&
'
(
!
" #
!
'
( )
) )
$ & *
+
! " # ! "
) *
$ &
$
) !
)
%
-& ' '
. )
!
#
/ ) !
$ &
0
12 2
! # 3 3
4
0 3 3 5 ( / " 2 * #
( ) ) * * ! + 6 # $" &
7 '8 3 ' 3
6 #
$" &
33 9 '8 8 9 3
# :;374 --7;3 -7 8 ;:9 9
* ' 8;37777 8-:;4777 '
0 1 4 8; 7 3 :;3 8;3: 3
# 9 3 :' - '3 3
1 # ' 8;- - 7 3;7 7 :;7 :8 3
1 #
$" &
- 3' 7 3'- 37 3
1 #
$ % &
38 : 7 '43 4 4 3
6 " # 94; 7 -4 7 9 3
6 , 377;:'77 37;3-7' 3' -;'8
-6 , 7-7;4: 77 3 77;3: 7
7
38 ';4'
9
8
)
$6 # &
-77; '777 9 777 7;3 9 < ';4 < 4 :
) $6
# &
3 777;:4777 47;3-47 -;4
-5 = +
:
0 3 1 5 ( / " 2 * #
&
0 $<&
2 0 20 $< &
2 0 20 $< &
0 0 $<&
20 $< &
20 $< &
* 12
C 6 . C6. $ &+
A . . . . . % . % . #
7 ' D 3 34 4' :4 D 9: 4
7 3- D 3 3 7 7' D 7 '4 87 9- D 9-
7 7 D 7 '-- ' D : 77 - 777 D 3 -77
'4 D -'-3-: 3- D 97' 374 D 3 739
38 D 88 D 4-4 7 D '33 3 D 48
3'8 3 - D 4
E !
+
$ end of pipe&
# $
&
8
,
-
'
0 !
! #
!
# !
$ &
#
+
!
9
)
* $'$
'*+
,
(
*
$ *
-! !
!
) = # * )
. "
"
7
# )
+
3 E
#
$recycle&
# !
# -;-7 <
(
#
! !
' $size&
$ @ 7
7 &
D'°1 cold storage #
!
)
! (
"
3
/ "
0 $ 1
5
(
* ! !
/
.
(
5 #
5
5 5 #
#
#
# # #
%
#
#
# #
#
6 ) ) $ &
= ) !
!
) +
3
! #
! %
!
! !
! !
"
! !
) )
!
E !
!
* $'$
'
.
'
(
(
*
,
2
$non$toxic&
#
F #
F !
. F
*
#
) ) #
$ & #
2
$ 2G & -7 3 777
2 )
2 3777
' #
E
0 !
"
) B
#
+
3 5
5
! )
) 5
5
,
'
#
% % !
-! $preventive strategy&
end of
pipe
+
A $zero discharge&
" ! )
#
# =
, ,
, ,
+
#
#
AF
! % *
4
! ) %
F
!
F +
3 E ! ! ! $shock loading&
E *
E !
' E G
F G !
0 G ! !
2
: #
# ! + discrete flocculent zone settling discrete
# flocculen !
! * !
Zone settling
#
E
sludge !
!
#
!
1 %
8 #
0
7 3 $378 & 3 $37: & 5 hydrophobic hydrophilic
1 hydrophobic 5
2 %
0 hydrophilic
%
5 - 37
1 polyelectrolyte
! ! 7 3
3 - # polyelectrolyte
0 3
#
9
0 3 ? 0 # 5
+
$/ )
( 3-7 -77 9 D 33 E
1 $2*& H 1 $*12 & → 1 12 H * 2
" 12 H 1 $2*& → " $2*& H 1 12
. :- -7 ' - D : E
. $ 2'& H 4* 2 → . $2*& H * 2'
6 1
6 1
- D 3-7 ' D : E
6 2':* 2 :7 D 77 ' D : E
6 1 H * 2 → 6 $2*& H *1
# D - 0 *
# 7 - D 3
( D 7 I J
, ,
#
) )
#
" ! !
'7
# !
. !
) ! .
$transfer& $ &
0 %
+
0 # 5 5
air diffusion> )
! !
# ! !
) D ! > !
!
# air diffusion
"
" ! K0
'3
# $ &
% E vortex baffle$ & '
# !
)
! ! 3
-E vortex
! % I J
( !
# !
,
# %
.
! 5 %
!
