Cálculos Generales Horno y Otros

8/17/2019 Cálculos Generales Horno y Otros

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DIMENSIONAMIENTO COLUMNA DE ADSORCIÓN

DATOS CLIENTEFlujo 1628.5 m3/hTonelaje/da 12 t/day of carbon

Flujo 1628.5 m3/h 7165.4 gpm

Parametro 25 4! gpm/ft2Parametro !".2" gpm/ft2

"rea 22.!4 m2 237.3 ft2

Da#e$%o 5.!" # 57.!2 ft

&a al '%()*o '+# ,- E+an-0n

Para #arb$n 6 % 16 malla& 3!.2! gpm/ft2 ' de e%pan&($n )j* 65

)n la columna+onelage 12 t/day,olumen 24 m3 "rea 22.!4 m3/m "ltura 1.!- m carbon en repo&o alor m(n 1 y ma% 1!5#on&(derando 65' ' )%pan&($n "ltura 1.8! m #arbon )%pand(do

"&0 la altura de la columna

Free board !.61 m 2 foot&Al$u%a #n. 2.1 # (n(ma

+(empo re&(denc(a

"rea 22.!4 m2 "ltura 1.8! m #arbon )%pand(do,olumen 3-.6 m3flujo 1628.5 m3/h+(empo e&(d* 1.46 m(n / column #olumn& 6 cant(dad

+(empo e&(d* 8.75 m(n / &(tema ad&orc($n

gwaldron:

Del gráfco para30,2 gpm/t2



8.!7!866142

25-!



DIMENSIONAMIENTO COLUMNA DE ELUSIÓN

DATOS CLIENTE#apac(dad 12 t

,olumen 24 m3 #arb$n en repo&oParametro !.5 rat(o "ltura / (amParametro 3 4 rat(o "ltura / (am

#alculando para ,olumen y "ltura 1.-7 m

uego(ametro 2.17 m)%pan&(on 1" ' "ltura 7.58 m

,olumen 27.-5 m3

"rea 3.6- m2 3-.67 ft2Flo 4 m3/h 17.6 gpmpec(f(c Flo !.44 gpm/ft2

ote*S$%++n' *olu#n &olu#e A*d 3a-4 Colu#n &olu#e 2.5 #!

gwaldron:

Volume= Pi * D2/4 * (h)Volume= Pi * L2/4 * (4*L)Volume= Pi * L3

L=(Volume / Pi)/3

gwaldron:

Del gráfco para 3,3! gpm/t2

gwaldron:

"lu#o para 2 $e% Volume/h2$V= 2t*2m3/t=24m32$V/h= &m3*2/h=2 m3/h



gwaldron:

Volume= Pi * D2/4 * (h)Volume= Pi * L2/4 * (4*L)Volume= Pi * L3

L=(Volume / Pi)/3

912*

gwaldron:

Del gráfco para 3,3! gpm/t2916*

gwaldron:

"lu#o para 2 $e% Volume/h2$V= 2t*2m3/t=24m32$V/h= &m3*2/h=2 m3/h

921*



#uaderno afael1 egenerac($n debe &er 1 por med(o o 1 cada tre& ece&. o m:&.2 a capac(dad del feeder del horno e& 1/2 de la cap. e la columna en 24 hora& proce&o no apagar el horno.3 a;< e& (mportante para la )= >1'?4 a# l(bre e& (mportante para el &tr(pp(ng >!1'?5 Para &tr(pp(ng e& (mportante la temp. 2-! @F y la contam(nac($n dela &oluc($n >(;2 #l ;4 #;3?

6 "nte& de poner la& do& columna& de &tr(pp(ng en &er(e debe llenar&e la &egunda para e(tar la eaporac($n Fla&h7 ebe drenar&e el 1! o 2!' de la& &oluc(one& por d0a para e(tar el enenenam(ento de la& &oluc(one&.8 a e%pan&(o en el &tr(pp(ng no e& &uper(or al 1!'.- e debe real(Aar un control de &oluc(one& barren en )=.

