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Page Number4@B4 Header  !HRH  Balloon TextCJOJQJ^JaJB'aB Comment ReferenceCJaJ<r<  Comment TextCJaJ@jqr@ Comment Subject5\FV@F FollowedHyperlink >*B* ph        !        zmnoprH0VH0H0VH0VH0v:H0(2H0H0H0mnopr000000000000000000000000000000l00Tl00l0 0 0 0 `\0 0\00H0000W00W00`00`00`00te00 e0!0"e0#0$f0%0&0'0(ؤ0)0*0+0,H0-0.=0/00 >0102X>0304>0506>0708?090:400mnopr @0@0@0@0@0 000  ^  l78,"$ԿP뤡A @ D F h0GCJOJQJ"h0G5CJOJQJ\]aJo(jh0GUh0GCJOJQJ^JaJh0Gh0Gh0GCJOJQJo( h0Go(. 0 2 6 8 < > B D H J L N P R T V X Z \ ^ $a$$a$gd0Ggd0G2 L ^ ` b d f h j l n p r t v x z | ~ .:p0GX> =!"#$%     *i !"#$%&'()J,-./012456789:<=>?@ABCDEFGHIhLMNOPQRSTUVWYZ[\]^_abcdefgvklmnopqrstuxyz{|}~Oh+'0 ,8L `l   tFigure 1 illustrates an example of a heat balance or distribution of heat for a clinker making facility in China Jim Davis Normal.dot galitsky5Microsoft Office Word@xA@`y@TUK՜.+,0` hp  A Alchas Inc.' qFigure 1 illustrates an example of a heat balance or distribution of heat for a clinker making facility in China TitleOle F1Table(+CompObjqWordDocument*,06F!What is PHAST!Object 12  FMicrosoft Office Word Document MSWordDocWord.Document.89q5F!What is PHAST!Object 6  FMicrosoft Office Word Document MSWordDocWord.Document.89qV@V Normal $1$a$$CJKHPJ_HaJmH nHsH tHDA@D Default Paragraph FontViV  Table Normal :V 44 la (k(No List >>  Footnote TextCJaJ@&@@ Footnote ReferenceH*6U@6  Hyperlink >*B*ph4 @"4 Footer  !.)@1.  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Page Number4@B4 Header  !H@RH  Balloon TextCJOJQJ^JaJB'@aB Comment ReferenceCJaJ<@r<  Comment TextCJaJ@jqr@ Comment Subject5\FV@F FollowedHyperlink >*B* phLKPriceB LKPi WZ  z +DEFSrs 0O0O0000000000+DEFSrsR T U W X Z [ ] ^ _ X0X0X0X0X0X0X0X0X0X0X0X0X0X0X0X0X0X0X0X0X0X0X0X0    8@0(  B S  ?*;4B+;,; -;?.;,/;W>> CC 9*urn:schemas-microsoft-com:office:smarttagsplaceB*urn:schemas-microsoft-com:office:smarttagscountry-region Pnv i =T BT U`fpR _ fiR _ :R _ R _ : ,Llp- =!"#$% Oh+'0 $ D P \hpx,Energy Assessment -Saving Tool for Cement  Jim Davis Normal.dot galitsky5Microsoft Office Word@`4<@`y@(Kd՜.+,0 hp   Alchas Inc.N ' +Energy Assessment -Saving Tool for Cement TitleOle F1Table47jCompObjjObjectPool69|uU,|uU,6F!What is PHAST!Object 10  FMicrosoft Word Document MSWordDocWord.Document.89q5F!What is PHAST!Object 9  FMicrosoft Word Document MSWordDocWord.Document.89q iN@N Normal $1$a$$CJKHPJ_HaJmH nHsH tH<A@< Default Paragraph Font66  Footnote TextCJaJ8&@8 Footnote ReferenceH*.U@.  Hyperlink >*B*ph, ", Footer  !&)@1&  Page Number,B, Header  !@R@  Balloon TextCJOJQJ^JaJ:'@a: Comment ReferenceCJaJ4r4  Comment TextCJaJ8qr8 Comment Subject5\>V@> FollowedHyperlink >*B* ph z@0@0@0 0@0@0@0@0 8@0(  B S  ? Jim DavisC:\Documents and Settings\Jim Davis\My Documents\Personal\Projects\Arvind\Description of PHAST -Cement for China jd edit 060709 .doc Jim DavisC:\Documents and Settings\Jim Davis\Application Data\Microsoft\Word\AutoRecovery save of Description of PHAST -Cement for China jd edit 060709 .asd: ,Llp-lllllGGG${ GGGGGOllOOOGXllOGO`OV@l` FX8  0=DxXO&8The PHAST-Cement tool can provide guidance in identifying possible energy-saving measures. PHAST-Cement can be used to estimate total energy savings resulting from each applicable energy saving measure for the clinker making equipment and estimate of total energy savings from application of one or more suggested energy saving measures. This information can be used to estimate reductions in greenhouse gas emissions using other tools. Results The PHAST-Cement tool results provide information on current energy use and distribution as a guide to identify areas of major heat or thermal energy losses. It enables the plant to consider methods to reduce energy losses such as kiln surface heat losses and or recover energy contained in exhaust gases or cooling air streams from clinker cooler for other uses such as steam and power generation. The results can be used to estimate financial benefits in for the selected measures in terms of (RMB/year), and the emissions reductions potential and savings for the selected measures (ton CO2/year). Emissions reductions will be based on energy savings achieved by using the energy saving measures identified during the auditing process.      jUB*CJH*OJQJphB*CJOJQJph5B*CJOJQJ\ph CJOJQJ7$8$H$? =!"#$%  Oh+'0 4 HT p | ZThe PHAST-Cement tool can provide guidance in identifying possible energy-saving measuresnhe  Jim DavisCeim  Normal.dote Jim Davise4m Microsoft Word 9.0o@0@(ST@*՜.+,0H hp  * Alchas Inc. ZThe PHAST-Cement tool can provide guidance in identifying possible energy-saving measures Title1Table;>CompObjjObjectPool=@|U,|U,WordDocument iN@N Normal $1$a$$CJKHPJ_HaJmH nHsH tH<A@< Default Paragraph Font66  Footnote TextCJaJ8&@8 Footnote ReferenceH*.U@.  Hyperlink >*B*ph, ", Footer  !&)@1&  Page Number,B, Header  !@R@  Balloon TextCJOJQJ^JaJ:'@a: Comment ReferenceCJaJ4r4  Comment TextCJaJ8qr8 Comment Subject5\>V@> FollowedHyperlink >*B* ph*  z* )1N`Rcd  ! $ ' + 0000 0 0 0 0 0 0 0 0 00000 0@0@0@0@0 * ) *  ) 8@0(  B S  ?       ! " $ % ' ( +        ! " $ % ' ( +        ! " $ % ' ( +  Jim DavisC:\Documents and Settings\Jim Davis\My Documents\Personal\Projects\Arvind\Description of PHAST -Cement for China jd edit 060709 .doc Jim DavisC:\Documents and Settings\Jim Davis\Application Data\Microsoft\Word\AutoRecovery save of Description of PHAST -Cement for China jd edit 060709 .asd: ,Llp- $ 22GX  ` V4@ FDXt ]0x3X&8Data Collection and Use of PHASTCement In order to prepare a heat balance that shows various areas of energy use for a clinker making process, it is necessary to collect operating data for the equipment. The data can be collected by plant personnel or by using services from an organization such as China Building Materials Academy (CBMA) - China Building Materials & Test Certification Center. The data collection process, in most cases, does not affect normal production; however, it requires installation or use of process monitoring instruments at several locations in the system. It is also necessary to collect information on the products and fuel used for the kilns and other fired equipment. In most cases such data are easily available from the plant personnel. The data may include variables such as: Composition of raw materials used and its feed rate in kg or tonnes per hour Production of clinker in terms of kg or tonnes per hour from each kiln, composition of clinker produced and discharge temperature. Type, composition and amount of fuels used in the kilns, precalciners etc. Measurements on exhaust gas composition and flow Measurements on clinker cooling air and its distribution after discharged from the clinker cooling Outside surface temperature for the kiln and other components where heat is lost to the ambient by radiation and convection. Information on other uses of heat such as cooling water or air used within the system, if any. Information on auxiliary equipment such as electric motors for fans, rotary kilns etc. that enables the model to estimate electrical energy used. Energy costs (in RMB) per tce of fuels used. PHAST-Cement offers the user the opportunity to use this data to do a quick assessment and establish current level of energy use with an opportunity to identify and analyze effect of several possible energy saving measures. Modeling Energy Use or Heat Balance The data collected during the assessment is used to prepare a heat balance that illustrates heat used in various areas of the kiln and associated equipment. Analysis of the heat balance allows plant personnel and the assessment team to identify major areas of heat loss and recoverable heat that can be used in the plant. The team discusses possible improvements and identifies energy-saving measures.     )c     " # % & * jU CJOJQJ5CJOJQJ\ )1N` R c d    ! " $ % ' ( ) h^h & F 1$ ) ) * ? =!"#$%SummaryInformation(?ADocumentSummaryInformation8Ole  EData BDOh+'0 $ @ L Xdlt|)Data Collection and Use of PHASTCement ordata Jim Davisctim  Normal.dott Jim Davist4m Microsoft Word 9.0 @0@(ST@Q՜.+,0 hp   Alchas Inc.9  )Data Collection and Use of PHASTCement Title5F!What is PHAST!Object 8  FMicrosoft Word Document MSWordDocWord.Document.89q5F!What is PHAST!Object 7  FMicrosoft Word Document MSWordDocWord.Document.89qDdG1 0  # A"qw$C~pU!VMD+@=Ew$C~pU!VHJ$rJx] pU޽!al(S~qI `7D?MOBD+L*ā #beFKJ'`sٗ}$‹ܗټ{sv>+GiL' *dl]eOg36D|c+8cy88v @H<! 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Hyperlink >*B*ph, ", Footer  !&)@1&  Page Number,B, Header  !@R@  Balloon TextCJOJQJ^JaJ:'@a: Comment ReferenceCJaJ4r4  Comment TextCJaJ8qr8 Comment Subject5\>V@> FollowedHyperlink >*B* ph  zX@0@0 0@0@0@0@0 8@0(  B S  ? Jim DavisC:\Documents and Settings\Jim Davis\My Documents\Personal\Projects\Arvind\Description of PHAST -Cement for China jd edit 060709 .doc: ,Llp-@Unknown Gz Times New Roman5Symbol3& z ArialU"CalibriCentury GothicC PMingLiUe0}fԚ;SimSun??5& zaTahoma?5 z Courier New;Wingdings"1h== .!0dD2q HX Jim Davis Jim Davis7 bjbjUU  7|7| lF82 > F>VVVVV111vxxxxxx$5 UP111119VV9991XVVv91v9$9]V@jVJ p1FX j 0xXj9&8 Figure 2. Comparison of energy use loss distribution for a clinker making system Before and after application of energy saving measures - developed using PHAST-Cement     5CJOJQJ\]aJ jU X$a$ ? =!"#$%SummaryInformation(IDocumentSummaryInformation8Ole $EData JLROh+'0\   $ 0<DLT ss Jim Davis im  Normal.dot Jim Davis4m Microsoft Word 9.0@V@(ST@՜.+,0 hp   Alchas Inc.  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V|H.b>(y"J;#.iH!ytҙV"ҕ7e^IWr~Y; =yʯr%UTr ?.<<")̓|<6V>,@}] @Kh*m1|ОKxoy1.2`d 2Y ,@VK \.2||2] .AO@ !cftt0t{!4́]χ--l>\J63s/lh6lilLݰ鰽ilblNTd$l&lDxvl<?>0p|bp+|d$p p3|g0?cӒ%znL~|&o), $;5-Bm@gyղd5 4YGe=eS5K^F&zDޠe3-7i)/[iA YJ?F/vzYޢWmZ#;h6NzCޡ-.m]]ޣޑ=Kާ=>*"/AO:$aȿ|B|F_:)Gr ZoK:+'[4k☳@1dХpc?}~`U֧_Y\SZyuٛ/m*gh+1߁m7^_98s?ɛtb-] sLYlކyg )i;Q˲Eً{G{ tg\3eM"H7(ZfDR %𙠎oaبgU/3`"Ŕ5‹FLmO5ǁ`?O㭘aLJaZJf`$ǔD)8+#Oy&IMYxx\OjO+TV9`ʢŁ!{&;_:DmXǗ\yt\y1eIxQiحCǠM"cwZ_qձ/|Guz -FlA=eZ抳ڪQoRk=}3,!^U1QGg~MYCL x->T$d\̹sS͇G&h*kfҒ* 8g|}hp4Mӿɡߔ5BRoW?՛):p3 7~9|9x~2\w;7svu-s/ڻa@~T1\7SV'ocJOK≠hK?/~:LYNՎw5W/EԾ~PMYQHfS";3pepAe{c*^42?,&[t{xB#  ,xw֪Ob TVpɫ{屖Ls8YUv}~]6+o, \^{p}ݨkf_uNn>k].Wpe1Table3CompObjKO&jObjectPool`qU,`qU,WordDocumentNP    !"#$%&'()*+,-./0123456789:;<=>?@ABCDEFGHIJKLMNOPQRSTUVWXYZ[\]^_`abcdefghijklmnopqrstuvwxyz{}~ iN@N Normal $1$a$$CJKHPJ_HaJmH nHsH tH<A@< Default Paragraph Font66  Footnote TextCJaJ8&@8 Footnote ReferenceH*.U@.  Hyperlink >*B*ph, ", Footer  !&)@1&  Page Number,B, Header  !@R@  Balloon TextCJOJQJ^JaJ:'@a: Comment ReferenceCJaJ4r4  Comment TextCJaJ8qr8 Comment Subject5\>V@> FollowedHyperlink >*B* ph z@0@0@0@0@0@0@0@0@0@0 0@0@0@0@0 8@0(  B S  ? Jim DavisC:\Documents and Settings\Jim Davis\My Documents\Personal\Projects\Arvind\Description of PHAST -Cement for China jd edit 060709 .doc: ,Llp-&(((((($ .LLaX&&$ VV@ hdFd9X  w0x3X3&8Figure 1 illustrates an example of a heat balance or distribution of heat for a clinker making facility in China. Figure 2 provides an example of the comparison of energy use at current operating conditions and possible energy use by taking certain energy-saving actions for the same kiln. PHAST-Cement can be used for a cement kiln with or without including precalciner, preheaters etc.  Figure 1. Energy use loss distribution for a clinker making system developed using PHAST-Cement     5CJOJQJ\]aJ jU CJOJQJ$a$> =!"#$%SummaryInformation(Q DocumentSummaryInformation8VBAVQU,X,ThisWorkbookaOh+'0 ,8L `l   qFigure 1 illustrates an example of a heat balance or distribution of heat for a clinker making facility in Chinatigu Jim Davisllim  Normal.dotl Jim Davisl4m Microsoft Word 9.0s@V@(ST@H՜.+,0` hp  A Alchas Inc. qFigure 1 illustrates an example of a heat balance or distribution of heat for a clinker making facility in China Title s \p薗g(gΘhekditor Ba=:ot  ptntqt ThisWorkbook=5!8@"1Arial1Arial1Arial1Arial1Arial1:Arial Rounded MT Bold1:Arial Rounded MT Bold1Arial1Calibri1 Calibri1Calibri14Calibri1 Calibri1Calibri1$Arial1Calibri1,8Calibri18Calibri18Calibri1 Arial1 Arial1>Calibri14Calibri1<Calibri1Arial1?Calibri1h8Cambria1Calibri1 Calibri1 Arial1Arial1Arial1Arial1Arial1Arial1 Arial1 Arial1 Arial1Arial1 Arial1@ Arial1@Arial1Arial1 Arial1 Arial1 Arial1Arial1 Arial1 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    Correction factor or density factor if applicable (1=Default)Apparent density of flue gases4Already accounted for in heating of charge material Mass of particulates in exhaust 2Heat in collected particulates in collector systemThis includes heat in gases not including water vapor and volatiles plus chemical heat in solids collected plus heat in unburned combustibles in gaseous formcTotal weight of solids collected (exhaust gas particulates plus collection from bag house ESP etc.)