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    RAW MATERIAL HANDLING

    AND GRINDING

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    INTRODUCTION

    In a cement plant the Cement Manufacturing Process consists of the

    following:

    Raw material handling

    Raw Material Grinding

    Coal handling

    Coal GrindingPyro – Process

    Cement Grinding

    Cement PackingThese processes are are shown in the flow chart.

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    Raw Material

    andling

    Raw Material

    Grinding

    Coal

    andling

    Coal

    Grinding

    Pyro ! Process

    Cement

    Grinding

    Cement Packing

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    Raw Material Handling

    The raw materials used in cement plants are mainly limestone"

    laterite" #au$ite and iron ore. The ma%or raw material is

    limestone" which is supplied from limestone mines. The

    limestone supplied from mines is of si&e up to one cu#ic meter

    and therefore re'uires crushing for reducing to the re'uired

    si&es. (ther raw materials are normally of re'uired si&e. The

    raw material handling consists of the following operations and

    is shown #y flow chart..

    )imestone crushing

     )imestone *tacking and *torage

    )imestone Reclaiming

    +eeding to limestone and additi,e hoppers

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    )imestone Crushing

    -elt con,eyors

    )imestone

    *tacking *torage

    )imestone

    Reclaiming

    -elt con,eyors

    )imestone opper 

    /dditi,e *tockyard

    -elt con,eyors

    /dditi,e

    opper no.0/dditi,e

    opper no.1

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    Raw Material Crushing

    )imestone mined from limestone mines ha,ing si&e up to

    one cu#ic meter ha,e to #e crushed to the re'uired si&esdepending on the type of raw material grinding system

    a,aila#le in the plant. There are different types of crushing

    as gi,en #elow.

    *ingle stage crushing

    Primary crushing

    *econdary crushingTertiary crushing

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    Different tyes !f "rushers used f!r li#est!ne "rushing are

    gi$en %el!w&

    2aw Crusher 

    Gyratory Crusher 

    2aw type Gyratory Crushers

    Cone Crusher 

    Roll Crusher 

    ammer Crushers

    Impact Crushers

    Impact!hammer crusher 

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    Different Tyes Crushers

    '( )aw Crusher: ! It is mainly designed for medium

    hard to ,ery hard materials and usually installed as primary crusher. There are two types of %aw

    crushers. *ingle toggle %aw crushers is ideally

    suited to hard and tough" #ut not so a#rasi,e

    materials. 3ou#le toggle %aw crusher are suited for

    highly a#rasi,e e$tremely hard and tough material.

    Capacities of 14 – 0566 tph are a,aila#le with a

    reduction ratio of 7!8: 0. *pecific powerconsumption of this crusher is 6.1 – 6.9 wh per

    ton of material.

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    *( Gyrat!ry Crusher: ! In cement industry

    gyratory crusher is used for primarycrushing of limestone of medium hard to

    ,ery hard for higher capacities of around

    0866 tph. It has a two to three times

    capacity of %aw crusher for the same si&es

    of feed opening and discharge slot. The

    reduction ratio of this crusher is ;:0 to

    04:0. The specific power consumption ofthis crusher is 0.5 to 5.7 times more than

    the %aw crusher.

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    +( )aw tye Gyrat!ry Crushers& ,

    These crushers are designed to handle e,en #igger feed lumps than the compara#le si&e of the

    gyratory crusher with the same cone diameter.

    These crushers can #e installed for single stage

    crushing. These crushers can #e installed for

    crushing all type of material from ,ery hard to

    soft e$cept wet or sticky material.

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    -( C!ne Crusher&

    In this type of crusher" the positions of the crushingcone and conical crushing ring are ad%acent to each

    other. These crushers are mainly installed as secondary

    or tertiary crushers. The reduction ratio is in the order

    of 8 to 0. It is used for hard to ,ery hard =moderatelya#rasi,e> to fria#le material. The specific power

    consumption of this crusher is 6.5 – 6.9 wh per ton

    of material.

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    /( Ha##er Crushers& ,

    These are widely used in cement industry. They areused for si&e reduction of hard to medium hard

    limestone and sometimes for wet and sticky material.

    ammer mills work with reduction ratios as high as

    0:96 to 0:76 as primary and 04:0 as secondarycrushers. It can #e installed for single stage crushing"

     primary crushing or secondary crushing. Two types

    of hammer crushers are manufactured? single shaft

    and dou#le shaft hammer crushers and work with theimpact effect of the hammers. Capacities up to 1666

    tph are a,aila#le. 

