AG-Metal Zenica - tretman otpadnih voda: - Tehnologija tretmana otpadnih voda, - Prodaja opreme za tretman otpadnih voda, - Consulting i potpora za projektante i investitore - Zakoni i propi…Descripción completa
AG-Metal Zenica - tretman otpadnih voda: - Tehnologija tretmana otpadnih voda, - Prodaja opreme za tretman otpadnih voda, - Consulting i potpora za projektante i investitore - Zakoni i propisi iz o...
pengbisFull description
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This document deals with the activated sludge process. What is activated sludge process and what are its variants? mechanisms and kinetics of treatment, and applications of the activated slu…Full description
Sludge applicationDescrição completa
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lumpurDeskripsi lengkap
The wastewater generated from the canteen, mess, college hostel in were collected and analyzed. In the present study, an attempt has been made to evaluate the treatability of wastewaters using lab-...
pengolahan lumpur/sludgeDeskripsi lengkap
pakan sludgeFull description
Deskripsi lengkap
Differentiation of Sell User in put
Row water Quantity (peration#ime "ater , Raw -aterial ProductionQuantity
Setting value
3!!! m3,day
"ater #emperature
1)* r 3&
Calculation value
1%+.&
(DasicUnit
$!.!
m ,t
%) t,day
(D
)!! ppm
-6SS
$&!! ppm
"ater#emperature
Content Content &+3 ppm
!.!& mm7 $%.& '
Specificravityof"ater
!.$99 cm,sec
"ater Area 6oad
%.%
Safety :actor
1.&
Area of Sand #an/
Sedimentation Rate of Sand Sedimentation :actor Sedimentation Distance of Sand Retention #ime Sand #an/ 8olume ).!! m <"= >
ravityofSand
!.&
31.) m
D1
!.19+ m,min 3.!
D
!.%! m D$
1).9 mi n &1.19 m
3
&.33 m <6= >
1.!!
m
$.!!
$
=
#an/ 8olume
9$.)$ m3
8olume of #an/ 6ower Part
rits 2 Sand Amount
.&
rits 2 Sand Density
).! 4
Sand #an/ Dept? 6ift "ater of Air 6ift Pump @nection of Air 6ift Pump 6ift Up of Air 6ift Pump Air of Air 6ift Pump Diameter of #removed Ru55er "ater#emperature
Area of :loatation #an/ $!).%& m$ :loatation Rate of Ru55er :loatation :actor for Stream :loatation Distance of Ru55er Retention #ime :loatation #an/ 8olume #an/ Si;e
!.!$3 m,min &.! !.)! m 13$.9 min 913.+ m3
19.9! m <"= >
19.3) m <6= >
Ru55er Particle Amount
1!3$ /g,day
ul/ density of Ru55er
!.& g,cm3
Ru55er Particle 8olume
$.!) m3
Ru55er Particle Density
1!.! 4
6ift "ater Quantity (peration time 6ift "ater :low 9
3.!! m
)$!.&9$ m3
3.!! m
$!.) m3,day 9.! * r !.!%) m3,min
Units
:loatation #an/ Dept? @nection of Air 6ift Pump 6ift "ater of Air 6ift Pump @nection of Air 6ift Pump 6ift Up of Air 6ift Pump
3.!! m !.) m
AirofAir6iftPump! .!3!$
Average "ater :low Safety :actor Units of Pump 6ift "ater Quantity Pump #ype PowerComsumption
m3,min>Units
9
8C0 1!!0
%$-ade in #A@"AE
1!.! *p
9.!! m <"= >
3.1 m <6= >
3.!! m
1%!!/g,day
3 Units
9.&! m<"=>
9.&! m<"=>
9). m3 -6SS
!.9! (D0/g,-6SS0/g>day "=
Airation#an/Si;e
m3,min
1.) 1%.!m*
$$.& /w>*r
1&.! mi n
Airation#an/Si;e
,min
3 Units
9). m3
(D6oad
3
1.&) m3,min
Pit 8olume
Pollution 6oad
m
1.&
Retention #ime #an/ Si;e
!.1$1
1%+.& m3,*r
+.&/w #otal Power Comsumption
Units B
99.99 m<6=>
$&!!ppm
Airation #an/ 8olume 3.!! m
3.!! m
1%!!
m3 3 Units
1.& > D 9).!! m<6=>
Airation #an/ 8olume
$
3 Units 1%)3 m3
(D 6oad Airation #an/ 8olum -6SS -6SS"eig?t
1%!! /g,day 1%!! m3 $&!! ppm 9&!! /g
"ater #emperature
$%.&
(Hygen Concentration of Airation
o
SaturatedD(at$!' C
!.+! !.&! ($0/g,(D0/g !.1& ($0/g,-6SS0/g>day
(Hygen Demand of Decompostion 1/g (D Constant of Activated Sludge for Autodigestion (Hygen Demand 1&+& ($0/g,day
(Hygen Demand of after Revision
$$&3
(Hygen Demand in *our
+.& /w 9.%% ($0/g,*r>Unit
(Hygen Supply of Airator UnitsofAirator
Airator #ype
($0/g,day
3. ($0/g,*r
-#01!
