Diseñando con agua residual
1
0.50% Ø 150 mm Ø 250 mm Ø 300 mm Ø 350 mm Ø 300mm Ø 300mm Ø 250 mm Ø 200 mm Ø 150 mm Ø 350 mm Ø 450 mm Ø 500 mm Ø 500 mm Colector principal 1 0.50% Colector principal 2 0.50% Colector principal 2 Fosa séptica 10.6 m 3 Biogás 110 m 3 Reactor Anaeróbico 9 m 3 Aguas negras 330l/d basura orgánica 12 l/d biogás 48 m3/d aguas grises 1320 l/d aguas pretratadas 1662 l/d sludge aguas grises colector secundario colector principal arqueta conexión 0.50% c.principal 1 Ø 150mm sector 1 pozo de registro arqueta conexión 0.50% c. terciario Ø 100mm Q = 0.11 l/s 0.50% colector secundario Ø 150mm Q = 0.78 l/s Q=0.98 l/s 0.50% c.principal 1 Ø 200mm sector 2 pozo de registro Q=1.96 l/s 0.50% colector principal 1 Ø 250mm sector 3 pozo de registro Q=2.94 l/s pozo de registro 0.50% c.principal 1 Ø 300mm sector 4 Q=3.93 l/s pozo de registro 0.50% c.principal 1 Ø 300mm sector 5 Q=4.91 l/s pozo de registro 0.50% c.principal 1 Ø 300mm sector 6 Q=5.89 l/s pozo de registro 0.50% c.principal 1 Ø 350mm sector 7 Q=6.87 l/s pozo de registro pozo de registro 0.50% colector principal 1 Ø 350mm sector 8 Q=7.85 l/s 0.50% colector principal 1 Ø 350mm sector 9 Q=8.83 l/s pozo de registro pozo de registro pozo de registro pozo de registro 0.50% colector principal 3 Ø 450mm sector 1 Q=16.34 l/s 0.50% colector principal 3 Ø 500mm sector 2 Q=19.31 l/s 0.50% colector principal 3 Ø 500mm sector 3 Q=22.27 l/s 0.50% colector principal 3 Ø 550mm sector 4 Q=25.24 l/s y bombeo y bombeo pozo de registro 0.50% colector principal 2 Ø 150mm sector 1 Q=0.91 l/s pozo de registro pozo de registro pozo de registro pozo de registro 0.50% c.principal 2 Ø 200mm sector 2 Q=1.82 l/s 0.50% c.principal 2 Ø 250mm sector 3 Q=2.73 l/s 0.50% colector principal 2 Ø 250mm sector 4 Q=3.63 l/s 0.50% colector principal 2 Ø 300mm sector 5 Q=4.54 l/s y bombeo pozo de registro y bombeo 20.00m 17.50m Tabla: Tecnologías a ser aplicadas en Cuba para el saneamiento de zonas periurbanas Rejas Desarenador Trampa de grasas Tanque Imhoff Tanque séptico Sed. Primario Laguna anaerobia Filtro percolador + Ssec. Biodiscos + SSec. Aireación extendida + Ssec. Laguna aireada + Ssec Laguna facultativa RAAV (filtro anaero- bio, UASB, otros) Zanja filtrante Laguna maduración Lecho filtrante Filtro de arena Pozo filtrante Filtro verde Humedal construido (lecho de juncos/ turba) Infiltración rápida Escorrentía Lecho de secado al sol Relleno sanitario ZONA 1 Población 7734p. Caudal 1238 m 3 /día ZONA 2 Población 2388p. Caudal 382 m 3 /día ZONA 2 Población 8388p. Caudal 1341 m 3 /día user BOD per user water consumption COD/BOD ratio daily flow wastewater BOD concentration COD concentration Settleable Solids COD per use Q greywater Q black water Q organic waste g/day l/day mg/l / mg/l m3/day mg/l mg/l mg/l l/pers*day l/pers*day l/pers*day 100 30 120 1,9 12 250 475 200 57 96 24 1,2 Vol sludge + scum Vol waste water Total Volume Q medium waste water Q max Volume incl. Sludge Q greywater Q black water Q organic waste m3 m3 m3 l/pers*day l/pers*day m3 m3 m3 m3 10 20 30 120 200 20000 9,6 2,4 0,12 302,777778 153,011696 daily black water flow time of most waste water flow max flow at peak hours COD inflow BOD inflow HRT inside tank settleable SS/COD ratio COD removal rate BOD removal rate COD