1! #on&umo de Bn C 1DgBn / Dg>"gE"g?11 Pulpa de Bn preparada al 5 a 1!'12 #on&umo de Pb;3 C 1DgPb;3 / Dg Bn o b(en 5! gpt13 Pulpa de Pb;3 preparada al 1!'14 ;2 d(&uelto ma%. 1 ppm15 en&(dad de d(&eo de prec(p(tado # 75 lb/ft316 Flujo m0n(mo en f(ltro& pren&a !25 gpm/ft2.17 Flujo m:%(mo en f(ltro& pren&a 125 gpm/ft2. !7 e& lo ma& u&ual18 )l f(ltro clar(f(cador t(ene la m(&ma :rea Gue el f(ltro pren&a.1- )l laado ac(do no e& nece&ar(o real(Aarlo toda& la& ece&. 1 eA por med(o e&ta b(en.2! a columna po&ee un flujo en el rango 25 a 4! gpm/ft2

21 )l cl(ente entrega la concentrac($n de "g y "u el flujo y la cant(dad de carb$n.22 Flujo de carb$n en la& l0nea& de bombeo e& 65 a 75 ft/& bajo e&to &ed(menta. 1! ft/& e& normal23 a& celda& de )= t(enen un &(&tema de e%tracc($n de ga&e& para el(m(nac($n el <2 generado en el c:todo.24 )l <2 y el calor producto de la (nef(c(enc(a de lo& contacto& elHctr(co& &e (nflama.25 a celda de )= de ,)) e& de (no%. I recub(erta con pol(et(leno.26 o& &ulfato& #l producen gran corro&($n en el c:todo y :nodo& pr(nc(palmente27 la con. e& a;< J1' y p<J12 lo& &ulfato& deben prec(p(tar&e con #al &e debe &aber la procedenc(a de lo& ulfato&28 o& ;4 y #l pre&ente& &e meAclan con <2 y generan :c(do& Gue atacan lo& c:todo&.2- a altura del pacD(ng en la eareat(on +oer e& (gual al d(:metro de la columna3!31



DIMENSIONAMIENTO DILUTED ACID TAN7

1? ,olumen de carbon conten(do en la columna de laado ac(do

"+; #K)+)

#apac(dad 12 t carbon 2646! b&

.L &ol(d& !.5,olume 24.!! m3

2? ,olumen "c(d a&h #olumn C ,olumen tr(pp(ng ,e&&el&

,olumen tr(pp(ng ,e&&el& 27.-5 m3,olumen "c(d a&h #olumn 27.-5 m3

! &olu#en Dlu$ed A*d Tan9 :D.A.T :&ol A. 3. C ; &ol Ca%<on *on$ = ++elne> 1?1

,olumen ".=.# 27.-5 m3#arbon #ontent 24.!! m3P(pel(ne ,olume 1 m3,olumen .".+ 5.45 m3

ote*

Dlu$ed A*d Tan9 :D.A.T &olu#en 5.5 #!

gwaldron:

'alcula%o trip colum olume

gwaldron:

+upueto m3 umatoriapipelie

gwaldron:

Volume car- cotei%o e .'olum



DIMENSIONAMIENTO @EAT EC@ANBER

#apac(dad 12 ten&(dad !.5 t/m3Flo 48 m3/h 2 9,/h

Flo 232.32 gpm

Flujo ,olu#e$%*o a Flujo Ma-*o

Flujo olumen 232.32 gpm 87- l/m(nen&(dad 8.33 lb/gallon 1.!! gr/ccFlujo m:&(co 116114 lb / hr 525-- Dg / h

oe% 8128 TU /4

oe% 2!81 93 n To$al

gwaldron:

"lu#o para 2 $e% Volume/h$V= t/0,! t/m3=2m3

2$V/h/t= 3 t/0,! t/m3 * 2 $/h

gwaldron:

2$V/h*, e gpm

gwaldron:

P1= 2025 (l/h)* ($67/l89")*:0(9")= 2035&,5 ($67/h);<PL1 P.. 2 m3/h



=2 m3/h



gwaldron:

"lu#o para 2 $e% Volume/h$V= t/0,! t/m3=2m32$V/h/t= 3 t/0,! t/m3 * 2 $/h =2 m3/h

96*

gwaldron:

