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