outflow BOD outflow m3/day h m3/h mg/l mg/l h mg/l / mg/l % % mg/l mg/l m3/d % % % ml/l d ºC l/kg org DM 2,4 12 0,20 475,00 250,00 24 0,42 0,36 0,61 302,78 153,01 COD/BOD = 1,9 BOD rem= 1,07 desludging interval inner width of septic tank min water depth at outlet point Volume incl. Sludge biogas 70% CH4 months m m m3 m3/d % mg/l months m3 m3 m3 m3 24 2 2 8,24 0,10 0,0042 inner width inner height inner length 2 2,5 2,06 0,69 1,37 sludge BOD rem. length of second chamber m inner length of first chamber m daily waste water flow time of most waste water flow max peak flow per hour COD inflow BOD inflow COD/BOD ratio settleable SS/CODratio lowest digester temp. desludging interval HRT in settler COD removal rate in settler removal rate in settler m3/day h m3/h mg/l mg/l mg/l ºC months h % % 12,12 12 1,01 1,06 COD inflow into baffled reactor BOD inflow into baffled reactor COD/BOD ratio COD rem, 25º, COD 1500 theor rem rate acc. To factor COD rem.rate baffle only COD out total COD rem. Rate total BOD rem. Rate BOD out f-overload f-strength f-temp f HRT mg/l mg/l % % mg/l % % mg/l 7,94 4,18 1,9 1 0,95 1 0,87 0,83 0,71 1,23307702 0,84 0,87 1,03 1,03 max upflow velocity number of upflow chambers depth at outlet m/h m 1,8 3 1,5 lenght of chambers area of single upflow chamber width of chambers width of chambers chosen actual upflow velocity width of downfall shaft actual volume of baffled reactor actual HRT org. Load BOD Biogas out of septic tank Biogas out of ABR Biogas m m2 m m m/h m m3 h kg/m3 day m3/day m3/day m3/day 0,75 0,56 0,75 2 0,67 0,25 9 16,97 0,01 0,02 - 0,02 0,00 - cod/bod rem. Factor factors to calculate COD removal rate of baffled reactor cod/bod rem. Factor daily flow black water + organic waste TS (DM) content org. DM/total DM org. DM content solids settleable within one day HRT lowest digester temp ideal biogas product. At 30ºC total gas production methan content m3/d % % % ml/l d ºC l/kg org DM f-HRT f-temp m3/d % 2,52 6 67 4,02 20 25 25 400 0,97 0,9 35,38 70 non dissolv. Methan prod. approx effluent COD desludging interval sludge volume liquid volume total digester volume gas storage capacity gas holder volume VG % mg/l months m3 m3 m3 m3 80 7,94 12 18,144 63 81,144 0,65 22,99 gas production factors Anaerobic Baffle Reactor Sección sector interior manzana hasta salida al colector secundario 1/50 Detalle planta manzana tipo y enlaces 1/100 Biogás Tanque séptico waste water production per capita general spread sheet for biogas plants, input and gas production data general spread sheet for baffled septic tank with integrated settler treatment data baffled septic tank dimension of baffled septic tank General spread sheet for septic tank, input and treatment data Dimensions of septic tank Secciones urbanas alcantarillado residual 1/2000 Datos Remedios 18637 habitantes 258.1 Ha 6740 Viviendas (161 son > 2 plantas) 169 manzanas Cálculo manzana tipo Sup: 3.400m2 Sup.construida = 30% Sup. libre = 70% 32 viviendas (3 pers. x vivienda) = 96 personas Aguas grises = 132 l/d Aguas negras = 33 l/d Residuos orgá nicos = 1.2 l/d Sistemas para ser aplicados en Cuba para el saneamiento Fuente: INGENIERIA HIDRÁULICA Y AMBIENTAL, VOL. XXX, No. 1, 2009 Tanque Biogás Reactor colector SOLID FREE SEWER Parque colector Tanque séptico colector secundario colector principal Parque gestión aguas Reja desbaste Biogás Reactor anaeróbico Diseñando con agua residual -urbano- 09 Redes urbanas Parque para la gestión del agua 100m 200m 400m 1/3.000