2$V/h*, e gpm

97*

gwaldron:

P1= 2025 (l/h)* ($67/l89")*:0(9")= 2035&,5 ($67/h);<PL1 P.. 2 m3/h

923*



DIMENSIONAMIENTO CELDAS DE E3

DATOS CLIENTE#apac(dad 12 t for &tr(pp(ng

,olumen 24 m3 #arb$n en repo&o9ed ,olume 48 m3/h 29,/hr Flo 211.2 gpmFlo 1!17!6.!5 ft3/m(n

eterm(nat(on of cathode&

epo&(tac($n 15!! g/h "mper& 21!! amp

a%a#e$%o 6" a#+ / *a$4od

cathod 35 cathode&

ellect ;ld 9a&Guet 18

;ld 9a&Guet Ft3 cathode&22 15! 4118 125 33

14 1!! 261! 75 1-7 5! 13

9a&Guet ,olume 72 ft3/cell 2!38.8168!7 (tro&

e&(dence t(me !.!! m(n/ cell er graf(co de ef(c(enc(a

gwaldron:

.mp= (0,4 (.mp*h/g) * !00 (g/h) )/ 0 e>= 200 amp or a &t plat



1.728



gwaldron:

.mp= (0,4 (.mp*h/g) * !00 (g/h) )/ 0 e>= 200 amp or a &t plat

#15*



DIMENSIONAMIENTO IINB,eloc(ty ange

"+; #arbon 6 a 75 ft/&Flo 17 m3/h olut(on& 7 a 1! ft/&Flo 74.8 gpm

,eloc(ty 7.5 ft/&(ameter 2.!2 (n

Pre&&ure 23 PK.L 2.7<ead >ft? 1-.7 ft<ead >m? 6.! m

Flo 74.8 gpm<ead >ft? 1-.7 ft.L 2.7ef(c(enc(a 4!' 'Poer >hp? 2.5 <PPoer >M=? 1.- M=

gwaldron:

V(t/)=0,405!*"lo?(gpm)/%2(i)2

gwaldron:

%(i)=(0,405!*"lo?(gpm)/V(t/))0,!

gwaldron:

@ea%(t)= P+A *2,3/+B

gwaldron:

@P = gpm*@ea%(t)*+B/(3&0 (e>))



gwaldron:

V(t/)=0,405!*"lo?(gpm)/%2(i)2#7*

gwaldron:

%(i)=(0,405!*"lo?(gpm)/V(t/))0,!#8*

gwaldron:

@ea%(t)= P+A *2,3/+B#16*

gwaldron:

@P = gpm*@ea%(t)*+B/(3&0 (e>))#24*



PN#""#" #;+)K; ) ;; P"+"

oAt gramo& lbt

2!!! 31.1!35 622!7 !.454 137 lb

,olumen 1 ft3en&(ty 137 lb/ft3ater 62.4 lb/ft3en&(ty 2.2! Dg/l o gr/cc

)&t(mado carga de f(ltro !6. Dg/day metal content ft3 cc l(tro& 16.58 l/ day olume

1 28316 28.3!.25 7.1

Producc($n e&t(madacarbon t carga g/t Dg/day metal content metal content

3 1!313 3!.-4 !.85 36.4

Lrade etalgold !.5 gr/m3&(ler 1 gr/m3total 1.5 gr/m3

Flo 86! m3/h ma%

Product(on 12-! gr/h ma%3!-6! gr/d

36.4 Dg/d prec(p >85' content?

Fundente& ' content ej Mg/day9ora% 3! 6! ' 45 16.4(l(ce 1! 4! ' 32 11.7#en(Aa de &oda 1! 3! ' 2! 7.3(trato de &od(o ! 1! ' 3 1.1

1!! 36.4



Retortas:

Frecuenc(a etorteo 1 &emana #alculat(on "ltura 9andeja& 2! cm<umedad 3! 'en&(dad Kn(c(al 25!4 Dg/m3 156.2 lb/ft3

en&(dad F(nal 1-47 Dg/m3 121.5 lb/ft3den&(dad Flu% 12!2 Dg/m3 75.! lb/ft3#apac(dad 12 p(e3urac($n c(clo 26 hr&

