長嶺焦化大表

1、 9表2-11 焦化裝置電機機泵效率匯總表中國石化長煉分公司焦化裝置能量平衡報告 序機泵名稱型 號介溫度流量壓力(mpa)有效功率 電流電壓功率因數(shù)消耗功率電機功率電機效率機組效率運行時間實際消耗號質(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3061580.17

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.

3、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381800.110.939.50117.2225.10.87940.869.650.5

4、760.9837.512.7512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輻射進料泵hdrb-125/4渣油3771640.183.6155.827.961200.863255.22480.000.5310.34724255.2215爐-1風(fēng)機空氣3052.6224.70.76615.6827.190.5760.4372415.6816爐-2風(fēng)機空氣3050.2

5、224.10.75614.7326.340.5590.4342414.7317空冷風(fēng)機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)動機泵效率匯總表序壓 力密流量有效功透平蒸 汽進 汽排 汽能 耗機組設(shè)備名稱規(guī)格型號m

6、pa度量溫度壓力溫度壓力效率備 注號入口出口kg/m3m3/hkw型式t/hmpampakw%1富氣壓縮機2mcl457-260.070.990.8356750297.66背壓150003903.42781.2812.50.37多變指數(shù)取0.9合 計中國石化長煉分公司焦化裝置能量平衡報告 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 號量口口差流量損失系數(shù)溫差修正面積號編 號別質(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92561351902200.505657.733

7、3.56118.86104.60.948480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.

8、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

9、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煉分公司焦化裝置能量平衡報告 11序管線名稱公稱直徑管線長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mmmmmm2kw/

10、m2mw/m2kw2對流出口-分餾塔管線21880222.130.23637.393對流入口管線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508043.020.1275.48

11、13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560027.5

12、100341.26146.2524爐-301外表面200553.4525爐-302外表面583.2626合 計2530.4 12中國石化長煉分公司焦化裝置能量平衡報告 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5063.000.88500.13939.656077.81-3

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蠟 油7000.000.91310.1572164.4080181.20-16.80-32.67-32.67-1.26小 計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 量相對壓力初始溫度焓基準焓能流量熱損失凈能流量單位能