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    0( I#a"t Crushers& ,

    These crushers are suita#le for non!a#rasi,e" from soft

    to hard" slightly wet materials. The predominant stressused is impact" howe,er cut and attrition are also used.

    The ma$imum reduction ratios are 96:0. There are two

    types? single rotor impact and dou#le rotor impact

    crushers. The specific power consumption of this

    crusher is 6.9 – 0.6 wh per ton of material

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    Impact crushers are capa#le of capacities of more

    than 1666 tph.

    The si&e reduction work of impact crushers is

    limited to certain 'uality characteristics of the

    crusher feed. These limits are:

    Compressi,e strength: !@ 54666 l# per s'.inch

    MohAs hardness: ! @ 9.4

    Moisture: ! ma$ 16BClay content: ! 6B

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    C A O C 3 3 C O

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    CRITERIA 2OR CRU3HER 3ELECTION

    0. Material to #e crushed:

    ! nature

    ! a#rasi,eness =B of silica>

    ! resistance to compression =kg per cm1>

    ! hardness

    ! moisture content

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    4RE,7LENDING O2 RAW MATERIAL

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    4RE 7LENDING O2 RAW MATERIAL

    Essentials !f 4re,%lending: ! Today with the technological

    ad,ancements in cement industry and increase in the specific

    kiln ,olumes" a uniform 'uality of kiln feed has #ecome pre!re'uisites not only for optimum kiln output #ut also for 'uality

    of the clinker. +or getting uniform 'uality of kiln feed the

     pneumatic homogeni&ation of ground raw meal alone is not

    sufficient and hence it has #ecome necessary to prehomogenise the raw material #y pre!#lending" #efore it is

    fed to the grinding mills. It has another ad,antage of pre!

    homogeni&ation of raw materials from non!homogeneous

    materials mined #y selecti,e mining" manual mining ormechani&ed mining o,er a wider area.

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    Tyes !f 4re,%lenders& ,

    Pre!#lending consists of stacking and reclaiming.3ta"5ing: ! The stacking is the process of

    depositing material of non!uniform 'uality in

    layers =longitudinal or circular> o,er a period of

    time. The following are different methods of

    stacking.

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    ' L!ngitudinal st!"5iles

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    '( L!ngitudinal st!"5iles

    a> Roof!type stockpiles =Che,ron – method>

     #> )ine!type stacking =Dindow – method>

    c> Com#ination of che,ron window method

    d> *trata method

    e> Conical method

    f> )ayer method

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    *( Cir"ular st!"5iles

    a> *ection – style Che,ron method

     #> Continuous che,ron stacking

    c> )ayer method

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    Ch M h d 8Li 9 I hi k

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    Che$r!n Meth!d 8Linear9: ! In this" a stacker

    continuously tra,els #ack and forth o,er the stockpile

    along its length and deposits the material in coneshaped layers. The stockpiling is performed either #y a

     #elt con,eyor tripper or #y a stacker with rigid #oom"

    which mo,es alongside the stockpile.The material

    dumped centrally o,er the ridge flows on each side ofthe pile to form the re'uired layers. The pile increases

    uniformly up to its ma$imum height. (ne draw#ack of

    this method is the segregation of the material into

    larger and smaller particles as it tum#les down thesides of the pile. 3ue to simplicity of operation this is

    the most commonly used method.

    Wind!w Meth!d 8Linear9: ! In this method piles are

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    p

     #uilt!up in a num#er of rows of limited cross section

    one a#o,e other. This method eliminates the

    disad,antage of material segregation as in che,ronmethod" #ut it is less adopted due to re'uirement of

    more ela#orate stacking arrangement.

    C!#%inati!n !f Che$r!n 6 Wind!w #eth!d8Linear9: ! +rom the ,iew point of #lending

    efficiency this is the #est" #ut is rarely adopted due to

    comple$ity of stacking arrangement.

    3trata Meth!d 8Linear9: ! *trata method is more

    intended reclaiming #y the side acting scrapper.

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    3e"ti!nal style Che$r!n 3ta"5ing 8Cir"ular9&

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    3e"ti!nal,style Che$r!n 3ta"5ing 8Cir"ular9& ,

    The stockpiling in circular #lending #ed is

     performed #y a #elt con,eyor" which is swi,el!

    mounted in the #edAs center point. The cross

    section of a circular stockpile can either triangular

    or trape&oidal.