Horno

Frecuenc(a Fu&($n 1 &emana#apac(dad 35 l(tro& 1.24 ft3 Actual Maricunga

#arga batch#alc(na 8! Dg 71.42857143

Fundente 32 Dg+otal 112 DgSolicitado Maricunga

#arga &emanalProce&ar en 1 d(a#alc(na 35! Dg 771.61 lb 11252.78-!8Fundente 14! Dg 3!8+otal 4-! Dg

,olumen 6.35 ft3etort 12 ft3 enou'4

FurnacePrec(pt catod(co 6.35 ft3Flu% 4.11 ft3+otal 1!.46 ft3

etal orH "g Lrade 24' ' "u Lrade 76' ' "g a&& 185.186 lb 27!!.634383 oAt "u a&& 586.424 lb 8552.!1!638 oAt

11252.645!2



#"#N; ) ,);#K" ) )#<;) #;N" ) ";#KO ) #"9O

"+;,eloc(dad gpm/ft2 3!.2Flujo m3/h 35!

,eloc(dad>m3/h? / ft2 6.- +ran&formac($n>m3/h? / m2 73.- 1m3/h C 44 gpm>m / h? 73.- 1 m2 C 1!76 ft2

#"#N; ) )" )QN)K"

"rea m2 4.74

#"#N; ) K")+; ) " #;N"

ad(o m 1.23(ametro m 2.46

Lraf(ca,eloc(dad d(ametro

25 4.2328 4.!!32 3.7435 3.584! 3.35

(ngre&ar en rojo #alculado&gpm/ft2 d(ametro

25 3.82 4.!8 4.33 4.56 4.7-28 3.61 3.86 4.!- 4.31 4.52

31 3.43 3.66 3.8- 4.1! 4.3!34 3.27 3.5! 3.71 3.-1 4.1!37 3.14 3.35 3.56 3.75 3.-34! 3.!2 3.23 3.42 3.61 3.78

Flujo 7!!.!! 8!!.!! -!!.!! 1!!!.!! 11!!.!!



24 26 28 3! 32 34 36 38 4! 42!.!!

1.!!

2.!!

3.!!

4.!!

5.!!

6.!!

#olumn#

#olumn

#olumn)

'+#

d a # e $ % o



228.6



P;I)#+; LN""#; K)K;"K)+; ) )P)";

"+"&ol(do l(Gu(do Rpe&o pulpa

2.7!! 1 12' 1.!82

m&ol(do ml(Gu(do mpulpa ,pulpa pulpa15!! 11!!! 125!! 11555.56 1.!82

+<K#M)) KBKL "? F;= "+)

+onelaje 125!! t/den&(dad 1.!82 t/m3Flujo 481 m3/hF 1!.6! cm/m(n 6.8- cm/m(n 4.13 m/h "rea 116.5 m2(ameter 12.2 m

9? I ;K F))+on 15!! t/d

ol(d& oad(ng 12 t/m2/deGu(red "rea 125 m2(ameter 12.6 m

$ :#n ! !.5 1 1.5 2 3 4 54 :*# 33.5 28.2 22.4 17.2 13 1!.1 - 8.

9y L

! 5 1! 15 2!

!

51!

15

2!

25

3!

35

4!

Al$a Le

Te#+o #n

A l $ u % a * #



#"#N; ) FK+; P)" 1m3/1ft3

odel 8!! mm mm "rea 238.! ft2 8!!+h(cDne&& !.1!4 1 (nch (n feet -14

,olumen 24.7- ft3 1!!!,olumen 7!2.!! l(ter& 1!67

12!!Flo 53.3 m3/h 2!!!aa(lab(l(ty -5'Factor de llenado 8!' mme&(gn Flo 7!.2 m3/h 12!!e&(gn Flo 3!8.8 gpm

Parametro& #ubuperf(c(al ,eloc(ty !.7 gpm/ft2 Flujouperf(c(al ,eloc(ty 1.7!8 m3/h/m2 ey "u

ey "g "rea #alculated 441.1 ft2 a&a "u "rea #alculated 41.! m2 a&a "g "pro% "rea eal 238.! ft2 a&a Bn

a&a 9ody Feed&ub total

ol(d& part(cle& g/m3 a&a Precoata&& Flo 843 g/h To$alen&(ty 1.2! g/cc,olumen 7!2.22 cc/h P)#;"+,olumen 16.85 l/d area

