data feed preheater BM 640000 co2 komposisi SiO2 21.28 Al2o3 6.04 fe2o3 3.51 cao 66.33 mgo 1.35 h20 0.76544 k20 0.18 na2o 0.21 so3 0.34 cl 0.00 total 100 menghitung caco3 118.451589285714 menghitung mgo 2.835 batu bara pre heater feed 53000 C 50.57 26802.1 H2 3.08 1632.4 N2 0.68 360.4 O2 21.92 11617.6 S 0.25 132.5 h20 13.4 7102 ash 10.1 5353 total 100 53000 co2 terbentuk 98274.3666666667 so2 yang terbentuk o2 yang diperlukan 71472.2666666667 o2 yang terbentuk o2 teori 73046.3666666667 o2 sesungguhnya 80351.0033333333 0.1 udara sesungguhnya 382623.825396825 n2 udara 302272.822063492 02 sisa pembakaran 7304.63666666667
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preheaterdatafeed outmasuk calcinerkeluar pre heaterfeed preheaterBMcaco3100cao56SiO221.2826688675.614346137SiO213.924955766675374.2721942164SiO275374.2721942164640000co244mgco384mgo40Al2o36.0362525150.4359462994Al2o33.949436501221377.8705543545Al2o321377.8705543545komposisife2o33.5067314611.0231097066fe2o32.294405874812419.3696432506fe2o312419.3696432506SiO221.28caco3118.4515892857493536.402413374caco377.5012682291419505.942051368caco337755.5347846231Al2o36.04mgco32.83511812.2155158847mgco31.854902046910040.383188502mgco3903.6344869652fe2o33.51h200.765443189.2565236257h2000cao213780.228069377cao66.33k200.17704737.6489012107k200.1158348707627.0015660291mgo4350.8327150175mgo1.35na2o0.21874.9789271026na2o0.1374001516743.7320880372h200h200.76544so30.337531406.341129833so30.22084130081195.389960358k20627.0015660291k200.18cl0.001466.0831868265cl0.00095525825.1707088025na2o743.7320880372na2o0.21total153.6036992857640000total100541289.131954918so31195.389960358so30.34cl5.1707088025cl0.00dust loss0.15total368533.036771031total100tanpa h20636810.7434763740.91dust loss95521.6115214561kalsinasi381750.407266745kalsinasi9136.7487015368masuk calciner541289.131954918cao terbentuk213780.228069377mgo terbentuk4350.8327150175co2 terbentuk167970.179197368co2 terbentuk4785.9159865193menghitung caco3caco2 sisa37755.5347846231mgco3 sisa903.6344869652118.4515892857menghitung mgoco2 hasil kalsinasi172756.0951838872.835batu bara pre heaterfeed53000co244C12h22So264h2018S32o232C50.5726802.1ghpco298274.3666666667komposisi ashfeed5353H23.081632.4n2302272.822063492sio230.241623.9438202247N20.68360.4h2014691.6al2o317.6945.1524879615O221.9211617.6so2265fe2o36.02323.2851123596S0.25132.5o27304.6366666667cao34.711863.9910714286h2013.47102total422808.425396825mgo2.25120.8291532905ash10.15353so38.86475.7983547352total10053000impuritis0total99.685353co2 terbentuk98274.3666666667so2 yang terbentuk265h20 terbentuk14691.6o2 yang diperlukan71472.2666666667o2 yang terbentuk132.5o2 terbentuk13059.2o2 total84663.9666666667o2 teori73046.3666666667o2 sesungguhnya80351.00333333330.1udara sesungguhnya382623.825396825n2 udara302272.82206349202 sisa pembakaran7304.6366666667feed outmassa out calcinermassa ashtotalNERMASSsio275374.27219421641623.943820224776998.2160144412UMPAN sp640000CO2 kalsinasi172756.095183887al2o321377.8705543545945.152487961522323.023042316UMPAN BATUBARA53000dust loss95521.6115214561fe2o312419.3696432506323.285112359612742.6547556102UDARA TERSIER382623.825396825umpan kiln373886.036771031caco337755.534784623137755.5347846231GHP422808.425396825mgco3903.6344869652903.6344869652h2o yang hilang3189.2565236257cao213780.2280693771863.9910714286215644.219140806h20 batubara7102mgo4350.8327150175120.82915329054471.6618683081n2 batubara360.4h2o000total1075623.82539683total1075623.82539683k20627.0015660291627.0015660291na20743.7320880372743.7320880372balance0so31195.389960358475.79835473521671.1883150932cl5.17070880255.1707088025impuritis00total368533.0367710315353373886.036771031
