W/m2.K 系數(shù)m2注1H-102$2000-240-16/25-2-1殼除氧水92561351902200.505657.7333.56118.86104.60.948480管蠟油105070306240195.005691.292H-103$2000-240-16/25-2-1殼除氧水13501351902200.50825.1812.1636.6650.040.937480管柴油5993022720950.50837.363H-104T-900-240-16/25-2-1殼除氧水1060680135235.00692.3348.4417.9381.070.991480管柴油3380020918078.90740.784H-105FB700-135-25-4殼軟化水3280053133330.764075.4437.8203.6120.080.91810管柴油3380018066318.004114.295H-106FB700-135-25-4殼軟化水4580053132320.003013.5938.85327.6616.80.914810管汽油5197015374285.003051.397L-101P9*3*4*3020*1562/70殼風(fēng)66管油氣.水2685610366786.005863.568L-102FH-900-240-16-殼循環(huán)水20425304251.20290.4824.6745.7614.220.93480管油氣.水2685667355.60315.169L-301-202殼循環(huán)水1155304385225.007220管油氣、水2810348570925.00722010L-701/1.2殼20204.8111.7449.0517.950.6749325管富氣5973.810239130.50216.5511L-702殼20214.6310.39165.1819.280.681325管富氣5973.810839135.60225.01表2-14 焦化裝置管線散熱損失匯總表中國石化長(zhǎng)煉分公司焦化裝置能量平衡報(bào)告 11序管線名稱公稱直徑管線長(zhǎng)度保溫厚度保溫材料表面溫度表面積熱流散熱系數(shù)散熱量備注號(hào)mmmmmm2kW/m2MW/m2kW2對(duì)流出口-分餾塔管線21880222.130.23637.393對(duì)流入口管線23980262.990.1528.664輻射入口線2548083.30.25865.75輻射出口-焦炭塔線7080273.780.24854.626重蠟油線19080169.120.28733.667輕蠟油線1008091.860.31523.868柴油線15580149.60.15322.929中段回流線23580213.410.15523.2710分餾塔頂循環(huán)線908090.150.09312.7811平衡線158034.410.0390.5712二層回流線508043.020.1275.4813揮發(fā)線13580234.690.3176.2814飽和蒸汽線15080147.170.13250.5515過熱蒸汽線60080638.680.1892.2216除氧水線658044.690.1818.1217換-105軟化水線808080.130.0120.9618換-106軟化水線808080.130.0241.99193.5MPa蒸汽線30080476.020.435151.6220換熱器外表面10078.3521焦炭塔外表面(201.203)540026.5100508.68405.6822容-101外表面320015.19100178.0272.7623分餾塔外表面560027.5100341.26146.2524爐-301外表面200553.4525爐-302外表面583.2626合 計(jì)2530.4 12中國石化長(zhǎng)煉分公司焦化裝置能量平衡報(bào)告 表2-16 焦化裝置回收輸出物流能量(熱出料、介質(zhì))匯總表序物流名稱流量相對(duì)壓出裝置物流規(guī)定參數(shù)焓差能流量熱損失凈能流量備號(hào)t/h密度力MPa溫度焓kJ/kg溫度焓kJ/kgkJ/kgkWkWkWMJ/t注 回收輸出(熱出料)1熱蠟油去催化26042.000.91310.2326810.9480182.25628.694547.874547.87176.212富 氣5063.000.88500.13939.656077.81-38.16-53.67-53.67-2.083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蠟 油7000.000.91310.1572164.4080181.20-16.80-32.67-32.67-1.26小 計(jì)160.14 回收輸出(能量)1自產(chǎn)蒸汽出7000.00-1.2252.02973.88150063.222910.665659.62132.775526.85213.892柴油軟化水45800.001.000.4133.0552.6653221.90330.764075.444075.44157.723汽油軟化水32800.001.000.4132.0541.9053221.90320.003013.593013.59116.63小 計(jì)12748.6512615.88488.23表2-17 焦化裝置回收循環(huán)物流、能量匯總表序物流名稱流 量相對(duì)壓力初始溫度焓基準(zhǔn)焓能流量熱損失凈能流量單位能量備 注號(hào)m3/h