/Density calculations for exhaust gas components3Exhaust - flue gases leaving the kiln or Preheated [Mass or weight collected in particulate collection equipment (bag house, ESP etc.) - total Cp (Average)*Cp (at temp) - Calculated&Cooling water loop name or designation/Specific heat of air VOLUMETRIC - calculations 'Available heat for combustion products 1Total content of heat in ash contained in clinkerChemical heat contained in combustibles in exhaust gases (CO, combustibles etc.plus particulates) + chemical heat in material collected in ESP or bag houses etc. ,Power factor (average value) (Default=0.85)4% Operating time (as % of total time) (Default=100%)ABC Cement Company Next Page Previous Page Go To ReportkJ/(nm^3 - deg. C.) E3M Inc.15216 Gravenstein WayNorth Potomac, MD 20878This is the temperature at which the finished clinker leaves the kiln (after or at the end of the cooling bed) . The units of measure are Degrees Celcius.cThis is the mass specific heat of the clinker material. The un< its of measure are kJ/(Kg-Degrees C)qMolecular weight of the volatiles (CO2 = 44). This can be chaged by the user if the volatiles are other than CO2yThis is the moisture content of the raw material as charged. The units of measure are in percent of the charge material.Name of the volatiles driven off from the raw material. This consists primarily of CO2. Give name if it is other than given here.This is the average surface emmisivity of the wall area bein calculated. Default is 0.8 but it can be changed by the user if necessary..cThis is the total outside area of the shell - wall area being calculated. Units are square meters.QName of the flue gases such as "charge end" or any other name for identificatioj.Water Vapor contained in the flue gases in percent by volume on a dry basis. Default is 4% but it can be changed by the user if necessary.,Name or nature of the particulates collectedAHeating Value of the collected combustible material in kJ per Kg.&Name of the opening for identification4The specific heat of the cooling air in kJ / (nm3-C)This is the mass specific heat of the other particulate material. The units of measure are: kJ/(Kg-Degrees C),The heating value of the fuel, in kJ per Kg.3Other Heat Losses or Gains to the system in kJ / hr)The destination of the air flow. Exhaust thru the system means the heat is recovered or recirculated or used internal to the system. Exhaust outside the system means the heat is recoverable by other means, for example recovery of heat from clinker cooling bed for its use in a waste heat boiler.-Number of elctric current phases (usually 3) FAverage power factor. Default is 0.85. It can be changed by the user.E-mail: athekdi@e3minc.comOffice Phone: (240) 715-4333Mobile: (240) 605-7545E3M Inc.Control Button Titles Menu Choices Print Report Print SheetE3M Inc.Return to Openings Data SheetXYZ Cement PlantDestination of Air FlowExhaust Thru SystemExhaust Outside the System!Recoverable Heat in outgoing air wCalculation of Total heat in exhaust gases related to fuel combustion (not including heat in water vapor and volatiles)GAir or Gas outlet temperatureNumber of FuelsNumber of Air StreamsHelpPHAST For CEMENT HELP FILE Clinker production ratefThis is the rate at which the raw material is charged into the kiln. The units of measure are Kg/hr.uThis is the temperature at which the charged raw material enters the kiln. The units of measure are Degrees Celcius.Water vapor from the raw material is driven off in the kiln. This is the discharge temperature of the water vapor as it leaves the kiln.aThis is the rate at which the finished clinker leaves the kiln. The units of measure are Kg / hr.7This is the heat of reaction for the remaining material6Additional Heat Lost in the kiln or added to the kiln.lThis is the ambient temperature of the room or area in which the kiln is located. Units are Degrees Celcius.hThis is the average surface temperature of the wall area being calculated. Units are in Degrees CelciusrThis is a correction factor based on conditions. For example, wind would increase the heat loss from the surface. Return To<Temperature of the exit gases at the flue in Degrees Celcius?Volumetric flow rate of the exit gases in cubic meters per hourDOxygen content of the flue gases in percent by volume on a dry basisLCarbon Dioxide content of the flue gases in percent by volume on a dry basisMCarbon Monoxide content of the flue gases in percent by volume on a dry basisWCarbon Monoxide content of the flue gases in parts per million by volume on a dry basisMSulpher Dioxide content of the flue gases in percent by volume on a dry basis^Total combustibles remaining in the flue gases at the exit in percent by volume on a dry basisVNitrogen Oxide content of the flue gases in parts per million by volume on a dry basisAParticulates contained in the flue gases in grams per cubic meter^Total weight of the particulates collected in the baghouse during the collection period in Kg.-Time length of the collection period in hoursWhat is PHAST?VPercent calcined material in material collected from particulate collection equipment HPercentage of the collected material which consists of calcined material|Percentage of the collected material which consists of combustible materials (unburned coal or other combustible materials)'Shape of Opening (Round or Rectangular)TIf there are multiple openings of the same size enter the quantity of these openings+Total area of each opening in square metersMAverage temperature of the kiln in the area of the opening in Degrees CelciusLAmbient temperature in the area where the kiln is located in Degrees CelciusGThickness in millimeters of the kiln wall where the opening is located.If the opening is rectangular, enter the length of the opening in meters. If the opening is round, enter the diameter of the openingkIf the opening is rectangular, enter the width of the opening in meters. If the opening is round, no entryXEstimate the radiation view factor using the chart, or enter if the view factor is knownXPercentage of time the opening is open, for example, a door may be open 50% of the time.=Enter the flow rate of the cooling water in liters per minute=The inlet temperature of the cooling water in Degrees CelciusJThe exit temperature of the cooling water from the kiln in Degrees Celcius=Emissivity of the radiation source (the inside of the kiln) RA correction factor to account for increased heat losses due to unusual conditionsGEnter the flow rate of the cooling air in normal cubic meters per hour.;The inlet temperature of the cooling air in Degrees CelciusHThe exit temperature of the cooling air from the kiln in Degrees CelciusWThe exit temperature of the cooling air from the clinker cooling bed in Degrees Celcius2Temperature of the particulate matter at dischargeRPercentage of the collected other material which consists of combustible materialsIThe quantity of fuel used in Kg/hr. This assumes a solid fuel like coal.8The moisture content of the fuel in percent, as charged.6The carbon content of the fuel in percent, as charged.?The volatile matter content of the fuel in percent, as charged.3The ash content of the fuel in percent, as charged.HThe temperature of the fuel as it reaches the burner, in Degrees Celcius'Name or designation of the motor or fanDVolumetric Flow Rate in normal cubic meters per hour (for fans only)*Pressure Rating (for fans only) in PascalsMotor Power Rating in KwSupply voltage in VoltsCurrent rating in Amps'Percentage of time the motor is running/Model number or description of the fan or motor#number for heat input to the system4Enter a positive number for heat loss or a negative 3Up to six additional losses or gains may be entered,Chemical Composition of the charge material:6Chemical composition of the charge material in percentOther material 0Percentage of the total composition that is SiO21Percentage of the total composition that is Al2O31Percentage of the total composition that is Fe2O3/Percentage of the total composition that is CaO/Percentage of the total composition that is MgO/Percentage of the total composition that is SO20Percentage of the total composition that is fCaO-Weight of the raw meal or charged material kJ/(kg. C)Cp (KJ/kg-C) = A + B*Temp (F) For 60 deg. FFor 1000 deg. FCp calc for SI units#Heat added in volatiles at exahsut %Calculations for heat input required (Calculations for volatile heat required Heat of foramtionRAW Meal;Heat for all water - solvent to boiling point or final temp)Heat of evaporation for water discharged Heat for superheating vapors3Heat for residual liquid to go to final temperature Heat for superheating vapors6 Heat for residual liquid to go to final temperature= Heat for all water - solvent to boiling point or final temp Temperature Total kJ/(kg-deg. C.)ClinkerKiln 1 Fuel/Energy 4< Fuel/Energy 5 Fuel/Energy 6 Cement Kiln 3Equipment (kiln or precalciner) name or designationCurrent Modified "Charge material name - designationkg/hr.Initial charge temperaturedeg. C. kJ/(kg.C)5% moisture (water) in the charge material as charged %"Water vapor discharge temperature >Name or type of volatiles discharged from the charge material "Molecular weight of the volatiles MMass of the volatiles discharged from the charge material (% of dry material)JMass of the volatiles discharged from the charge material in terms of ratekJ/kg<Volatiles discharge temperature from the kiln or precalciner;Heat of reaction for the remaining devolataliized material 2Temperature of the residual material at discharge kJ/hr9Additional heat loss/used (+ve) or released/added ( -ve) - 1-Modified&Losses from the furnace wall surfaces Number of wall surfaces Outlet temperaturef(x) =  + 92.85714285700499 * x - 57.589285713967165 * x^2 + 89.58333333320397 * x + 112.67857142839111 * x + 123.74999999979063 * x + 15.624999999800524 * x^3 - 49.99999999970236 * x^2 - 70.98214285673158 * x^2 - 99.99999999951825 * x^2 + 10.416666666480479 * x^3 + 15.624999999744734 * x^3 + 31.249999999699078 * x^3 + 26.84166666841611 * x + 39.39166667187432 * x + 29.458333334781596 * x + 64.56666668066461 * x - 4.354166667853229 * x^2 - 11.604166669748727 * x^2 - 4.520833334469769 * x^2 - 29.916666674500892 * x^2 - 0.0833333330461522 * x^3 + 1.8541666670689478 * x^3 - 0.6874999996066529 * x^3 + 7.145833333961459 * x^3 + 0.10416666665553202 * x^4 - 0.14583333321793268 * x^4 + 0.2708333332730645 * x^4 - 0.8333333328744414 * x^4 - 0.008333333336867471 * x^5 + 0.004166666639021022 * x^5 - 0.020833333330372142 * x^5 + 0.037499999908537356 * x^5Ratio(Dia/Thk.) CylindricalSquare2x1 RectangularCooling water flow rate2Correction factor or density factor if applicable Cooling air or gas flow rate Motor phasePower factor (average value) Deg. C.from control sheet nm^3/hrkg/hr/Exhaust - flue gas location name or designationKiln charge sideOxygen - O2 (dry) % : Carbon dioxide - CO2 (dry) %:Carbon monoxide - CO (dry) % Carbon monoxide - CO (dry) ppmvppmvTotal combustibles - (dry) %Particulates if any Mass flow rate of gasesLPMWater Inlet temperatureWater Outlet temperature$Air cooling loop name or designation:Specific heat of the volatiles discharged (average value) 5Temperature of gases at exit end of the kiln - heater&Specific heat of the gases (if known) kJ/(kg.deg. C) Name or designation of gases $Composition - measured or estimated ,Time or number of hours - collection period Nature or name of particulates Air or gas inlet temperature*Air flow - leakage area name - designation/% combustible material in particulates (if any)Energy ConversionENERGY CONVERSION FACTORS From one:To:EJBtceBtoeTcm NGQuadExajoule'Billion metric tons coal equivalent [2]&Billion metric tons oil equivalent [3]%Trillion cubic meters natural gas [4]Quadrillion Btud[1] These factors are as per footnote 1 on p. 2, and follow the U.S. convention of high-heat values.[2] Chinese conversion factors for coal and other fuels are low-heat values. Chinese average raw coal contains 20.93 GJ/metric ton (low heat), or 22.51 GJ/t (high heat), assuming that low-heat values for coal are 93% of high-heat values. China typically converts all its energy statistics into  metric tons of standard coal equivalent (tce), a unit that bears little relation to the heating value of coals actually in use in China. One tce equal 29.31 GJ (low heat) equivalent to 31.52 GJ/tce (high heat).[3] China uses a conversion factor for its oil of 41.87 GJ/metric ton (low heat), equivalent to 44.07 GJ/ t (high heat), assuming that low-heat values for oil are 95% of high-heat values.[4] China uses a conversion factor for its natural gas of 38.98 GJ/thousand cubic meters (low heat), equivalent to 43.31 GJ/tcm (high heat), assuming that low-heat values for natural gas are 90% of high-heat values.'Name or designation of the drive motor kWMotor power (name plate)Pressure (for fans only)Flow (for fans only)Kiln drive motorOther drive motors Other useSupply voltage Average current NOx ppmvSulfur Dioxide (SO2) :"Chemical analysis of the material Raw mealSiO2Al2O3Fe2O3CaOMgOSO2fCaOAll in percentage (%)Coal AshLoss *Data for charge and final product materialCEquipment (kiln or precalciner) name, location or other designationHMotor driven system name designation - (select one form the list below)Electric motor or fan ModelOptions for selection -Fans for combustion air, exhaust or other useCurrent Total$Heat used for the load - component 1Btu/hrForm base material spreadsheet %Heat used for the load - component 2 From other spreadsheets $Heat used for the load - component 3Demand Btu/cycle Heat exchanger (HTX) waterRated water flow rategpm)Load factor - low flow as % of rated flow"Percentage cycle time at low flow Inlet temperatureDeg. F.