一条日产5000td水泥熟料生产线设计 毕业设计

XXXXA1A0A2A3A4A5A7A8A6A101日产5000吨熟料水泥厂设计摘要本次设计的题目是设计一条日产5000T/D水泥熟料生产线。水泥品种是PO425（50）和PO525（50），袋散比为3070。本次设计的主要内容包括1配料计算2生产过程和主机选型3计算和确定带悬浮预热器的新型回转窑和悬浮预热器的型号及规格，以及窑尾气体平衡的计算，同时还编写了全厂工艺流程概述和本次毕业设计的评述及展望。4最后设计了整个水泥厂的工艺布局。在本次设计中，还采用了一些新的工艺技术，例如高效率立式磨和高效选粉机等。本次设计采用了利用窑尾废气预热生料和粉煤灰的有效方法来降低系统热耗，把篦冷机出来的多余热气体作为热源来G9900G5190煤粉。本次设计的工艺设G3803G18129G14033有效G3332降低系统热耗。关键词配料，平衡，选型，设计,预热器，G2010G16311G9821XXXXA1A0A2A3A4A5A7A8A6A1025000TONPERDAYCEMENTCLINKERDESIGNABSTRACTTHETITLEOFTHISGRADUATINGDESIGNISTOCONSTRUCTACEMENTPLANTWITH5000TONSPERDAYPRODUCTIONLINETHEPRODUCTIONISPO425ANDPO525CEMENT,BOTHTHEIRPERCENTAGESARE50ANDTHECEMENTSALEINBAGSACCOUNTFOR30THEMAINCONTENTOFTHISDESIGNIS1CALCULATEDRATIOOFRAWMATERIALS2MANUFACTURINGPROCESSANDSELECTIONOFTHEMAINMACHINE3THEPHASESOFTHISDESIGNISTOCALCULATEANDDESIGNPREHEATEDANDPRECLAIMERANDALSOTHEBALANCINGOFTHEMAINMACHINEATTHETHISTIME,ICOMPOSETHESUMMARIZATIONOFTECHNOLOGYFLOWFORWHATFACTORYANDQUALITYCONTROLOFTHEWHOLEFACTORYANDPROSPECTSOFTHEDESIGNPROJECTFORGRADUATION，ETC1THELASTSTEPOFTHEDESIGNISTHELAYOUTOFTHEWHOLEPLANTINTHEDESIGN,SOMENEWTECHNOLOGIESANDTECHNIQUESAREINTRODUCEDSUCHASVERTICALSPINDLEMOLLANDHIGHEFFICIENCYCLASSIFIERSANDACTSTOREDUCETHETOTALENERGYCONSUMPTIONANAFFECTIONMETHODISUSEDTOREUSETHEKILNEXHAUSTEDGASESFROMTHECOOLERISALSOUSEDASTHERMALSOURCESOFTHEDRIERTODRYPUZZLING,ALLTHESETECHNIQUESAREEFFECTIVETOREDUCETHETOTALTHERMALCONSUMPTIONKEYWORDSRATIOOFRAWMATERIALSA9BALANCEA9SLECTION,DESIGN,PREHEATER,CALCINERXXXXA1A0A2A3A4A5A7A8A6A103目录A11A121A13A14A15A16A17A13A18A162A19A203A21A225A23A24A25A26A27A28A29A30A31A32A33A34A35A36A376A38A39A40A39A41A42A43A446A38A39A40A45A46A47A48A497A23A50A25A51A52A29A5310A38A45A40A39A46A47A54A5510A38A45A40A45A48A56A57A5810A38A45A40A59A60A61A47A6211A23A63A25A64A52A65A6617A38A59A40A39A67A68A69A70A71A72A73A74A75A76A77A73A74A78A47A6217A38A59A40A45A48A79A80A81A61A82A83A84A85A78A47A6218A23A86A25A87A88A65A6623A89A40A39A90A91A90A92A93A94A78A95A9624A38A89A40A45A71A61A97A95A9624A38A89A40A59A98A9724A38A89A40A89A99A100A97A101A10225A38A89A40A103A104A105A9425A38A89A40A106A107A94A108A109A11025A23A111A25A112A113A65A6627A38A103A40A39A48A80A61A114A115A116A117A11827A38A103A40A45A71A61A11927A38A103A40A59A120A121A122A11928A38A103A40A89A90A123A122A11928A38A103A40