4!.5

#ycle +(me 37.81 day&9ody Feed

"rea calculada 41.! m2 &oluc(on>m3/h?Flujo m(n 53.3 m3/h 53.3Flujo ma% 7!.2 m3/h 2!!,eloc. (n 1.3! m3/h/m2,eloc. a% 1.71 m3/h/m2

"rea eal 4!.5 m2Flujo m(n 53.3 m3/hFlujo ma% 7!.2 m3/h,eloc. (n 1.32 m3/h/m2

,eloc. a% 1.73 m3/h/m2



!.!28316846632 mm e&pe&or

"rea )ffec.>m2? ,olumen >lt? umero placa& "rea )ffec.>m2? ,olumen >lt?!.- 15.6 45 4!.5 7!2.!

!.! !.!

1.45 24.-! 44 63.8 1!-5.6!.! !.!

2.!1 34.6! 62 124.6 2145.2!.! !.!

mm12!! Flujo 16"." m3/h

Flujo e&(gn 21!.5 m3/h ,eloc. e&(gn 1.7 m3/h/m2

53.3 m3/h "rea total 123.3 m2!.6 g/m3 "rea real / f(ltro 41.1 m2

!.8 g/m3 umero F(ltro& !."" un32 g/h Flujo e&(gn/ f(ltro 5!.! m3/h43 g/h75 g/h

6-3 g/h843 g/h

g/h8! g/h

e&pe&or olumen den&(dad ma&a t Dg l(tro&!.!!16 !.!648 1.!- !.!7!632 ".6 64.8

Dg/m3 Dg/h Dg/d!.!13 !.6-33333333 16.6 )"!.!16 3.125 5 P)S$n



)" <K



#"#N; ) FK+; P)" 1m3/1ft3

odel 1!!! mm mm "rea 371.4 ft2 8!!+h(cDne&& !.1!4 1 (nch (n feet -14

,olumen 38.6- ft3 1!!!,olumen 1!-5.6! l(ter& 1!67

12!!Flo )rr*522 m3/h 2!!!aa(lab(l(ty -5'Factor de llenado 8!' mme&(gn Flo )rr*522 m3/h 12!!e&(gn Flo )rr*522 gpm

Parametro& #ubuperf(c(al ,eloc(ty !.7 gpm/ft2 Flujouperf(c(al ,eloc(ty 1.7!8 m3/h/m2 ey "u

ey "g "rea #alculated )rr*522 ft2 a&a "u "rea #alculated )rr*522 m2 a&a "g "pro% "rea eal 371.4 ft2 a&a Bn

a&a 9ody Feed&ub total

ol(d& part(cle& g/m3 a&a Precoata&& Flo )rr*522 g/h To$alen&(ty 1.2! g/cc,olumen )rr*522 cc/h P)#;"+,olumen )rr*522 l/d area

63.8

#ycle +(me )rr*522 day&9ody Feed

"rea calculada )rr*522 m2 &oluc(on>m3/h?Flujo m(n )rr*522 m3/h )rr*522Flujo ma% )rr*522 m3/h 2!!,eloc. (n )rr*522 m3/h/m2,eloc. a% )rr*522 m3/h/m2

"rea eal 63.8 m2Flujo m(n )rr*522 m3/hFlujo ma% )rr*522 m3/h,eloc. (n )rr*522 m3/h/m2

,eloc. a% )rr*522 m3/h/m2



!.!28316846632 mm e&pe&or

"rea )ffec.>m2? ,olumen >lt? umero placa& "rea )ffec.>m2? ,olumen >lt?!.- 15.6 45 4!.5 7!2.!

!.! !.!

1.45 24.-! 44 63.8 1!-5.6!.! !.!