PowerComsumption
1.$9 Units
#otal Power Comsumption
+.)% mg,6
1.& ppm
Dissolved (Hygen :actor
Airator #ype
%.%9 mg,6
Saturated D(
1!.! *p $! Units
1&!.! /w
AR0 3&01!!
PowerComsumption
3.+! /w 3.)9 ($0/g,*r>Unit
9. *p
$&.% Units
$) Units
(Hygen Supply of Airator UnitsofAirrator #otal Power Comsumption
Dept?ofDiffuser
).$ /w
$.&! m
(Hygen#ransfer Demand of Air
$.9 m3,min>Unit
lower#ypeR SS0
$!!
Rotate lower Capacity
3!.1 m3,min>Unit
Raw water -6SS "ater Surface 6oad Settling #an/ Settling #an/ Area Retention #ime
Delivery Air of lower
$+.)
Units
m3,min m3,min>Unit
$!! +%!r.p.m
lower Capacity
3!.1
m3,min>Unit
3!.! *p
#otal Power Comsumption
m3,min>Units
3$
& Units
PowerComsumption
!.! /w
!.3!
UnitsofDiffuser
Unitsoflower
Rotate
3!.! *p
#otal Power Comsumption
13+.%
lower#ypeR SS0
+%!r.p.m
PowerComsumption
9.1 4
Demand of Air
9 Units
Delivery Air of lower
$.&! m
(Hygen#ransfer
11+.) m3,min
Unitsoflower
Delivery Aer of Diffuser
Dept?ofDiffuser
9.% 4
11$.& /w
Delivery Aer of Diffuser
!.1&
UnitsofDiffuser
1
m3,min>Units Units
1%+.& m3,*r $&!! mg,6 1.% m3,m$>day
Surface 6oad in *our
1 U nits $$+.9 m$,Units $.& *r (ver
3
!.%$&
m3,m$>*r
9)%.% m3,Unit
Settling #an/ 8olum Settling #an/ Si;e
Direct #run/ D B
19.$1 m <6= > 1.&! m
Slope #run/ D B
1.&! m
Division ofottom
1).!! m <"= >
3.!! m
) AI
6engt? %.!!
I
9.+9
Slope #run/ 8olum
13&.$ m3
Area of #an/
$$+.9 m$
#an/ 8olum
9+).3 m3
aI
1.!!
$
Side 5I
Ds I 1.&!
9)%.% m3
A Ds
a
Ratio of Dd and Ds Dd : !.& Ds : !.&
5
Structure of t?e Settling #an/ <@magination :igure=
Amount for (verflow "eir 1m
%
(verflow "eir 6engt?
Return Sludge -6SS
%!!! ppm
-6SS
$&!! ppm
Return Sludge Amount Safety :actor
%&.$ m3,*r 1.&
6ift "ater of Pump
1$+.% m3,*r
Pump Capacity
$.13 m3,min
) Units
8C0 %!0$&
-ade in #A@"AE
PowerComsumption
&.! *p
!.)$
3.%/w #otal Power Comsumption (peration time
$9.! *r ) Units !.3)
@nection of Air 6ift Pump @nection of Air 6ift Pump
m3,min >Unit
!.) m
6ift Up of Air 6ift Pump Air of Air 6ift Pump (ne Unit
$.! m <*= !.+&
m3,min>Unit
#otal Air of Air 6ift Pump
9.&$ m3,min
Row water Quantity
3!!! m3,day
(D Airation #an/ 8olum -6SS
1%.!m*
3!.! /w>*r
Units of Air 6ift Pump 6ift "ater of Air 6ift Pump
m3,m>*
$3.9 m
!.3) m3,min
Pump #ype
)!! ppm 1%!! m3 $&!! ppm a :!.&&
ConversionRatefrom(DtoSludge
9
m3
3
1.!!
Dd
391.1
m3,min
) Units
Rate of Autodigestion (day01) Amount of Produced Sludge Return Sludge -6SS
5: %!!! ppm
Amount of FHcess Sludge
%9
m3,day
Air 6ift Pump of Sand #an/
!.3
m3,min
Air 6ift Pump of :lotation #an/
!.1$
m3,min
Air 6ift Pump of Return Sludge
9.&$
m3,min
#otal Air
@nection of Air 6ift Pump lower Capacity of Air lower#ype PowerComsumption
!.!+
)+& /g,day
&.&) m3,min
$.9 m <*s0-aH= &.&) m3,min>Unit RSS0
1 Unit
%!
m3,min>Unit
).&&
+.& *p
Rotate
13!! r.p.m
#otal Flectrical Comsumption of FKuipment
Power Comsumption of Aeration System Pump Pit Pump lower of Air 6ift Pump #otal Comsumption Return Sludge 8ertical Pump Used for 8ertical Pump
#ur5o et
Su5mersi5le
Airator
PumpAirator
1&!.!