&Load factor - high flow as % of rated #Percentage cycle time at high flow Heat loss for low flowHeat loss for high flow&Heat loss related to HTX water cooling"Heat loss related to water coolingHot Zone - Insulation Give a drop-down menu for commonly used materials with specific heat and density. Allow user defined material with required property values Number of layersLayer 1 ThicknessinchAreaft^2Initial temperature*deg. FFinal temperature* Heat storageBtuLayer 2Layer 30Total heat storage for hot zone, Insulation etc. Calculated deg. F.Summary Calculated"Heat for water evaporation & vaporLatent heat of moistureSpecific heat of water Heat in remaining water in load kJ/(kg C)Equation for perfect gaspv P is in Pa v in m^3/kg T in deg. KCp = 1R = Ru/MRu = J/(kg. mol K)M = One atmosphere kg/m^3 T in deg. Cdensity lb/ft^3Nm^3/hr.Volume (std. condition) of volatiles reelased kJ/kg C$Specific heat of water vapor (steam)NewDeg. F Btu/hr-ft^2 Calculations kg/nm^3Calculations - RectangularMass flow of waterft^/hrLbs./hr Heat lossDeg. CkJ/kg-KDiff%ConstABconst + A*X + B*X^2Density of Air at 0 deg. C. Specific Heat of air kJ/(nm^3-C)Temp Cp (at temp) Btu/(ft^3 F)Diff kJ/(nm^3-K)Average air temp Equation Cp= *Temp CFor 10% Xs airAv. Heat = A + B* Temp (F) !Available Heat for Coal (Typical).Correction for Air Temperature and Excess Air Cp for Air+ * Temp (F) Excess Air =, 100*8.52381*(%O2/100)/(2-9.52381*(%O2/100))Ex. Air vs. % O2Av. HeatXs air correctionPreheated air correctionFurnace Flue Gas Temperature Oxygen in flue Gases Excess Air Combustion Air Temperature Available Heat Av. Heat 1Pht. Air correction Cp air% of gross Heating ValueEfficient Combustion - newWall Loss - currentWall Loss -newAir infiltration - draft data Air infilt. Sack ht. Data Steel Charge Pht current Steel Charge Pht newCooling water - current Cooling water - modified/ =100*8.52381*(17.1/100)/(2-9.52381*(17.1/1<00))% O2 = 3100*8.52381*(%Xs air/100)/(2-9.52381*(%Xs air/100))*Wall Loss Higher Temperature Calc Current Cooling air savingsOpening loss - current Opening loss - newAirinfiltration - draft 1-1Airinfiltration - draft 1-2Initial Gas temperature (F)Final Gas temperature (F)CpSp. VolSp. Wt Sp. GravityMean CPGasTemp (F)Temp Btu/(#mole.F)Mol wtBtu/(#F)SCF/##/SCF wrt Air @stpBtu/SCFOxygenNitrogenCarbon MonoxideHydrogenWater vapor (H2O)Carbon Dioxide Methane - CH4 Methane - CH5 Ethylene C2H4 Ethylene C2H5 Ethane C2H6 Ethane C2H7 Source - Gas Engineers Handbook For Air at 60 F., 80% Humidity Composition of gas mixture % Vol% massMean CP Btu/scfCp-60 FCp 1000FOxygen Nitrogen & Other Water vapor Mean value cp for airCoeff for Cp - Air%Excess Air - O2 relationship for Coal"% O2 = Const + A*Xs air + B*Xs airy = 0.6105x2 + 2.6827x + 1.2445 R2 = 0.9986'Excess Air = Const1 + A1*%O2 + B1*%O2^2Const 1A1B1% O2 % Excess AirFor Bituminous Coal Typical air fuel ratio - stoich scf/100 Btu nM3/100kJscf/btunM3/btunM^3/kJnM^3/hrBtu/lb.For SI Units - pressure in Pa(short cut for std. conditions (0 deg. C)&sp. Volume = (22.42)/Mol. Wt (kg/mole)Density= Mol. Wt./22.42Mol. WtConstant at 0 deg. CFor US Units - pressure in psigP is in lbs/ft^2 v in ft^3/lb T in deg. F T in deg. Rft-lb/(lbm-mol-R)*short cut for std. conditions (32 deg. F.)&For US Units - pressure in inch of Hg &sp. Volume = 358.95/Mol. Wt (lb. mole)Density= Mol. Wt./358.95Constant at 32 FCp Mol. Wt.Density(kg/nm^3)Carbon dioxide"Water vapor in combustion productsNitrogen approx. %% !Volume flow rate of exhaust gasesVolume flow rate of volatiles :Total mass flow rate of combustion products and excess air+Total mass flow rate of total exhaust gases kJ/nm^3 C Btu/SCF-FCp (Btu/scf -F)Cp (kJ/nm^3-C)Deg C(Heat in exhaust gases based on av. Heat Excess air Exhaust ags data sheet Combustion air temperature Primary air used ;Available Heat: Coal Combustion for typical 20% excess air Av. Ht. CalculatedErrorAvailable heat 0Total heat input in the kiln (coal + Other fuel)Heat in volatiles 1Heat in moisture evaporated from charge material 7Heat in charge material (Total - vapors and volatiles) Heat of formation kJ/kg clinkerkCal/kg of clinkerkJ/kg of clinker!Total heat for clinker formation Heat of clinker formation Heat used for clinker formation Weight of clinker formed Final clinker temperatureHeat for clinker formation Sensible heat in clinker 5Specific heat of the clinker material (average value)!Heat contained in waste products Total going into the system)Theoretical (Stoichiometric) air required)total volume of exhaust gases - measured Total volatile gases in exhaust HideDefaultOUTPUTHeat loss for water coolingHeat loss in air !Heat in particulates from exhaustDHeat in completely combusted combustion products and excess air used$Specific heat of combustion products kJ/nm^3-CVolume of water vapor water vaporCO2PTotal heat in exhaust gases including water vapor, volatiles, combustibles etc. ZTotal volume of combustion products (measured FG volume - volatiles - water vapor) value A3Sensible heat in exhaust gases (item above value A)6Heat in particulates collected - chemical heat content Preheater Heat used for ash discharge Moisture vapor volumeSpecific heat of clinker - ashHeat supplied in fuel#Total volume of moisture from coal 8Sensible heat in clinker - supplied to raise temperature hb Tybc[Nx(u7beQpencY(zbR㉉p) Tybc[Nx9Clinker Production Energy Usage By Areas ( kJ/Kg Clinker)qeuNnO(uk ( CS&q / CSKQqe)Energy Usage (KJ/Kg Clinker)nO(u (CS&q / CSKQqe)/Distribution of Energy Usage-Clinker Production qeuNnO(uR^qePgevkp0USMO:NCS&q/(CSKQ-Ddl^)ue(Wz-Nʑ>ev4ll0ُ/f4lly_4llzev)n^0 #ueNuv%cSbR0%cSbR;N1uN'lSx~b0Yg N/f ~Q Ty0(%cSbRvRP[ϑN'lSx:N44 0,gSpeSNf9eYg;N%cSbR N/fN'lSx0qeQes0USMO:NCSKQ/\e0 iRYOPgevS^p0ueۏes USMO:NCSKQ/\e0eQzuev)n^0USMO:NDdl^0qeQzev)n^(QtS^KNTb+gz)0USMO:NDdl^0vQNp_c1YbReQ4llzvpϑUevSf[bRTybRv~vRk 0N'lSEx(SiO2)@b`SkO N'lSNݔ(Ai2O3)@b`SkO N'lSN(Fe2O3)@b`SkO 'lS(CaO)@b`SkO 'lSA(MgO)@b`SkO N'lSkx(SO2)@b`SkO8ny'lS(fCaO)@b`SkOvQNbR@b`SkO{zX:SWvs^GWhb)n^0USMO:NDdl^0@b(WMOnvsX)n^0USMO:NDdl^0${zX:SWvs^GWhbS\|pe0:w:N0.8 Yg ,gSpeSN9eS0{zX-X:SWv;`vYhby0USMO:Ns^es|0!hck|pe0OYΘORhbvp_c1Y0plv Ty0OY e+gz bNUOvQN(uNƋv Ty0ply_{Sev)n^0USMO:NDdl^0 QtS4lAmϑ(GS/R)QtS4l(WۏSYv)n^Ddl^ QtS4ly_zev)n^Ddl^ !hck1uNvQN^ck8^`Q[pϑ_c1YXRv!hckVP[|~vQNpϑ_c1YbXR(CS&q/\e)Yg/fpϑ_c1YeQckpe &TReQpe eQ|~vpϑ;`pegYSNeQ6*NYvpϑ_c1YbXRn 5u:gbΘ:gv Tybc[Nx Θ:gb5u:gvWSbcSR[([Θ:g)(USMO/f^eaS) 5u:gRs[CSt 5uAmvMOpe8^:N3 O5u5uSOyr 5uAm[[W 5u:gЏLeN~vRkh:y qeO(upeϑ(CSKQ/\e)GP[Ǒ(uV`qe OYdq 6RYTqe-N4lRkON~vRkh:y 6RYTqe-NxbRkON~vRkh:y 6RYTqe-N%cSir(kON~vRkh:y 6RYTqeTppbRkON~vRkh:y qe0Rqppev)n^Ddl^ qep@3Other heat loss or generation- unaccounted if known,@vQN*geQb*gwpϑ_c1YbNuB63Other heat loss or generation- unaccounted if known~ f? 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RZ!English @kJ/kg of clinker @ CS&q / CSKQqeBkJ/kg of clinkerk 8 UZ!English @tce/tonne clinker"@ (ThQdq / (TqeBtce/tonne clinker 8h 8! RZ!English @kJ/kg of clinker @ CS&q / CSKQqeBkJ/kg of clinkerk 8  UZ!English @tce/tonne clinker"@ (ThQdq / (TqeBtce/tonne clinker 9~ ?l:" #VZ!English )@Heating of charge raw material@peRpB!Heating of charge raw material#`Rg+ Z D #`X Dtr! DD#`Rg+ Z D #l`X Dtr!?m DD@ Lf;x" PZ!English !@Kiln shell heat losses@zXp_c1YBKiln shell heat losses%*pZ Z { Ltrv LD%*pZ Z l{ Ltr?}mo LD@n<X XZ!English )@Exhaust - flue gas heat losses@^lp_c1YB!Exhaust - flue gas heat losses% Z Z ^y2u%G% Z Z l^y2u?#@t<\  ^Z!English +@ Openings - radiation heat losses@_Sp\_c1YB# Openings - radiation heat losses%"mZ GZ 6%"mZ GZ l?&,~ @o<] YZ!English $@Water cooling heat losses@4lQtS[p_c1YBWater cooling heat losses%-ZZ LZ \%-ZZ LZ l\?]_{~ @o<] YZ!English "@Air cooling heat losses @ zzlQtS[p_c1YBAir cooling heat losses% >Z QZ 0c?G% >Z QZ l0c?B XA~ @=$\ rZ!English 9@.Hot products - mat'l sensible heat carried out"@ &^Q'YϑpϑvpNTB1.Hot products - mat'l sensible heat carried out%Z UZ %Z UZ l@ @l<0^ VZ!English #@Combustion and other air@RqTvQNzzlBCombustion and other air%'Z ZZ vk3%6T4Z ZZ l<1?"@v<] `Z!English -@"Other or waste products discharged@vQNNTbp#nB%"Other or waste products discharged%s!Z _Z ^,VG%s!Z _Z l^,?#$@>(" Z!English 2@'Other losses (+ve) or heat input (-ve)<@vQNp_c1Y(+ve) b pϑeQ (-ve)B*'Other losses (+ve) or heat input (-ve)%Z cZ n%Z cZ nAS? =Z!English @ Summary :@Gl;`B Summary :h@  RZ!English @kJ/kg of clinker @ CS&q / CSKQqeBkJ/kg of clinkerm@ !WZ!English "@GJ /Tonne of clinker@ T&q / (TqeBGJ /Tonne of clinker Ah@  RZ!English @kJ/kg of clinker @ CS&q / CSKQqeBkJ/kg of clinkerm@ WZ!English "@GJ /Tonne of clinker@ T&q / (TqeBGJ /Tonne of clinker BC #Z!English 6@+Total kiln - preheater heat demand + losses4@z - phVpϑBl + _c1Y ;`ϑB.+Total kiln - preheater heat demand + losses#  %)nD.A#ie %#W %)&D.A# %&@ DlD4 VZ!English !@Energy input from Fuel@1uqeeQvϑBEnergy input from Fuel%aJZ gZ ):lD.A %B"?WZ gZ ) D.A mE WZ!English  @Difference - Error % @ ]+R - ] %BDifference - Error %+[6iDDDA +ėDDDA  (@ DF Z!English Z@OElectrical power user equipment (kwh per kg of clinker)2@5uR(u7bY (CSte / (Tqe)BROElectrical power user equipment (kwh per kg of clinker)%bZ vZ  %bZ vZ m GHIIJIIJDI,l&$/^h+V>om|x%  J ! " ;# J $ J%  & +@ ( ) * + , - . / 0  GHIIJIIJ!GQ! ;Z!English @Summary@Gl;`B Summary!"G~"GH  #hZ!English /@$Energy use/tonne of clinker produced"@ nO(u / (TqeB'$Energy use/tonne of clinker produced["Ix EZ!English @ GJ /Tonne@ T&q / (TB GJ /Tonne3"n Z kZ  "3"&"Z kZ   "7#G#H "}Z!English @@5Recoverable heat from exhaust and clinker cooling air&@ N^lTQtSzzlV6epϑB85Recoverable heat from exhaust and clinker cooling air[#J "EZ!English @GJ/hour@ T&q / \eB GJ/hour.#"Z ZZ  #.#Wv#Z ZZ   #7$GHIIJIIJ %&" &D Return to Control Page && D  Next Page (K(X*D- Office Phone: (240) 715-4333)K )D+15216 Gravenstein Way)XL(D.Mobile: (240) 605-7545*K|)D,North Potomac, MD 20878*X&D/E-mail: athekdi@e3minc.com +V ,V -V .V /W0$,yQw~P  Q  Qs2(   i@eR0|:(  |j | 0NMM?`]`P  s "P??3` #'` #'PH@0(  п3d23 M NM4 3QQ< C:Q< C:Q3_43_ O *  MM< 43_ O ̙/  MM< 43_ O 3f0  MM< 43_ O 4  MM< 4E4D $% M@3O&Q4$% M@3O&Q4FAi3O> 3" $% XM@3OQ '43_ M NM  MM< 444% XM 3OQ'44e?e?e  | VA# ?@ CommandButton23%7']` 1 6$TȀForms.CommandButton.1P>@<d&&&!!""##""##       7j&&yK #'Chart-Energy use distribution'!A1J&&yK 'Control page'!D23//yK yK Lmailto:athekdi@e3minc.comyX;H,]ą'c Sheet1ggD s  83Ҹx4t$<+25  dMbP?_*+%h63&LEnergy Use Analysis for Cement Kilns - Preheaters0-&LE3M Inc.&RJune-29-2009&CABC Cement CompanyM\\JIM-CASS\HP DeskJet 812C (CoC odXXLetterDINU"H$%#| HSMTJ8HP DeskJet 812CInputBinFORMSOURCERESDLLUniresDLLPSAlignmentFileHPV880ALPSHelpFileHPVDJ200OrientationPORTRAITPaperSizeLETTERResolutionr300x300PMPlainNormalColorMediaTypeSTANDARDPQNormalColorModeColor24HPHTDLLNameHPVIMG50$$$$"dXX??cU} } $'}  }  |}  u}  @} m @} 3 @ wA wA wA A A  A  hA   A  wA  wA  wA wA wA  JA  JA  JA  JA  JA  JA  JA  JA  JA  JA  JA  JA  JA  JA  A  JA  JA r[ Z\Z!English )@Cement Plant Heating Equipment@4llSRpYB!Cement Plant Heating Equipment|"h[ fZ!English /@$Summary of Heat (Energy) Requirement @ p(n)YGl;`B'$Summary of Heat (Energy) Requirement#####$    !N |Y  8Z!English @:@:BReturn to Control Page  ~ ?k+X  UZ!English &@Raw meal - charge materials@ue-peBRaw meal - charge materials,,,,,-N DY  8Z!English @:@:B Next PagefLX PZ!English %@Number of charge materials@pepeBNumber of charge materials?Z!X[ D  CurrentD[ D  Modified N XY  8Z!English @: @: B Print Sheet #  $ Z>v Dtr Z?   X X>ZZABC Cement Company %  $ & Z-  D tr  Z-   X ' $  Z-   D tr  Z-   X U  ?Z!English @KJ/hr@CS&q/\eBKJ/hrO  9Z!English @TCE@(ThdqBTCEU  ?Z!English @KJ/hr@CS&q/\eBKJ/hr O  9Z!English @TCE@(ThdqBTCE X ~ XX hZ!English /@$Total heat for load - all components"@ ;`p}@b gN B'$Total heat for load - all components # k %    D tr# k %   g D tr U AtZ u?Z!English @Current@S_MRpencB Current '()XXXXV ApY u@Z!English @Modified@O9epencB Modified~ @m X WZ!English &@Kiln Shell wall heat losses@zXXp_c1YBKiln Shell wall heat lossesXdXW NZ!English @Number of wall areas@zX:SWpeBNumber of wall areas@tZ! 4[ D  Current`Z D  Modified X}W gZ!English 4@)Heat used for kiln Shell wall heat losses@zXXp_c1YϑB,)Heat used for kiln Shell wall heat lossesZ6   DtrZ6 P DtrXX X~ @v`W `Z!English )@Exhaust - Flue gas heat losses @ cl-{Slp_c1YB!Exhaust - Flue gas heat lossessX$W ]Z!English (@No. of exhaust points - zones@clp-:SWpevB No. of exhaust points - zones?Z! $[ D  CurrentLZ D  Modified XyV cZ!English ,@!Heat loss in Exhaust - Flue gases @ cl-{Slp_c1YB$!Heat loss in Exhaust - Flue gases?HcZKLd( Dtr?HZZK Ld(m DtrX X     X~ @    ~   ~ $@  ~ @U@   ~ T@ Dl*#e;Y24HHH! JA " JA # JA $ JA % JA & JA ' JA ( A ) JA * JA + JA , A - JA . JA / JA 0 JA 1 JA 2 JA 3 JA 4 JA 5 JA 6 JA 7 JA 8 JA 9 JA : JA ; JA < JA = JA > JA ? JA @ JA ! ! !~ ![@!" " ""V@# dD"# # ##.@$ dD#$ $ $$T@&D $% % %~ %^@%& & &S&'=D33333 @<*DdDdD!D &' ' 'S'(=D33333 @<*D"dD#dD%D$'( ((!(* D&D'()* * *!*3 D(D*+  X~ ,@ ,, ,  ,- -!-~ -@- . .". .u . / /!# /$~ // 0 0!% 0&~ 0r@0 1 1!' 1(~ 1i@1 2 2!) 2(~ 2h@2 3 3!* 3+@3:*D/ D0*4*5D2D13 4 5 5,5 5u 5 6 6!# 6$~ 66 7 7!% 7&~ 7r@7 8 8!' 8(~ 8i@8 9 9!) 9(~ 9@9 : :!* :+@:A*D6 D7*;*<D9D8: ;! < <-< <u < = =!# =$~ == > >!% >&~ >r@> ? ?!' ?(~ ?i@? @ @!) @(~ @y@@ D+ lH]]YH[_JDFHHHH~FHHHH~FHHHA JA B JA C A D JA E JA F JA G JA H JA I JA J JA K wA L JA M JA N JA O JA PA QJA RJA SJA TJA UJA VJA WJA XJA YA ZJA [JA \JA ]JA ^A _JA ` JA A A!* A+@AC*D= D>*B*CD@D?A B C C". C#+C$mD3D:DA-C$$% D ~ E@tEV ^Z!English +@ Openings - Radiation heat losses@_Sp\_c1YB# Openings - Radiation heat lossesEFuFXTV E_Z!English .@#Number of radiation heat loss zones@p\:SWpeB&#Number of radiation heat loss zonesF@Z! F[ D  CurrentFF8Z D  Modified FGGU F{Z!English :@/Total radiation loss from openings in all zones*@@b g:SW-N_Sp\_c1Y;`ϑB2/Total radiation loss from openings in all zonesGGZ"uG DGtrGZ"u GG DGtrGH&'((() I ~ J@kJU GUZ!English $@Water cooling heat losses@4lQtSp_c1YBWater cooling heat lossesJKKXhU JnZ!English 5@*Number of water air cooling loops or zones"@ 4lQtSVb:SWpevB-*Number of water air cooling loops or zonesK@FZ! K[ FD  CurrentKK$Z FD  Modified KLsL$U K]Z!English ,@!Water cooling systems heat losses@4lQtSp_c1YB$!Water cooling systems heat lossesLL*GZ&LG DLtrL*GZ& LLG DLtrLM+,---./N.