Transcript of Diseñando con agua residual
0.50
%
Ø 150
mm
Ø 250
mm
Ø 30
0 m
mØ
350 m
m
Ø 3
00m
m
Ø 3
00
mm
Ø 2
50 m
m
Ø 2
00 m
mØ
150
mm
Ø 350 m
m
Ø 450 m
m
Ø 500 mmØ 500 mm
Colector principal 1
0.50
%
Cole
ctor
prin
cipal
2
0.50%
Colector principal 2
aguas grises
colector secundario
colector principal
Fosa séptica10.6 m3
Biogás 110 m3
Reactor Anaeróbico9 m3
Aguas negras330l/d
basura orgánica12 l/d
biogás48 m3/d
aguas grises1320 l/d
aguas pretratadas 1662 l/d
sludge
Datos generales
Super�cie total 137 ha
Población 18.637 p
Aguas grises 132l/d
Aguas negras 33 l/d
Residuos orgánicos 1.2l/d
ZONA 1Población 7734p.Caudal 1238 m3/día
ZONA 2Población 2388p.Caudal 382 m3/día
ZONA 2Población 8388p.Caudal 1341 m3/día
Manzana tipoSuperficie: 3.400 m2 (no constr. 30% = 928 m2)dimensiones: 65 x 50m32 viviendas96 personas
aguas grises
colector secundario
colector principal
Fosa séptica10.6 m3
Biogás 110 m3
Reactor Anaeróbico9 m3
Aguas negras330l/d
basura orgánica12 l/d
biogás48 m3/d
aguas grises1320 l/d
aguas pretratadas 1662 l/d
sludge
Datos generales
Super�cie total 137 ha
Población 18.637 p
Aguas grises 132l/d
Aguas negras 33 l/d
Residuos orgánicos 1.2l/d
ZONA 1Población 7734p.Caudal 1238 m3/día
ZONA 2Población 2388p.Caudal 382 m3/día
ZONA 2Población 8388p.Caudal 1341 m3/día
Manzana tipoSuperficie: 3.400 m2 (no constr. 30% = 928 m2)dimensiones: 65 x 50m32 viviendas96 personas
arqu
eta
cone
xión
0.50%c.principal 1
Ø 150mmsector 1
pozo
de
regi
stro
arqu
eta
cone
xión
0.50%c. terciario
Ø 100mmQ = 0.11 l/s
0.50%colector secundario
Ø 150mmQ = 0.78 l/s Q=0.98 l/s
0.50%c.principal 1
Ø 200mmsector 2
pozo
de
regi
stro
Q=1.96 l/s
0.50%colector principal 1
Ø 250mmsector 3
pozo
de
regi
stro
Q=2.94 l/s
pozo
de
regi
stro
0.50%c.principal 1
Ø 300mmsector 4
Q=3.93 l/s
pozo
de
regi
stro
0.50%c.principal 1
Ø 300mmsector 5
Q=4.91 l/s
pozo
de
regi
stro
0.50%
c.principal 1
Ø 300mmsector 6
Q=5.89 l/s
pozo
de
regi
stro
0.50%
c.principal 1
Ø 350mmsector 7
Q=6.87 l/s
pozo
de
regi
stro
pozo
de
regi
stro
0.50%
colector principal 1
Ø 350mmsector 8
Q=7.85 l/s
0.50%
colector principal 1
Ø 350mmsector 9
Q=8.83 l/s
pozo
de
regi
stro
pozo
de
regi
stro
pozo
de
regi
stro
pozo
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regi
stro
0.50%
colector principal 3
Ø 450mmsector 1
Q=16.34 l/s
0.50%
colector principal 3
Ø 500mmsector 2
Q=19.31 l/s
0.50%
colector principal 3
Ø 500mmsector 3
Q=22.27 l/s
0.50%
colector principal 3
Ø 550mmsector 4
Q=25.24 l/s
y bo
mbe
o
y bo
mbe
o
pozo
de
regi
stro
0.50%
colector principal 2
Ø 150mmsector 1
Q=0.91 l/s
pozo
de
regi
stro
pozo
de
regi
stro
pozo
de
regi
stro
pozo
de
regi
stro
0.50%
c.principal 2
Ø 200mmsector 2
Q=1.82 l/s
0.50%
c.principal 2
Ø 250mmsector 3
Q=2.73 l/s
0.50%
colector principal 2
Ø 250mmsector 4
Q=3.63 l/s
0.50%
colector principal 2
Ø 300mmsector 5
Q=4.54 l/s
y bo
mbe
o
pozo
de
regi
stro
y bo
mbe
o
20.00m
17.50m
Tabla: Tecnologías a ser aplicadas en Cuba para el saneamiento de zonas periurbanas
Rejas
Desarenador
Trampa de grasas
TanqueImho�
Tanqueséptico
Sed. Primario
Lagunaanaerobia
Filtro percolador + Ssec.