A103A124A125A81A122A11929A38A103A40A106A126A61A78A122A11929XXXXA1A0A2A3A4A5A7A8A6A104A38A103A40A127A99A100A122A11929A38A103A40A128A129A130A11930A23A131A25A26A27A132A133A134A13531A38A106A40A39A48A61A76A13631A38A106A40A45A67A68A76A13632A38A106A40A59A99A100A97A76A13633A38A106A40A89A137A138A139A14033A23A141A25A142A143A144A145A26A27A29A5335A38A127A40A39A146A147A82A83A61A8335A38A127A40A45A114A148A149A150A151A152A153A76A154A47A6236A23A155A25A142A143A144A14541A38A128A40A39A151A152A153A156A157A78A47A62A158A8441A38A128A40A45A114A148A149A156A157A78A158A8442A159A160A161A16249A163A16450XXXXA1A0A2A3A4A5A7A8A6A105前言毕业设计是G4410生G4448G6116G6164有G10714G16782G16850和G4466G20576G4466G1076G16850程后的一个G6957G4410G10627G14422，G4439是在G6957G5084G6363G4560G991，G11013G4410生G13520G2524G17828用G6164G4410过的G3534G11796G11705G16794和G4466G17353生产G11705G16794，G7609G6226工G1867G1082和G2520种技术G17176料G17810G2052计算G451G13484G3282G451编写G16840G7138G1082等来G16311G1927G4466G19481生产技术G19394题的G6957G4410G10627G14422。G1075是G1186G1119技术工作的一次G9448G1076，G994G1820G2081的G6957G4410过程G11468比，G1867有G17751G5390的G13520G2524G5627G451G4466G17353G5627和G6518G13046G5627。G3G17902过毕业设计G993G1177G1363G4410过的G11705G16794G5483以G5053G3278G451G6564高，G13792G1000G17839一G8505G3533G1871G6117G1216G10432立G5617G13783G451设计及G16311G1927G4466G19481技术G19394题的G14033G2159，G1363G14270G5061的G4410G16794和工程G4466G17353G14033G2159有一个G5468G3835的G17839G8505，最G13468G4448G6116在G7669的G4410G1076G1231G2165。G3本设计为G20046G5224水泥G2469展G17247G2195，G6564高G6117G999业G4410生的G13520G2524G13044G17148和G17878G5224G14033G2159，设计带G2010G16311G9821预热器窑。预G2010G16311窑是在悬浮预热器窑的G3534G11796G990G2469展G17227来的，G11013预热器G451G2010G16311G9821G451回转窑和高效篦式冷G2376机等G1972G18108G2010G13464G6116。预G2010G16311窑的G10317G9869在G1122G4570G11911G18252G11428的G2010G16311过程转G12239G14279窑G3818G2010G16311G9821中G17839G15904，生料G20075G12902在预热器系统G3800G1122悬浮G10378G5589G7143G1122热G1144换，G13792G1000速度快，G1363生料迅速G2469生G2010G16311反G5224，入窑生料的G2010G16311率可G178108590，G1186G13792G3835G3835减轻了窑的负荷。G3预G2010G16311窑G994其G4439窑型G11468比，有其G10432G10317的优G9869G31预G2010G16311窑生产的熟料单位热耗低，单机生产G14033G2159G3835，并可利用窑尾余热G9900G5190物料，虽电耗略高，但其G13520G2524G14033耗低。G32G11013G1122原料和生料的预均化技术的G2469展，G3G1363G5190法生产的熟料G17148量G5483G2052了保证，并G11013G1122采用了新技术等措施，G993断改G17839燃烧系统，增G5390了新型G5190法生产对原料的G17878G5224G5627。