    *tacking in this method is relati,elystraightforward and can #e compared to

    longitudinal #eds. owe,er" this method produces

    su#stantial ,ariations in the 'uality in the transition

    &ones from one section to other.

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    0. *ide Reclaiming

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    1. +ront end Reclaiming

    a> )uffing *craper Chain /ssem#ly

     #> ori&ontal *craper Chain

    c> -ucket Dheel Reclaimer 

    d> -arrel Reclaimer 

    5. E$ca,ating

    a> -ucket Dheel on Pi,oted -ooms

     #> -ucket Chain *ystem

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    '( 3ide Re"lai#ing: ! E'uipment for side reclaiming

    i f li # di h il

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    comprises of a tra,eling #oom e$tending o,er the pile

    and reclaiming is achie,ed #y the scraping action of a

    luffing scraper chain assem#ly on one face of the pile.The material rakes down the #ase of the pile where it is

    remo,ed #y a longitudinal #elt con,eyor under floor or

    to one side of the stockpile. *uch reclaiming is normally

    used for stockpiles #ased on strata system or conicalsystem.

    *( 2r!nt end Re"lai#ing: ! It comprises a tra,eling #ridge

    operating on rail tracks on either side of the stockpile.

    The reclaimed material is remo,ed #y a #elt con,eyor.The reclaiming in this case is done #y any of the

    following methods

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    iii> 7u"5et Wheel Re"lai#er: ! In this case one or

    # k h l i % i i h

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    more #ucket wheels operate in con%unction with a

    raking down de,ice. The raking down de,ice dislodges

    the material and #rings it down within the reach of #uckets. These two mo,e automatically across the face

    of the pile and their direction of mo,ement is re,ersed

    with the help of limit switches at the #ridge ends.

    *imultaneously" the #ridge mo,es forward in thelongitudinal direction for a present distance. The

    material scooped #y the #uckets is fed on to a #elt

    con,eyor mounted on the #ridge and in turn on to a

    longitudinal #elt con,eyor for onward transmission.

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    i9 7u"5et Wheel !n 4i$!ted 7!!#s: ! In this the #ucket

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    wheel itself #ites its way through the entire height of

    the dump in certain num#er of slices depending on the

     #ucket wheel diameter. This method is suited forcoarse!grained moist or sticky material.

    ii9 7u"5et Chain 3yste#: ! +or certain materials" it is

     prefera#le to go in for a storage pit instead of astockpile. /#o,e the pit two gantries run on tracks.

    +rom the upper gantry" raw material is dumped into

    the pit from a distri#ution #elt. Running on the lower

    gantry is a #ucket ladder e$ca,ator" which remo,es thedumped material.

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    4RE,7LENDING E22ICIENC

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    Efficiency of pre!#lending stockpile is measured

     #y the ratio of standard de,iation of CaC(5

    content of input material to standard de,iation of

    CaC(5 content of output material. It is possi#le to

    achie,e a #lending efficiency of ;:0 to 06: 0.

    2a"t!rs affe"ting 7lending Effi"ien"y: ! The

    factors affecting the #lending efficiency are:

     ,ariation in the incoming material

     method of formation of stockpile

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    RAW MATERIAL GRINDING

    The raw material grinding is a process" which in,ol,es

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    The raw material grinding is a process" which in,ol,es

     preparation of raw mi$ for making clinker. The crushed

    limestone along with the additi,es such as laterite" #au$ite

    or iron ore in the re'uired proportions are ground raw

    mills for getting raw meal of re'uired fineness.

    The right choice of a raw grinding system is influenced #y

    a series of techno!economic considerations including thelocal conditions. The system which has the highest

    operational economy" coupled with low in,estment cost

    and high relia#ility" has to #e aimed at.

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    C. (perating Cost

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    i> Energy

    ii> Dear 

    iii> Manpower 

    3. In,estment Costs

    i> Plant and Machinery

    ii> Electricals and control system

     iii> Ci,il construction

    E. En,ironmental Regulation

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    g

    i> 3ust

    ii> Hi#ration

    +. Maintaina#ility Relia#ility

    i> 3amage and Replacement of compounds

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    i> 3amage and Replacement of compounds

    ii> *kill of plant operating staff 

    iii> Comple$ity of design" replacement and

    a,aila#ility

    The most important factors in relation to a

    modern dry process plant are the moisture

    and grinda#ility of raw material and

    specific power consumption.