Biodiscos + SSec.
Aireaciónextendida + Ssec.
Laguna aireada + Ssec
Laguna facultativa
RAAV (�ltro anaero-bio, UASB, otros)
Zanja �ltrante
Laguna maduración
Lecho �ltrante
Filtro de arena
Pozo �ltrante
Filtro verde
Humedal construido (lecho de juncos/ turba)
In�ltración rápida
Escorrentía
Lecho de secado al sol
Relleno sanitario
aguas grises
colector secundario
colector principal
Fosa séptica10.6 m3
Biogás 110 m3
Reactor Anaeróbico9 m3
Aguas negras330l/d
basura orgánica12 l/d
biogás48 m3/d
aguas grises1320 l/d
aguas pretratadas 1662 l/d
sludge
Datos generales
Super�cie total 137 ha
Población 18.637 p
Aguas grises 132l/d
Aguas negras 33 l/d
Residuos orgánicos 1.2l/d
ZONA 1Población 7734p.Caudal 1238 m3/día
ZONA 2Población 2388p.Caudal 382 m3/día
ZONA 2Población 8388p.Caudal 1341 m3/día
Manzana tipoSuperficie: 3.400 m2 (no constr. 30% = 928 m2)dimensiones: 65 x 50m32 viviendas96 personas
user BOD per userwater
consumptionCOD/BOD
ratiodaily flow
wastewaterBOD
concentrationCOD
concentrationSettleable Solids COD per use
Q greywater Q black water Q organic
wasteg/day l/day mg/l / mg/l m3/day mg/l mg/l mg/l l/pers*day l/pers*day l/pers*day
100 30 120 1,9 12 250 475 200 57 96 24 1,2
Vol sludge + scum
Vol waste water
Total VolumeQ medium
waste waterQ max Volume incl.
SludgeQ greywater Q black water
Q organic waste COD inflow BOD inflow 350 l Methan/1 kg BOD
m3 m3 m3 l/pers*day l/pers*day m3 m3 m3 m3 mg/l mg/l 200l Methan/1 kg COD10 20 30 120 200 20000 9,6 2,4 0,12 302,777778 153,011696
daily black water flow
time of most waste water
flow
max flow at peak hours
COD inflow BOD inflowHRT inside
tanksettleable
SS/COD ratio
COD removal
rate
BOD removal
rate
COD outflow
BOD outflow
daily flow black water
+ organic waste
TS (DM) content
org. DM/total
DM
org. DM content
solids settleable within one
day
HRTlowest
digester temp
ideal biogas product. At
30ºC
total gas production
methan content
m3/day h m3/h mg/l mg/l h mg/l / mg/l % % mg/l mg/l m3/d % % % ml/l d ºC l/kg org DM f-HRT f-temp m3/d %2,4 12 0,20 475,00 250,00 24 0,42 0,36 0,61 302,78 153,01 2,52 6 67 4,02 20 25 25 400 0,97 0,9 35,38 70
COD/BOD = 1,9 BOD rem= 1,07
desludging interval
inner width of septic tank
min water depth at
outlet point
Volume incl. Sludge
biogas 70% CH4
non dissolv. Methan
prod.
approx effluent
COD
desludging interval
sludge volume
liquid volume
total digester volume
gas storage capacity
gas holder volume VG
months m m m3 m3/d % mg/l months m3 m3 m3 m324 2 2 8,24 0,10 80 7,94 12 18,144 63 81,144 0,65 22,99
0,0042
inner width inner height inner length
2 2,5 2,06
daily waste water flow
time of most waste water
flow
max peak flow per hour
COD inflow BOD inflowCOD/BOD
ratiosettleable
SS/CODratio
lowest digester
temp.