G33G11013G1122收尘设G3803及技术G2469展，G1363G5190法厂在G10627境污染方面有了G5468G3835的改善。G34G994产量G11468同的湿法窑G11468比，预G2010G16311窑的G17148量轻，占G3332面积小，G3534建投G17176少。G3鉴G1122此，这次毕业设计的G1231G2165选为5000T/D熟料的预G2010G16311窑。G3XXXXA165A166A167A168A169A170A171A172A173A1746第一章工艺设计的指导思想与原则11指导思想水泥工业及水泥工厂设计有如G991G1972个G10317G9869G451水泥厂需要用G3835量的矿物原料（如石灰石）等，因此水泥厂G3835G18129G14270G15904开采矿山，并靠近矿源建厂。G451产品（水泥）G451燃料（煤）等物料G17828输量G3835，G1000价格底，因此要求要有良好的G17828输条件。G451水泥工业G14033耗和电耗G17751G3835，因此，在水泥厂设计中要注意确保G14033源供G5224，并充G2010重视G14422约G14033源的G19394题。G451水泥厂采用的主机多属重型设G3803，重量G3835，建构筑物荷重G1075G3835。因此，一般要求在工程G3332G17148条件好的场G3332建厂。G451水泥厂设G3803种类多，布置复杂。因此，工艺布置G5224同土建设计紧密结G2524。G451水泥厂用水量G3835，G1000水无卫生要求。因此，一般水泥厂多建在远离城市的G3332方，G1000G14270G3803水源。G451水泥厂存在粉尘和噪音两G3835污染。因此，设计时必须加G5390收尘措施，尽量搞好厂区绿化。G451G1186G2469展来G11487，水泥工业的G2469展G17892G9188G17247G2533G3835型化和G14270G2172化。因此在设计时，G5224尽量采用新技术，新方G7708并要重G9869G13783G15397G14422约G14033源。G1186水泥厂的整体设计来G16840，工艺设计是主体，G4439的主要G1231G2165是确定工艺流程，G17839G15904工艺设计的选型和布置。但工厂设计是G2520G999业G1861同G4448G6116的一个整体。因此，工业设计G994其G4439G999业的设计有G11540密G2011的G13864系，G10317G2047是工艺布置和其土建的G1863系G7368密G2011。生产设G3803的布置G11464G6521G5445G2721G2052建筑物的结构G5430式和G4622G4556。因此，工艺G1166G2604G2494有G994其G1194G1166G2604G11468G1126配G2524，XXXXA165A166A167A168A169A170A171A172A173A1747G1861同G11752G12362，G6177G14033产生G1144好的方G7708。12设计原则G451G7693G6466计G2022G1231G2165G1082规定的产品品种G451G17148量G451规G8181G17839G15904设计。计G2022G1231G2165G1082规定的产品规G8181G5460G5460有一定的G14551G3272，设计规G8181在G16825G14551G3272G1055内G6122略G17241出G16825G14551G3272，G18129G16760为是G2524G17878的G727但如G19492G1122设G3803选型，设计G17810G2052的规G8181略低G1122G16825G14551G3272，G2029G16840G7138原因，G2474G5483G990G13435同意后，G6177G14033G13499G13505设计。对G1122产品品种，如G7536G16760为计G2022G1231G2165G1082的规定在技术G990G6122G13475G8994G990有G993G5415G1055G3800，G1075G5224G19428G7138G10714G11013，建G16770G16855整，并G2474G5483G990G13435G18108G19388的同意。窑G451磨等主机的产量，G19512了G2454G13783设G3803G16840G7138G1082和G13475G20576G1856式计算G3818，还G5224G7693G6466G3281内同类型主机的生产G6980G6466并G2454G13783G3281内G3818近G1296规格的主机产品G17839G15904G7643定。在工厂建G6116后的G17751G11713时G7411内，主机G5224G14033G17810G2052G7643定的产量，同时G7643定的主机产量G5224G12538G2524优G17148G451高产G451低G9052耗和设G3803G19283G7411G4445全G17828转的要求。