balance_flot_corccohuayco block caving - ley dic11

7/21/2019 Balance_Flot_Corccohuayco Block Caving - Ley Dic11

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DIAGRAMA FLOTACIÓN

1ª Limpieza

RELAVE2 LIMPIEZAda

REMOLIENDA

CONCENTRADO 1RA

LIMPIEZA

RELAV

1 RA LIMPIE

CONCE

RO

OVERFLOW HIDROCICLONESMOLIENDA SECUNDARIA

2ª Limpieza

CONCENTRADO 2DA

LIMPIEZA



DIA

OVERFLOW HIDROCIMOLIENDA SECUN

UNDERFLOW

MOLIENDA

OVERFLOWMOLIENDA

ALIMENTACIÓNMOLINO SAG

REMOLIE$%A 2 &e(m)ll; 1*25" +,

!I%RO-I-L.$2 /a(e)as de 0 !c)clones

MOLI$O A3#' 17'; 1"*7"" 4

MOLI$O /OLA2#' #"'; 13*1"" 4



RELAVE AESPESAMIENTO

DOR

RELAVE3 LIMPIEZA

CONCENTRADO Cu-M

RELAVESCAVENGER

LIMPIEZA

-A&E$ER# celdas; 257 m3

PIEZA ; 12'x36'



CASE 3-A & 3-B - UNDERGROUND

CASE 3-A & 3-B - UNDERGROUND

AREA 31""PRIMARY CRUSHER

& STOCK PILE

O- PILE#0*""" OAL -APA-I O$$E

5

1

PRIMAR -RU!ER5"8 658; 375 4

O&ERLA$% -O$&EOR

9$o(e 1:

RO-/REAER



RE-GRINDING 2 &e()m)ll; 1*25" +,

--LO$E -LUER2 -lus(es o 0 %15 92 s*<=:

ROU!ER7 cells o 3"" m3

1 l)ne 1>2>2>2

1s( -LEA$ER6 cells o 2"" m3

1 l)ne 2>2>2

2nd -LEA$# cells o 11 l)ne 2>

21

11

12

13

14

10AR

?LOAIO$



INE - 24 KTPD - NEW PLANT LOCATED AT COROCCOHUAYCO OR ANTAPACCA

INE - 24 KTPD - NEW PLANT LOCATED AT COROCCOHUAYCO OR ANTAPACCA

A MILL3#' 17' ; 1"*7"" 4

/ALL MILL2#' #"' ; 13*1"" 4

2 PE//LE -RU!ER!P #""'; 20# 4

AREA 32""RI$%I$ A$% PE//LE

-RU!I$

1 -LUER O?13 %3" --LO$E 92 */:

10

2

3

4

6

7

89

$OE@

1> $E4 -RU!ER ALER$AI&E@ MA /E UE

2 &I/RAI$ -REE$91 */:

IM/OL A$% $OME$-LAURE

$ORMAL OPERAIO$ E&E$UAL OPERAIO$ -O$I$UAIO$ O? -URRE$ ?LO4 ?LO4 $UM/ER-

!OPPER

?LOA



3d -LEA$ER columns; 3*7 m; 11m

-A&E$ER# cells o 16" m3

1 l)ne 2>2

CONC

WASH WATER

-O$-E$RAE !I-E$ER%)ame(e@ 32 m

AILI$!I-E$ER

%)ame(e@ #5 m

PRE ?ILER2 o 126 m2

16

17

18

192223

24

26

15

27

28

29

M40092-3000-110-PFD-0009

RI$%I$ Ta! "o T#$%&''(

F!")a"&

-O$-E$





M40092-3000-110-PFD-0010

W

% -RU!ER I$ I$AA 5#8 758

IO$ ?EE% /O

RE-GRINDING

2 &e()m)ll; 1*25" +,

--LO$E -LUER2 -lus(es o 0 %15 92

AREA 31""PRIMARY CRUS

& STOCK PIL

10

PRIMAR -RU5"8 658; 375

O&ERLA$% -

9$o(e 1:



AREA 3#""NTRATE THICKENINGAND FILTERING

AREA 37""TAILING STORAGE

FACILITY

25

30

31

R&$o*&)&d +a"&) "o ,)o$&

R&$o*&)&d +a"&) "o ,)o$&

R&$o*&)&d +a"&) "o ,)o$&

AREA 36""RAE ORAE A$% %IPA-!



CASE 3-A - UNDERGROUND MINE - 24 KTPD - NEW PLANT LOCATE

A MILL3#' 17' ; 1"*7"" 4

s*<=:

ERE

2 PE//LE -RU!ER!P #""'; 20# 4

AREARI$%I$

-RU

ROU!ER7 cells o 3"" m3

1 l)ne 1>2>2>2

-A&E$ER# cells o 16" m3

1 l)ne 2>2

1s( -LEA$ER 3

1

16

17

11

12

13

14

15

2

3

4

5

6

7

1

AREA 33""?LOAIO$ A$% RE>RI$%I$

ER4

O$&EOR

2 &I/RAI$ -REE$91 */:

!OPPER

RO-/REAER

O- PILE#0*""" O$$E OAL -APA-I



3d -LEA$ER2 columns; 3*7 m; 11m

1 l)ne 2>2>2

2nd -LEA$ER

# cells o 16" m3

1 l)ne 2>2

19

20

21

23





D AT COROCCOHUAYCO

/ALL MILL2#' #"' ; 13*1"" 4

32"" $% PE//LE

!I$

AREA 3#""

AREA 37""TAILING STORAGE

FACILITY

1 -LUER O?3 %3" --LO$E 92 */:

-O$-E$RAE !I-E$ER%)ame(e@ 32 m

AILI$!I-E$ER

%)ame(e@ #5 m

18

10

89

28

29

30

31

Ta! "o T#$%&''(

R&$o*&)&d +a"&) "o ,)o$&

R&$o*&)&d +a"&) "o ,)o$&

W

?LOAIO$ ?EE% /O



CONCENTRATE THICKENING

AND FILTERING

WASH WATER

PRE ?ILER2 o 126 m2

24

25

26

27

R&$o*&)&d +a"&) "o ,)o$&

F!")a"&

AREA 36""-O$-E$RAE ORAE A$% %IPA-!

