trabajo final ptar bbc

7/24/2019 Trabajo Final Ptar Bbc

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UNIVERSIDAD MANUELA BELTRAN

ESPECIALIZACION EN AGUA Y SANEAMIENTO AMBIENTAL

TRABAJO FINALPLANTA DE TRATAMIENTO DE AGUAS RESIDUALES

BOGOTA BEER COMPANY

COLOCAR FOTO DE LA PTAR BBC

Elaborado por:

Sandra Milena Ca!a"eda Medina # Con!r$%!or en Ar&$i!e%!$ra e In'enier(a

Edna Ro%(o )errera Ca!illo # In'* Fore!al

Paola Me+(a Rodr('$e, # In'* Sani!aria

Seba!i-n G$!i.rre, Fl/re, # In'* A0bien!al

ASIGNATURA: DISE1O DE PLANTAS DE TRATAMIENTO DE AGUAS RESIDUALES II

DOCENTE: ING* ROBERTO BALDA

Bo'o!-2 34 de No5ie0bre de 6437


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BOGOTA BEER COMPANY

Fecha de Entrega:10 de Noviembre de 2014

Pgina 2

TABLA DE CONTENIDO

P-'*

3* DETERMINACION DE LA CAPACIDAD DE LA PLANTA**************************************1.1 TANQUE DE IGUALAMIENTO..............................................................................1.2 TANQUE DE PRE ACIDIFICACIN......................................................................1.3 REACTOR EGSB..................................................................................................1.4 SEDIMENTADOR SECUNDARIO.........................................................................1.5 REACTOR AEROBIO............................................................................................1.6 CAPACIDAD DE LA PLANTA................................................................................

6* BALANCE DE CARGAS***************************************************************************************8* 9OLUMEN DE LODOS PTAR BBC**********************************************************************3.1 ALTERNATIVA DE DESHIDRATRACIN............................................................

1.1.1 Lec!" #e Sec$#!.......................................................................................12

1.1.2 Ce%&'()*+$#!' #e L!#!"................................................................................12

7* REUSO DEL EFLUENTE**************************************************************************************


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Pgina 3

3* DETERMINACION DE LA CAPACIDAD DE LA PLANTA

3*3 TANUE DE IGUALAMIENTO

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Q=39,20

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Pgina 5

V=ASH

V=7,073,0

V=21,21m3

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3*< REACTOR AEROBIO

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F*e%&e RAS.

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V=AHL

V=3,03,05,75

V=51,75m3


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Pgina 10


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6* BALANCE DE CARGAS

D$&!" (%(c($,e"

Q 2 ,?"DQO 3221 /+?,DBO 231 /+?,SST 85 /+?,G7A 1 /+?,N 24 /+?,F /+?,

L$ PTAR BBC 'e"e%&$ e, "(+*(e%&e &'$&$/(e%&! EGSB 9 E)(c(e%c($ 'e/!c(% #e DBO #e, 88 Se#(/e%&$#!' "ec*%#$'(!9 E)(c(e%c($ 'e/!c(% #e DBO #e, L!#!" $c&($#!" E)(c(e%c($ 'e/!c(% #e DBO #e, 88

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C$adro 6 Balan%e de Car'a PTAR BBC

PARAMETRO

AFLUENTE EGSBEF(!

SEDIMENTADORSECUNDARIO

EF(!

LODOS ACTI"ADOSEF(!

EFLUENTE

# ($%d&a!' )*+,, # ($%d&a!' )*+,,#

($%d&a!')*+,

,# ($%d&a!' )*+,,

#($%d&a!'

)*+,,

-g%$ .g%d&a -g%$ .g%d&a -g%$ .g%d&a -g%$ .g%d&a -g%$ .g%d&a

DQO 3221 556.59 322.10 55.66 90 32.21 5.57 90 22.55 3.90 30 22.55 3.90

DBO 2310 399.17 231.00 39.92 90 161.70 27.94 30 16.17 2.79 90 16.17 2.79

SS 95 16.42 9.50 1.64 90 1.90 0.33 80 0.95 0.16 50 0.95 0.16

! " # 1 0.17 0.10 0.02 90 0.06 0.01 40 0.04 0.01 30 0.04 0.01

P 8 1.38

N 24 4.15


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Pgina 13

8* 9OLUMEN DE LODOS PTAR BBC

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DBO 'e/!(#$ e% @+?#=$

DBOremovida=DBOinicialDBOeluen!e

DBOr=399,172,79

DBOr=396,38 "# /da

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$LBS=DBOremovidaac!or

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$LBS=396,3810

100

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$LBH= $LBS

(s%lidos/100)

$LBH= 39,64

(2 /100)

$LBH=1981,9 "# /dia


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Pgina 14

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VL=1943,04 l /dia

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8*3 ALTERNATI9A DE DES)IDRATRACI;N

3*3*3 Le%o de Se%ado

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3*3*6 Cen!ri$'ador de Lodo6

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7* REUSO DEL EFLUENTE

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