G7094要充G2010G2469G6393设G3803的G14033G2159，但G2460G993G14033过G2010G17873求G5390化G6817作。G451主要设G3803的G14033G2159G5224G994工厂规G8181G11468G17878G5224G3835型工厂G5224配G3883G994G1055G11468G17878G5224的G3835型设G3803，G2554G2029G4570G17908G6116工艺线过多的G10628G16949。在G10628G1207G3835中型水泥厂的设计中，一般G2494采用一条G6122两条G11013G3835型设G3803G13464G6116的工艺线。G451选G6333技术G1820G17839G13475G8994G451G2524G10714的工艺流程和设G3803工厂的工艺流程和主要设G3803确定以后，整个工厂设计可G16871G3835局G5062定。在选G6333生产工艺流程和设G3803时，G5224尽量G13783G15397G14422G11477G14033源，采用G3281内G3818G17751G6116熟的G1820G17839G13475G20576和G1820G17839技术。如在原料的G11784G11874方面，采用一G13435反G1999式反G1999式G19192式G11784G11874机G1207G7379G1120G13435G6122G989G13435G11784G11874系统G727在G5190法生料粉磨工G5219G7234G17953采用G9900G5190G1872粉磨系统G727在水泥粉磨系统采用G17758G2399G451机G10711磨G451高效选粉机（如OG252SEPA选粉机等）的G9163G2524粉磨系统。对G1122新技术G451新工艺G451新设G3803，必须G13475过生产G4466G17353鉴定G2524格后，G6177可G5224用G1122新建厂的设计中。XXXXA175A176A177A178A179A180A181A182A183A1848工艺流程和设G3803的选G6333G5224G17839G15904方G7708比G17751，以G17810G2052技术G1820G17839G451G13475G8994G2524G10714的目的。在G17839G15904G1867体设G3803的选型时，G5224注意G991G2027一些G19394题尽量选用结构新G451体型小G451G17148量轻G451效率高G451G9052耗G11477G1000G6817作可靠G13512G1474方G1427G451供G5224有保证G6122G14033G14270G15904加工G2058G17908的设G3803。G2520种G19480属设G3803的型号G451规格G5224尽量统一，以G1427G1122生产G12661G10714和减少配G451G3803件的种类。G451全面G16311G1927工厂生产G451厂G3818G17828输和G2520种物料G1660G3803的G1863系G11013G1122工厂生产要求G19283G7411G17842G13505G17828转，G13792回转窑G451磨机和G11784G11874机等设G3803G2029需一定的时G19400G17839G15904计G2022G7828G1474G727同时G2475G2520种复杂条件如厂G3818G17828输等因G13044的G2058约，G6164以G2520种物料G18129G5224有G17878G5415的G1660G3803。G2520种G3546场G451G1660G5223的容量，G5224G9397G17287G2520种物料G1660存G7411的要求。G1660存G7411的确定G5224G1363生产有一定的机G2172G5627，以利G1122工厂均衡G17842G13505G3332生产。但G1660存G7411G1075G993G5224G3838G19283，以G1825增加G3534建工程量和G17165用及占用工厂的流G2172G17176G18341。G451注意G13783G15397工厂建G6116后生产G6378G9520的可G14033和G11053有工厂G2469展余G3332工厂G1186设计G2052建G6116投产G5460G5460要好G1972G5192时G19400，G13792生产技术G2376是G2533G2081G2469展的。因此设G3803G14033G2159G5224G14033G2011G4466G9397G17287生产要求并G11053有余G3332。此G3818G5224结G2524设计的G3281内G3818G7422来时G7411水泥需求G5785G1929的预测，以及G5415G2081G3281民G13475G8994G2469展的方针政策，G13783G15397在设计中是G2554需要G6122G5224G11053有多G3835的扩建余G3332。