$OE@

1> $E4 -RU!ER ALER$AI&E@ I$AA 5#8 758 -RU!ER -OUL% /E UE%



CASE 3-C -

CASE 3-C -

PRIMAR -RU!ER5"8 658; 375 4

AREA 31""PRIMAR -RU!ER

O- PILEO- PILE

#0B""" OAL -APA-I O$$E

9$o(e 2:9$o(e 1:

RO-/REAER



?LROU!ER 9$eC:7 cells o 3"" m3

1 L)ne 1>2>2>2

RE-GRINDING (modifed) 2 &e()m)ll; 1B25" +, 9neC: 1 &e()m)ll; 2"" +, 9Ex)s()nD:

--LO$E -LUER2 o 0 %15 c=clones 92 s*<=: 9$eC:1 o 0 %1" c=clones 9Ex)s()nD:

16

23

12

13

15

2nd -LE# cells o

1 cell 1



NDERGROUND MINE - 24 KTPD - EXPANDED PLANT LOCATED AT TINTAYA

NDERGROUND MINE - 24 KTPD - EXPANDED PLANT LOCATED AT TINTAYA

/ALL MILL 9$eC:2"' 3"' ; 6*6"" 4

AREA 32""-RU!I$ A$%

RI$%I$

1 -LUER O?0 %26 --LO$ 92 */:

EII$ -LUER3 /ALL MILL

9Ex)s()nD:

O- PILE?I$E

-RU!ER 3°9Mod))ed:

2

3

4

57

8

9

1

1

$OE@

1> -A$ /E2> 2 /A$A3> 1 -RU!#> /A$A$A5> 2 MO

1 -RU6> 2 LER

1 LER

-RU!ER 2°9Mod))ed:

9$o(e 3:

9$o(e #:

9$o(e 5:

9$o(e 6:



!OPPER



Ta! "o T#$#&''(REA 33"" A$% RE>RI$%I$

-A&E$ER 9Mod))ed:5 cells o 1"3 m3 9Ex)s()nD:

1 cell o 13" m3 9$eC:1 l)ne 2>2>2

ER 9$eC: 2"" m3

>2>2

-

-O$-E$R

Wa# +a"&)

-O$-E$RAE !I-E$ER 9Ex)s(%)ame(e 3" m

3d -LEA$ER 9Mod))ed:# columns; 2*5 m ; 12 m 9Ex)s()nD:

1 columns; 2*5 m ; 12 m 9$eC:

17

18

19

20

21

2224

25

26

28

29

30

M40092-3000-110-PFD-0011

ed:)nD::

PRE ?ILER# o 32 m2 9Ex)s()nD:1 o 12# m2 9$eC:


$ORMAL OPERAIO$ E&E$UAL OPERAIO$ -O$I$UAIO$ O? -URRE$ ?LO4

?LO4 $UM/ER-



10

11

6

12

M40092-3000-110-PFD-0012

W

UE% -RU!ER O? 5#8 758 EII$ I$ I$AAA -REE$ 1"' 2#' 9EII$:ER RAPOR L11"" 9EII$:-REE$ 12' 27' 9$E4:

-RU!ER 7' ! 9EII$:;ER RAPOR L 6""! 9$E4:-REE$ 7' 2"' 9EII$:;-REE$ 7' 2"' 9EII$; RE>LO-AE%:

?LOAIO$ ?EE% /O



AREA 3#""$RAE !I-E$I$ A$%

?ILERI$

AREA 37""$ ORAE ?A-ILI

REA 36"" ORAE A$% %IPA-!

")a"&

R&$o*&)&d +a"&) "o ,)o$&

ILI$ !I-E$ER 9Ex)s()nD:%)ame(e 76 m

7

31

32

33

R&$o*&)&d +a"&) "o ,)o$&

R&$o*&)&d +a"&) "o ,)o$&



CASE 3-C - UNDERGROUND MI

PRIMAR -RU!ER5"8 658; 375 4

AREA 33""?LOAIO$ A$% RE>RI$%I$ROU!ER 9$eC:

7 cells o 3"" m3

1 L)ne 1>2>2>2

1s( -LEA$ER 9$eC:6 cells o 2"" m3

1 l)ne 2>2>2

RE-GRINDING (modifed) 2 &e()m)ll; 1B25" +, 9neC: 1 &e()m)ll; 2"" +, 9Ex)s()nD:

--LO$E -LUER2 o 7 %15 c=clones 92 s*<=: 9$eC:1 o 0 %1" c=clones 9Ex)s()nD:

16 18

12

13

14

15

AREA 31""PRIMAR -RU!ER

O- PILE

-RU!ER 2°9Mod))ed:

9$o(e 3:

9$o(e #: 9$o(

9$o(e 2:9$o(e 1:

RO-/REAER

O- PILE#0B""" O$$E OAL -APA-I



3d -L# columns; 2

2

23

2nd -LEA$ER 9Mod))ed:# cells o 13" m3 9Ex)s()nD:

1 cell o 16" m3 9$eC:1 L)ne 1>2>2


$ORMAL OPERAIO$ E&E$UAL OPERAIO$ -O$I$UAIO$ O? -URRE$ ?LO4 $UM/ER-



NE - 24 KTPD - EXPANDED PLANT LOCATED AT TINTAYA

Ta! "o T#$#&''(

/ALL MILL 9$eC:2"' 3"' ; 6*6"" 4

AREA 32""-RU!I$ A$%

RI$%I$

-A&E$ER 9Mod))ed:5 cells o 1"3 m3 9Ex)s()nD:

1 cell o 1"3 m3 9$eC:1 l)ne 2>2>2

AREA 37""AILI$ ORAE ?A-ILI

R&$o*&)&d +a"&)

1 -LUER O?0 %26 --LO$E 92 */:

-O$-E$RAE !I-E$ER 9Ex)s()nD:

2 AILI$ !I-E$ER 9Ex)s()nD:%)ame(e 76 m

EII$ -LUER3 /ALL MILL

9Ex)s()nD:

-RU!ER 3°9Mod))ed:

19

20

10

11

2

3

4

5

6

7

8

9

1

1

30

31

9$o(e 5:

6:

!OPPER

?I$E OREO- PILE



AREA 3#""-O$-E$RAE !I-E

?ILERI$

AREA 36""-O$-E$RAE ORAE A$% %

Wa# +a"&)

F!")a"&

ame e m

()nD:9Ex)s()nD:

17

21

24

25

26

27

28

29

R&$o*&)&

PRE ?ILER# o 32 m2 9Ex)s()nD:1 o 11# m2 9$eC:

$OE@

1> EII$ 5#8 758 -RU!ER A 2> 2 /A$A$A -REE$ 1"' 2#' 9EI3> 1 -RU!ER RAPOR L11"" 9EII#> /A$A$A -REE$ 12' 27' 9$E4:5> 2 MO$ -RU!ER 7' ! 9EI

1 -RU!ER RAPOR L 6""! 9$E46> 2 LER -REE$ 7' 2"' 9EII$

1 LER -REE$ 7' 2"' 9EII$



"o ,)o$&

12

32

33

R&$o*&)&d +a"&) "o ,)o$&

W

?LOAIO$ ?EE% /O



$%

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"o ,)o$&

OUL% /E UE%

-AE%:



BALANCE DE MASA, LEYES Y FINOS FLOTACIÓN R Cu Ley CuT!"#$%" N'!$#, ()*+ 24, FACTOR DE DISEO ./2 GLO!"L #$%&' (2%)0'U('#'0$1'!, 2 C*ectiva #$%&' (2%)0'L"5 A#'"!($1'! C6, ./4 +,rmedi pryect ,*an -iner.uni 2011 -*y 100%00' 0%0'