~ O@kOT LUZ!English "@Air cooling heat losses@zzlQtSp_c1YBAir cooling heat lossesOP`PXT OJZ!English @Number of components@NpeBNumber of componentsP Z!LPZ KD  CurrentPPZ KD  Modified PQwQT PaZ!English *@Air cooling systems heat losses @ zzlQtS|~p_c1YB"Air cooling systems heat lossesQQ*LZ )QL DQtrQ*LZ ) QQL DQtrQR.~ S@|S*S TfZ!English 1@&Hot products - materials heat losses *@pNTp_c1Y *B)&Hot products - materials heat losses *STTV0T QjZ!English 5@*Number of areas for hot products discharge@pNTQe:SWpeB-*Number of areas for hot products dischargeT?KZ!TZ PD  CurrentTTY PD  Modified TUUWtS S|Z!English ?@4Heat losses associated with Hot products - materials&@ 1uNpNT[vpϑ_c1YB74Heat losses associated with Hot products - materialsU^U_QZUQ DUtrU_QZ UUQ DUtrUPPPPPPV012334W~ X @dX@S UNZ!English Combustion and other airRqbvQNzzlBCombustion and other airXYYTR XxZ!English 7@,Number of air sources (cooling air or leaks)*@zzln(QtSzzlbl2)pevB/,Number of air sources (cooling air or leaks)Y@TZ!YZ TD  CurrentYYY TD  Modified YZZR YsZ!English 2@'Data for combustion air and leakage air*@RqzzlTl2zzl[p_c1YB*'Data for combustion air and leakage airZZ5Z@ZU DZtrZ5Z @ ZZU DZtrZ[012334\~ ]"@u]PR Z_Z!English ,@!Other or waste products discharge@vQNQeb^eB$!Other or waste products discharge]^~^TQ ]hZ!English 3@(Waste product discharge sources or areas@^eQenb:SWB+(Waste product discharge sources or areas^@YZ!^Z YD  Current^^Y YD  Modified ^__tQ ^Z!English M@BHeat losses associated waste products or other areas of the system.@N^eb|~vQN:SWvsQvp_c1YBEBHeat losses associated waste products or other areas of the system__5UZ O_Z D_tr_5UZ O __Z D_tr_`6Dl~iCYSUUeoQa JA b JA c XA d JA e JA f JA g JA h JA i JA j JA k ;Al ;Am JA n w8!o 8p g8!q h8r ;8s J8!t J8!u J8!v J8!w w8!x w8!y h8z h8{ h8| h8} h8~ h8 h8 h8~ a$@a $Q _Z!English 1@&Other losses (+ve) or heat input (-ve)<@vQNp_c1Y (+ve) bpϑeQ (-ve)B)&Other losses (+ve) or heat input (-ve)abbUP aZ!English UNNumber of additional heat sources (+ve heat input) or sinks(-ve heat supplies)@vQNpnpevBQNNumber of additional heat sources (+ve heat input) or sinks(-ve heat supplies)b@^Z!bZ ^D  CurrentbbY ^D  Modified bccO bZ!English V@KHeat contained in leaving the system (+ve) and/or entering the system (-ve)>@|~pϑ_c1Y(+ve)bۏeQ|~vpϑ(-ve)BNKHeat contained in leaving the system (+ve) and/or entering the system (-ve)cc_Zc_ Dctrc_Zc6c_ Dctrcd~ e&@ke  cUZ!English @Fuel - Energy input @ qe - neQBFuel - Energy inpute      fvfT# e`Z!English -@"Number of fuel supplies or sources@qeO^npevB%"Number of fuel supplies or sourcesf@cZ!fZ bD  CurrentffY bD  Modified fgg fwZ!English 8@-Heat input from fuel and other energy sources(@ NqeTvQNneQvpϑB0-Heat input from fuel and other energy sourcesgglZ_gc DgtrglZ_ g6hi_id vIZ!English  @TOTAL FOR ALL SOURCES@;`TBTOTAL FOR ALL SOURCESi jjZ fD  CurrentjjY fD  Modified jk%kM iyZ!English 6@+Total kiln - preheater heat demand + losses,@z-R㉉ppϑBlT_c1Y;`TB.+Total kiln - preheater heat demand + losseskUk'%p?DcD_DZDUDQDLDGDDD k:g DktrUk?Hc?DcD_DZDUDQDLDGDDD  k/kLd( Dktrkl%llN($ gVZ!English #@Heat input in the system@eQ|~vpϑBHeat input in the systemlllDglk DltrlbDg lm&dmOH kNZ!English @Difference - error@]+R(])BDifference - error m+mEkDkDlDkAm+mk DkDlDkA mn:;;;777o~oP# lhZ!English /@$Energy use/tonne of clinker produced"@  / (TqeuNB'$Energy use/tonne of clinker producedVoQ{ m@Z!English @GJ/tonne@ T&q/(TB GJ/tonne1o/nxDkZ  o01o1&oDkZ   o237ppR oZ!English @@5Recoverable heat from exhaust and clinker cooling air.@NclbqeQtSzzl-NV6evpϑB85Recoverable heat from exhaust and clinker cooling airWpS{ oAZ!English @GJ/hour@ T&q/\eB GJ/hour*p4oDZD p5*p6WvpDZD  p787q9:;;;777rrԏ pZ!English C@8* Note: Already included in charge material calculations.@* lʑ: ]~Sb(Wpe{-NB;8* Note: Already included in charge material calculationsr777s s>>>t(@" DeqtĎ r[Z!English *@Electrical power user equipment@5uRO(uYB"Electrical power user equipmenttuuX t|Z!English ?@4Number of electrical power driven equipment (motors)&@ 5uRqRY(5u:g)pevB74Number of electrical power driven equipment (motors)u@fZ!uZ jD  CurrentuuY jD  Modified uvvЍ uZ!English M@BEnergy used by electrically driven systems such as electric motors.@5uRqRY(Y5u:g)@b(u;`5uBEBEnergy used by electrically driven systems such as electric motorsLv$ p6Z!English  @kW@CStBkWvvZ BvvgZ B vw= w>>>x=x[ uD Return to Control Page x>>y= y>>>z= z>>>{= {>>>|= |>>>}= }>>>~= ~>>>= >>>= >>>DilCNoT h8 h8 h8 h8 h h h h h h h h h h h h h h h h h h h h h h h h h h h h= >>>= >>>= >>>= >>>?888?888?888?888?888?888?888?888?888?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@Dhl  h h h h h h h h h h h h h h h h h h h h h h h h h h h h h h h h?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@Dl  h h h h h h h h h h h h h h h h h h h h h h h h h h h h h h h h?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@Dl  h h h h h h h h h h h h h h h h h h h h h h h h h h h h h h h h?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@Dl  h h h h h h h h  h  h  h  h  h h h h h h h h h h h h h h h h h h h  h?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@ ? @@@ ? @@@ ? @@@ ? @@@ ? @@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@?@@@ ? @@@Dl ! h" h# h$ h% h& h' h( h) h* h+ h, h- h. h/ h0 h1 h2 h!?!@@@"?"@@@#?#@@@$?$@@@%?%@@@&?&@@@'?'@@@(?(@@@)?)@@@*?*@@@+?+@@@,?,@@@-?-@@@.?.@@@/?/@@@0?0@@@1?1@@@2?2@@@(T   pv @P 0(  0^B 0 c $D@AA]`Ֆrj 0 0NMM?]`֖  s "??3` #'R` #'SPH`0(  пп3d23 M NM4 3QQ = Q = Q3_43_ O *  MM< 43_ O ̙/  MM< 43_ O 3f0  MM< 43_ O 4  MM< 4E4D $% M@3O&RQ4$% M@3O&SQ4FA3O]3" $% XM@3OQ '43_ M NM  MM< 444% XM 3OQ'44e?e?e rj 0 0NMM? 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M4% OhMZ3O &\Q kW'4523  43" 44% Q !MP3O*&ZQ b/Energy Use - Losses Electric Resistance Furnace'44e?e??e f^r  0 c $A jJnn] `xmf^  0 c $A jJnn] `Ɩf^r  0 c $A jJnn] `Dؖ 0 VA ?@ CommandButton40x z5]` h[1 6$T̀Forms.CommandButton.1HP>f@xxxRJooooppppJJIIRRNNLLFFkm FFKKKKPPOOSSXXWWTTTTPPQQeedd]]\\``aaZZ__GGEEDD YYYY^^^^ggiiffffhhuuuuttbbbbrrjjjjjjcc7JxxyK 'Control page'!D24 Sheet5gg@ s  $VYZ  dMbP?_*+%63&LEnergy Use Analysis for Cement Kilns - Preheaters&LE3M Inc.&RJune-07-2009M\\JIM-CASS\HP DeskJet 812C (CoC od,,LetterDINU"H$%#| HSMTJ8HP DeskJet 812CInputBinFORMSOURCERESDLLUniresDLLPSAlignmentFileHPV880ALPSHelpFileHPVDJ200OrientationPORTRAITPaperSizeLETTERResolutionr300x300PMPlainNormalColorMediaTypeSTANDARDPQNormalColorModeColor24HPHTDLLNameHPVIMG50$$$$"d,,??cU}  } } I } I} m } $ "  R <Z!@English@  :@:BReturn to Control PageV$ @Z!@English@ @:@:B Next PageV8 @Z!@English@ @:@:B Previous PageVT # @Z!@English@ @: @: B Print SheetV  @Z!@English@ @:'@:'B2/Distribution of Energy Usage-Clinker Productiondsjnl# @ # HZDReturn to Control Page# B #D Previous Page# Bl # D Next Page  xt #  ^F(  v  <NMM?  ],`IlpZdT9(  s M\\JIM-CASS\HP DeskJet 812C (CoC od,,LetterDINU"H$%#| HSMTJ8HP DeskJet 812CInputBinFORMSOURCERESDLLUniresDLLPSAlignmentFileHPV880ALPSHelpFileHPVDJ200OrientationPORTRAITPaperSizeLETTERResolutionr300x300PMPlainNormalColorMediaTypeSTANDARDPQNormalColorModeColor24HPHTDLLNameHPVIMG50$$$$"d,,??3` ,` ,` ,PH0(  ?3d23 M NM4  3QQ ;Q ;Q3_ O   MM< 4 3_ O "  MM< 43_ O   MM< 43_ O   MM< 43_ O   MM< 43_ O 3f  MM< 4E4D$% M@3O&Q4$% M@3O&Q4FA3O43" :dd 23O m% M3O&!Q423 M NM44$% M@3OQ '43_ M NM  MM< 444% lMZ3O&&Q b/Distribution of Energy Usage-Clinker Production'4% LM 3O3Q '4% -M 3O 3Q '4% nzM 3O 3Q '4% AM 3Ot3Q '4% :M 3O&3Q ' 4% $ M 3O<Q '4%  M 3O3Q '4%  M 3O5<Q '4% M 3OQ '4% M 3O3Q '4% ; M 3OE<Q '44 eEHeating of charge raw material5Kiln shell heat lossesEExhaust - flue gas heat lossesI Openings - radiation heat losses;Water cooling heat losses7Air cooling heat lossese.Hot products - mat'l sensible heat carried out9Combustion and other airM"Other or waste products dischargedW 'Other losses (+ve) or heat input (-ve)e Q'@*5pp@cp@"m@o-Z?w >׏?QHb@'x@K8*}E@ e   VA ?@ CommandButton41#P%-]` 1 6$ˀForms.CommandButton.1P> @$$$7J##yK 'Control page'!D23h## yK =$p$6'PHAST Summary Report'!A1h## yK "'Chart- energy use comparison'!A1 Sheet28ggD s  +w}}  dMbP?_*+%63&LEnergy Use Analysis for Cement Kilns - Preheaters0-&LE3M Inc.&RJune-07-2009&CABC Cement CompanyM\\JIM-CASS\HP DeskJet 812C (CoC od,,LetterDINU"H$%#| HSMTJ8HP DeskJet 812CInputBinFORMSOURCERESDLLUniresDLLPSAlignmentFileHPV880ALPSHelpFileHPVDJ200OrientationPORTRAITPaperSizeLETTERResolutionr300x300PMPlainNormalColorMediaTypeSTANDARDPQNormalColorModeColor24HPHTDLLNameHPVIMG50$$$$"d,,??cU}  }  } I } } m } $ } +         R  # <Z!@English@  :@:BReturn to Control PageN   8Z!@English@  ::B Next PageN   8Z!@English@  ::B Previous Page|  Z! EnglishN   8Z!@English@  : : B Print SheetN   8Z!@English@  ::BABC Cement CompanyR 4  <Z!@English@  :#@:#B<9Clinker Production Energy Usage By Areas ( kJ/Kg Clinker)R  <Z!@English@  :$@:$BEnergy Usage (KJ/Kg Clinker)U  ?Z!English @Current@S_MRpencB CurrentV   @Z!English @Modified@O9epencB Modifiedsbdkyg" @ # X@ * #d dZD Return to Control Page# CH #D  Previous Page # * (} * # ^F(  v  <NMM?@ !]`TՖ  s M\\JIM-CASS\HP DeskJet 812C (CoC od,,Letter Print Sheet +uArialp@2iwJ` >J` -` 0 ` 0 PH0(  пv@3d23 M NM4  3Q: CurrentQ ;Q ;Q3_4E4  3Q: ModifiedQ ;QQ3_ O   MM<4E4D$% M@3O&Q4$% M@3O&Q4FA0 3O0 3 b#M!  43*#M! M! M NM4% CMZ3O&Q <Energy Usage (KJ/Kg Clinker)'43" :2dG Y3OG |% M3O&Q4444c3/ ?3O% M3O&/Q423 M NM444% OHgMP3ON2&Q v9Clinker Production Energy Usage By Areas ( kJ/Kg Clinker)'44 eEHeating of charge raw material5Kiln shell heat lossesEExhaust - flue gas heat lossesI Openings - radiation heat losses;Water cooling heat losses7Air cooling heat lossese.Hot products - mat'l sensible heat carried out9Combustion and other airM"Other or waste products dischargedW 'Other losses (+ve) or heat input (-ve)e Q'@ Q'@*5pp@*5pp@cp@cp@"m@"m@o-Z?o-Z?w >׏?w >׏?QHb@QHb@'x@26T4@K8*}E@K8*}E@  e   VA$ ?@ CommandButton42 "0$]` &1 6$/πForms.CommandButton.1P> @%%%7j## yK #'Chart-Energy use distribution'!A1J##yK 'Control page'!D23 Sheet29ggD s   r  dMbP?_*+%63&LEnergy Use Analysis for Cement Kilns - Preheaters&LE3M Inc.&RJune-07-2009MAdobe PDFS oSXXLetterPRIV ''''0\KhCFFSMTJAdobe PDF ConverterResolution1200dpiPageSizeLetterPageRegionLeadingEdgeInputSlotOnlyOne0EBDAStandard"SXX??cU} T} $8P} P} It} $,} } $ } } m9} $/r@A ,A0AJA AAA c A A A AAAcAAAAAAA AA J   W>X :AZ!English @ Cement Kiln@4llzB Cement Kiln??BBBBUVVWWWWWX~ w?@|& ZZ! Heat input to charge materialAABXX}t HgZ!English >@3Equipment (kiln or precalciner) name or designation@:B63Equipment (kiln or precalciner) name or designationRu, <Z!English @Kiln 1@z 1B Kiln 1UC $?Z!English @Current@S_MRpencB CurrentVE( @Z!English @Modified@O9epencB Modified RA4( <Z!@English@  :@:BCopy Current to ModifiedUJw` 4Z!English  @$ @$ B%"Charge material name - designationVv< @Z!English @ RAW Material@ueB RAW MaterialDFRA' <Z!@English@  :@:BDone Entering Data S  z  A,P& &DHelpJx 4Z!English  @$ @$ B0-Weight of the raw meal or charged material V~$) @Z!English @kg/hr.@CSKQ/\eB kg/hr. &' u NA& 8Z!@English@  : : BHelp  [  A-QJx̕ 4Z!English  @$ @$ BInitial charge temperatureS~) =Z!English @deg. C.@Ddl^B deg. C.ghNA& 8Z!@English@  : : B Print Sheet  |  A.QJxD' 4Z!English  @$ @$ BFinal clinker temperatureS~4' =Z!English @deg. C.@Ddl^B deg. C.ghRA' <Z!@English@  :@:BABC Cement Company    A/ QJ yD 4Z!English  @$ @$ BFCSpecific heat of the clinker material (average value, Default=1.03)e |) OZ!English @ kJ/(kg.C)$@ CS&q/(CSKQ-Ddl^)B kJ/(kg.C) (Y@(Y@    c9 QJ zؔ 4Z!English  @$ @$ B85% moisture (water) in the charge material as charged ~ )*    A1 QJ zx' 4Z!English  @$ @$ B%"Water vapor discharge temperature S ~( =Z!English @deg. C.@Ddl^B deg. C. gh  A0 QJ zX 4Z!English  @$ @$ BA>Name or type of volatiles discharged from the charge material  GHI  A2 QJ y 4Z!English  @$ @$ B2/Molecular weight of the volatiles (Default=44)  +F@'F@   A3Q  ~-,ĝTo?8ZZZ-,ĝTo?8ZZZ !  Q  O-69D !dDDDD  BO-9D !dDDDD  B ""  Q  {4.OD dDDd4.'D dDDd   QJx| 4Z!English  @$ @$ B?<Volatiles discharge temperature from the kiln or precalcinerS~( =Z!English @deg. C.@Ddl^B deg. 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Exhaust - flue gases losses J. 4Z!English  :@:BDone Entering Data^ T, HZ!English @Kiln charge side@zezBKiln charge sider H \Z!English '@clinker dust, ash and carbon@qe|\0ppTxBclinker dust, ash and carbonJ0 4Z!English  : @: BHelpL1 DDHelpJ 4Z!English  @$ @$ BFCEquipment (kiln or precalciner) name, location or other designation/ D  Kiln 1U/ K?Z!English @Current@S_MRpencB CurrentV/ @Z!English @Modified@O9epencB ModifiedJ0 4Z!English  : @: B Print Sheet  A  PJ0 4Z!English  @$ @$ B2/Exhaust - flue gas location name or designation(-  D Kiln charge side J- 4Z!English  :@:BABC Cement Company  A  A J x 4Z!English  @$ @$ B63Exhaust - flue gases leaving the kiln or Preheated  A A J < 4Z!English  @$ @$ B Name or designation of gases   b* D  Charge end c+  D  Charge end A A J  4Z!English  @$ @$ B85Temperature of gases at exit end of the kiln - heaterS `0 T=Z!English @Deg. C.@Ddl^B Deg. C.  A  J  4Z!English  @$ @$ B$!Volume flow rate of exhaust gasesW 1 KAZ!English @nm^3/hr@hQzes|B nm^3/hr  A     DN | A   DN |  AJ@ 4Z!English  @$ @$ B'$Composition - measured or estimated E  A  J1 4Z!English  @$ @$ BOxygen - O2 (dry) %[1 EZ!English @% dry@% `Sr^l~vRkB% dry FO  A  AJd4 4Z!English  @$ @$ BCarbon dioxide - CO2 (dry) %[<2 EZ!English @% dry@% `Sr^l~vRkB% dry FO  A  A JH2 4Z!English  @$ @$ B Carbon monoxide - CO (dry) % [2 EZ!English @% dry@% `Sr^l~vRkB% dry GP  A  A!   