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    The ,ertical roller mills are different types such as Ring Roller

    Mills" Ring -all Mills" -owl Mills" etc. The characteristic of

    th ill i th t th i d ti i ff t d # ll

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    these mills is that the si&e reduction is effected #y rollers on

    compara#le grinding elements tra,eling o,er a circular #ed of

    material. The material after passing under the rollers is su#%ectedto a preliminary classifying action #y a stream of air sweeping

    through the mill. The air at high ,elocity lifts the material to the

    classifier" which separates the coarse and fine particles. The fine

     particles are entrained and the separated coarse particles fall

     #ack to the ta#le. The separator could #e either static or

    dynamic. The fine particles are collected later in an E*P or -ag

    +ilter. In Hertical roller mills with e$ternal recirculation" the

    no&&le ring ,elocity is lower = 96!76 m.per sec> than the mills

    without e$ternal recirculation =;6!86 m. per sec>.

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    Raw Mi; 2ineness: !

    The ad$antages !f in"reasing the raw #i; fineness are:

    *h t ti i d f h ti f d d i i

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     *horter time re'uired for preheating of suspended raw mi$ in

     preheater.

     +aster calcination and clinkeri&ation reactions.

     Increase in clinker production rate.

     Reduction in specific fuel consumption.

    The disad$antages !f in"reasing the raw #i; fineness are:

     Increase in specific power consumption of raw mi$ grinding.

    3epending on chemical and physical characteristics of the raw mi$"

    optimum fineness has to fi$ed #y considering all the a#o,e

    mentioned factors.

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    4r!"ess !f drying raw #aterials in Raw Mills

    The characteristic feature of the drying!grinding process is that

    two different processes are generally performed in the grinding

    mill The heat re' ired for dr ing the ra material is s pplied #

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    mill. The heat re'uired for drying the raw material is supplied #y

    hot gases from preheater or cooler or hot air generator and #y theheat generated #y comminution in the grinding process.

    In #all mills for drying of raw material a drying compartment is

    arranged in front of the grinding compartment of the mill. The

    drying cham#er is e'uipped with lifters" #ut has no grindingmedia.

    In the traditional #all mill the drying capacity is limited #y its

    geometry. E,en at sufficient hot gas amount it was difficult to get

    all necessary gas flow to pass the mill. The gas flow and dryingcapacity was normally decreased with mill si&e =grinding

    capacity>.

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    Meth!d !f De,dusting raw #ill gases

    3e!dusting of raw mill e$haust gases are done #y the

    following methods:

    Gra$ity settling "ha#%ers:

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    y g

    Cy"l!nes

    Multi"l!nes

    7ag 2ilters

    Gra$el %ed filter

    Ele"tr!stati" 4re"iitat!r

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    C

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    Cyclones are low cost dustcollectors and it consists of twosections? a cylindrical and conicalone. /t the top of the cylindricalsection the dust laden gas enterstangentially. It spirals along the

    walls downward and upward to theoutlet thim#le. 3ust is separatedfrom the gases #y the centrifugalforces. The efficiency of cyclonesdecreases with decreasing particlesi&es and in,ersely proportional toits diameter. It is used as a pre!collector.

    MULTICLONE3

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      Multicyclones are units ofcyclones installed in

    com#inations of series and

     parallel for high throughput

    and high efficiency. The

    efficiency of multicyclones

    is in the range of 84!9B.

    2a%ri" 2ilters: ! These are generally of #ag type" i.e. tu#es

    with 566 mm diameter or less" and up to 06 m high? they

    consists of wo,en or felted cloth" made from natural or

    synthetic fi#ers. +a#ric filters can handle small particles in the

    su# micron range at high efficiencies of .4B. The dust laden

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    gases flow through the porous medium of ! the filter fa#ric!and deposits particles in the ,oids. /fter filling the ,oids" a

    cake starts to #uild up on the fa#ricAs surface" which does most

    of the filtering. Dhen the dust layer #ecomes too thick" an

    increase in pressure drop results? this re'uires cleaning of the

    fa#ric. 3epending on the characteristic of the dust and type offa#rics" the following methods are applied for cleaning.

    a> -ag swinging

     #> Re,erse air 

    c> Pulse pressure

    d> *onic cleaning

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    Ele"tr!stati" 4re"iitat!r 8E349&  ! The principle of dust

    collection is #ased on the utili&ation of the effect of gas

    ioni&ation in a strong electric field" which is formed #y discharge

    electrodes =corona effect" negati,e> and #y collecting electrodes

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    electrodes =corona effect" negati,e> and #y collecting electrodes

    =positi,e>. Collection of efficiencies of .;4B is attaina#leunder fa,ora#le conditions.