./78 +-im ,*an -iner LO- 0%00 tpd cnc -NOMINAL DIARIO

E($*$

A#'"!($1'! C!1"!(9$+ R"#$:" R"16*"9

T!"#$%" L"5 C6 F'!) T!"#$%" L"5 C6 F'!) T!"#$%" L"5 C6 F'!) M"(

(<+ (<+ (<+ (<+ (<+ (<+

G#=$# C6, C#"1(':$ 24, ./4 24> 7? 32/? 222 23,32. /.. 27 >/4

R6@"9 2&3000 1%0& 2&# (362$ 6%& 2(2 203()1 0%0# 16 3/8

R"#'"!+$ 432$1 4%(( 2#2

)3$)0 4%($ &(0 43020 #%& &1$ )3462 0%$( )0 $)%61

.9$ L'*'"0$ )3$)0 4%($ &(0 (3(4# 11%0 (6$ &3612 1%(0 60 #6%00

S1$:"!@"9 &3612 1%(0 60 13662 (%0 40 23$40 0%(4 10 #2%$0

2+$ L'*'"0$ &3606 1(%2& 610 13$2) 2&%0 &62 236#0 4%40 1&) )4%#2

3$ L'*'"0$ 13$2) 2&%00 &62 6)$ (2%) 222 132&# 1$%2) 2&0 4>/2() )& 130&4

2# 6(BALANCE CONDICIÓN INSTANTANEA 2 UTILIACIÓN

E($*$A#'"!($1'! C!1"!(9$+ R"#$:" R"16*"9

T!"#$%" L"5 C6 F'!) T!"#$%" L"5 C6 F'!) T!"#$%" L"5 C6 F'!) M"((< (< (< (< (< (<

G#=$# C6, C#"1(':$ .,>? ./4 .. 3/?4 32/? . .,87 /.. . >/4

R6@"9 130#) 1%0& 11 16& 6%& 11 $2( 0%0# 1 $&

R"#'"!+$ 2&0 4%(( 1(

(61 4%($ 1$ 22) #%& 1$ (&2 0%$( ( $#

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S1$:"!@"9 20$ 1%(0 ( )4 (%0 2 1(& 0%(4 0 #(

2+$ L'*'"0$ 20$ 1(%2& 2# #) 2&%0 21 121 4%40 ) )6

3$ L'*'"0$ #) 2&%00 21 (1 (2%) 10 4) 1$%2) 11 &#

BALANCE CONDICIÓN DISEO FACTOR2

E($*$A#'"!($1'! C!1"!(9$+ R"#$:" R"16*"9

T!"#$%" L"5 C6 F'!) T!"#$%" L"5 C6 F'!) T!"#$%" L"5 C6 F'!) M"((< (< (< (< (< (<

G#=$# C6, C#"1(':$ .,34 ./4 .4 37/ 32/? .2 .,27? /.. . >/4

R6@"9 13(0& 1%0& 1& 1$) 6%& 1( 1310) 0%0# 1 $&

R"#'"!+$ 2## 4%(( 14

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S1$:"!@"9 241 1%(1 ( $1 (%0 ( 160 0%(4 1 #(

2+$ L'*'"0$ 241 1(%2( (( 104 2&%0 24 1&) 4%4& # )6

3$ L'*'"0$ 104 2&%00 24 () (2%) 12 6# 1$%2) 1( &#

.9$ L'*'"0$-S1$:"!@"9

.9$ L'*'"0$-S1$:"!@"9

.9$ L'*'"0$-S1$:"!@"9



BALANCE DE MASA, LEYES Y FINOS FLOTACIÓN R Cu Ley CuT!"#$%" N'!$#, ()*+ 24, FACTOR DE DISEO ./2 GLO!"L #$%&' (2%)'U('#'0$1'!, 2 C*ectiva #$%&' (2%)0'L"5 A#'"!($1'! C6, ./4 +,rmedi pryect ,*an -iner.uni 2011 -*y 100%00' 0%0'

./78 +-im ,*an -iner LO- 0%00 tpd cnc -NOMINAL DIARIO

E($*$

A#'"!($1'! C!1"!(9$+ R"#$:" R"16*

T!"#$%" L"5 C6 F'!) T!"#$%" L"5 C6 F'!) T!"#$%" L"5 C6 F'!) M"(

(<+ (<+ (<+ (<+ (<+ (<+

G#=$# C6, C#"1(':$ 24, ./4 24> 7? 32/? 222 23,32. /.. 27 >/4

R6@"9 2&3000 1%0& 2&# (362$ 6%& 2(2 203()1 0%0# 16 $&

R"#'"!+$ 432$1 4%(( 2#2

)3$)0 4%($ &(0 43020 #%& &1$ )3462 0%$( )0 $#

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S1$:"!@"9 &3612 1%(0 60 13662 (%0 40 23$40 0%(4 10 #(

2+$ L'*'"0$ &3606 1(%2& 610 13$2) 2&%0 &62 236#0 4%40 1&) )6

3$ L'*'"0$ 13$2) 2&%00 &62 6)$ (2%) 222 132&# 1$%2) 2&0 &#

BALANCE CONDICIÓN INSTANTANEA 2 UTILIACIÓN ESCENARIO A TONELAE NOMINAL LEY MXIMA

E($*$A#'"!($1'! C!1"!(9$+ R"#$:" R"16*

T!"#$%" L"5 C6 F'!) T!"#$%" L"5 C6 F'!) T!"#$%" L"5 C6 F'!) M"((< (< (< (< (< (<

G#=$# C6, C#"1(':$ 130#) 1%64 1# &$%0 (2%) 16 130(# 0%1# 2 #$%&

R6@"9 130#) 1%64 1# 262 6%& 1) #24 0%1& 1 $&

R"#'"!+$ (#2 4%(( 20

4)4 4%($ (1 (62 #%& (0 4&6 0%$( 4 $#

.9$ L'*'"0$ 4)4 4%($ (1 2&2 11%0 2) ((( 1%(0 & #6

S1$:"!@"9 ((( 1%(0 & 120 (%0 & 21( 0%(4 1 #(

2+$ L'*'"0$ ((( 1(%2& && 1($ 2&%0 (( 1$( 4%40 11 )6

3$ L'*'"0$ 1($ 2&%00 (( &$ (2%) 16 $0 1$%2) 1) &#

1%4$BALANCE CONDICIÓN DISEO FACTOR2 ESCENARIO B TONELAE DISEO LEY 8 AOS

E($*$A#'"!($1'! C!1"!(9$+ R"#$:" R"16*

T!"#$%" L"5 C6 F'!) T!"#$%" L"5 C6 F'!) T!"#$%" L"5 C6 F'!) M"((< (< (< (< (< (<

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R6@"9 13(0& 1%0& 1& 1$) 6%& 1( 1310) 0%0# 1 $&