2.!1 34.6! 62 124.6 2145.2!.! !.!

mm12!! Flujo 16"." m3/h

Flujo e&(gn 21!.5 m3/h ,eloc. e&(gn 1.7 m3/h/m2

)rr*522 m3/h "rea total 123.3 m2!.6 g/m3 "rea real / f(ltro )rr*522 m2

!.8 g/m3 umero F(ltro& E%%G522 un)rr*522 g/h Flujo e&(gn/ f(ltro E%%G522 m3/h)rr*522 g/h)rr*522 g/h)rr*522 g/h)rr*522 g/h

g/hE%%G522 g/h

e&pe&or olumen den&(dad ma&a t Dg l(tro&!.!!16 !.1!2!8 1.!- !.1112672 111.! 1!2.!8

Dg/m3 Dg/h Dg/d!.!13 )rr*522 E%%G522 )"!.!16 3.125 5 P)S$n



)" <K



#"#N; ) FK+; P)"

odel 8!! mm mm mm "rea 713.!!1426!!3 ft2 8!! 8!!+h(cDne&& !.1!4 1 (nch -14 -14

,olumen 74.27 ft3 1!!! 1!!!,olumen 1!24.!! l(ter& 1!67 1!67

12!! 12!!Flo 32! m3/h 1! 2!!! 2!!!aa(lab(l(ty -5'Factor de llenado 8!' mm mme&(gn Flo 421.1 m3/h 12!! 12!!e&(gn Flo 1852.6 gpm

Parametro& "ngo&turauperf(c(al ,eloc(ty !.7 gpm/ft2 Flujo 246uperf(c(al ,eloc(ty 1.7!8 m3/h/m2 ey "u !.52

ey "g 2.47 "rea #alculated 2646.6 ft2 a&a "u 127.-2 "rea #alculated 245.- m2 a&a "g 6!7.62 "pro% "rea 344.445133335 ft2 a&a Bn 735.54

a&a 9ody Feed 52!&ub total 1--1.!8

ol(d& part(cle& g/m3 a&a Precoata&& Flo 1--1 g/h To$al 11en&(ty 1.2! g/cc,olumen 165-.23333333 cc/h P)#;"+,olumen 3-.8216 l/d area e&pe&or

32.! !.!!16

#ycle +(me 24.43 day&9ody Feed

"rea calculada 245.- m2 &oluc(on>m3/h? Dg/m3Flujo m(n 32! m3/h 4! !.!13Flujo ma% 421.1 m3/h 2!! !.!16,eloc. (n 1.3! m3/h/m2,eloc. a% 1.71 m3/h/m2

"rea eal 32.! m2Flujo m(n 32! m3/hFlujo ma% 421.1 m3/h,eloc. (n 1!.!! m3/h/m2

,eloc. a% 13.16 m3/h/m2

P)S;

mm mm12!! 12!!



!.!2831685

m2 placa& "rea +otal m2 mm m3 ft2 1ft ft3!.64 5! 32.! 32.! 1.! 344.445133 !.1!4 35.87-7!14!.84 53 44.3 32.! 1.4 476.582768 !.1!4 4-.644!384

1.!! 46 46.! 32.! 1.5 4-5.13-87- !.1!4 51.577!7!71.14 55 62.6 32.! 2.! 674.!!2648 !.1!4 7!.2!86!-21.44 46 66.2 32.! 2.1 713.!!1426 !.1!4 74.27!-81-4.!! 55 22!.! 32.! 7.! 2368.!6!2- !.1!4 246.672-47

m2 placa& "rea +otal m2 mm m3 ft2 1ft ft31.44 46 66.2 32.! 2.1 713.!!1426 !.1!4 74.27!-81-

m3/h por f(ltro >2 operando?g/m3

g/m3 Placa& numero Flujo "reag/h 16! m3/h 12! m2g/h 8!! 5! 16! m3/h 32.! m2g/h -14 53 16! m3/h 44.3 m2g/h 1!!! 46 16! m3/h 46.! m2g/h 1!67 55 16! m3/h 62.6 m2g/h 12!! 46 16! m3/h 66.2 m2g/h 2!!! 55 16! m3/h 22!.! m2

olumen den&(dad ma&a t Dg l(tro&!.!512 1.!- !.!558!8 55.8 51.2 )" <K

Dg/h Dg/d!.52 12.8 )"