G13783G15397工厂扩建的原G2029是G7094要G1427G1122今后的扩建，G1363工厂扩建时尽量G993G5445G2721原有的生产，G2460要尽可G14033G993增加G5415G2081建厂的占G3332面积的投G17176。G451G2524G10714G13783G15397机械化G451G14270G2172化装G3803水平机械化水平G5224G994工厂规G8181和装G3803水平G11468G17878G5224，G10317G2047是G17842G13505生产过程中G3835宗物料的装G451G17828G451卸，必须G4466G10628机械化。重G3835设G3803的G7828G1474G451G17227重以及需要减轻繁重体G2159劳G2172的场G2524，G1075G5224尽可G14033G4466G10628机械化。生产控G2058G14270G2172化，G1867有反G5224灵敏控G2058及时G16855整精确的G10317G9869，是保证G10628G1207化G17842G13505G5627G3835生产G4445全稳定G17839G15904的必G993可少的手段。如在原料配料和粉磨过程中，新型G5190法生产广泛G3332采用电子秤X荧光G2010析仪电子计算机G14270G2172G16855G14422系统，控G2058原料配料，G4466G10628了原料配料的G14270G2172控G2058。在水泥粉磨系统G5062广泛采用电子定量喂料秤G451G14270G2172化仪表G451电子计算机控G2058生产。其主要利用电耳G451G6564升机负荷和选粉机回料量等G17839G15904磨XXXXA175A176A177A178A179A180A181A182A183A1849机负荷控G2058。G451重视G9052音G19512尘，G9397G17287G10627保要求贯彻执G15904G3281家G10627保G451工业卫生等方面的规定。G6117G3281水泥生产最高容许排放浓度为50MG/M3。今后，G11013G1122对G10627保要求愈睐愈高，G5224采G2474积极措施，减少G10627境污染，以保护职工身体健康和延G19283设G3803生产寿命。为减少G10627境污染，G5224广泛的采用新型高效G19512尘设G3803，在物料G1660存设计G990采用以“圆G5223”为主方G7708。G994此同时，G1075G5224重视噪音防治G451污水治G10714G451绿化G10627境，G1363水泥厂工业G4466G10628文G7138生产G451方G1427施工G451G4445装G451方G1427生产G451G13512G1474工艺布置做G2052生产流程G20046畅G451紧凑G451G1427捷。G2159求缩G11713物料的G17828输距离，并充G2010G13783G15397设G3803G4445装G451G6817作G451G7828G1474和G17902G15904的方G1427，以及其G4439G999业对工艺布置的要求。XXXXA175A176A177A178A179A180A181A182A183A18410第二章配料计算21设计内容A185A186A187A188A189A190A191A192A193A194A195A196A197A1985000T/DA199A200A201A202A185A186A203A204A205PO525A206PO42A2075A197A198A208A209A210A211A212A213A214A215A216A217A218A201A202A185A186A21922原始数据1原材料G6980G6466A220A221A222A223A224A225A226A227A228A229A230LOSSSIO2AL2O3FE2O3CAOMGOSO3A231A232A233A234A235A236A23540332A237A238A239065511316A240A241109610606207103606A242A24322613122734722936815A244A245A246176519320425152511230A247A248325A245A2465423119432352156XXXXA249A250A251A252A253A254A255A8A0A10112煤工业G2010析A1A2A3A2A11A4A5A6A7A9MADA113A114CADA113A114AADA113A114VADA113A114MARA113A114A115A12A13QNETA99ADA113KJ/KGA11415049024224323257003其G1194G3（1）G5192平均气温15G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3（2）G5415G3332气G2399752MMHGG3G3G3G3（3）G3332G991水位G3G3G312MG3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G3G323配料计算231确保熟料率值的组成为了获G5483G17751高的熟料G5390度，良好的物料G7143烧G5627以及控G2058生产，选G6333G17878宜的熟料G989率值是非常必要的。