    The complete electrostatic precipitation process consists of fi,e

     #asic steps that operate on a continuous #asis:

    0. Gas distri#ution into treatment &one

    1. Particle charging L corona discharge =gas conduction>

    5. 3eposition of dust on collecting electrodes

    9. /ccumulation of dust

    4. Remo,al of the collected material

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     The process condition in E*P ,aries during raw mill and coal mill

    shutdowns and the E*P performance ,aries.

     The tripping of E*Ps with increase in C( content in the kiln e$haust

    gases due to process fluctuations are ,ery common

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    gases due to process fluctuations are ,ery common.

      The disad,antage of #ag filter is it can not withstand high

    temperatures" which happens during plant start!up and upset

    conditions.

     -ag filter system re'uires regular maintenance of cleaning system

    and timely replacement of filter #ags.

      The disad,antage of E*P is the snapping of electrodes and plant

    stoppage for its rectification.

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    Tyes !f 7lending

    omogeni&ation of cement raw mi$ can #e performed on a #atch

    #asis as well as continuously

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     #asis as well as continuously.

    7at"h %lending: ! +or #atch system two #lending silos? normally

    one is called as #lending silo and other as storage silo. The

    homogeni&ation process starts during the filling of #lending silo.

    /fter filling the #lending silo" homogeni&ation process continues for

    a#out one hour. Then it is discharged to the storage silo normallylocated at the #ottom of the #lending silo" where it is homogeni&ed

    continuously and e$tracted for kiln feed. -atch type homogeni&ation

    is applied in cases where the 'uality of the raw material widely

    fluctuates and in relati,ely long time inter,als.

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    R!le !f 7lending 3il! in ?uality C!ntr!l !f Raw Mi;

    -lending silos ha,e a ma%or role in achie,ing uniform and consistent

    'uality of raw mi$" which is essentially re'uired for getting ma$imum

    output from the kiln and optimi&ing specific fuel and power

    consumption. -lending silos" #y #lending process reduces the 'uality

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    ,ariation in the raw mi$. There are ,arious types #lending silos ha,ing #lending factor from 7:0 to 04:0. The #asic principle of #lending

     process is one or com#ination of the following mechanisms.

    3istri#ution of input raw meal at the #lending silo top.

    Pneumatic dry #lending #y aeration of raw meal #y the aerationunits placed at the #ottom of silo.

    *egmental aeration =octant or 'uadrant system> with difference in

    the pressure of air supplied for aeration of ,arious segments for

    thorough mi$ing of raw mi$.

    Method of e$traction to kiln feed

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    7lending 2a"t!r

    +or calculation of #lending factor of a silo" input and output raw meal

    samples are to #e collected in regular inter,als and to #e tested for

    CaC(5 content.

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    *ilo input samples to #e collected for a period of one theoretical filling

    of silo with an inter,al not e$ceeding 0.4 hours and a minimum 96

    samples are to #e collected. +or optimum #lending efficiency silo should

     #e filled more than ;6B. The output samples are to #e collected at an

    inter,al of 5 to 4 minutes after the input samples are collected and aminimum of 16 samples are to #e collected.

    The standard de,iation of the input samples as well as output samples

    are to #e calculated. The #lending factor is the ratio of standard

    de,iation of input raw meal to standard de,iation of output raw meal.

    The more the #lending factor" the #lending is more effecti,e.

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      Fui&

    0.3escri#e the o,er all processes found in cement industry

    1.Dhat is raw material handling 3escri#e it in #lock diagram

    5.)ist at least three types of crushers

    9.There are two types of crushing . 3escri#e in detail

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    4.Dhat is pre#lending7.Mention the e'uipments used for pre#lending

    ;.Dhat is stacking

    8.ow many methods of stacking are there Mention stackers under

    them.Drite all types of #all mill

    06.Dhat is separator 

    00.Is tandem mill air swept mill

    01.Dhat is the ad,antage of ,ertical roller mill o,er #all mill05.Hertical roller mill is air swept mill. True or +alse