3.125 5 P)S$n

m2 placa& "rea +otal m2 mm m3 ft2 1ft ft31.44 56 8!.6 32.! 2.6 868.!!1736 !.1!4 -!.4168475

Parametro& pe$n

Flujo 1!! m3/h por f(ltro >2 operando?ey "u 3 g/m3



ey "g 7! g/m3a&a "u 3!! g/ha&a "g 7!!! g/ha&a Bn 73!! g/ha&a +otal 146!! g/h



1.!16!!!!1.4!57626

1.46!5!!!1.-88!8642.1!312!!6.-85!!!!

m32.1!312!!

umero f(ltro&

3.84375 52.778!2-48 32.673-13!4 31.-64326!8 21.856884!6 2!.55-!-!-1 1

m32.56!32!!



11/12/"8? San$a'o? C4leDiscusión y resultados Filtros prensa proyecto CUBA

ado un flujo de 16! m3/h y una eloc(dad &uperf(c(al de d(&eo de 17 m3/h lo& re&ultado&obten(do& para el d(men&(onam(ento de lo& f(ltro& clar(f(cadore& &on lo& &(gu(ente&. a&concentrac(one& &um(n(&trada& por el cl(ente &on del orden de "uC!6 g/m3 y "gC!8 g/m3.

)l rea +otal de f(ltrado e& 123 m2. )l t(empo total de f(ltrado e& del orden de 8! d0a& dado Guela& concentrac(one& de metale& noble& &on dema&(ado baja&.

Para el ca&o de 8!! % 8!! mm &e reGu(eren 4 f(ltro& operando en paralelo con un flujo nom(nal de4!m3/h por f(ltro. )l area calculada e& 3!7 m2 y el olumen e& de 1!24 l(tro& con un total de 5!placa&. )l t(empo del c(lclo e& 77 d0a&. a eloc(dad de d(&eo e& 17 m3/h/m2 y la real 125m3/h/m2. )l factor de llenado e& de 8!' y la d(&pon(b(l(dad de -5'.

Para el ca&o de 1!!! % 1!!! mm &e reGu(eren 3 f(ltro& operando en paralelo con un flujo nom(nalde 54m3/h por f(ltro. )l area calculada e& 41 m2 y el olumen e& de 14!8 l(tro& con un total de 44placa&. )l t(empo del c(lclo e& 8! d0a&. a eloc(dad de d(&eo e& 17 m3/h/m2 y la real 121

m3/h/m2. )l factor de llenado e& de 8!' y la d(&pon(b(l(dad de -5'.

Para el ca&o de 12!! % 12!! mm &e reGu(eren 2 f(ltro& operando en paralelo con un flujo nom(nalde 8!m3/h por f(ltro. )l area calculada e& 615 m2 y el olumen e& de 212! l(tro& con un total de46 placa&. )l t(empo del c(lclo e& 8! d0a&. a eloc(dad de d(&eo e& 17 m3/h/m2 y la real 121m3/h/m2. )l factor de llenado e& de 8!' y la d(&pon(b(l(dad de -5'.



#"#N; ) FK+; P)"

odel 2!!! % 2!!! % 48 mm mm "rea 2!66.67!8!!!1 ft2 8!! 8!!+h(cDne&& !.1!4 1 (nch -14 -14

,olumen 215.28 ft3 1!!! 1!!!,olumen 6144.!! l(ter& 1!67 1!67

num 12!! 12!!Flo 246 m3/h 13 2!!! 2!!!aa(lab(l(ty -5'Factor de llenado 8!' mm mme&(gn Flo 323.7 m3/h 12!! 12!!e&(gn Flo 1424.2 gpm

Parametro& #ubauperf(c(al ,eloc(ty !.7 gpm/ft2 Flujo 246uperf(c(al ,eloc(ty 1.7!8 m3/h/m2 ey "u !.52

ey "g 2.47 "rea #alculated 2!34.6 ft2 a&a "u 127.-2 "rea #alculated 18-.! m2 a&a "g 6!7.62 "pro% "rea 28-.333-12!!1 ft2 a&a Bn 735.54

a&a 9ody Feed 41--&ub total 567!.!8

ol(d& part(cle& g/m3 a&a Precoata&& Flo 567! g/h To$al 56"en&(ty 1.2! g/cc,olumen 4725.!6666667 cc/h P)#;"+,olumen 113.4!16 l/d area e&pe&or

18-.! !.!!16

#ycle +(me 51.51 day&9ody Feed&oluc(on>m3/h? Dg/m3

323.! !.!132!! !.!16

P)S;

mm mm12!! 12!!