本次设计为一台窑G3818G2010G16311窑，在生产工艺G990要求煅烧高饱和比高硅率的生料，这样G14033G6564高熟料的G17148量并G14033减少预热器G2010G16311G9821系统的堵塞和回转窑烧G6116带的结圈。生产P0425G3PO525号硅G18252G11428水泥熟料。对G1122新型G5190法水泥生工艺，水泥熟料率值G3835致为KH088091，SM2427，IM1418。故G7693G6466生产G4466G17353和设计工艺条件确定熟料的率值KH090002SM25501IM1601XXXXA14A15A16A17A18A19A20A21A22A2312232熟料热耗的确定随G11540新型G5190法水泥煅烧技术的G993断G6564高，熟料的热耗G993断降低，单位熟料热耗依G3281内新型G5190法厂G10628G10378，熟料热耗G24742885KJ/KG熟料233计算煤灰掺入量AADAAR（100MAD）（100MAR）G5062G11705AAD242G3G3MAR23G3G3MAD15G3AADG252空气G5190燥G3534灰G2010G3AARG252收G2052G3534灰G2010G3MARG252收G2052G3534水G2010G3G5483G3AAR241G3QNETAR（QNETAD25MAD）（100MAR）（100G3MAD）25MARG3G3G3QNETARG252收G2052G3534低位G2469热值QNETADG252空气G5190燥G3534低位G2469热值G3MADG252空气G5190燥G3534水G2010G3G3G3G3G3G5062G11705QNETAD25700G3G3MADG315G3G3MAR23G3G3G3G3G3G5483QNETAR2547127KJ/KGG3最后G5483出煤灰掺入量GAQAARS/QNET,AR29502411002547127279G3QARG252煤的收G2052G3534低位G2469热值G3G3QG252熟料的热耗G3G3AARG252煤收G2052G3534灰G2010G3G3SG252煤灰沉降率一般G2474100G3234用EXCEL计算干生料的配合比为了获G5483G17751高的熟料G5390度，良好的物料G7143烧G5627以及G7143G1122控G2058生产，选G6333G17878宜的G989率值是非常必要的。G11013G1122其牵涉G2052非线G5627方程的求G16311，用手工计算需反复试凑，难以G17810G2052结G7536最优，G13792G2520种简化计算方法G993容G7143掌握，采用办G1856软件EXCEL做配料计算，可G11464G6521G17902过表哥计算求G16311，G1972秒钟就可算G5483最优G16311，G6817作简G1427，结G7536准确，本设计G2454G13783G457用办G1856软件做配料计算G458（G2347G1152化工G3835G4410材料G4410G19510简G9168G3839，G5364G15195G457水泥G458XXXXA14A15A16A17A18A19A20A21A22A2313200010）等G17176料采用这种方法G17839G15904计算。（1）在EXCEL表中输入G6980G6466在EXCEL表中输入G990述G6980G6466,本设计为G3247G13464G1233配料，因此可以控G2058G989个率值KHG451SMG451IM。（2）G1563设原料配比在EXCEL表中G3647入G1563设的G2520原料配比，可以G4570G2033G3999配比设为石灰石20G451G20041G473320G451G19093矿20,最后G11734G4733一G20045G5224G3647G990“G729100（G21748G7643G9869）石灰石配比的单G1815格G20041G4733配比的单G1815格G19093矿配比的单G1815格”，G1889G6982回G17722G19202，这样G6177G14033保证配比G1055和为100。（3）计算生料G6116G2010在EXCEL表中G17878G5415的位置计算G7693G6466G1563设的原料配比G13792G5483G2052的生料G6116G2010。生料化G4410G6116G2010G2520原料化G4410G6116G2010G994其配比的G1068积G1055和。方法是在生料化G4410G6116G2010对G5224的LOSS单G1815格中输入“SUMPRODUCTB5B8,I5I8/100”回G17722。其中B5B8为G2520原料LOSSG2559量G6164在的单G1815格，I5I8为G2520原料配比G6164在的单G1815格。生料的其G1194化G4410G6116G2010可以G17902过对生料LOSS单G1815格的G6314G6301来获G5483。