HN  A  A J3 4Z!English  @$ @$ BSulfur Dioxide (SO2)  FO  A  A"J2 4Z!English  @$ @$ BTotal combustibles - (dry) %[0 EZ!English @% dry@% `Sr^l~vRkB% dry GP  A  A#J2 4Z!English  @$ @$ B NOx ppmv   A  A$J 4Z!English  @$ @$ B41Water vapor in combustion products (Default=4.0%) I@Q@  A  AJ@3 4Z!English  @$ @$ BParticulates if any [03 EZ!English @gms/m^3@KQ / zes|B gms/m^3 JR  A  AJ$ 4Z!English  @$ @$ B^[Mass or weight collected in particulate collection equipment (bag house, ESP etc.) - totalL3 6Z!English  @kg@CSKQBkg K  A  AJ 4Z!English  @$ @$ B/,Time or number of hours - collection period O4 9Z!English @hours@\eBhours LS  A  AJ3 4Z!English  @$ @$ B"Nature or name of particulates d D clinker dust, ash and carbone  D clinker dust, ash and carbon  A  A J 4Z!English  @$ @$ BYVPercent calcined material in material collected from particulate collection equipment  MS  A(  AJ 4Z!English  @$ @$ B2/% combustible material in particulates (if any)  LS  A  AJ0 4Z!English  @$ @$ BFCHeating value of combustible particulate material (Default=19,200)U84 ?Z!English @kJ/kg@CS&q/CSKQBkJ/kg@@ Au Au  A  A{  AuDQl=k:U#PPP ?2_ A!A"h # $ %A&A'A(A)A*A+A,A-A.A/ 0 1 2 3  4 5 6 7 8 9 : ; < = > ?  { !{ ! "`N "u#u$u%{ %v %A%w@YD%w@&D%&{ &v &X0&wY@%dDDD'0&wY@)dDDD'&'{ '({ (v (AOv(I)8?+`DDUDDWD%dD%d@DV@D&DTD%ddv(I%?+`DDUDDWD%dD%d@DV@D&DTD%dd(){ )v  )X-),ZZZ-)?ZZZ)*{ *: *;.*<EZ6Z0Z0.*<EZ6Z0Z0*+{ +v +X!+) D D(!+, D D(+,{ ,v ,A!,0 D+D)!,4 D+D),-{ -ww.{ .A . /A /u/|x?/Z/|@@1Z 0A 0u(/0|@@6ZX? @/0|@@3ZX? @ 1A 1u1 5o?X@3Z1%Z2Au 3C 3DC3E i-D1dZZZ9Z?DA,3E8D1dZZ 4B 4F-4GRZ8Z2Z2-4G4Z8Z2Z2 4t 5) 5*+,~ 5؎ A 6- 6.&6/MDD &6/MDD )6H}%@U_)Ǻ?؎ A%6H}%@=_)Ǻ?D5I613D HzA@{Gz?D ?zG? 7-l 7.m7/8Z 7/8Z 77 8J 8K=8N='D6D D7?(\@=8N='D6D D7?(\@'8(DYDFD  93 94-9gED6DdD-9g?D6DdD :@ :./0 ;J ;K!;L6 DD~ ;M|@%;|yX!8A62U0*@D5 <-l <.m<L9Z <L<Z  =J =K==LI'D;D D7Q?(\@==LI'D;D D7Q?(\@%=H}%@;_)Ǻ?D5>-./0 ?3 ?4-?59D;DdD3?66D;D6DdDD<l n$zz(^^,r~x^@ AX B, C, D E FAGAHAI:AJKgP LMANAO:AP AQ R AS AT AU AV W X Y  @|. Ah AiWAjKADd@Dd@@HzB@zG?D WAjKADd@Dd@@HzB@zG?D B7899C7899 DA DF-DG0Z.Z(Z(-DG<Z.Z(Z( EE=D4FD* nm^3/hr6E>F Z<Z6Z6ZX6E>F Z<Z6Z6ZX EtF{ F?F=T4DDE nm^3/hr(F<GD D*DE(F<GD D*DEFG{ GHGB0GI?HADYDFD Z M0GI?HADYDFD Z MGH{HBIII{ IO IO!IPO D8D=!IPO D8D= It IPPPJuKJK@ 4Z!English  @$K @$K BzwCalculation of Total heat in exhaust gases related to fuel combustion (not including heat in water vapor and volatiles)YK0 CZ!English @kJ/hr@CS&q / \eBkJ/hr!KC?H6 DGDA!KD?H* DGDA KK K   K ALuM{ MA MA!MN D;D6!M|@N D;D6MN{ NA NA/N7DMDdZ N/N7DMDdZ NNO{ OOOO!OP DNDI!OP; DNDI Ott OPPPP{ PQuR{ RA RA'R?HRDKD4DD'R?HDKD4DDR RS{ SA SA S SS SNT{ TA~ TA<@%TI9n?(DTQk6@TIEf?UZ TU{ UA~ UA@@%UI p5?WDUQk6@UI }?VZU V~ Vu2@%V$?TDVQk6@VVz?WZ W~ WuF@%W~7-zf?VDWQk6@W1[+4?&ZX Y_Y2x?*IDTD&DUDDVDDWDDDD%D&8 ~  z Zzzff F x    / / o3 MF MF  R  vaT olaU \0V B0(  ^B  c $D@]`urjB  @ 0DԔGG] `urjB @ 0DԔA:A@]`u  TA. ?@CommandButton3   ]` Pu1 6$4ӉxForms.CommandButton.1@\  A( ?@ <CommandButton12yK control_page!D6 b ]` u1 6$pӉ<Forms.CommandButton.1X  VA ?@ CommandButton26 Z x]` 4su1 6$ӉForms.CommandButton.1P>@<d2KK 7lyK =$h$7Exhaust___flue_gases_losses Sheet17 s  $&o7  dMbP?_*+%Jt63&LEnergy Use Analysis for Cement Kilns - Preheaters0-&LE3M Inc.&RJune-07-2009&CABC Cement CompanyMAdobe PDFS o_XXLetterPRIV ''''0\KhCFFSMTJAdobe PDF ConverterResolution1200dpiPageSizeLetterPageRegionLeadingEdgeInputSlotOnlyOne0EBDAStandard"_XX??cU} } I0} } } $} }} I}}  }} I } $} $} $ } &}  w@ ` ` ` ` ` ` ` ` ` ` ` ` ` ` ``````````````` ` @ \ۚ? 4 @}m@ "=*@   }V}< @Z!@English@ @: @: BHelp     }V @Z!@English@ @:@:BCopy Current to Modified    }V @Z!@English@ @:@:BDone Entering Data     }V}< @Z!@English@ @: @: B Display Chart  V}4> @Z!@English@ @: @: B Print SheetϠ=@=7@}}A@V}? @Z!@English@ @:@:BABC Cement Company :@   }    }    }    }    }     ~ ~\ۚ?~@\ۚ?@@m6W@D@@@@ڶmL@@D@@@@KI?/@D@@@~4 @@4 @@@1UUUeV@@D@@@@V\H@@D@@@@SUU$@@D@@@~m@@m@@@<۶m+\@@D@@@@[jm۾Q@@D@@@@?/@@D@@@~~ 4@~-+~1@~@\ۚ?@@m6W@D@@@@ڶmL@@D@@@@KI?/@D@@@~3@@4 @@@1UUUeV@@D@@@@V\H@@D@@@@SUU$@@D@@@~W|6@@m@@@<۶m+\@@D@@@@[jm۾Q@@D@@@@?/@@D@@@~~ D@~QuP>@~@\ۚ?@@m6W@D@@@@ڶmL@@D@@@@KI?/@D@@@~@@@4 @@@1UUUeV@@D@@@@V\H@@D@@@@SUU$@@D@@@~uPB@@m@@@<۶m+\@@D@@@@[jm۾Q@@D@@@@?/@@D@@@~~ N@~:C@~@\ۚ?@@m6W@D@@@@ڶmL@@D@@@@KI?/@D@@@~D@@4 @@@1UUUeV@@D@@@@V\H@@D@@@@SUU$@@D@@@~yPuH@@m@@@<۶m+\@@D@@@@[jm۾Q@@D@@@@?/@@D@@@~~ T@~:CG@~@\ۚ?@@mہ]6W@D@@@@ڶmL@@D@@@@KI?/@D@@@~@H@@4 @@@1UUUeV@@D@@@@V\H@@D@@@@SUU$@@D@@@~uPK@@m@@@<۶m+\@@D@@@@[jm۾Q@@D@@@@?/@@D@@@~~ ?~I@@Ϡ=@@@~ww:@@L@@@@/ j@@L@@@@TUU?L@@@@l?@L@@@@<'0?L@@@~A?A ~ w@ ` jiZ! !Radiation losses from openings  aE |Z! English!U}!\ gZ!English >@3Equipment (kiln or precalciner) name or designation@:B63Equipment (kiln or precalciner) name or designation!3 D* Kiln 1! !A !A_"< pDHelp"= `DxShape of opening "_" "P "  "A] "A^#Q# "Dy%"Name or designation of the opening#2 ,D- Opening 1#? *D+ Current#? #D, Modified#$Q$ #Dz,)Number of openings of same size and shape$%Q%= $D{Total opening areaO%= g9Z!English @m^2@s^es|Bm^2 %b%@@% %&%% . D%I +%@%% - D%I +%@F%A 0Z!English  $!@$!BRectangular/Square&Q&8 %D|)&Average zone or radiation source temp.S&$> =Z!English @Deg. C.@Ddl^B Deg. C.& &0)& @@' D&? )& @@' D&? F&AE %0Z!English  $"@$"BRound'Q'h> &D}Ambient TemperatureS'$B &=Z!English @Deg. C.@Ddl^B Deg. C.' '0)' @@+ D'? )' @@+ D'? (Q(> 'D~.+Wall thickness or opening depth (Thickness)L(X> '6Z!English  @mm@ks|Bmm( )Q )"oN)B (8Z!English @meters@s|B meters) *Q *"p*d> )nD"Rectangular/Square @Z!English @meters@s|@"@B* R*A= `<Z!English @Kiln 1@z 1B Kiln 1+Q+ (D41View factor - user defined if known or from chart++aC / D Display Chart++ % + +- L+ % + + PU+AF b?Z!English @Current@S_MRpencB Current,Q, +D*'Emissivity of the source (Default=0.9),,V@V@,, ?& + , ?& + V,A2 b@Z!English @Modified@O9epencB Modified-Q-L ,D% Open time (Default=100%)--Y@Y@-- Y@+ - Y@. + W-A0 #AZ!English @ Opening 1@_S 1B Opening 1.Q# . p. 2Z(?  D, D& D' @@D+ D% D-dp. 2Z(?  D, D& D' @@D+ D% D- dW.A AZEnglish @ Opening 2@_S 2B Opening 2/Q / / %/ A D. d`T?%/ / D. d`T?W/A0 .AZEnglish @ Opening 3@_S 3B Opening 30Q0$? ~DView factor calculated000D+00D+0   W0A0 /AZEnglish @ Opening 4@_S 4B Opening 41Q1 0D63Ratio X (lowest of height or length/wall thickness) 1uj1UUUU1TD"Rectangular/Square %)*BD(D)D(B/1UUUU- %)*BD(12Q2 1DRadiation loss^2,A ]HZ!English @Btu/hr @ VpϑUSMO/\eB Btu/hr23D. 23D. 23R3@ 2DRadiation lossU3? q?Z!English @kJ/hr@CS&q/\eBkJ/hr%3uD2d`T?%3uD2d`T?34U5U6}6 !gZ!English >@3Equipment (kiln or precalciner) name or designation@:B63Equipment (kiln or precalciner) name or designation63 !D* Kiln 167U7|A -DxShape of opening 7_7 7 7  8U8 7Dy%"Name or designation of the opening8p0 -D. Opening 28A #D+ Current8A 8D, Modified89U9  bDz,)Number of openings of same size and shape9  :Uu: 9D{Total opening areaO: @ %9Z!English @m^2@s^es|Bm^2 : :@@: :&%: ? D:I +%@%: ? D:I +%@;U; :D|)&Average zone or radiation source temp.S;H@ h=Z!English @Deg. C.@Ddl^B Deg. C.;   ;0); @@< D;? ); @@< D;? <U<A ;D}Ambient TemperatureS<A ;=Z!English @Deg. C.@Ddl^B Deg. C.<   <0)< @@= D<? )< @@= D<? =U=P <D~.+Wall thickness or opening depth (Thickness)L=t@ f6Z!English  @mm@ks|Bmm=  = : = =? L= : = >U >oN>X@ i8Z!English @meters@s|B meters>> ?; = > ?; = ?U ?p|?@ *fD7Rectangular/Square <Z!English @meters@s|" B?? Y@@ = ? Y@@ = D l#q$x0&{$~q17$@ A A ;AB AC A D AE 8F G H ` I @J @ K 0L ;M J N J O P Q R S T  U  V ;W X  Y Z [ \ ] ;  ^ ,_ J@ @U@ D41View factor - user defined if known or from chart@ @< +D Display Chart @ p@ GZ(?  D> D; D< @@D= D: D? dp@ GZ(?  D> D; D< @@D= D: D? dAUAX @D*'Emissivity of the source (Default=0.9)AAV@ V@ A A%A FD@ d`T?%A A D@ d`T?5A P?> D  B A PBUB|B AD% Open time (Default=100%)BBY@Y@ BCUDUEUE@ 3DView factor calculatedEE0D@EED@ EFD ED63Ratio X (lowest of height or length/wall thickness) FujFUUUU1TD7Rectangular/Square %>?BD=D>D=B/FUUUUF%>?BD=FGr FDRadiation loss^GD 2HZ!English @Btu/hr @ VpϑUSMO/\eB Btu/hr!GH D@ DA !GH D@ DA GH GDRadiation lossUHLA 3?Z!English @kJ/hr@CS&q/\eBkJ/hr%HS DGd`T?%HV DGd`T?IJ}K 6gZ!English >@3Equipment (kiln or precalciner) name or designation@:B63Equipment (kiln or precalciner) name or designationK2 6D* Kiln 1KAAAA LHC 8DxShape of opening L_L LL AA M LDy%"Name or designation of the openingM@0 8D/ Opening 3MC 8D+ CurrentMlC MD, ModifiedMAAAA N =Dz,)Number of openings of same size and shapeN AAAA OE ND{Total opening areaOOA :9Z!English @m^2@s^es|Bm^2 O O@@O O&%O T DOI +%@%O T DOI +%@ O AA P OD|)&Average zone or radiation source temp.SPB <=Z!English @Deg. C.@Ddl^B Deg. C.P   P0)P @@Q DP? )P @@Q DP?  P AA QC PD}Ambient TemperatureSQC P=Z!English @Deg. C.@Ddl^B Deg. C.Q   Q0)Q @@R DQ? )Q @@R DQ?  Q AA RT QD~.+Wall thickness or opening depth (Thickness)LR@B =6Z!English  @mm@ks|BmmR  R O R RT LR O R R AA SoNS8@ >8Z!English @meters@s|B metersSS ?P R S ?P R S AA Tp|TLB ?fDLRectangular/Square <Z!English @meters@s|" BTT Y@U R T Y@U R T AA U BD41View factor - user defined if known or from chartU Ux= @D Display Chart U pU \Z(?  DS DP DQ @@DR DO DT dpU \Z(?  DS DP DQ @@DR DO DT d U AA V UD*'Emissivity of the source (Default=0.9)VVV@ V@ V V%V UDU d`T?%V V DU d`T?5V P?S D  B V PWHD VD% Open time (Default=100%)WWY@Y@WAAAAA XAAAAA YAAAAA ZB HDView factor calculatedw@3Equipment (kiln or precalciner) name or designation@:B63Equipment (kiln or precalciner) name or designation`= KD* Kiln 1`AA a? MDxShape of opening a_a a a  bt aDy%"Name or designation of the openingb> MD0 Opening 4b0 MD+ Currentb2 +D, ModifiedbAA c RDz,)Number of openings of same size and shapec AA d zD{Total opening areaOdC O9Z!English @m^2@s^es|Bm^2 d d@@d d&%d i DdI +%@%d i DdI +%@e  {D|)&Average zone or radiation source temp.SeC Q=Z!English @Deg. C.@Ddl^B Deg. C.e   e0)e @@f De? )e @@f De? fTE eD}Ambient TemperatureSfB e=Z!English @Deg. C.@Ddl^B Deg. C.f   f0)f @@g Df? )f @@g Df? g }D~.+Wall thickness or opening depth (Thickness)Lg D R6Z!English  @mm@ks|Bmmg  g d g gi Lg d g hoNh(@ S8Z!English @meters@s|B metershh ?e g h ?e g ip|iD TfDaRectangular/Square <Z!English @meters@s|" Bii Y@j g i Y@j g jE WD41View factor - user defined if known or from chartj j\= [D Display Chart j pj qZ(?  Dh De Df @@Dg Dd Di dpj qZ(?  Dh De Df @@Dg Dd Di dk D*'Emissivity of the source (Default=0.9)kkV@ V@ k k%k jDj d`T?%k k Dj d`T?5k P?h D  B k Plh D% Open time (Default=100%)llY@Y@lAAA mAAA nAAA oD ]DView factor calculatedooZDjooDjo888 pt oD63Ratio X (lowest of height or length/wall thickness) pujpUUUUk TDaRectangular/Square %hiBDgDhDgB/pUUUUp%hiBDgp qD DRadiation loss^q= GHZ!English @Btu/hr @ VpϑUSMO/\eB Btu/hr!qr Dj Dk !qr Dj Dk q r@ DRadiation lossUrD H?Z!English @kJ/hr@CS&q/\eBkJ/hr%r, Dqd`T?%r, Dqd`T?}u gZ!English 2@'Total of ALL Radiation - Opening Losses@zS;`p\_c1YB*'Total of ALL Radiation - Opening LossesUuE r?Z!English @kJ/hr@CS&q/\eBkJ/hr-u"DHD3D]Dr-u> DHD3D]Druvwx^xA@+ uHZ!English @Shape of opening@_Sb_rBShape of openingvy x`Z!English -@"Name or designation of the opening@_S TybNxB%"Name or designation of the openingz csZ!English 4@)Number of openings of same size and shape(@  T7h'Y\T:\[vzSvpeϑB,)Number of openings of same size and shapeb{\ dLZ!English @Total opening area@;`_SbyBTotal opening area|H yjZ!English 1@&Average zone or radiation source temp."@ s^GW:SWb\n)n^B)&Average zone or radiation source temp.a} fKZ!English @Ambient Temperature@sX)n^BAmbient Temperature~4 gqZ!English 6@+Wall thickness or opening depth (Thickness)$@ XSb_Sm^(S^)B.+Wall thickness or opening depth (Thickness)i SZ!English  @Length of opening (L)@_S^(L)BLength of opening (L)e &OZ!English @Diameter of Opening@_Sv_@BDiameter of Opening@`Dtk#-$w@@@@@@@@i SZ!English  @Height of opening (H)@_Sؚ^(H)BHeight of opening (H)@ jZ!English <@1View factor - user defined if known or from chart,@SƉVP[((u7b[INbegVh)B41View factor - user defined if known or from chart koZ!English 2@'Emissivity of the source (Default=0.9)&@ >e\|pe(:w=0.9)B*'Emissivity of the source (Default=0.9)0 liZ!English &@% Open time (Default=100%),@% Sb_e(:w=100%)B% Open time (Default=100%)j1 bTZ!English !@View factor calculated@Ɖ҉VP[{@3Ratio X (lowest of height or length/wall thickness).@k@d888Z "3"" 77 ""77 LLLL aaaa 7****:4** ""77 LLLL a  D"Round N6H 7A ;>66>>6>69@HCD :47A ;>66>>6>69@HCD  D >+j@A::++@@UUjj :4@A::++@@UUjj@HCD  D ???? :4??::++@@UUjj@HCD  D ???? ???::++@@UUjj@HCD D K^ K^  :4K^ ::++@@UUjj@HCD   if $c$31<3NK^ U^K^ KSK^KK^^STXY :4U^K^ KSK^KK^^STXY  D F`r jr`r `h`r``himn :4jr`r `h`r``himnXY  D ****:4**`r `h`r``himnXY  D"Round ????:4??`r `h`r``himnXY  D7Round  :4??`r `h`r``himnXY  D TTTT :4TT`r `h`r``himnXY  D :4TT`r `h`r``himnXY @ @ DLRound iiii :4ii`r `h`r``himnXY  D :$ii`r `h`r``himnXY  D`Round T@@yK =$h$7radiation_vf!A1T++yK =$h$7radiation_vf!A1TUUyK =$h$7radiation_vf!A1TjjyK =$h$7radiation_vf!A1r"3yK =$h$4Radiation_Losses_from_OpeningsX 2 l English  %!"%!"""""X 2 l English  %!"%!"""aaTlMust be Whole Number $$99NNccX 2t l English  %!"%!"""77X 2t l English  %!"%!"""LL Sheet11 s  [T-D7  dMbP?_*+%563&LEnergy Use Analysis for Cement Kilns - Preheaters0-&LE3M Inc.&RJune-07-2009&CABC Cement CompanyMAdobe PDFS oRXXLetterPRIV ''''0\KhCFFSMTJAdobe PDF ConverterResolution1200dpiPageSizeLetterPageRegionLeadingEdgeInputSlotOnlyOne0EBDAStandard"RXX??cU} 3} C} $} }  }} m} I} } m } } } $ } [  w w hAAAA  A A    h@  h@  h @!Z!  z{~ w@5 LiZ! 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DS  Kiln 1U 7 ?Z!English @Current@S_MRpencB CurrentV 8E @Z!English @Modified@O9epencB Modified x yB  ,Z!English  $N $VB)&Cooling water loop name or designation ? T DU  Loop 2   BP ,Z!English  $O $WBCooling water flow rate  Z[  Q  R)  D<ʉv?)  