rotary kilndataumpan masuk kiln373886.036771031komposisimassa out calcinermassa ashtotalkomposisisio275374.27219421641623.943820224776998.2160144412cao terbentuk21143.0994793889sio276998.2160144412al2o321377.8705543545945.152487961522323.023042316co2 terbentuk16612.4353052342al2o322323.023042316fe2o312419.3696432506323.285112359612742.6547556102fe2o312742.6547556102caco337755.5347846231037755.5347846231mgo terbentuk430.3021366501cao236787.318620194mgco3903.63448696520903.6344869652co2 terbentuk473.3323503151mgo4901.9640049581cao213780.2280693771863.9910714286215644.219140806k20627.0015660291mgo4350.8327150175120.82915329054471.6618683081total kalsinasi17085.7676555492na20743.7320880372h2o000so31671.1883150932k20627.00156602910627.0015660291total cao236787.318620194cl5.1707088025na20743.73208803720743.7320880372total mgo4901.9640049581impuritis0so31195.389960358475.79835473521671.1883150932total356800.269115482cl5.170708802505.1707088025impuritis000total368533.0367710315353373886.036771031jumlahbatu bara53000komponenGHPashfeed5353c50.5726802.1co298274.3666666667sio230.241623.9438202247h23.081632.4n2302633.222063492al2o317.6945.1524879615n20.68360.4h2o14691.6fe2o36.02323.2851123596o221.9211617.6so2265cao34.711863.9910714286s0.25132.5o27304.6366666667mgo2.25120.8291532905h2o13.47102total423168.825396825so38.86475.7983547352ash10.15353impuritis0total10053000total99.685353CO2 terbentuk98274.3666666667so2 terbentuk265h2o terbentuk14691.6o2 terbentuk71472.2666666667o2 terbentuk132.5o2 terbentuk13059.2total o284663.9666666667o2 teoritis73046.3666666667o2 sesungguhnya80351.00333333330.1udara primer12669.44udara sesungguhnya382623.825396825udara sekunder369954.385396825n2 udara302272.822063492n2 total302633.222063492o2 sisa pembakaran7304.6366666667h2o total21793.6komposisiklinker panasmassaashtotalsio276998.21601444121623.943820224778622.1598346659masuk kiln373886.036771031co2 hasil kalsinas17085.7676555492al2o322323.023042316945.152487961523268.1755302775batu bara53000GHP423168.825396825fe2o312742.6547556102323.285112359613065.9398679697primer12669.44klinker362153.269115482cao236787.3186201941863.9910714286238651.309691623sekunder369954.385396825h20 batubara7102mgo4901.9640049581120.82915329055022.7931582487n2 batubara360.4k20627.0015660291627.0015660291na20743.7320880372743.7320880372total809509.862167857809509.862167857so31671.1883150932475.79835473522146.9866698284cl5.17070880255.1707088025balance0impuritis000total356800.2691154825353362153.269115482