方法是G9869G1999生料LOSS单G1815格,G4570G21748G7643G12239G2052G16825单G1815格的G2503G991G16294，G4570光G7643G2476为G21669G2325G4395时，G6365G991G21748G7643G5050G19202，G2533G2503G6314G6301G14279生料G6116G2010对G5224的SO3单G1815格H9,G7506开G21748G7643G5050G19202G2375可。G3（4）计算G9808烧G3534生料G6116G2010水泥生料在煅烧后，原料中的LOSS就G8821有了，因此为了计算熟料G6116G2010，就必须计算生料G2447G19512LOSS后的化G4410G6116G2010，G2375G9808烧G3534生料G6116G2010。生料G9808烧G3534G6116G2010原生料G6116G2010/1LOSS/100。方法是在EXCEL表中G11468G5224G9808烧生料SIO2的单G1815格中C10输入“C9/1B9/100”回G17722。其中C9为原生料SIO2的单G1815格位置，B9为原生料LOSS的单G1815格位置。G9808烧生料的其G1194化G4410G6116G2010G1075可G17902过对SIO2单G1815格的G6314G6301来获G5483。（5）计算煤灰掺入量G13464G6116熟料的一小G18108G2010是燃料燃烧后产生的煤灰。煤灰掺入量计算G1856式是煤灰掺入量（煤灰占熟料的G11346G2010比）烧G6116热耗煤热值煤灰G2010。G1122是在对G5224的煤灰比例中（本例为I11）输入“A15/A17A19”回G17722。其中A15为烧G6116热耗G6164在单G1815格，A17为煤热值G6164在单G1815格，XXXXA14A15A16A17A18A19A20A21A22A2314A19为煤灰G2010G6164在单G1815格。熟料的G2490一G18108G2010为G9808烧生料，其比例为100煤灰比例。G1122是在对G5224的G9808烧生料比例中I10输入“100I11”回G17722，G5483G2052G9808烧生料在熟料中的比例。其中I11为煤灰比例G6164在单G1815格。（6）计算熟料G6116G2010和率值有了G9808烧生料G451煤灰的化G4410G6116G2010和比例就可以方G1427G3332算出熟料G6116G2010。方法是在EXCEL表中G11468G5224熟料SIO2的单G1815格中C13输入“SUMPRODUCTC10C11,I10I11/100”回G17722。其中C10C11为G9808烧生料G451煤灰的SIO2单G1815格位置，I11I12为G4439G1216的比例单G1815格位置。G5483G2052熟料的SIO2值，G1889G17902过对SIO2单G1815格的G6314G6301可以获G5483熟料其G1194化G4410G6116G2010。在EXCEL表中G17878G5415的位置计算熟料的率值，计算KH时输入“F12165D12035E12/28/C12”回G17722，计算SM时输入“C12/（D12E12）”回G17722，计算IM时输入“D12/E12”回G17722。（7）求G16311原料配比G9869G1999G14768单“工G1867”，选G6333“规G2022求G16311”G5389出G12395G2487，G9177空“设置目G7643单G1815格（E）”,在“可G2476单G1815格（B）”中选G6333EXCEL表中石灰石G451G11734G4733G451G19093粉比例单G1815格，G2375为I5I7。G6365“G9167加A”加约G7475条件KH，在“单G1815格G5353用位置”选G6333熟料G4466G19481KH值单G1815格C21,中G19400约G7475G12538选“”，约G7475值选EXCEL表中熟料目G7643KH单G1815格A21。G1889G6365“G9167加A”加G2490一约G7475条件SM，G1122“单G1815格G5353用位置”选G4466G19481SM单G1815格C23，中G19400约G7475G12538选“”，约G7475值选熟料目G7643SM单G1815格A23。G1889G6365“G9167加A”加G2460一约G7475条件IM，G1122“单G1815格G5353用位置”选G4466G19481IM单G1815格C25，中G19400约G7475G12538选“”，约G7475值选熟料目G7643IM单G1815格A25。G6365“确定”G17832回，G1889G6365“求G16311”就G1262G5483G2052最后的求G16311结G7536。G9869G1999“确定”保存规G2022求G16311结G7536。