D<ʉv?BD7 ,Z!English  $P $XBWater Inlet temperature  \]  S%  D ,O@%  D ,O@B ,Z!English  $Q $YBWater Outlet temperature  \]  T   8  "D ?DDD8  "D ?DDDB ,Z!English  $R $ZBA>Correction factor or density factor if applicable (1=Default)^?_?  c  d% e zG?D % e zG?D 5P? D  B P !} gZ!English >@3Equipment (kiln or precalciner) name or designation@:B63Equipment (kiln or precalciner) name or designationC DS  Kiln 15 E D  CurrentV$C @Z!English @Modified@O9epencB Modified  x  yB7 ,Z!English  $N $VB)&Cooling water loop name or designationD DV  Loop 3    B  ,Z!English  $O $WBCooling water flow rate  Z[  Q  R)  D<ʉv?)  D<ʉv?B ,Z!English  $P $XBWater Inlet temperature  \]  S%  D ,O@%  D ,O@B 8 ,Z!English  $Q $YBWater Outlet temperature  \]  T   8  "D ?DDD8  "D ?DDDBP ,Z!English  $R $ZBA>Correction factor or density factor if applicable (1=Default)^?_?  c  d% e zG?D % e zG?D 5P?D  B P !}H gZ!English >@3Equipment (kiln or precalciner) name or designation@:B63Equipment (kiln or precalciner) name or designationC DS  Kiln 1UlA ?Z!English @Current@S_MRpencB CurrentVXA @Z!English @Modified@O9epencB Modified  x  yB ,Z!English  $N $VB)&Cooling water loop name or designation ? B P ,Z!English  $Q $YBWater Outlet temperature  `] T  8 ! "D ?D DD!8 ! "D ?D DD!B! ,Z!English  $R $ZBA>Correction factor or density factor if applicable (1=Default)!!a?_? ! c ! d%! e zG?D %! e zG?D 5!P?D  B !P" !#$]& !GZ!English Total for Water Cooling@TBTotal for Water CoolingQ&D8 &;Z!English  kJ/hr@CS&q/\eBkJ/hrB&#,D!D! DD DD D -&$D! 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I'2?D  QJ d 4Z!English  @$ @$B52Correction factor or density factor if applicable   `?u?   4 )DD DDD 4 )DD DDD  R"} @ gZ!English >@3Equipment (kiln or precalciner) name or designation@:B63Equipment (kiln or precalciner) name or designation x5 D* Kiln 1U hL ?Z!English @Current@S_MRpencB CurrentV D @Z!English @Modified@O9epencB ModifiedJ  4Z!English  @$@$B'$Air cooling loop name or designation x7 +D, Loop 2  fd CU&  DD&  DDJD 4Z!English  @$@$BCooling air or gas flow rateF~L 0Z!English  $@$!B nm^3/hr \r @  ]  C^/ $C? $C? I'2?D / $C? $C? I'2?D J 4Z!English  @$@$B Air or gas inlet temperatureF~TN 0Z!English  $@$"B Deg. C. \r A    4  DD DDD4  DD DDDJL !4Z!English  @$@$B Air or Gas outlet temperatureF~$M !0Z!English  $@$#B Deg. C. \r BJ "4Z!English  @$@$B.+Specific heat for air or gas (Default=1.21)F~@ "0Z!English  $@$$BkJ/(nm^3 - deg. C.) s@^@t@^@ CJ #4Z!English  @$ @$B52Correction factor or density factor if applicable `?u? l D5 P? D  B  P} gZ!English >@3Equipment (kiln or precalciner) name or designation@:B63Equipment (kiln or precalciner) name or designationh5 D* Kiln 1UM ?Z!English @Current@S_MRpencB CurrentVB @Z!English @Modified@O9epencB ModifiedJ 4Z!English  @$@$B'$Air cooling loop name or designationN ,D- Loop 3   fd  CU&  DD&  DDJ 4Z!English  @$@$BCooling air or gas flow rateF~M 0Z!English  $@$!B nm^3/hr \r   ]  C^/ $C? $C? I'2?D / $C? $C? I'2?D JT 4Z!English  @$@$B Air or gas inlet temperatureF~DN 0Z!English  $@$"B Deg. C. \r     4  DD DDD4  DD DDDJN 4Z!English  @$@$B Air or Gas outlet temperatureF~L 0Z!English  $@$#B Deg. C. \r Jh 4Z!English  @$@$B.+Specific heat for air or gas (Default=1.21)F~ 0Z!English  $@$$BkJ/(nm^3 - deg. C.) s@^@t@^@ J@ 4Z!English  @$ @$B52Correction factor or density factor if applicable ??"5 P? D  B  P}p gZ!English >@3Equipment (kiln or precalciner) name or designation@:B63Equipment (kiln or precalciner) name or designationX5 D* Kiln 1U|6 ?Z!English @Current@S_MRpencB CurrentV? @Z!English @Modified@O9epencB ModifiedJ 4Z!English  @$@$B'$Air cooling loop name or designation6 -D. Loop 4   fd  CU&  D!D"&  D!D"Da"lG"fV`K#gr g#gr Y  ! ;" # $ %  ) J  * + , - . 1 2 `3 4 5 6 7 8 9 : ; < = > ? J  4Z!English  @$@$BCooling air or gas flow rateF ~I 0Z!English  $@$!B nm^3/hr \r ] C^/ $C?! $C? I'2?D / $C?! $C? I'2?D J!K 4Z!English  @$@$B Air or gas inlet temperatureF!~4M 0Z!English  $@$"B Deg. C. !\r !E !  ! 4!  D D D"D!D$4!  D D D"D!D$J" 4Z!English  @$@$B Air or Gas outlet temperatureF"~L 0Z!English  $@$#B Deg. C. "\r "FJ# 4Z!English  @$@$B.+Specific heat for air or gas (Default=1.21)F#~ 0Z!English  $@$$BkJ/(nm^3 - deg. C.) #s@^@t@^@ #FJ$ 4Z!English  @$ @$B52Correction factor or density factor if applicable $$?? $G5$ P? 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P  ` h(  hj h 0NMM?Ld]`hu  s "h??3` #` #` #PHp0(  п3d23 M NM4 3QQ ; 5H Q ; 5H Q3_4E4 3QQQQ3_ O NM  MM<4JK4D $% M@3O&Q4$% M@3O&Q4FA=U 3O=U 3*#M! M43*#M! M4523  O43d" q33Oq% M3OQ443_ M NM  MM<444% C  @M 3Oy*PQ'44eee ZR h C A@+k]`$u h TA ?@CommandButton6Z]` u1 6$ZForms.CommandButton.1L\ h A ?@ <CommandButton15yK control_page!D6  ]` tu1 6$Z| Forms.CommandButton.1X  h VA) ?@ CommandButton29< G]`  Zu1 6$([| Forms.CommandButton.1P>@!!!Z    7&$    $ :4   $  D  .   :4   D  F% "$%%% %% :4"$%%% %%  D$  &    :4  %% %%  D  X yK =$j$2Air_cooling_loops Sheet13 s  F  dMbP?_*+%63&LEnergy Use Analysis for Cement Kilns - Preheaters0-&LE3M Inc.&RJune-07-2009&CABC Cement CompanyM\\JIM-CASS\HP DeskJet 812C (CoC odXXLetterDINU"H$%#| HSMTJ8HP DeskJet 812CInputBinFORMSOURCERESDLLUniresDLLPSAlignmentFileHPV880ALPSHelpFileHPVDJ200OrientationPORTRAITPaperSizeLETTERResolutionr300x300PMPlainNormalColorMediaTypeSTANDARDPQNormalColorModeColor24HPHTDLLNameHPVIMG50$$$$"dXX??cU} m3} $} $}  } u} u} w hw J @ AAA A A A A AhA SSS YS ~ w@ hZ!Clinker discharge WSS}8 gZ!English >@3Equipment (kiln or precalciner) name or designation@:B63Equipment (kiln or precalciner) name or designationNS 8Z!English @:@:B Kiln 1US ?Z!English @Current@S_MRpencB CurrentVS @Z!English @Modified@O9epencB Modifiedoh YZ!English *@Hot products name - designation@pNT TyB"Hot products name - designationQR ;Z!English @Clinker@qeB Clinker N  8Z!English @:@:BCopy Current to Modified% R DHelp nZ!English +@ Correction factor (Default=1.00),@!hck|pe (:w@2   7XyK =$h$7Clinker_discharge Sheet14bb, s  $ 2  dMbP?_*+%763&LEnergy Use Analysis for Cement Kilns - Preheaters0-&LE3M Inc.&RJune-29-2009&CABC Cement CompanyMAdobe PDFS odXXLetterPRIV ''''0\KhCFFSMTJAdobe PDF ConverterResolution1200dpiPageSizeLetterPageRegionLeadingEdgeInputSlotOnlyOne0EBDAStandard"dXX??cU} $} m} } } } } u}  u}  } I} &} m}   `  J  w  w  @ @ ;A A  ;A YA A A  wA  A wA JA    I@ @       @  @0         I@  @Z! z{~ w@ WS #Z!$!Clinker bed cooling and other airSNT  8Z!English @: @: BHelpPS 6DHelp} gZ!English >@3Equipment (kiln or precalciner) name or designation@:B63Equipment (kiln or precalciner) name or designationNd] ,8Z!English @:@:B Kiln 1U] +?Z!English @Current@S_MRpencB CurrentVp^ 9@Z!English @Modified@O9epencB ModifiedN$ 8Z!English @:@:BCopy Current to Modified `$T 0Z! EnglishQJ\ 4Z!English  @$ @$ B-*Air flow - leakage area name - designation]M BGZ!English @Cooler Air flow@QtSlAmBCooler Air flow N 8Z!English @:@:BDone Entering Data    HQJ4T 4Z!English  @$ @$ BAir volume flow rate]\ 9GZ!English @nm^3/hr@hQzes|/\eB nm^3/hrP  o  JQ dpd   \ C㥛 ?  p QJ`T 4Z!English  @$ @$ BAir inlet temperatureS\ =Z!English @Deg. C.@Ddl^B Deg. C.PNA@; 8Z!English @: @: B Print Sheet  n  B QJ  ^ 4Z!English  @$ @$ BAir outlet temperature S `^ =Z!English @Deg. C.@Ddl^B Deg. C. N S 8Z!English @:@:BABC Cement Company S q C Q dr d o 6Nx ?7 .n?!DSDSD DSD  SS r  RJ X_ 64Z!English  @$ @$ BDestination of Air Flow      ];ZExhaust Thru System K  I U  ,];ZExhaust Outside the System L S U ` @DF;8The following are calculated values based on input data:      M SU DG(%Specific heat of the air (volumetric)s ]Z!English @kJ/(nm^3-deg. C.)*@CS&q/(hQzes|-Ddl^)BkJ/(nm^3-deg. C.)9 B+OM?#DQDPDODD 9 B+OM?#DQDPDODD  SSS U^ DHHeat in exiting airU] ?Z!English @kJ/hr@CS&q/\eBkJ/hr2<DDD D@2<DDD D@S  C X  } gZ!English >@3Equipment (kiln or precalciner) name or designation@:B63Equipment (kiln or precalciner) name or designationb_ LZ!English @ Air to cogen@0Rp5uTNvzzlB Air to cogenU8_ ?Z!English @Current@S_MRpencB CurrentV\ @Z!English @Modified@O9epencB Modified  XO  P J 4Z!English  @$ @$ B-*Air flow - leakage area name - designation[(K HEZEnglish @ Secondary air@N!kzzlB Secondary air   XN    J 24Z!English  @$ @$ BAir volume flow rate]_ 0GZ!English @nm^3/hr@hQzes|/\eB nm^3/hr wz  X lpe  x{X  J@ ,4Z!English  @$ @$ BAir inlet temperatureS^ =Z!English @Deg. C.@Ddl^B Deg. C. X  J /4Z!English  @$ @$ BAir outlet temperatureS_ =Z!English @Deg. C.@Ddl^B Deg. C. X  lre oy7}.n?@!DSDSDDSDX  J| 4Z!English  @$ @$ BDestination of Air Flow    f  DF;8The following are calculated values based on input data: T DG(%Specific heat of the air (volumetric)s] (]Z!English @kJ/(nm^3-deg. C.)*@CS&q/(hQzes|-Ddl^)BkJ/(nm^3-deg. C.)9 B+OM?#DQDPDODD9 B+OM?#DQDPDODD \; DHHeat in exiting airU_ ?Z!English @kJ/hr@CS&q/\eBkJ/hr8="DDDDD@8="DDDDD@ 5P?D  B  P }@ gZ!English >@3Equipment (kiln or precalciner) name or designation@:B63Equipment (kiln or precalciner) name or designationN0; 8Z!English @:@:B Kiln 1U8 ?Z!English @Current@S_MRpencB CurrentV\ @Z!English @Modified@O9epencB Modified  DlG_qut|2>0F}&pu  @! @" # $  % @ & 0' ( )   *  + :@, @- . / 0 1  2 @ 3 04 5 6   7 h@9 : ; A< = > ? J  4Z!English  @$ @$ B-*Air flow - leakage area name - designation W t] AZ!English @ Other air@vQNzzlB Other air J! 4Z!English  @$ @$ BAir volume flow rate!]!H9 GZ!English @nm^3/hr@hQzes|/\eB nm^3/hr !w~!J" 4Z!English  @$ @$ BAir inlet temperature"S"_ =Z!English @Deg. C.@Ddl^B Deg. C. "J# 4Z!English  @$ @$ BAir outlet temperature#S#X9 "=Z!English @Deg. C.@Ddl^B Deg. C. # $lr$e $o$y ?7$}.n? !DSDSD#DSD#$J%L 4Z!English  @$ @$ BDestination of Air Flow % % %&' DF;8The following are calculated values based on input data:'( 'DG(%Specific heat of the air (volumetric)(s(^ 5]Z!English @kJ/(nm^3-deg. C.)*@CS&q/(hQzes|-Ddl^)BkJ/(nm^3-deg. C.)9(v B+OM?)#DQDPDOD"D#9(v B+OM?)#DQDPDOD"D#)9 (DHHeat in exiting air)U)_8 ?Z!English @kJ/hr@CS&q/\eBkJ/hr8)>"D)D(D!D#D"@8)>"D)D(D!D#D"@5)P?(D  B ) P*}+ gZ!English >@3Equipment (kiln or precalciner) name or designation@:B63Equipment (kiln or precalciner) name or designation+N+ ; 8Z!English @:@:B Kiln 1U+_ ?Z!English @Current@S_MRpencB CurrentV+: @Z!English @Modified@O9epencB Modified+J,l -4Z!English  @$ @$ B-*Air flow - leakage area name - designation,\,HL FZ!English @Additional air@YzzlBAdditional air,PJ-9 !4Z!English  @$ @$ BAir volume flow rate-]-9 !GZ!English @nm^3/hr@hQzes|/\eB nm^3/hr-zP .p. . ..J/ "4Z!English  @$ @$ BAir inlet temperature/S/9 #=Z!English @Deg. C.@Ddl^B Deg. C. /J0X #4Z!English  @$ @$ BAir outlet temperature0S0P^ /=Z!English @Deg. C.@Ddl^B Deg. C.0 1lr1e 1mo~ 1y?71}.n?6!DSDSD0DSD01J2 %4Z!English  @$ @$ BDestination of Air Flow 2i 2 2234  )DF;8The following are calculated values based on input data:45` FDG(%Specific heat of the air (volumetric)5s58 -]Z!English @kJ/(nm^3-deg. C.)*@CS&q/(hQzes|-Ddl^)BkJ/(nm^3-deg. C.)95 B+OM?6#DQDPDOD/D095 B+OM?$#DQDPDOD/D06 GDHHeat in exiting air6U6: )?Z!English @kJ/hr@CS&q/\eBkJ/hr86B"D6D5D-D0D/@-65D6D1D.D056P?SD  B 6 P9U9^ +?Z!English @Current@S_MRpencB Current 9V9T +@Z!English @Modified@O9epencB Modified 9:d: ;NZ!English @All in nm^3/hr@hQzes|/\eBAll in nm^3/hrU:<: :?Z!English @kJ/hr@CS&q/\eBkJ/hrU:H: :?Z!English @kJ/hr@CS&q/\eBkJ/hrd: :NZ!English @All in nm^3/hr@hQzes|/\eBAll in nm^3/hrU:h: :?Z!English @kJ/hr@CS&q/\eBkJ/hrU:t: :?Z!English @kJ/hr@CS&q/\eBkJ/hr;F;: 0Z!English  $ @$ BExhaust Thru SystemF; ;0Z!English  $ @$ BExhaust Outside the SystemF;X ;0Z!English  $ @$ B$!Recoverable Heat in outgoing air F;: ;0Z!English  $ @$ BExhaust Thru SystemF;  0Z!English  $ @$ BExhaust Outside the SystemF; 0Z!English  $ @$ B$!Recoverable Heat in outgoing air <: DCooler Air flow9<5#D D   $ B9<=#D D   $ B9<#D D   $ B9<?#D D   $ B9<?#D D   $ B9<#D D   $ B=] <D Secondary air9=<#DD   $ B9=<#DD   $ B9=(#DD   $ B9=<#DD   $ B9=<#DD   $ B9=)#DD   $ B>T =D  Other air9>?#D%D   $! B9>=#D%D   $! B9>?#D%D   $) B9>=#D%D   $! B9>=#D%D   $! B9>?#D%D   $) B?S >D,Additional air9?>#D2D   $- B9?>#D2D   $- B9?@#D2D   $6 B9?>#D2D   $- B9?>#D2D   $- B9?@#D2D   $6 BB!X}p^g >yp^\@ (` A ` B ` C ,D ,E ,F ,G ,H ,I ,J ,K L M ;  N ; O ; P ; Q ; R J  S T U V ; W X Y Z [ \ ] ^ _ @ +|Z!English ;@0TOTAL HEAT TO COMBUSTION AIR and Clinker Cooling*@qpzzlNqeQtS@b;`pB30TOTAL HEAT TO COMBUSTION AIR and Clinker Cooling@Z@@@ -@K@@@@@@@@@@@AoppppppB8 :{Z!English <@1Total Recoverable Heat In clinker cooling bed air(@ qeQtS^zzl;`SV6epϑB41Total Recoverable Heat In clinker cooling bed air BBBD@ BB?D@BZC  D E  F  F 4Z!English C@8The following are calculated values based on input data:&@  NR~gWNeQpenc{B;8The following are calculated values based on input data:G  wG 5aZ!English 0@%Specific heat of the air (volumetric)@zzlSOykpB(%Specific heat of the air (volumetric)H  iH 6SZ!English @Heat in exiting air@cQzzl@b+TpϑBHeat in exiting airI  J   K !K? D@D@K MksMk Mk}_MkIDDDDD!D"D-D/DDD!D-_MkMIDDDDD!D"D-D/DDD!D- NnNoppq OrZOsit> Ottu PrYPv2\k? Pttu QruQwN ^P@ Qttu Rxv Ryw Rzz{ ST.n?SS-C6*?-S:0yU1   Su TXXT TSY TSZTwUXSSw VxV SSw WS W[W XUX XSV XS2 XwW~ YY~ YS Y@7Y.n?e!DSDSDYDSDY(YBwV?@DYDYDY~ ZY@ZZZ/$?Zv/?[Z+Ze !DSDSLDSLZ]nLdYZZe LLL~ [i@[Z["~j?[u$~?\Z[9яsZZ~ \r@\ \Xn?\\ Ac?]Z\B|f[Z~ ]y@] ]XJ +?]jt?^Z]3z>\Z~ ^@@^ ^Xrh|?^ c?_Z^O2w?]Z~ _@_ _Xm?_y&1?`Z_+-֦ w?^ZDl1= 000,m> (Bhhhh` a b c d e  f g h i j k l m n o p q r s t u v w x y z { | } ~  ~ `@` ~ `X`\@`OjM?aZ`s@?_Z~ a@a aX"~?ab48?bZaҥxK?`Z~ b @b bXn?brh|?cZb 0Ռ?aZ~ c@@c ~ cX]@c:H?dZc+hei?bZ~ d0@d dXx&?d?eZd/AA?cZ~ e@eg~ e@^@e??YZeu#x?dZDldhhdhd  (0 < GM GM ' (   j  0NMM?h-]`u  s "??3` #r` #s` #t` #u` #vPH0(  @п3d23 M NM4 3QQ ;YeQ ;YeQ3_4E4 tt3QQQQ3_ O NM  MM<4JK4D $% M@3O&uQ4$% M@3O&tQ4FAE3OE3*N%#M! M! M43*????