R"#'"!+$ 2## 4%(( 14

&(( 4%($ 2( 2)( #%& 2( &11 0%$( & $#

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S1$:"!@"9 241 1%(0 ( $0 (%0 ( 160 0%(4 1 #(

2+$ L'*'"0$ 240 1(%2& (( 104 2&%0 24 1&6 4%40 # )6

3$ L'*'"0$ 104 2&%00 24 () (2%) 12 6# 1$%2) 1( &#

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.9$ L'*'"0$-S1$:"!@"9

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FLUJO NUMERO 10 10A 12 11 11' (11)

NOMINAL NA 220 NA

SOLI DOS t / h 1,000 500 849 151 151 551

AGUA 2,125 1,063 1,775 350 389 39 19 1,024

PULPA t / h 3,125 1,563 2,624 501 540 1,575

PULPA 2,486 1,243 2,086 400 439 1,210

INSTANTANEO 240 300

SOLIDOS t / h 1,087 543 923 164 164 599

AGUA 2,310 1,155 1,929 380 423 42 21 1,113

PULPA t / h 3,397 1,698 2,852 545 587 1,712

PULPA 2,702 1,351 2,267 435 477 1,315

DISEÑO

SOLI DOS t / h 1,304 652 1,107 197 197 719

AGUA 2,772 1,386 2,315 456 507 51 25 1,335

PULPA t / h 4,076 2,038 3,422 654 704 2,054

PULPA 3,243 1,621 2,720 522 573 1,578

OTROS

GE SOLIDO 2.77 2.77 2.73 3.00 3.00 2.95

DENSIDAD DEL LIQUIDO 1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.00

DENSI DAD DE PULPA 1.26 1.26 1.26 1.25 1.23 1.30

PO!EN"A#E DE SOLIDO $ 32.0 32.0 32.3 30.2 28.0 35.0

LE% !&" $ 1.04 1.04 0.08 6.4 6.4 5.3

U"ILIA!ION $ 92 92 92 92 92 92 92 92 A!"O DE DISEO $ 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2

*3 / h

*3 / h

*3 / h

*3 / h

*3 / h

*3 / h

t / *3

t / *3

A L I +

E N " A

! I ,

N

L O " A

! I , N

O U G - E

A L I +

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! I , N

L O " A

! I , N

O U G - E

( P . L 0 1

3 )

E L A

4 E

O U G - E

! O N ! E N " A D O

O U G - E

S I N

D I L U

I

! O N ! E N " A D O

O U G - E

D I L U

I D O

A G U A

A

! O N ! E N " A D O

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A G U A

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( P . L 5 1

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N

! I ! L O

N E S

E + O L I E

N D A



14 14A 16 (15) (15A) 15 15' 18 17 (17)

NA

165 332 332 192 140 140 123 69

135 1,190 1,190 831 19 9 359 378 568 263 13.8

301 1,522 1,522 1,023 499 518 691 332

191 1,301 1,301 899 402 420 612 287

1,798 361 1,294

180 361 361 209 152 152 134 75

147 1,294 1,294 903 21 10 391 411 617 286 15.1

327 1,655 1,655 1,112 543 563 751 361

208 1,414 1,414 977 436 457 665 312

1,954

216 433 433 251 183 183 160 90

176 1,552 1,552 1,084 25 12 469 493 740 343 18.1

392 1,986 1,986 1,334 651 676 901 434

249 1,696 1,696 1,173 524 548 798 375

2.95 3.01 3.01 2.82 3.32 3.32 2.79 2.86

1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.00

1.57 1.17 1.17 1.14 1.24 1.23 1.13 1.16

55.0 21.8 21.8 18.8 28.0 27.0 17.8 20.8

5.3 5.4 5.4 1.3 11.0 11.0 0.35 3.0

92 92 92 92 92 92 92 92 92 92 92 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2

S ! A G A

+ O L I N

O

E + O L I E

N D A

( P .

E

8 & 0 9

. )

A L I +

E N " A

! I O

N

P I +

E A

L I + P I E ' A

A L I +

E N " A

! I O

N

P I +

E A

L I + P I E ' A

( P . : 5 1

3 )

E L A

4 E

P I +

E A

L I + P I E ' A

A G U A

A

! O N ! E N " A D O

P I +

E A

L I + P I E ' A

" O " A

L

A G U A

A

! O N ! E N " A D O

P I +

E A

L I + P I E ' A

( P . : 5 1

3 )

! O N ! E N " A D O

P I +

E A

L I + P I E ' A

S I N

D I L U

I

! O N ! E N " A D O

P I +

E A

L I + P I E ' A

D I L U

I D O

E L A

4 E

S ! A 4 E N G E

! O N ! E N " A D O

S ! A 4 E N G E

S I N

D I L U

I

A G U A

A

! O N ! E N " A D O

S ! A 4 E N G E



21 20A 20 28 22 23 (2

112 40 80 972 28 52

435 144 288 2,343 55 110 100 326 1

547 184 369 3,314 129 378

471 154 309 2,697 107 340

121 44 87 1,056 31 57

473 157 313 2,546 60 120 109 354 1

595 200 401 3,603 140 410

512 168 336 2,932 116 369

225.786637

146 52 105 1,267 37 68

568 188 376 3,056 72 144 131 425 1

713 240 481 4,323 168 492

615 201 403 3,518 139 443

3.12 3.89 3.9 2.74 4.5 3.64

1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.

1.16 1.19 1.19 1.23 1.21 1.11

20.4 21.8 21.8 29.3 22.0 13.8

5.5 24.0 24.0 0.11 32.7 19.3

92 92 92 92 92 92 92 92 91.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1

E L A

4 E

S E G U N D A

L I + P I E ' A

A L I +

E N " A

! I ,

N

! O L U

+ N A S

" E ! E A

L I + P I E ' A

( P .

E

8 & 0 9

. )

A L I +

E N " A

! I ,

N

! O L U

+ N A S

" E ! E A

L

I + P I E ' A

E L A

4 E

" O " A

L A

E S P E S A + I E N " O

A G U A

L A 4 A D O

E S P U + A

" E ! E A

L I + P I E ' A

( P .

E 8 & 0 9

. )

A G U A

L A 4 A D O

E S P U + A

" E ! E A

L I + P I E ' A

! O N ! E N " A D O

! O L E

! " I 4

O !

& ; + .