).$
!.!
11$.&
$$.&
$$.&
$$.&
$$.&
+.&
+.&
+.&
+.&
1%!.! < 3!.! =
1$).$ < 3!.! =
1$!.! < 3!.! =
19$.& < 3!.! =
< $1!.! =
< 1&).$ =
< 1&!.! =
< 1+$.& =
&
lower 2 Diffuser
lower 2 Diffuser
Menghitung Debit Air Limbah per Hari dgn menggunakan V-Notch Debit air yg mengalir pada salurankeluar = Debit air treatment x 1.5 (Return Sludge 50%) Debit air "aktu#perasipabrik
= =
Debitairkeluar
=
4500 m3 !ari $4 am (4500$4)x1.5 $&1.$5
m3 am
'kuran #t*! 5 ! !$
40
4 !
!$
5
!
30
5 1
$ !
&
!
0 4
5
!
5 $
3
+ebarsalurankeluar ,umla! #t*!
Debit /ir 1 #t*!
= = = = = =
Debit /ir +imba! per ari
1$ m (+ebar saluran keluar lebar #t*!) - 1 ( 1$00 40 ) - 1 30 - 1 = $b! Debit air keluar ,umla! #t*! $&1.$5 $ = .0 m3 am = = =
Debit 1 #t*! x ,umla! #t*! x "aktu 2per .0 m3 x $ b! x $4 am .51.$0 m3 !ari
8iscosity of "ater SedimentationRateofSand "ater Area 6oad Safety :actor Area of Sand #an/ Sedimentation Rate of Sand Sedimentation :actor Sedimentation Distance of Sand
!.$99c m,sec
Droping Sand #an/
1.&
D1
!.19+ m,min 3.!
D
!.%! m
Sand #an/ 8olume
&1.19 m3 &.33 m <6= >
D$
1.$3
m
$.9+
=
31.) m
8olume of #an/ Direct Part
#an/ 8olume
&$.&) m3
8olume of #an/ 6ower Part
6ift "ater Quantity (peration time
$
1).& m3,day ).! 4 $+&.! m3,day 9.! *r
1 Units Sand #an/ Dept?
3.+ m
3.+!
$
Area of #an/
rits 2 Sand Density
:lotation #an/
31.) m$
1).9 min
rits 2 Sand Amount
g,cm3
$.&!
%.% m3,m$・*r
Retention #ime
).!! m <"= >
ravityofSand
g,cm3
!.%3% Centi Poi
3.9$
m3
13.19 m3
@nection of Air 6ift Pump 6ift "ater of Air 6ift Pump @nection of Air 6ift Pump 6ift Up of Air 6ift Pump Air of Air 6ift Pump
Diameter of #removed Ru55er "ater#emperature
!.) m
m3,min
3.1 m <*s= 1.& m <*= !.$)
m3,min>Units
1
Units B
!.3 m
!.$! mm7 $%.& '
Specificravityof"ater
!.&
8iscosity of "ater :loatationRateofRu55er "ater Area 6oad Safety :actor
,min
3
!.!3% cm,sec
ravityofRu55er
g,cm3
!.%3% Centi Poi !.%
g,cm3
1.9 m3,m$・*r 1.&
Area of :loatation #an/ $!).%& m$ :loatation Rate of Ru55er :loatation :actor for Stream :loatation Distance of Ru55er Retention #ime :loatation #an/ 8olume #an/ Si;e
!.!$3 m,min &.! !.)! m 13$.9 min 913.+ m3
).!! m <"= >
39.9+ m <6= >
Ru55er Particle Amount
1%!! /g,day
ul/ density of Ru55er
!.& g,cm3
Ru55er Particle 8olume
3.)! m3
Ru55er Particle Density
1!.! 4
6ift "ater Quantity (peration time 6ift "ater :low 9
3.+! m
+)&.33& m3
3).! m3,day 9.! *r !.1&! m3,min
Units
:loatation #an/ Dept? @nection of Air 6ift Pump 6ift "ater of Air 6ift Pump @nection of Air 6ift Pump 6ift Up of Air 6ift Pump
3.+! m !.) m
AirofAir6iftPump! .!3!$
Average "ater :low
m3,min>Units
1%+.& m3,*r
9
Units B
!.1$1
m
,min
3
3.+!
Safety :actor Units of Pump 6ift "ater Quantity Pump #ype PowerComsumption