#M! M! M4523  43d" 3_ M NM  MM<444% <MP3O? &rQ D Specific Heat of Air in SI units'4% * @ 3O*&sPs v s!v"s+Q23 M 4'44eee    TA ?@CommandButton8<]` ^u0 6$ Forms.CommandButton.1\   A* ?@ <CommandButton17yK control_page!D6  ]` 6u1 6$ԒDForms.CommandButton.1T X   VA ?@ CommandButton31]` 7u1 6$DForms.CommandButton.1 P>@<d% %% 4 BBKK  +,+,''""##%%((    9999--//0022445566!!))++,,7 ))  :4)   +,+,''"  D) 6+6 :4+6  +,+,''"  D6 & :4 +,+,''"  D x yK =$i$4"Clinker_bed_cooling_and_other_airC =  1-11&&  WExhaust Thru System if Sent to Flue; Exhaust Outside System if Sent to Separate Exhaust2rlEnglish  % % ""22 WExhaust Thru System if Sent to Flue; Exhaust Outside System if Sent to Separate Exhaust2rlEnglish  % % ""  WExhaust Thru System if Sent to Flue; Exhaust Outside System if Sent to Separate Exhaust2rlEnglish  % % "" WExhaust Thru System if Sent to Flue; Exhaust Outside System if Sent to Separate Exhaust2rlEnglish  % % "" WExhaust Thru System if Sent to Flue; Exhaust Outside System if Sent to Separate Exhaust2rlEnglish  % % ""%% WExhaust Thru System if Sent to Flue; Exhaust Outside System if Sent to Separate Exhaust2rlEnglish  % % ""%% WExhaust Thru System if Sent to Flue; Exhaust Outside System if Sent to Separate Exhaust2rlEnglish  % % ""22 WExhaust Thru System if Sent to Flue; Exhaust Outside System if Sent to Separate Exhaust2rlEnglish  % % ""  Sheet18bb,ggD s  Nd/GV[  dMbP?_*+%63&LEnergy Use Analysis for Cement Kilns - Preheaters0-&LE3M Inc.&RJune-29-2009&CABC Cement CompanyMAdobe PDFS oJXXLetterPRIV ''''0\KhCFFSMTJAdobe PDF ConverterResolution1200dpiPageSizeLetterPageRegionLeadingEdgeInputSlotOnlyOne0EBDAStandard"JXX??cU} m3} $} m} } u} u} $ } } } $ } N     J  w  w   ;       A  S S    ;    @         ;    @ Z! z ZZ~ w @ WX *Z!$!Other or waste products dischargeXNS 8Z!English @:@:B Kiln 1N$ 8Z!English @: @: BHelpP0 DHelp D163Equipment (kiln or precalciner) name or designation_ -D Kiln 1_ 8D= CurrentW D> ModifiedJ 4Z!English  :@:BCopy Current to ModifiedQP D2Product name - designation: >DBSlag F 0Z!English  ::BDone Entering DataQ D3/,Mass or weight of products collected - totalU DCkg |F 0Z!English  : : B Print SheetQ4 D4.+Time or number of hours - collection periodZ DDhours  uNF 0Z!English  ::BABC Cement CompanyQ D5+(Temperature of the products at discharge|V DE deg. C.  u 7 !DDD DZ7  !DDD DZ Q l D6<9Specific heat of the products (mass based) (Default=1.05) 8 DFkJ/(kg-deg. C.) @Z@|@Z@ u 2 p DDD D d2 p DDD D d Q   D72/% combustible material in particulates (if any)  | un !  DD !  D D  Q ( D8EBHeating value of combustible particulate material (Default=24,000) V DHkJ/kg p@zp@ R' P UXU   XM<7DDD DZD dD @  D163Equipment (kiln or precalciner) name or designation D Kiln 1 9 D= CurrentHX D> Modified\X D2Product name - designationZ DBSlag \W 2D3/,Mass or weight of products collected - totalTW BDCkg  D4.+Time or number of hours - collection periodX DDhours  uND iw ModifiedY 1D2Product name - designationZ DBSlag 7  !DDD DZ D3/,Mass or weight of products collected - totalX FDCkg 2  DDD"D!d 3D4.+Time or number of hours - collection periodZ CDDhours  uN! ) D D  4D5+(Temperature of the products at dischargetY DDE deg. C.  u 7 !DDD DZDlMow%<&2Y  @! " @ # 0$ % g@( vA) ;A* :A+ A, :A- gA . A/ A1 2 3 4 5 6 7 8 = > ?  Z D6<9Specific heat of the products (mass based) (Default=1.05) 8 DFkJ/(kg-deg. C.) @Z@@Z@ u 2 !DDD"D!d! D72/% combustible material in particulates (if any) ! ! !un !!!) DD "x D8EBHeating value of combustible particulate material (Default=24,000)"XY DHkJ/kg"p@p@#5# ? D  B # % (S(T (Tu (Tu )A )T3)*D DD D!D# 3)D D D D D#  *O *O*,Z O*,Z O +OO ,O ,O%,-Z 9Z ?%,-Z 9Z ?- HDM~{Total Heat in products other discharged (particulates etc.) in exhaust gases and collected in particulate control equipmentU-Y M?Z!English @kJ/hr@CS&q/\eBkJ/hr#- %),#-* %),1 Z!English >@3Equipment (kiln or precalciner) name or designation0@Y(zbR㉉p) Tybc[NxB63Equipment (kiln or precalciner) name or designationn2W XZ!English !Product name - designation @ NT Tybc[NxBProduct name - designation3X jZ!English 7@,Mass or weight of products collected - total@6eƖNT;`͑ϑB/,Mass or weight of products collected - total48 kZ!English 6@+Time or number of hours - collection period@6eƖ6ke^B.+Time or number of hours - collection periodz5 dZ!English 3@(Temperature of the products at discharge@QeNT)n^B+(Temperature of the products at discharge6 Z!English D@9Specific heat of the products (mass based) (Default=1.05)6@NTkp(WN(ϑ)(:wA$_ =@Z!English @Modified@O9epencB Modified?A6Y 4^nTgiB C D E F G H M NBY 8Z!English @Slag@w#nBSlagLCZ 6Z!English  @kg@CSKQBkgODY 9Z!English @hours@\eBhoursSEdY =Z!English @deg. C.@Ddl^B deg. C.kFZ UZ!English @kJ/(kg-deg. C.)$@ CS&q/(CSKQ-Ddl^)BkJ/(kg-deg. C.) GUHZ "?Z!English @kJ/kg@CS&q/CSKQBkJ/kgM -Z!English {Total Heat in products other discharged (particulates etc.) in exhaust gases and collected in particulate control equipment@@^lbd\Y-N_vire(Y|I{)-N@b+T;`pϑB~{Total Heat in products other discharged (particulates etc.) in exhaust gases and collected in particulate control equipment]Y_ee$ tal pro er ((  ( ( TA ?@CommandButton9@W]` ,u1 6$<±Forms.CommandButton.1 \ ( VA- ?@ CommandButton18 `mR]` Uu1 6$x±Forms.CommandButton.1X X ( VA, ?@ CommandButton32m ]` Vu1 6$± Forms.CommandButton.1 P>@  R  7   :4   D  " "  ?"  D"  ### ?## D#  > :4  D  >#"# #!!## :4"# #!!##  D#  x yK =$i$4"Other_or_waste_products_discharge Sheet15 s  \hyqӗ  dMbP?_*+%MAuto NEC SuperScript 1400 on E4C odXXLetterDINU"4^ "dXX??U} A} I } } m}  } $}  }  } I} \  X,,,;  XA ,A  ;       B B             %k &' ()* (i )Y *Z()rhX@*J + +j ,-  ZZq>   Y ݖA?    m !ݖA? 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D\l.,@tSMGAH@ PA PB PC PD PE PF PG PH PI PJ PK PL PM PN PO P@PP@@5@P2:-?@3@`hפ?A4@{98@A4 @ AP@A5APr?K ڕ?A3A5\Ҧ?B4A{@B4 A BPp@B5BPdL\Y?B3B @R          7 Sheet23 s  ]  dMbP?_*+%" ?? U} I   Y           @  @  @  @           ~ ? L7A`? I +?~ @ tV?   @?P@  '1Z?~ p@  ~ @ ʡE?~ ? ?5^I ? d;OGE@  ~ @ /$? '1Z? ?y@  `Z@ @  Zd;O? S㥛?~  ? - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - "~bnXndd$$$>@:       7 yK _parentyK http://books.nap.edu/openbook.php?record_id=9736&page=92yX;H,]ą'cp2000a4298940092002 yK _parentyK http://books.nap.edu/openbook.php?record_id=9736&page=92yX;H,]ą'cp2000a4298940092003yK _parentyK http://books.nap.edu/openbook.php?record_id=9736&page=92yX;H,]ą'cp2000a4298940092004 Sheet24 s  4H-=IKRX^Wg8qځ  dMbP?_*+%NMAdobe PDFS oF,,LetterPRIV ''''0\KhCFFSMTJAdobe PDF ConverterResolution1200dpiPageSizeLetterPageRegionLeadingEdgeInputSlotOnlyOne0EBDAStandard"F,,??cU} m } I5} :} $ } I>]} *Ah ;:W:: W W : I ,,,,,,,,,,;  ;J ( 4Z!English  @$@$BPHAST For CEMENT HELP FILE   A7 Py Z! Heat input to charge material8 ()NA 8Z!English @: @: B Return To9  D*'Return To Heat input to charge material*Pu Z 0-Weight of the raw meal or charged material J@@ 4Z!English  @$@$BifThis is the rate at which the raw material is charged into the kiln. The units of measure are Kg/hr.(ԃ D DBP*'Return To Heat input to charge material ] A49 *u Z Initial charge temperatureJ@# 4ZEnglish  @$@$BxuThis is the temperature at which the charged raw material enters the kiln. The units of measure are Degrees Celcius. @ A59 *t Z Final clinker temperatureJ@" 4ZEnglish  @$@$BThis is the temperature at which the finished clinker leaves the kiln (after or at the end of the cooling bed) . The units of measure are Degrees Celcius.P > A69 *0x Z FCSpecific heat of the clinker material (average value, Default=1.03)J@! 4ZEnglish  @$@$BfcThis is the mass specific heat of the clinker material. The units of measure are kJ/(Kg-Degrees C) > A.9 ,v Z 85% moisture (water) in the charge material as charged J@  4ZEnglish  @$@$B|yThis is the moisture content of the raw material as charged. The units of measure are in percent of the charge material. @ A 9  *u Z %"Water vapor discharge temperature J @ 4ZEnglish  @$ @$ BWater vapor from the raw material is driven off in the kiln. This is the discharge temperature of the water vapor as it leaves the kiln. > A/ 9  *w Z A>Name or type of volatiles discharged from the charge material J @ 4ZEnglish  @$ @$ BName of the volatiles driven off from the raw material. This consists primarily of CO2. Give name if it is other than given here. @ A0 9  *pv Z 2/Molecular weight of the volatiles (Default=44)J @ 4ZEnglish  @$ @$ BtqMolecular weight of the volatiles (CO2 = 44). This can be chaged by the user if the volatiles are other than CO2 > A1 9  ,v Z  Clinker production rateJ @ 4ZEnglish  @$ @$ BdaThis is the rate at which the finished clinker leaves the kiln. The units of measure are Kg / hr. > A2 9  ,w Z LIHeat of reaction for the remaining devolataliized material (Default=100)J @ 4ZEnglish  @$ @$ B:7This is the heat of reaction for the remaining material > A39 , Z <9Additional heat loss/used (+ve) or released/added ( -ve) J@ 4ZEnglish  @$@$B96Additional Heat Lost in the kiln or added to the kiln. > A7 : U@V: WQJ@d 4ZEnglish  @$@$B96Chemical composition of the charge material in percent +R A8: ,A Z SiO2J@ 4ZEnglish  @$@$B30Percentage of the total composition that is SiO2 +T A9: ,A Z Al2O3J@8 4ZEnglish  @$@$B41Percentage of the total composition that is Al2O3 +U A:: ,A Z Fe2O3J@ 4ZEnglish  @$@$B41Percentage of the total composition that is Fe2O3 +V A;: ,A Z CaOJ@ 4ZEnglish  @$@$B2/Percentage of the total composition that is CaO +W A<: ,A Z !MgOJ@` 4ZEnglish  @$@$B2/Percentage of the total composition that is MgO +X A=: ,A Z "SO2J@ 4ZEnglish  @$@$B2/Percentage of the total composition that is SO2 +Y A>: ,A Z #fCaOJ@  4ZEnglish  @$@$B30Percentage of the total composition that is fCaO +Z A?: .A Z $LossJB 4ZEnglish  @$@$BOther material XS A@5 t Z! Kiln shell wall heat losses6 (x D DBP(%Return To Kiln shell wall heat losses (/<Op2`IQNcC# :!:"W#:$I %,&,',(,),*,+,,,-,5 6;78:9,:,;:<:=:>:?: 1 y D(%Return To Kiln shell wall heat losses -| Z)&Average surface temperature (measured)J 0  4ZEnglish  @$ @$ BkhThis is the average surface temperature of the wall area being calculated. Units are in Degrees Celcius 0 AA!1 !-y ZAmbient TemperatureJ!0 "4ZEnglish  @$!@$!BolThis is the ambient temperature of the room or area in which the kiln is located. Units are Degrees Celcius. !1 !AB"1 "- z !Z $!Surface emissivity (default =0.8)J"0\ #4ZEnglish  @$"@$"BThis is the average surface emmisivity of the wall area bein calculated. Default is 0.8 but it can be changed by the user if necessary.. "0 "AC#1 #-|z "Z Total outside surface areaJ#0p $4ZEnglish  @$#@$#BfcThis is the total outside area of the shell - wall area being calculated. Units are square meters. #0 #AD$1 $2x #Z 0-Correction factor (based on local conditions)J$38 4ZEnglish  @$$@$$BurThis is a correction factor based on conditions. For example, wind would increase the heat loss from the surface. $3 $AE %&! &&! '&! (&! )&! *&! +&! ,&! -&!!65  8 [ Exhaust - flue gases losses66 7()81 ,{ (PD8(%Return To Exhaust - flue gases losses8-{ $Z  Name or designation of gases J8@ !4ZEnglish  @$8@$8BTQName of the flue gases such as "charge end" or any other name for identificatioj.(8z 8D D6BP(%Return To Exhaust - flue gases losses 8@ 8AF91 9-  8Z 85Temperature of gases at exit end of the kiln - heaterJ9@4U :4ZEnglish  @$9@$9B?<Temperature of the exit gases at the flue in Degrees Celcius 9@ 9AG:1 :-4| 9Z $!Volume flow rate of exhaust gasesJ:@ ;4ZEnglish  @$:@$:BB?Volumetric flow rate of the exit gases in cubic meters per hour :@ :A;1 ;* | :Z Oxygen - O2 (dry) %J;@  <4ZEnglish  @$;@$;BGDOxygen content of the flue gases in percent by volume on a dry basis ;@ ;A<1 <*| ;Z Carbon dioxide - CO2 (dry) %J<@ =4ZEnglish  @$<@$<BOLCarbon Dioxide content of the flue gases in percent by volume on a dry basis <@ <A%=1 =*\} <Z  Carbon monoxide - CO (dry) % J=@4 >4ZEnglish  @$=@$=BPMCarbon Monoxide content of the flue gases in percent by volume on a dry basis =@ =A&>1 >*}=Z "Carbon monoxide - CO (dry) ppmvJ>@ ?4ZEnglish  @$>@$>BZWCarbon Monoxide content of the flue gases in parts per million by volume on a dry basis >@  >A'?1 ?*} >Z Sulfur Dioxide (SO2) J?@ @4ZEnglish  @$?@$?BPMSulpher Dioxide content of the flue gases in percent by volume on a dry basis ?@! ?A(6r"L BQ  @:AXBWC:DXE,F,G:HWI; M,N O;P Q,R,S:T,U:V:W:XWY:Z:[,\I @1 @* ~ ?Z Total combustibles - (dry) %J@@ 84ZEnglish  @$@@$@Ba^Total combustibles remaining in the flue gases at the exit in percent by volume on a dry basis @@" @A)A1 A*~ @Z  NOx ppmvJA@4  B4ZEnglish  @$A@$ABYVNitrogen Oxide content of the flue gases in parts per million by volume on a dry basis A@# AA*B1 B*~ AZ 41Water vapor in combustion products (Default=4.0%)JB@  C4ZEnglish  @$B@$BBWater Vapor contained in the flue gases in percent by volume on a dry basis. Default is 4% but it can be changed by the user if necessary. B@ BA+C1 C*T BZ Particulates if any JC@  D4ZEnglish  @$C@$CBDAParticulates contained in the flue gases in grams per cubic meter C@$ CA D1 D* CZ ^[Mass or weight collected in particulate collection equipment (bag house, ESP etc.) - totalJD@  E4ZEnglish  @$D@$DBa^Total weight of the particulates collected in the baghouse during the collection period in Kg. D@% DA E1 E* DZ /,Time or number of hours - collection period JE@@ F4ZEnglish  @$E@$EB0-Time length of the collection period in hours E@& EA F1 F*| EZ "Nature or name of particulates JF@ G4ZEnglish  @$F@$FB/,Name or nature of the particulates collected F@ FA G1 G*` FZ YVPercent calcined material in material collected from particulate collection equipment JG@ H4ZEnglish  @$G@$GBKHPercentage of the collected material which consists of calcined material G@) GAH1 H*O GZ 2/% combustible material in particulates (if any)JH@$ I4ZEnglish  @$H@$HB|Percentage of the collected material which consists of combustible materials (unburned coal or other combustible materials) H@* HAI1 I4O HZ FCHeating value of combustible particulate material (Default=19,200)JIB 94ZEnglish  @$I@$IBDAHeating Value of the collected combustible material in kJ per Kg. IB IAM!!O5 $ Q [" !Radiation losses from openingsO6 P()Q2 X 6DQ+(Return To Radiation losses from openingsQ-N IZ""Shape of openingJQ>p@ 4Z!English  @$Q@$QB*'Shape of Opening (Round or Rectangular)(Q؇ QD DOBP+(Return To Radiation losses from openings Q>+ QA`R3 R-N QZ"#%"Name or designation of the openingJR>9 S4Z!English  @$R@$RB)&Name of the opening for identification R> RAaS3 S-DN RZ"$,)Number of openings of same size and shapeJS>9 T4Z!English  @$S@$SBWTIf there are multiple openings of the same size enter the quantity of these openings S>, SAbT3 T-N SZ"%Total opening areaJT>: U4Z!English  @$ N T@$TB.