E L A

4 E

! O L U

+ N A S

" E ! E A

L I + P I E

' A

A G U A

D I L U

! I ,

N

! O N ! E



FLUJO NUMERO 10 11 12 13 14 15 16 17

NOMINAL

SOLI DOS t / h 1,000 151 849 220 332 140 192 69

AGUA *3 / h 2,125 350 1,775 753 1,190 359 831 263

PULPA t / h 3,125 501 2,624 973 1,522 499 1,023 332

PULPA *3 / h 2,486 400 2,086 828 1,301 402 899 287

INSTANTANEO

SOLIDOS t / h 1,087 164 923 240 361 152 209 75

AGUA *3 / h 2,310 380 1,929 818 1,294 391 903 286

PULPA t / h 3,397 545 2,852 1,058 1,655 543 1,112 361

PULPA *3 / h 2,702 435 2,267 900 1,414 436 977 312

DISEÑO

SOLI DOS t / h 1,304 262 1,471 382 575 242 333 120

AGUA *3 / h 2,772 606 3,076 1,305 2,062 623 1,440 456

PULPA t / h 4,076 868 4,547 1,687 2,638 865 1,773 576

PULPA *3 / h 3,243 694 3,614 1,434 2,254 696 1,558 498

OTROS

GE SOLIDO 2.77 3.00 2.73 2.95 3.01 3.32 2.82 2.86

DENSIDAD DEL LIQUIDO t / *3 1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.00

DENSI DAD DE PULPA t / *3 1.26 1.25 1.26 1.18 1.17 1.24 1.14 1.16

PO!EN"A#E DE SOLIDO $ 32.0 30.2 32.3 22.6 21.8 28.0 18.8 20.8

LE% !&" $ 1.04 6.4 0.08 5.3 5.4 11.0 1.3 3.0


A L I +

E N " A

! I ,

N

L O " A

! I ,

N

O U G - E

! O N ! E N " A D O

O U G - E

S I N

D I L U

I

E L A

4 E

O U G - E

O 4 E L O

7

! I ! L O

N E S

E + O L I E

N D A

A L I +

E N " A

! I O

N

P I +

E A

L I + P I E ' A

! O N ! E N " A D O

P I +

E A

L I + P I E ' A

S I N

D I L U

I

E L A

4 E

P I +

E A

L I + P I E ' A

! O N ! E N " A D O

S ! A 4 E N G E

S I N

D I L U

I



23 24 25 26 27 29 30 31 24A

52 28 28 972 14

326 19 97 3 16 675 1,667 203 9

378 47 31 1,647 24

340 25 9 1,030 13

57 31 31 1,056 15

354 20 106 3 17 734 1,812 220 10

410 51 34 1,790 26

369 27 10 1,119 14

90 49 49 1,267 18

564 33 169 5 28 881 2,175 264 12

654 82 54 2,148 31

589 44 16 1,343 16

3.64 4.45 4.45 2.74 4.45

1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.00

1.11 1.87 3.40 1.60 1.87

13.8 60.0 91.0 59.0 60.0

19.3 32.7 32.7 0.1 32.7

92 92 92 92 92 92 92 92 92 1.6 1.6 1.6 1.6 1.6 1.2 1.2 1.2 1.2

EL A 4 E

! O L U

+ N A S

" E ! E A

L I + P I E

' A

U N D E L O

7

E S P E S A D O

D E

! O N ! E N " A D O

A G U A

E ! U P E A D A

E S P E S A D O

D E

! O N ! E N " A D O

! O N ! E N " A D O

I L " A D O

A G U A

I L " A D A

A

E S P E S A D O

D E

! O N ! E N " A D O

U N D E L O

7

E S P E S A D O

D E

E L A

4 E S

A G U A

E ! U P E A D A

E S P E S A D O

D E

E L A

4 E S

E ! U P E A ! I ,

N

A G U A

P E S A

D E

E L A

4 E S

A L I +

E N " A

! I O N

I L " O S

( P . 8

& 0 9

. )



20A 20 28 0 0 (2

40 80 972 0 0

144 288 2,343 55 110 1

184 369 3,314 0 0

154 309 2,697 0 0

44 87 1,056 0 0

157 313 2,546 60 120 1

200 401 3,603 0 0

168 336 2,932 0 0

52 105 1,267 0 0

188 376 3,056 72 144 1

240 481 4,323 0 0

201 403 3,518 0 0

3.89 3.9 2.74 0.00 0.00 0.

1.00 1.00 1.00 1.00 1.00 1.

1.19 1.19 1.23 0.00 0.00 0.

21.8 21.8 29.3 0.0000 0.0000 0.0

24.0 24.0 0.11 0.00 0.00 0.

92 92 92 92 92 91.2 1.2 1.2 1.2 1.2 1

A L I +

E N " A

! I ,

N

! O L U

+ N A S

" E ! E A

L I + P I E ' A

( P .

E

8 & 0 9

. )

A L I +

E N " A

! I ,

N

! O L U

+ N A S

" E ! E A

L

I + P I E ' A

E L A

4 E

" O " A

L A


A G U A

L A 4 A D O

E S P U + A

" E ! E A

L I + P I E ' A

( P .

E 8 & 0 9

. )

A G U A

L A 4 A D O

E S P U + A

" E ! E A

L I + P I E ' A

A G U A

D I L U

! I ,

N

! O N ! E



BALANCE FLOTACIÓN ROUGHER Y REMOLIENDA 2.>8-23-..-PFD-.4

FLUJO NUMERO 21 31 31A 32 33 34 35 36 37

NOMINAL

SOLI DOS t / h 500 1,000 500 849 151 276 22

AGUA 1,063 2,125 1,063 1,775 389 19 512 79 75

PULPA 1,243 2,486 1,243 2,086 439 605 82INSTANTANEO

SOLIDOS t / h 543 1,087 543 923 164 300 24

AGUA 1,155 2,310 1,155 1,929 423 21 556 86 81

PULPA 1,351 2,702 1,351 2,267 477 658 90

DISEÑO

SOLI DOS t / h 652 1,304 652 1,107 197 359 28

AGUA 1,386 2,772 1,386 2,315 507 25 668 103 98

PULPA 1,621 3,243 1,621 2,720 573 789 1,0

OTROS

GE SOLIDO 2.77 2.77 2.77 2.73 3.00 2.95 2.9

DENSIDAD DEL LIQUIDO 1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.0DENSI DAD DE PULPA 1.26 1.26 1.26 1.26 1.23 1.30 1.1

PO!EN"A#E DE SOLIDO $ 32.0 32.0 32.0 32.3 28.0 35.0 22

LE% !&" $ 1.04 1.04 1.04 0.08 6.4 5.3 5.

U"ILIA!ION $ 92 92 92 92 92 92 92 92 92A!"O DE DISEO $ 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.

*3 / h

*3 / h

*3 / h

*3 / h

*3 / h

*3 / h

t / *3

t / *3

O 4 E L O

7

! I ! L O

N E S

+ O L I E

N D A

( P . <

3 t 5 3 )

A L I +

E N " A ! I , N

L O " A

! I , N

O U G - E

A L I +

E N " A ! I , N

L O " A

! I ,

N

O U G - E

( P . L 0 1

3 )

E L A

4 E

O U G - E

! O N ! E N " A D O

O U G - E

D I L U

I D O

A G U A

A

! O N ! E N " A D O

O U G - E

( P . L 5 1

3 )

A L I +

E N " A

! I O N

! I ! L O

N E S

E + O L I E

N D A

( P .