desludging interval
HRT in settler
COD removal rate in settler
removal rate in settler
m3/day h m3/h mg/l mg/l mg/l ºC months h % %12,12 12 1,01
1,06
COD inflow into baffled reactor
BOD inflow into baffled reactor
COD/BOD ratio
COD rem, 25º, COD 1500
theor rem rate acc. To
factor
COD rem.rate
baffle onlyCOD out
total COD rem. Rate
total BOD rem. Rate
BOD out
f-overload f-strength f-temp f HRTmg/l mg/l % % mg/l % % mg/l7,94 4,18 1,9 1 0,95 1 0,87 0,83 0,71 1,23307702 0,84 0,87 1,03
1,03
max upflow velocity
number of upflow
chambers
depth at outlet
m/h m1,8 3 1,5
lenght of chambers
area of single upflow
chamber
width of chambers
width of chambers
chosen
actual upflow velocity
width of downfall shaft
actual volume of baffled
reactoractual HRT
org. Load BOD
Biogas out of septic tank
Biogas out of ABR
Biogas
m m2 m m m/h m m3 h kg/m3 day m3/day m3/day m3/day0,75 0,56 0,75 2 0,67 0,25 9 16,97 0,01 0,02 - 0,02 0,00 -
baffled septic tank
dimension of baffled septic tank
gas production factors
general spread sheet for biogas plants, input and gas production data
general spread sheet for baffled septic tank with integrated settler - NO SETTLER
cod/bod rem. Factor
treatment data
factors to calculate COD removal rate of baffled reactor
cod/bod rem. Factor
0,69 1,37
General spread scheet for septic tank, input and treatment data
Dimensions of septic tank
sludge BOD rem.
waste water production per capita
length of second chamber
m
inner length of first chamber
m
user BOD per userwater
consumptionCOD/BOD
ratiodaily flow
wastewaterBOD
concentrationCOD
concentrationSettleable Solids COD per use
Q greywater Q black water Q organic
wasteg/day l/day mg/l / mg/l m3/day mg/l mg/l mg/l l/pers*day l/pers*day l/pers*day
100 30 120 1,9 12 250 475 200 57 96 24 1,2
Vol sludge + scum
Vol waste water
Total VolumeQ medium
waste waterQ max Volume incl.
SludgeQ greywater Q black water
Q organic waste COD inflow BOD inflow 350 l Methan/1 kg BOD
m3 m3 m3 l/pers*day l/pers*day m3 m3 m3 m3 mg/l mg/l 200l Methan/1 kg COD10 20 30 120 200 20000 9,6 2,4 0,12 302,777778 153,011696
daily black water flow
time of most waste water
flow
max flow at peak hours
COD inflow BOD inflowHRT inside
tanksettleable
SS/COD ratio
COD removal
rate
BOD removal
rate
COD outflow
BOD outflow
daily flow black water
+ organic waste
TS (DM) content
org. DM/total
DM
org. DM content
solids settleable within one
day
HRTlowest
digester temp
ideal biogas product. At
30ºC
total gas production
methan content
m3/day h m3/h mg/l mg/l h mg/l / mg/l % % mg/l mg/l m3/d % % % ml/l d ºC l/kg org DM f-HRT f-temp m3/d %2,4 12 0,20 475,00 250,00 24 0,42 0,36 0,61 302,78 153,01 2,52 6 67 4,02 20 25 25 400 0,97 0,9 35,38 70
COD/BOD = 1,9 BOD rem= 1,07
desludging interval
inner width of septic tank
min water depth at
outlet point
Volume incl. Sludge
biogas 70% CH4
non dissolv. Methan
prod.
approx effluent
COD
desludging interval
sludge volume
liquid volume
total digester volume
gas storage capacity
gas holder volume VG
months m m m3 m3/d % mg/l months m3 m3 m3 m324 2 2 8,24 0,10 80 7,94 12 18,144 63 81,144 0,65 22,99
0,0042
inner width inner height inner length
2 2,5 2,06
daily waste water flow
time of most waste water
flow
max peak flow per hour
COD inflow BOD inflowCOD/BOD
ratiosettleable
SS/CODratio
lowest digester
temp.