+Total area of each opening in square meters T>- TAcU3 U-M TZ"&)&Average zone or radiation source temp.JU>: V4Z!English  @$U@$UBPMAverage temperature of the kiln in the area of the opening in Degrees Celcius U>. UAdV3 V-M UZ"'Ambient TemperatureJV>|; W4Z!English  @$V@$VBOLAmbient temperature in the area where the kiln is located in Degrees Celcius V>/ VAeW3 W-LM VZ"(.+Wall thickness or opening depth (Thickness)JW>< X4Z!English  @$W@$WBJGThickness in millimeters of the kiln wall where the opening is located. W>0 WAfX3 X-ti WZ")Length of opening (L)JX>< Y4Z!English  @$X@$XBIf the opening is rectangular, enter the length of the opening in meters. If the opening is round, enter the diameter of the opening X>1 XAgY3 Y-i XZ"*Height of opening (H)JY>= Z4Z!English  @$Y@$YBnkIf the opening is rectangular, enter the width of the opening in meters. If the opening is round, no entry Y>2 YAhZ3 Z-L YZ"+41View factor - user defined if known or from chartJZ>> [4Z!English  @$Z@$ZB[XEstimate the radiation view factor using the chart, or enter if the view factor is known Z>3 ZAi[3 [-L ZZ",*'Emissivity of the source (Default=0.9)J[>@? \4Z!English  @$[@$[B@=Emissivity of the radiation source (the inside of the kiln) [>8 [Aj\4 \2`L [Z"-% Open time (Default=100%)J\?? Q4Z!English  @$\@$\B[XPercentage of time the opening is open, for example, a door may be open 50% of the time. \?4 \Ak8_\AN' Ty =#,b c;d;e,f,g:hI { |;} ~:,!c5 D e [Water cooling loopsc6 d5)e1  ODe Return To Water cooling loopse*0L \ZCooling water flow rateJe>9 R4Z!English  @$e@$eB@=Enter the flow rate of the cooling water in liters per minute(ed eD DcBP Return To Water cooling loops e>5 eAHf1 f*K eZWater Inlet temperatureJf>T7 g4Z!English  @$f@$fB@=The inlet temperature of the cooling water in Degrees Celcius f>6 fAIg1 g*K fZWater Outlet temperatureJg>7 h4Z!English  @$g@$gBMJThe exit temperature of the cooling water from the kiln in Degrees Celcius g>7 gAJh1 h4HK gZA>Correction factor or density factor if applicable (1=Default)Jh>h8 e4Z!English  @$h@$hBURA correction factor to account for increased heat losses due to unusual conditions h?9 hAK!|5 @ ~ [ Air cooling loops|6 }()~. p cD~Return To Air cooling loops~- K hZ Cooling air or gas flow rateJ~>6 f4Z!English  @$~@$~BJGEnter the flow rate of the cooling air in normal cubic meters per hour.(~  ~D D|BPReturn To Air cooling loops ~>: ~A_/ -J ~Z  Air or gas inlet temperatureJ>4 4Z!English  @$@$B>;The inlet temperature of the cooling air in Degrees Celcius >; A`I3G:I  ; I / -J Z  Air or Gas outlet temperatureJ>5 4Z!English  @$@$BKHThe exit temperature of the cooling air from the kiln in Degrees Celcius >< A/ -5 4Z!English  @$@$B74The specific heat of the cooling air in kJ / (nm3-C) > Af0 2I Z 52Correction factor or density factor if applicable J?6 ~4Z!English  @$@$BURA correction factor to account for increased heat losses due to unusual conditions ?9 AK!5 L  [Clinker discharge6 ()6 |DReturn To Clinker discharge2I Z# Correction factor (Default=1.00)J?3 4Z!English  @$@$BURA correction factor to account for increased heat losses due to unusual conditions( D DBPReturn To Clinker discharge ?9 AKx'G ; :,: !5 Ԉ  [ $!Clinker bed cooling and other air6 ()2  D.+Return To Clinker bed cooling and other air!-dI  [ Air volume flow rateJ>4( 4Z!English  @$@$BJGEnter the flow rate of the cooling air in normal cubic meters per hour.( D DBP.+Return To Clinker bed cooling and other air >: Ai3 !-8I  [ Air inlet temperatureJ>$ 4Z!English  @$@$B>;The inlet temperature of the cooling air in Degrees Celcius >; A`3 !-I  [ Air outlet temperatureJ>0% 4Z!English  @$@$BZWThe exit temperature of the cooling air from the clinker cooling bed in Degrees Celcius >= A4 !2H  [ Destination of Air FlowJ?% 4Z!English  @$@$B,)The destination of the air flow. Exhaust thru the system means the heat is recovered or recirculated or used internal to the system. Exhaust outside the system means the heat is recoverable by other means, for example recovery of heat from clinker cooling bed for its use in a waste heat boiler. ? AxW ; :,,I:; !5   [$$!Other or waste products discharge6 (). ( D.+Return To Other or waste products discharge,|H Z$/,Mass or weight of products collected - totalJ@<3 4Z!English  @$@$Ba^Total weight of the particulates collected in the baghouse during the collection period in Kg.(Љ D DBP.+Return To Other or waste products discharge @% Aa/ ,$H Z$.+Time or number of hours - collection periodJ@H0 4Z!English  @$@$B0-Time length of the collection period in hours @& A/ ,G Z$+(Temperature of the products at dischargeJ@0 4Z!English  @$@$B52Temperature of the particulate matter at discharge A> Ab/ ,\G Z$ <9Specific heat of the products (mass based) (Default=1.05)J@ 1 4Z!English  @$@$BThis is the mass specific heat of the other particulate material. The units of measure are: kJ/(Kg-Degrees C) > Ac/ ,F Z$ 2/% combustible material in particulates (if any)J@2 4Z!English  @$@$BURPercentage of the collected other material which consists of combustible materials @? Ad0 .tF Z$ EBHeating value of combustible particulate material (Default=24,000)JB2 4Z!English  @$@$BDAHeating Value of the collected combustible material in kJ per Kg. B AeW]$ ;I,,,,,I;  ;!5 ؋  [Fuel - energy input6 () D Return To Fuel - energy input74F Z !Quantity (amount) of fuel usedJ>/ 4Z!English  @$@$BLIThe quantity of fuel used in Kg/hr. 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Control pagePlant General Information PHAST summary reportPHAST energy use distributionChart-Energy use distributionChart- energy use comparison1- Charge material1- charge material 21- charge material 32 - Wall lossesDensity calculations 3- Exhaust gases 4-Radiation losses from opening5-Kiln cooling water6-Kiln cooling air7-Clinker discharge 8-Clinker bed cooling-other air9-other prod dischrge dataCoeff. for calculations (2)10-Fuel-Energy input 11 Power- Motor driven systems12 Other heat lossAv. Heat for coal typical Cp calculations Sheet1Help radiation_vf TranslationWhat is PHASTAir_cooling_loops"Clinker_bed_cooling_and_other_airClinker_dischargeExhaust___flue_gases_lossesFuel___energy_inputHeat_input_to_charge_materialKiln_shell_wall_heat_losses4Other_heat_loss_or_generation__unaccounted_if_known"Other_or_waste_products_discharge%Power__electric_motor_driven_systems '1- Charge material'!Print_Area#'10-Fuel-Energy input '!Print_Area-'11 Power- Motor driven systems'!Print_Area '12 Other heat loss'!Print_Area'2 - Wall losses'!Print_Area'3- Exhaust gases'!Print_Area-'4-Radiation losses from opening'!Print_Area"'5-Kiln cooling water'!Print_Area '6-Kiln cooling air'!Print_Area!'7-Clinker discharge'!Print_Area-'8-Clinker bed cooling-other air'!Print_Area('9-other prod dischrge data'!Print_Area*'Chart- energy use comparison'!Print_Area+'Chart-Energy use distribution'!Print_Area'Control page'!Print_Area+'PHAST energy use distribution'!Print_Area"'PHAST summary report'!Print_Area)'Plant General Information '!Print_AreaRadiation_Losses_from_OpeningsWater_cooling_loops  Worksheets Named Ranges 8@ _PID_HLINKSAT/0'What is PHAST'!A13g#'PHAST energy use distribution'!A1OC !'Plant General Information '!A1=s '6-Kiln cooling air'!A1 V 'PHAST summary report'!B1EX '12 Other heat loss'!B13  &'11 Power- Motor driven systems'!B11wi'10-Fuel-Energy input '!A14; '9-other prod dischrge data'!B7VY%'8-Clinker bed cooling-other air'!A1\'7-Clinker discharge'!A1_'5-Kiln cooling water'!A1I%'4-Radiation losses from opening'!A1q'3- Exhaust gases'!Print_Area['2 - Wall losses'!A1o"'1- Charge material'!A6%Nmailto:athekdi@e3minc.comdt'Control page'!D23?t#'Chart-Energy use distribution'!A1ds'Control page'!D24U "'Chart- energy use comparison'!A1 U'PHAST Summary Report'!A1dt'Control page'!D23dt'Control page'!D23?t#'Chart-Energy use distribution'!A1%K/control_page!D6%wHelp!B5%K pcontrol_page!D6DR Kiln_shell_wall_heat_losses%Kcontrol_page!D6X~ Exhaust___flue_gases_losses%Kxcontrol_page!D6Nv Radiation_Losses_from_Openings'K radiation_vf!A1'K radiation_vf!A1'K radiation_vf!A1'K radiation_vf!A1%KHcontrol_page!D6pv Biff8Excel.Sheet.89qRoot Entry F(ڈ@<Workbook6_VBA_PROJECT_CUR" D?@ABKDEFGHIJ=LMNORSTUVWXYp~p   %$  "#A&'1)*+,-./0!43?6789:;<=>@BWLDEFGHIJK2MOmPQRSTUVZjY[\]^h`abcdefgXiklnoqr|tuvwxyz{}~ N       !"#$%&'()*+,-./0123456789:;<=>?@ABCDEFGHIJKLMNOPQRSTUVWXYZ[\]^_`acdefghijklmnopqrstuvwxyz{|}~      !"#$%&'()*+,-./0123456789:;<=>?@ABCDEFGHIJKLMNOPQRSTUVWXYZ[\^_`abcdefghijklmnopqrstuvwxyz{|}]      !"#$%&'()*+,-./0123456789:;<=>?@ABCDEFGHIJKLMNOPQRSTUVWXYZ[\]^_`abcdefghijklmnopqrstuvwxz{|}~\ / !"#$%&()*+,-.K123456789:;<=>@ABCDEFGHIJMNOPQRSUVWXYZ[_`abcdefghijklmnopqrstuvwxyz{|}~՜.+,D՜.+,h$ PXl t|  E3M Inc.' ; Control pagePlant General Information PHAST summary reportPHAST energy use distributionChart-Energy use distributionChart- energy use comparison1- Charge material1- charge material 21- charge material 32 - Wall lossesDensity calculations 3- Exhaust gases 4-Radiation losses from opening5-Kiln cooling water6-Kiln cooling air7-Clinker discharge 8-Clinker bed cooling-other air9-other prod dischrge dataCoeff. for calculations (2)10-Fuel-Energy input 11 Power- Motor driven systems12 Other heat lossAv. Heat for coal typical Cp calculations Sheet1Help radiation_vf TranslationWhat is PHASTAir_cooling_loops"Clinker_bed_cooling_and_other_airClinker_dischargeExhaust___flue_gases_lossesFuel___energy_inputHeat_input_to_charge_materialKiln_shell_wall_heat_losses4Other_heat_loss_or_generation__unaccounted_if_known"Other_or_waste_products_discharge%Power__electric_motor_driven_systems '1- Charge material'!Print_Area#'10-Fuel-Energy input '!Print_Area-'11 Power- Motor driven systems'!Print_Area '12 Other heat loss'!Print_Area'2 - Wall losses'!Print_Area'3- Exhaust gases'!Print_Area-'4-Radiation losses from opening'!Print_Area"'5-Kiln cooling water'!Print_Area '6-Kiln cooling air'!Print_Area!'7-Clinker discharge'!Print_Area-'8-Clinker bed cooling-other air'!Print_Area('9-other prod dischrge data'!Print_Area*'Chart- energy use comparison'!Print_Area+'Chart-Energy use distribution'!Print_Area'Control page'!Print_Area+'PHAST energy use distribution'!Print_Area"'PHAST summary report'!Print_Area)'Plant General Information '!Print_AreaRadiation_Losses_from_OpeningsWater_cooling_loops  Worksheets Named Ranges 8@ _PID_HLINKSAT/0'What is PHAST'!A13g#'PHAST energy use distribution'!A1OC !'Plant General Information '!A1=s '6-Kiln cooling air'!A1 V 'PHAST summary report'!B1EX '12 Other heat loss'!B13  &'11 Power- Motor driven systems'!B11wi'10-Fuel-Energy input '!A14; '9-other prod dischrge data'!B7VY%'8-Clinker bed cooling-other air'!A1\'7-Clinker discharge'!A1_'5-Kiln cooling water'!A1I%'4-Radiation losses from opening'!A1q'3- Exhaust gases'!Print_Area['2 - Wall losses'!A1o"'1- Charge material'!A6%Nmailto:athekdi@e3minc.comdt'Control page'!D23?t#'Chart-Energy use distribution'!A1ds'Control page'!D24U "'Chart- energy use comparison'!A1 U'PHAST Summary Report'!A1dt'Control page'!D23dt'Control page'!D23?t#'Chart-Energy use distribution'!A1%K/control_page!D6%wHelp!B5%K pcontrol_page!D6DR Kiln_shell_wall_heat_losses%Kcontrol_page!D6X~ Exhaust___flue_gases_losses%Kxcontrol_page!D6Nv Radiation_Losses_from_Openings'K radiation_vf!A1'K radiation_vf!A1'K radiation_vf!A1'K radiation_vf!A1%KHcontrol_page!D6pv Water_cooling_loops%Khcontrol_page!D6Air_cooling_loops%K$control_page!D64Clinker_discharge%K control_page!D6&"Clinker_bed_cooling_and_other_air"Other_or_waste_products_discharge%K control_page!D6eFuel___energy_input4%Power__electric_motor_driven_systemsbo4Other_heat_loss_or_generation__unaccounted_if_known i9http://books.nap.edu/openbook.php?record_id=9736&page=92p2000a4298940092004 i9http://books.nap.edu/openbook.php?record_id=9736&page=92p2000a4298940092003 i9http://books.nap.edu/openbook.php?record_id=9736&page=92p2000a4298940092002th '12 Other heat loss'!A1 %'11 Power- Motor driven systems'!A1wi '10-Fuel-Energy input '!A148 '9-other prod dischrge data'!A1VY%'8-Clinker bed cooling-other air'!A1\'7-Clinker discharge'!A1=s'6-Kiln cooling air'!A1_'5-Kiln cooling water'!A1At-'4-Radiation losses from opening'!Print_Area@'3- Exhaust gases'!A1o"'1- Charge material'!A1['2 - Wall losses'!A1I%'4-Radiation losses from opening'!A1VB'Control page'!A1VB'Control page'!A1VB'Control page'!A1VB'Control page'!A1DocumentSummaryInformation8}&CompObj m

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