!.!2831685

m2 placa& "rea +otal m2 mm m3 ft2 1ft ft3!.64 42 26.- 32.! !.- 28-.333-12 !.1!4 3!.138-4-2!.84 55 45.- 32.! 1.5 4-4.567!24 !.1!4 51.5173-83

1.!! 46 46.! 32.! 1.5 4-5.13-87- !.1!4 51.577!7!71.14 55 62.6 32.! 2.! 674.!!2648 !.1!4 7!.2!86!-21.44 46 66.2 32.! 2.1 713.!!1426 !.1!4 74.27!-81-4.!! 48 1-2.! 32.! 6.1 2!66.67!8 !.1!4 215.2782!8

m2 placa& "rea +otal m2 mm m3 ft2 1ft ft31.44 46 66.2 32.! 2.1 713.!!1426 !.1!4 74.27!-81-

m3/h por f(ltro >2 operando? Flujo numero Flujog/m3 32!! 13 246.153846

g/m3g/hg/hg/hg/hg/hg/hg/h

olumen den&(dad ma&a t Dg l(tro&!.3!243!82- 1.!- !.32-64-6!31 !2.6 3!2.43 )" <K

Dg/h Dg/d4.1-- 1"".8 )"3.125 5 P)S$n

m2 placa& "rea +otal m2 mm m3 ft2 1ft ft31.44 56 8!.6 32.! 2.6 868.!!1736 !.1!4 -!.4168475

Parametro& pe$n

Flujo 1!! m3/h por f(ltro >2 operando?ey "u 3 g/m3



ey "g 7! g/m3a&a "u 3!! g/ha&a "g 7!!! g/ha&a Bn 73!! g/ha&a +otal 146!! g/h



!.85344!!1.45881!3

1.46!5!!!1.-88!8642.1!312!!6.!-6!!!!

m32.1!312!!

m32.56!32!!



""Flo #arb$n 12!!! Dg/h Flo #arb$n 12!!! Dg/hFlo =ater 12!!! Dg/h Flo =ater 12!!! Dg/h

atente "gua -72- cal/mol atente "gua 38.6 9+N/mol

atente "gua 54!.5 cal/g atente "gua 2.14 9+N/gatente 6486!!! Mg/hT#al/g atente 25738.1 Mg/hT9+N/g

6486!!! Mcal/h 25738.1 M9+N/h18!2 Dcal/& 7543 M=7531 MU/&7531 M= M=

+emperature a% 373 @M +emperature a% 373 @M+emperature (n 273 @M +emperature (n 273 @M#P "gua 1 cal/>g @M? #P "gua 1 cal/>g @M?#alor en&(ble m #P + #alor en&(ble m #P +

12!!!!! Dg/hTcal/>g@M?T@M 12!!!!! Dg/hTcal/>g@M?T@M

12!!!!! Dcal/h 12!!!!! Dcal/h333 Dcal/& 333 Dcal/&

13-3 MU/& 13-3 MU/&13-3 M= 13-3 M=

#p #arb$n cuaderno #p #arb$n cuaderno#alor #arb$n 1!6.8 D= #alor #arb$n 1!6.8 D=

Mcal/h D Mcal/h D1!!! 1.161 1!!! 1.161

Flo #arb$n 264!!Flo =ater 264!!

#P>t?

+emperature

T#pT+



3.412155!74235- 6-1.351-312

Mbtu/h D



+orre de de&a(reac($n

Flujo 6-!! m3/h 3!36! gpmnumero 3 unFlujo/l(nea 23!! m3/h 1!12! gpm

,eloc(d upe. 1!2.48 m3/h/m2 42 gpm/ft2

Cálculos Generales Horno y Otros

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