desludging interval
HRT in settler
COD removal rate in settler
removal rate in settler
m3/day h m3/h mg/l mg/l mg/l ºC months h % %12,12 12 1,01
1,06
COD inflow into baffled reactor
BOD inflow into baffled reactor
COD/BOD ratio
COD rem, 25º, COD 1500
theor rem rate acc. To
factor
COD rem.rate
baffle onlyCOD out
total COD rem. Rate
total BOD rem. Rate
BOD out
f-overload f-strength f-temp f HRTmg/l mg/l % % mg/l % % mg/l7,94 4,18 1,9 1 0,95 1 0,87 0,83 0,71 1,23307702 0,84 0,87 1,03
1,03
max upflow velocity
number of upflow
chambers
depth at outlet
m/h m1,8 3 1,5
lenght of chambers
area of single upflow
chamber
width of chambers
width of chambers
chosen
actual upflow velocity
width of downfall shaft
actual volume of baffled
reactoractual HRT
org. Load BOD
Biogas out of septic tank
Biogas out of ABR
Biogas
m m2 m m m/h m m3 h kg/m3 day m3/day m3/day m3/day0,75 0,56 0,75 2 0,67 0,25 9 16,97 0,01 0,02 - 0,02 0,00 -
baffled septic tank
dimension of baffled septic tank
gas production factors
general spread sheet for biogas plants, input and gas production data
general spread sheet for baffled septic tank with integrated settler - NO SETTLER
cod/bod rem. Factor
treatment data
factors to calculate COD removal rate of baffled reactor
cod/bod rem. Factor
0,69 1,37
General spread scheet for septic tank, input and treatment data
Dimensions of septic tank
sludge BOD rem.
waste water production per capita
length of second chamber
m
inner length of first chamber
m
user BOD per userwater
consumptionCOD/BOD
ratiodaily flow
wastewaterBOD
concentrationCOD
concentrationSettleable Solids COD per use
Q greywater Q black water Q organic
wasteg/day l/day mg/l / mg/l m3/day mg/l mg/l mg/l l/pers*day l/pers*day l/pers*day
100 30 120 1,9 12 250 475 200 57 96 24 1,2
Vol sludge + scum
Vol waste water
Total VolumeQ medium
waste waterQ max Volume incl.
SludgeQ greywater Q black water
Q organic waste COD inflow BOD inflow 350 l Methan/1 kg BOD
m3 m3 m3 l/pers*day l/pers*day m3 m3 m3 m3 mg/l mg/l 200l Methan/1 kg COD10 20 30 120 200 20000 9,6 2,4 0,12 302,777778 153,011696
daily black water flow
time of most waste water
flow
max flow at peak hours
COD inflow BOD inflowHRT inside
tanksettleable
SS/COD ratio
COD removal
rate
BOD removal
rate
COD outflow
BOD outflow
daily flow black water
+ organic waste
TS (DM) content
org. DM/total
DM
org. DM content
solids settleable within one
day
HRTlowest
digester temp
ideal biogas product. At
30ºC
total gas production
methan content
m3/day h m3/h mg/l mg/l h mg/l / mg/l % % mg/l mg/l m3/d % % % ml/l d ºC l/kg org DM f-HRT f-temp m3/d %2,4 12 0,20 475,00 250,00 24 0,42 0,36 0,61 302,78 153,01 2,52 6 67 4,02 20 25 25 400 0,97 0,9 35,38 70
COD/BOD = 1,9 BOD rem= 1,07
desludging interval
inner width of septic tank
min water depth at
outlet point
Volume incl. Sludge
biogas 70% CH4
non dissolv. Methan
prod.
approx effluent
COD
desludging interval
sludge volume
liquid volume
total digester volume
gas storage capacity
gas holder volume VG
months m m m3 m3/d % mg/l months m3 m3 m3 m324 2 2 8,24 0,10 80 7,94 12 18,144 63 81,144 0,65 22,99
0,0042
inner width inner height inner length
2 2,5 2,06
daily waste water flow
time of most waste water
flow
max peak flow per hour
COD inflow BOD inflowCOD/BOD
ratiosettleable
SS/CODratio
lowest digester
temp.