6 3 t 5 3

)

A G U A

A

E + O L I E

N D A

O 4 E L O

7

! I ! L O

N



FLUJO NUMERO 12 12A 14 13 13' (13) (13A)

NOMINAL NA

SOLI DOS t / h 1,000 500 849 151 151 551

AGUA 2,125 1,063 1,775 350 389 39 19 1,024

PULPA t / h 3,125 1,563 2,624 501 540 1,575

PULPA 2,487 1,244 2,087 400 439 1,210

INSTANTANEO 963

SOLIDOS t / h 1,087 543 923 164 164 599

AGUA 2,310 1,155 1,929 380 423 42 21 1,113

PULPA t / h 3,397 1,698 2,852 545 587 1,712

PULPA 2,704 1,352 2,268 435 477 1,315

DISEÑO

SOLI DOS t / h 1,304 652 1,107 197 197 719

AGUA 2,772 1,386 2,315 456 507 51 25 1,335

PULPA t / h 4,076 2,038 3,422 654 704 2,054

PULPA 3,244 1,622 2,722 522 573 1,578

OTROS

GE SOLIDO 2.76 2.76 2.72 3.00 3.00 2.95

DENSIDAD DEL LIQUIDO 1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.00

DENSI DAD DE PULPA 1.26 1.26 1.26 1.25 1.23 1.30

PO!EN"A#E DE SOLIDO $ 32.0 32.0 32.3 30.2 28.0 35.0

LE% !&" $ 1.04 1.04 0.08 6.4 6.4 5.3


*3 / h

*3 / h

*3 / h

*3 / h

*3 / h

*3 / h

t / *3

t / *3

A L I +

E N " A

! I ,

N

L O " A

! I , N

O U G - E

A L I +

E N " A

! I , N

L O " A

! I , N

O U G - E

( P . L 0 1

3 )

E L A

4 E

O U G - E

! O N ! E N " A D O

O U G - E

S I N

D I L U

I

! O N ! E N " A D O

O U G - E

D I L U

I D O

A G U A

A

! O N ! E N " A D O

O U G - E

A G U A

A

! O N ! E N " A D O

O U G - E

( P . L 5 1

3 )

A L I +

E N " A

! I O

N

! I ! L O

N E S

E + O L I E

N D A



110

90

200

127

120

98

218

139

144

118

261

166

2.95

1.00

1.57

55.0

5.3

921.2

U N D E L O

7

! I ! L O

N E S

E + O L I E

N D A

( P .

6 3 t 5 3 )



16 16A 18A 18 (17) (17A) 17 17' 20 19

NA NA

110 332 166 96 192 140 140 123 69

90 1,196 598 418 837 19 9 359 378 574 270

200 1,528 764 514 1,029 499 518 697 339

127 1,307 653 453 905 402 420 618 294

905

120 361 180 104 209 152 152 134 75

98 1,300 650 455 910 21 10 391 411 624 294

218 1,661 831 559 1,118 543 563 757 369

139 1,420 710 492 984 436 457 671 320

984

144 433 217 125 251 183 183 160 90

118 1,560 780 546 1,091 25 12 469 493 748 352

261 1,993 997 671 1,342 651 676 909 443

166 1,704 852 590 1,181 524 548 806 384

2.95 3.01 3.01 2.82 2.82 3.32 3.32 2.79 2.86

1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.00

1.57 1.17 1.17 1.14 1.14 1.24 1.23 1.13 1.15

55.0 21.7 21.7 18.7 18.7 28.0 27.0 17.6 20.4

5.3 5.4 5.4 1.3 1.3 11.0 11.0 0.35 3.0

92 92 92 92 92 92 92 92 92 92 92 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2

S ! A G A

+ O L I N

O

E + O L I E

N D A

( P .

E

8 & 0 9

. )

A L I +

E N " A

! I O

N

P I +

E A

L I + P I E ' A

A L I +

E N " A

! I O

N

P I +

E A

L I + P I E ' A

( P . : 5 1

3 )

E L A

4 E

P I +

E A

L I + P I E ' A

( P . : 5 1

3 )

E L A

4 E

P I +

E A

L I + P I E ' A

A G U A

A

! O N ! E N " A D O

P I +

E A

L I + P I E ' A

" O " A

L

A G U A

A

! O N ! E N " A D O

P I +

E A

L I + P I E ' A

( P . : 5 1

3 )

! O N ! E N " A D O

P I +

E A

L I + P I E ' A

S I N

D I L U

I

! O N ! E N " A D O

P I +

E A

L I + P I E ' A

D I L U

I D O

E L A

4 E

S ! A 4 E N G E

! O N ! E N " A D O

S ! A 4 E N G E

S I N

D I L U

I



22' 23 22A 30 24 25 (24

80 112 16 972 28 52

285 441 59 2,349 22 100 332

365 553 75 3,320 129 384

305 477 63 2,705 107 346

87 121 17 1,056 31 57

309 480 64 2,553 24 109 360

397 601 81 3,609 140 417

332 519 68 2,940 116 376

105 146 21 1,267 37 68

371 576 77 3,064 29 131 433

476 721 98 4,331 168 500

398 622 82 3,528 139 451

3.9 3.12 3.89 2.73 4.5 3.64

1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.

1.20 1.16 1.19 1.23 1.21 1.11

22.0 20.2 21.5 29.3 22.0 13.6

24.0 5.5 24.0 0.11 32.7 19.3

92 92 92 92 92 92 92 91.2 1.2 1.2 1.2 1.2 1.2 1.2 1

! O N ! E N " A D O

S E G U N D A

L I + P I E ' A

D I L U

I D O

E L A

4 E

S E G U N D A

L I + P I E ' A

A L I +

E N " A

! I ,

N

! O L U

+ N A S

" E ! E A

L I + P I E ' A

( P .

E

8 & 0 9

. )

E L A

4 E

" O " A

L A


A G U A

L A 4 A D O

E S P U + A

" E ! E A

L I + P I E ' A

( P .

E 8 & 0 9

. )

! O N ! E N " A D O

! O L E

! " I 4

O !

& ; + .