还可在EXCEL表中的G17878G5415位置输入其G1194G2454G6980（如G11345生料G10714G16782料耗G451生料配煤量G451G5190湿G3534换算G451生料CACO3G9416定值）的计算G1856式，就可G5483G2052G11468G5224的G2454G6980。如G991表XXXXA14A15A16A17A18A19A20A21A22A2315A24A25A26A27A28A29A30A31A32A24ABCDEFGHIA110A117A33A34A35A36A37A38A113A119A114A120A121A106A39A122A40A41A41SIO2AL2O3FE2O3A125A42A40A127A43A40SO3A129A44A131A45A46A45A121A47A99A120A120A99A117A110A47A99A111A131A131A110A110A99A120A133A133A99A48A133A111A69A49A110A48A111A99A110A47A99A111A47A99A111A117A47A99A50A110A47A99A120A111A120A99A121A120A117A50A62A51A117A99A117A111A110A120A99A110A117A99A117A50A120A99A121A50A117A99A117A48A120A99A111A133A110A99A121A48A117A99A117A110A133A133A51A63A46A110A99A50A111A131A110A99A48A120A117A99A47A121A117A99A131A110A131A99A117A131A110A99A110A117A131A99A120A50A131A48A52A34A120A111A99A47A121A48A99A117A117A131A117A99A111A133A110A117A99A120A111A121A121A131A99A50A120A110A99A120A110A110A47A99A47A120A120A110A47A136A53A52A34A110A121A99A121A117A117A99A48A131A121A117A99A121A117A48A121A111A99A133A121A117A99A121A110A111A47A99A47A120A120A48A50A99A117A117A110A110A63A46A131A121A99A117A120A110A99A110A48A121A99A120A117A120A99A131A117A110A99A131A111A117A99A50A50A133A110A117A68A34A110A131A99A131A120A120A99A50A120A133A117A99A121A133A117A121A131A99A111A121A117A99A120A48A117A47A99A47A120A120A110A120A110A121A53A37A12A54A113A137A55A56A137A43A68A34A114A110A131A117A133A133A131A110A111A63A115A12A13A113A137A55A114A110A50A117A131A50A47A47A110A133A63A46A38A110A48A117A121A99A117A117A47A68A34A39A57A137A58A68A34A59A60A137A58A117A110A47A99A133A48A47A99A133A48A47A117A117A68A34A39A57A41A127A68A34A59A60A41A127A117A120A117A99A131A117A99A121A48A48A117A121A68A34A39A57A144A127A68A34A59A60A144A127A117A131A110A99A131A110A99A131A47A47XXXXA14A15A16A17A18A19A20A21A22A2316235将干料配比折算成湿料配比原料G6817作水G2010石灰石16G11734G4733为06G19093粉15粉煤灰3G2029湿原料G17148量配比是湿石灰石8898（100G71316）9043湿G11734G4733343（100G71306）345湿G19093粉222（100G71315）225粉煤灰537（100G7133）554G2524计10167G4570G990述G17148量比换算为G11346G2010比湿石灰石9043101678894湿G11734G473334510167339湿G19093粉22510167221粉煤灰55410167545XXXXA14A15A16A17A18A19A20A21A22A2317第三章物料平衡G17902过物料平衡可计算G5483G2052G2520种原料燃烧的需要量以及G1186原料G17839厂G11464G14279G6116品出厂，G2520工G5219G6164需G3800G10714的物料量，依G6466这些G6980G6466可以G17839一G8505确定工厂的物料G17828输量G451工艺设G3803选型以及G3546场G1660G5223等设施的规G8181，因此，物料平衡计算是