desludging interval
HRT in settler
COD removal rate in settler
removal rate in settler
m3/day h m3/h mg/l mg/l mg/l ºC months h % %12,12 12 1,01
1,06
COD inflow into baffled reactor
BOD inflow into baffled reactor
COD/BOD ratio
COD rem, 25º, COD 1500
theor rem rate acc. To
factor
COD rem.rate
baffle onlyCOD out
total COD rem. Rate
total BOD rem. Rate
BOD out
f-overload f-strength f-temp f HRTmg/l mg/l % % mg/l % % mg/l7,94 4,18 1,9 1 0,95 1 0,87 0,83 0,71 1,23307702 0,84 0,87 1,03
1,03
max upflow velocity
number of upflow
chambers
depth at outlet
m/h m1,8 3 1,5
lenght of chambers
area of single upflow
chamber
width of chambers
width of chambers
chosen
actual upflow velocity
width of downfall shaft
actual volume of baffled
reactoractual HRT
org. Load BOD
Biogas out of septic tank
Biogas out of ABR
Biogas
m m2 m m m/h m m3 h kg/m3 day m3/day m3/day m3/day0,75 0,56 0,75 2 0,67 0,25 9 16,97 0,01 0,02 - 0,02 0,00 -
baffled septic tank
dimension of baffled septic tank
gas production factors
general spread sheet for biogas plants, input and gas production data
general spread sheet for baffled septic tank with integrated settler - NO SETTLER
cod/bod rem. Factor
treatment data
factors to calculate COD removal rate of baffled reactor
cod/bod rem. Factor
0,69 1,37
General spread scheet for septic tank, input and treatment data
Dimensions of septic tank
sludge BOD rem.
waste water production per capita
length of second chamber
m
inner length of first chamber
m
Anaerobic Baffle ReactorSección sector interior manzana hasta salida al colector secundario 1/50
Detalle planta manzana tipo y enlaces 1/100
BiogásTanque sépticowaste water production per capita general spread sheet for biogas plants, input and gas production data general spread sheet for baffled septic tank with integrated settler
treatment data
baffled septic tank
dimension of baffled septic tank
General spread sheet for septic tank, input and treatment data
Dimensions of septic tank
Secciones urbanas alcantarillado residual 1/2000
Datos Remedios18637 habitantes258.1 Ha6740 Viviendas (161 son > 2 plantas)169 manzanas
Cálculo manzana tipo Sup: 3.400m2Sup.construida = 30%Sup. libre = 70% 32 viviendas (3 pers. x vivienda) = 96 personasAguas grises = 132 l/dAguas negras = 33 l/dResiduos orgá nicos = 1.2 l/d
Sistemas para ser aplicados en Cuba para el saneamiento
Fuente: INGENIERIA HIDRÁULICA Y AMBIENTAL, VOL. XXX, No. 1, 2009
Reja
des
bast
eTanqueséptico
Biogás Reactoranaeróbico
colectorsecundario
SOLID FREE SEWER
Parquegestión aguas
colectorprincipalRe
ja d
esba
steTanque
sépticoBiogás Reactor
anaeróbicocolector
secundario
SOLID FREE SEWER
Parquegestión aguas
colectorprincipal
Reja
des
bast
eTanqueséptico
Biogás Reactoranaeróbico
colectorsecundario
SOLID FREE SEWER
Parquegestión aguas
colectorprincipal
Reja
des
bast
eTanqueséptico
Biogás Reactoranaeróbico
colectorsecundario
SOLID FREE SEWER
Parquegestión aguas
colectorprincipal
Reja desbaste
Tanq
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ogás
Reac
tor
anae
róbi
coco
lect
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cund
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SOLI
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SEW
ER
Parq
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uas
cole
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prin
cipa
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Reja
des
bast
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Biogás Reactoranaeróbico
colectorsecundario
SOLID FREE SEWER
Parquegestión aguas
colectorprincipal
Reja
des
bast
eTanqueséptico
Biogás Reactoranaeróbico
colectorsecundario
SOLID FREE SEWER
Parquegestión aguas
colectorprincipal
Reja desbaste
Tanq
uesé
ptic
oBi
ogás
Reac
tor
anae
róbi
coco
lect
orse
cund
ario
SOLI
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REE
SEW
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Parq
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uas
cole
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prin
cipa
l
Diseñando con agua residual-urbano-
09 Redes urbanas 100m
200m
500m1/10.000
Parque para la gestión del agua100m
200m
500m 100m
200m
400m1/10.000
50m
100m
250m1/5.000
1km
2km
5km1/100.000
10m
20m
50m1/1.000
1/1.250
5m 15m
10m
1m
2m
5m1/100
50cm
1m
2,5m1/50
2m
4m
10m1/200
20cm
40cm
100cm1/20
10m
20m
50m1/670
20m
40m
100m1/2.000
1/3.000