E L A

4 E

! O L U

+ N A S

" E ! E A

L I + P I E

' A

A G U A

D I L U

! I ,

N

! O N ! E



FLUJO NUMERO 12 12A 14 13 13' (13) (13A) 0

NOMINAL

SOLI DOS t / h 1,000 500 849 151 151 0 0 551

AGUA *3 / h 2,125 1,063 1,775 350 389 39 19 1,024

PULPA t / h 3,125 1,563 2,624 501 540 0 0 1,575

PULPA *3 / h 2,487 1,244 2,087 400 439 0 0 1,210

INSTANTANEO

SOLIDOS t / h 1,087 543 923 164 164 0 0 599

AGUA *3 / h 2,310 1,155 1,929 380 423 42 21 1,113

PULPA t / h 3,397 1,698 2,852 545 587 0 0 1,712

PULPA *3 / h 2,704 1,352 2,268 435 477 0 0 1,315

DISEÑO

SOLI DOS t / h 1,304 652 1,107 197 197 0 0 719

AGUA *3 / h 2,772 1,386 2,315 456 507 51 25 1,335

PULPA t / h 4,076 2,038 3,422 654 704 0 0 2,054

PULPA *3 / h 3,244 1,622 2,722 522 573 0 0 1,578

OTROS

GE SOLIDO 2.76 2.76 2.72 3.00 3.00 0.00 0.00 2.95

DENSIDAD DEL LIQUIDO t / *3 1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.00

DENSI DAD DE PULPA t / *3 1.26 1.26 1.26 1.25 1.23 0.00 0.00 1.30

PO!EN"A#E DE SOLIDO $ 32.0 32.0 32.3 30.2 28.0 0.0 0.0 35.0

LE% !&" $ 1.04 1.04 0.08 6.40 6.40 0.00 0.00 5.33


A L I +

E N " A

! I ,

N

L O " A

! I ,

N

O U G - E

A L I +

E N " A

! I , N

L O " A

! I , N

O U G - E

( P . L 0 1

3 )

E L A

4 E

O U G - E

! O N ! E N " A D O

O U G - E

S I N

D I L U

I

! O N ! E N " A D O

O U G - E

D I L U

I D O

A G U A

A

! O N ! E N " A D O

O U G - E

A G U A

A

! O N ! E N " A D O

O U G - E

( P . L 5 1

3 )

A L I +

E N " A

! I O N

! I ! L O

N E S

E + O L I E

N D A



0

110

90

200

127

120

98

218

139

144

118

261

166

2.95

1.00

1.57

55.0

5.33

921.2

U N D E L O

7

! I ! L O

N E S

E + O L I E

N D A

( P .

6 3 t 5 3 )



0 16 16A 18A 18 (17) (17A) 17 17' 20 19

110 332 166 96 192 0 0 140 140 123 69

90 1,196 598 418 837 19 9 359 378 574 270

200 1,528 764 514 1,029 0 0 499 518 697 339

127 1,307 653 453 905 0 0 402 420 618 294

120 361 180 104 209 0 0 152 152 134 75

98 1,300 650 455 910 21 10 391 411 624 294

218 1,661 831 559 1,118 0 0 543 563 757 369

139 1,420 710 492 984 0 0 436 457 671 320

144 433 217 125 251 0 0 183 183 160 90

118 1,560 780 546 1,091 25 12 469 493 748 352

261 1,993 997 671 1,342 0 0 651 676 909 443

166 1,704 852 590 1,181 0 0 524 548 806 384

2.95 3.01 3.01 2.82 2.82 0.00 0.00 3.32 3.32 2.79 2.86

1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.00

1.57 1.17 1.17 1.14 1.14 0.00 0.00 1.24 1.23 1.13 1.15

55.0 21.7 21.7 18.7 18.7 0.0 0.0 28.0 27.0 17.6 20.4

5.33 5.39 5.39 1.30 1.30 0.00 0.00 11.00 11.00 0.35 3.00

92 92 92 92 92 92 92 92 92 92 92 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2

S ! A G A

+ O L I N

O

E + O L I E

N D A

( P .

E

8 & 0 9

. )

A L I +

E N " A

! I O

N

P I +

E A

L I + P I E ' A

A L I +

E N " A

! I O

N

P I +

E A

L I + P I E ' A

( P . : 5 1

3 )

E L A

4 E

P I +

E A

L I + P I E ' A

( P . : 5 1

3 )

E L A

4 E

P I +

E A

L I + P I E ' A

A G U A

A

! O N ! E N " A D O

P I +

E A

L I + P I E ' A

" O " A

L

A G U A

A

! O N ! E N " A D O

P I +

E A

L I + P I E ' A

( P . : 5 1

3 )

! O N ! E N " A D O

P I +

E A

L I + P I E ' A

S I N

D I L U

I

! O N ! E N " A D O

P I +

E A

L I + P I E ' A

D I L U

I D O

E L A

4 E

S ! A 4 E N G E

! O N ! E N " A D O

S ! A 4 E N G E

S I N

D I L U

I



22' 23 22A 30 0 24 25 (24

80 112 16 972 0 28 52

285 441 59 2,349 22 100 332

365 553 75 3,320 0 129 384

305 477 63 2,705 0 107 346

87 121 17 1,056 0 31 57

309 480 64 2,553 24 109 360

397 601 81 3,609 0 140 417

332 519 68 2,940 0 116 376

105 146 21 1,267 0 37 68

371 576 77 3,064 29 131 433

476 721 98 4,331 0 168 500

398 622 82 3,528 0 139 451

3.89 3.12 3.89 2.73 0.00 4.45 3.64 0.

1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.

1.20 1.16 1.19 1.23 0.00 1.21 1.11 0.

22.0 20.2 21.5 29.3 0.0 22.0 13.6 0

24.00 5.50 24.00 0.11 0.00 32.70 19.27 0.

92 92 92 92 92 92 92 91.2 1.2 1.2 1.2 1.2 1.2 1.2 1

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DIMENSIONAMIENTO ESTANQUESPlanta Flotación Colectiva

Cajón RemolienaB$)") CJ#16#

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DIMENSIONAMIENTO COLUMNAS DE FLOTACIÓN 3$ LIMP

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CLCULO DEL REA TRANSVERSAL

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CLCULO DE LOS FLUOS DE AIRE Y AGUA DE LAVADO

:e*cidad upericia* de* aire g cm/ 2 +0$.23&

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CLCULO DE LA ALTURA DE LA COLUMNA

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@t 40&*/20&* 1.0

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Molino Re1.e'io,

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Pt@ "t: 1,719

Pt@ "t: -P 2,305

Pt@ +: (!t:F) 930

-P 1250

NH* E&> &t 1.9

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MUESTREO METALRGICO Y EN LNEA

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ROUGHER

"*imentaci9n A

Cncentrad *Anea 1 .