nerpanpanas kiln feedoutputT ref25oCKomponenMassa(kg/h)Cp (kcal/kg. oC)T oCQ(kkal)Panas yang dibawa hot klinker (Tref = 25 oC)kiln feedCCRKomponenMassa(kg/h)Cp (kcal/kg. oC)T(oC)Q(kkal)SiO276,9980.2382114096833.3879239SiO278622.15983466590.2374813074078.9589066Al2O322,3230.2158213820362.16346196Al2O323268.17553027750.2157483616921.54530398Fe2O312,7430.238212332925.23265711Fe2O313065.93986796970.237482172735.14064469CaCO337,7560.238216912283.30836879CaO238651.3096916230.2374839685326.28862MgCO39040.23821165437.401873585MgO5022.79315824870.23748835240.274285171CaO215,6440.2382139480143.6402987SO3627.00156602910.2274899730.8690925826MgO4,4720.23821818671.854849839K2O743.73208803720.22748118298.025923194K2O6270.22821109800.514243009 Na2O2146.98666982840.22748341499.699702898Na2O7440.22821130242.363257072Cl5.17070880250.033748123.3679413199Cl1,1950.03382131400.5034786853Total59943954.1704204SO350.22821905.4945255015362153.2691154820.2774870695939.6640332Total373,41067899005.8649381
Menghitung Heat Udara Sekunder (Tref = 25oC)N2 dari batu baraKomponenMassa(kg/h)Cp (kcal/kg.oC)T(oC)Q(kkal)KomponenMassa(kg/h)Cp (kcal/kg.oC)T(oC)Q(kkal)Udara369954.3853968250.24688678358558.55336N2 dari batu bara360.40.2686480960.256Total78358558.55336Panas Gas Hasil Pembakaran (Tref = 25 oC)Menghitung Sensibel Heat Batu Bara (Tref = 25oC)KomponenMassa(kg/h)Cp (kcal/kg. oC)T(oC)Q(kkal)KomponenMassa(kg/h)NHV(kcal/kg)T(oC)Q(kkal)CO298274.36666666670.25586421025309.3765Batubara53000491370260389000SO22650.18586441131.975Total260389000H2O14691.60.58646163126.2N2302633.2220634920.2686466016411.0609302 Menghitung Heat Udara Primer (Tref = 25oC)O27304.63666666670.2458641501504.59001667KomponenMassa(kg/h)Cp (kcal/kg.oC)T(oC)Q(kkal)Total94747483.2024468Udara12669.440.2463015583.4112
Total15583.4112Panas Hasil CO2 Kalsinasi (Tref = 25 oC)KomponenMassa(kg/h)Cp (kcal/kg. oC)T(oC)Q(kkal)CO217,0860.2558643655414.56106648Total3655414.56106648
Panas Reaksi Disosiasi (Tref = 25 oC)Panas Penguapan H2O dalam BatubaraKomponenMassa (kg)Hf(kcal/kg)T (oC)Q (kkal)KomponenMassa(kg/h)Cp (kcal/kg. oC)T(oC)Q(kkal)CaCO337755.5347846231376100014196081.0790183H2O7,1020.47100250345.5MgCO3903.6344869652375.51000339314.749855425Total14535395.8288737Panas Laten Penguapan H2OKomponenMassa (kg)Hf(kcal/kgoC)T (oC)Q (kkal)komponenH2O7102539.11003828688.2batubara53,0000.2770643950Total3828688.24079033.770695939.664033294747483.20244683655414.56106648250345.53828688.2173258831.3835479804670034483998391539248582662.274825total421841493.658372total421841493.658372head loss58.9279779282efisiensi7.0372650503efisiensi41.0720220718
komponeninputoutputkiln masuk67899005.8649381heat sekunder78358558.55336panas sensibel batu bara260389000heat primer15583.4112reaksi disosiasi14535395.8288737panas laten batubara643950panas klinker70695939.6640332panas n2 dari batu bara80960.256GHP94747483.2024468panas Co2 kalsinasi3655414.56106648panas penguapan h2o batubara250345.5panas laten penguapan h2o batubara3828688.2o2 sisa pembakaran7304.6366666667173266136.020213panas yang hilang248575357.638159panas hilangtotal421841493.658372421841493.65837200total421841493.658372
Sheet1hmasukh batubaraNHVHudara=HkeluarQlossHflue gasHreaksi67899005.8649381x491378374141.9645659943954.1704204248582662.2748251642069914535395.828873729772.6740951553339482711.274119146273147.8294985424x339452938.600024h batubara=193179790.770526m batubara35522.0916040906komponen10380trialc31.13215.3187250996h24.4454.9003984064n20.4849.625498008o228.572953.7509960159s0.110.3386454183h2o19.872054.2888446215ash15.881641.7768924303total100.410380
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