Cncentrad *Anea 2 2Re*ave *Anea 1 3Re*ave *Anea 2 4

Re*ave g*a* B

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SC":E>GER

Cncentrad g*a* ..Re*ave *inea 1 .2Re*ave *inea 2 .3

2a L@-,@EK"Cncentrad c*umna .4

(a L@-,@EK"Cncentrad c*umna C .8

( 14

Snda dedicada 9 cnectad cn OS"+,r tamaJ *uB n e puede muetreen *Anea

Snda dedicada 9 cnectad cn OS"+,r tamaJ *uB n e puede muetreen *Anea

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METALURGICO

EN LINEA



METODO DE 2RE+S 299.524928 477.50351

E<S F+AJ 15/20 ALOES DISEO!K@: D*t () 15 &:F &:F!@ + D>C D>C$ !F !@&:t 150$ 150$ 150$A:*t@ >@, th 240 382 411@t >C 1.0 1.6 2NM <t> 2.0 2.0 28*uB pr aterAa3 m(/7r 658 1049 1128$ S: / 35.0$ 35.0$ 35.0$$ ?/? 15$ 15$ 15$ P>& (>) 20 20 20

0.890 0.890 0.890

0.840 0.840 0.840

1.257 1.257 1.257

54 54 54

1.390 1.390 1.390

1.140 1.140 1.140 !?= 1.250 1.250 1.250!@ !@: (*3/h) 207 207 207N @@:> &> /3! 43$ 434N @@:> tt: 5 6 6GE 2.95 2.95

P'e,ión ciclón !7 ",i valo' ti"o "a'a 'emoliena8 e ,olio, lin9eao a :alance

!3; 43/ CURVA PARA / 6 )6$%6006(46 #40 Ga*/mi

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MOLINOS DE BOLAS GUANACO

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$/=>$;= $!=>$0= $5=>$0=!@ t

th 382.0 382.0 382.0* 150 150.0 150.0

* 45 45.0 45.0 I= h/>t 16.3 16.3 16.3Grado de llenado % 36.0 36.0 36.0:@ @t@ * 6.3 6.3 6.3:@ F * 5.0 4.6 4.6:@. !t@ $ 07 ;5 ;5" >@F P:: P:: P::EQUIPO REQUERIDO

D*t +:, =t t $/37 $!37 $537LF +:, =t t $;37 $037 $037E>> L> &:F 6.0 6.0 6.0D*t +:, t t 12.0 11.0 13.0LF +:, t t 16.5 17.5 17.5Pt@ & *: 1,144 940 1,361

- 1,534 1,260 1,825@t t>*> (M/1) 0.96 0.96 0.96Pt@ >t: 1,192 979 1,418

- 1,598 1,313 1,901+t @*@: - $?6;7 $?477 !?777METODO DE +ONDEc.ación P'eictivaS> (-/"@ :>) ;0.400 ;0.325 ;0.475< (&:F) 1.0 1.0 1.0 (-/"@ :>) 10.1 9.3 9.7@ (-/"@ :>) 11.7 10.8 11.2" ("@ :>) 97.4 86.8 121.3Pt@ ( *:) 1,144 940 1,361

- $?4/5 $?!67 $?0!48actr re re<uerid para m*er 1.00 1.00 1.00

"*C :*t@ 80

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TONELAES DISEO

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ROUGHER 236## 13(0& -8.RE-OL@E>=" 2$2 2## -.

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C$=' $99"@#

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(a L@-,@EK" N6":$)

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Rem*ienda )4 m( 100 m( A6"!( :#6"! "*im% C*umna 2a L (4 m( 40 m( S" "#''!$ "*im% 2a Limpieza 40 m( N6": "*im% 1aLimp.Scv #4 m( 120 m( N )" 9";6'"9" )'Q ,arece <u

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1& ce*da (00m(% +2*inea arreg* 1.2.2.2

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2 c*umna φ(36& ce*dacnvencina*e de 160m( +arreg* 2.2

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BLOCK CAVING OPEN PIT

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(4 &%2$ (0 &%26

0 5 10 15 20 25 30 35 40

1.5

2

2.5

3

3.5

4

4.5

5

f(x) = 2.73 exp( 0.0148 x )

R² = 1f(x) = 2.6696222116 exp( 0.0132179874 x )

R² = 0.9968035113

f(x) = 2.7974296889 exp( 0.0167033938 x )

R² = 0.9025774976

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n#apaa&

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AREA 28 ESPESAMIENTO Y FILTRADO DE C "ctua*

"*imentaci9n P Cncentrad ( *impieza

,rducci9n de* pryect5ne*aBe nmina*3 t/7 P 2#%(5ne*aBe intantne3 t/7 P (15ne*aBe dieJ3 t/7 P &$

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Frea etimada de epeamient3 m2 P )(1%4Cncentraci9n 9*id en *a decarga3 ' P 60=imetr de* epeadr3 m P (1

FILTRACION DE CONCENTRADO DE COBRE

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Frea de cmara3 m2 P 60%( Frea i*trante te*a3 m2 P 1215ranprte de cncentrad3 t/7 P &$

=enidad de* cncentrad3 t/m( P (%&Capacidad viva de dieJ de acpi3 d P )Capacidad viva de dieJ de acpi3 t P $000

8actr de i*trad t/7r/m2 0%24&

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=enidad *i<uid 1 +" )#'+) $1

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AREA 27 ESPESAMIENTO Y CONDUCCIÓN D

"*imentaci9n P5ne*aBe nmina* a* epeadr3 t/7 P5ne*aBe intantne a* epeadr3 t/7 P5ne*aBe dieJ a* epeadr3 t/7 P8*uB pu*pa nmina* a* epeadr3 m(/7 P8*uB pu*pa intantne a* epeadr m(/7 P8*uB pu*pa dieJ a* epeadr m(/7 P

8*uB agua a tran<ue nmina* tta*3 m(/7 P8*uB agua a tran<ue intantne tta* m(/7 P8*uB agua a tran<ue dieJ tta* m(/7 P8*uB pu*pa a tran<ue nmina*3 m(/7 P8*uB pu*pa a tran<ue intantne3 m(/7 P8*uB pu*pa a tran<ue dieJ3 m(/7 P

,rcentaBe 9*id a*imentaci9n epeadr3 ' P=enidad en *a a*imentaci9n3 t/m( PGravedad epecAica P5ip de epeadr P>umer de e<uip P8actr de dieJ3 ' P5aa de epeamient3 t/7/m2 P5aa de epeamient3 m2/t/7Cnum de 8*cu*ante3 g/t

"rea etimada de epeamient3 m2 P=imetr de* epeadr3 m PCncentraci9n 9*id en *a decarga3 ' P

antapacay 5aa de epeamient3 t/7/m25aa de epeamient3 m2/t/7

DUECHU"5aa de epeamient3 t/7/m2,RO-E=@ 5aa de epeamient3 t/7/m2

=enidad LA<uid3 gr/cc 1=enidad S9*id3 gr/cc 234)S9*id3 ' 44=enidad ,u*pa3 gr/cc 1%406006&



E RELAVES

C*a rug7er y cavenger C$)2 E

13046 E1326) E236$) E23$(2 E(341# E

6)4 E)(& E##1 E10(0 E111$ E1(&( E

2$ C1%2( E2%)& !

Hig7 rate "/C1 "/C

20 C0%#0 !/C

1%240 E

14#&%( C/E&&%$ C/E4$ "/C

0%6$1%&&0%#40%#0



C*a rug7er y cavenger $)6

13061132)(2366$23$01(3&#1

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10(&112&1(&#

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Hig7 rate1

200%#01%240

14$1%1&4%04$

0%6$&&&&&&&&1%&&0%#40%#

balance_flot_corccohuayco block caving - ley dic11

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