87 97< E
' 5
) 5
*
# . 6
= E ) . $E. & 6 @ = $6 =&
? !
1
1 !
, 4 3 !
!
-12 $ & 7 - 1 ,
3 ! ) 3 A
97<
Anaerobic Filter Reactor
!
) !
# Upflow Anaerobic Sludge Blanket (UASB)
) (
'
( #
!
# E.
! (
! ) 3-7
$ & - 37
E ! I J
! 7 4 7 9 !
5 377
3-7 ! ! 94
12 $ &
Fluidized Bed Reactor (FBR). #
5 7 777 5 !
87< ! '
12 $ &
# '
"
) ) !
) #
"
% ! $volatile fatty acid& .
% #
''
# 37<
!
1 !
+
1 *42 H * 2 → 1 *'2 H 12 H *
12 =
. % !
+
1 *'2 → 12 H 1*'
1* 122 H * 2→ 1*' H *12
*12 H '* → 1*' H 2* H * 2
# 2 3 777
#
! $ 9; 8 1&
$'9;-: 1& ,
!
#
! * 4 4 : 4 *
:
.
! * *
'-? 3 2
, , ,
+
$$ #
#
# #
E
I J
2
! 6
+
3 '
)
$
/4 *
.
* 2 * 2
* 2
'4 E
6
%
%
! 5 $ 0$ 1
5
%
) 5
. +
5 6
!
# !
! ) #
*
( )
5
':
5 .
5
%
5 .
, %
2
5
3 8 ' 4 5
L
I J
$ ' 0 1 0 !
) )
. ( 393'
% C + plug$
flow activated sludge, complete$mix activated sludge, extended aeration, oxidation
ditch system, intermittently aerated and decanted system, oxygen activated
sludge
! " # #
'8
$ # #
E
"
! .
$ #
*
!
# $
! ! 5 !
$ #
! ! M !
F )
$ # %
# .
'9
! "
E 3 !
7 34 $ & 97< (
! !
12 .
!
* )
!
# ! !
) 5
!
.
. !
. #
2 477 3 77 (
-7
5 ! #
!
. %
!
& ' ( 03 1 = 1
'7< #
3 '
# = 1 )
# !
? ! I J
$ & E ! !
= 1 +
-3
/
'-
'
(
(
*
4
'
6
) +
)
% !
! $ & 12 2
% $ &
!
/ # . ( $/#.(& 6 )
' 3
)
/
/#.(
$ & >
6 ) '
2 '
-#A"A=/5 ..B
5.=.50A=/ 0/5 (/" .* 1./=
6/ /5 5/"/. /2(2?/
5E.B0/0. (/" .* 1./= .B.(/ . *. /( #A"A=/5 ..B
5E.B0/0. (/" .* 1./=
*. /( #A"A=/5 ..5
E.B0/0. (/" .* 1./= #A"A=/5 ..5
E.B0/0. (/" .* 1./= $ A /0 (/" .*&
*. /( #A"A=/5 ..B 5.=.50A=/ 0/5
(/" .* 1./=
.B.(/ . *. /( #A"A=/5 ..B 5.=.50A=/ 0/5
(/" .* 1./=
5E.(/0. (/" .* 1./=
5.=.50A=/ 0/5 E" A=
&.*3 ) & ) & /
&.*3 / 3 6 &7 /) &
5.=A50A=/ 0/5 #AB??EB..B ./= A= /*
-#AB??EB..B
(.*.B
.1E.B / ./B 5E.(/0. (/" .* 1./=
0.B .= 5E.(/0. ./= . .B #ABA=/". 0.B .= 5E.(/0. ./= #A=A0E=.B #A" E.B?.B
(/" .* 1./=
0.0.(A0.5 52"#2BAB
(.*.B
5A0A= A /..B (.*.B
(E. (.*.B M.B? 0A= A /.
(25. / . .B ./= #ABA=/".
& )*& &7) &7 & &.*3 &7) &7 &
AB0E5 . .B ./= #ABA=/".
? + ' 5 (
)
-'
4
5
# +
) )
-# 5 !
!
0 %
--. #A5 0A5B/
8 / & 8)&* *7 8&7* / & / 3
? + ' # 0 # ( 1
.0. (/" .*
1./= 5E.(/0.
(/" .* 1./=
5E.B0/0. (/" .* 1./=
5.=.50A=/ 0/5 .B A /0 (/" .*
1./=
#/(/*.B / 0/" #ABM.(E=.B (/" .*
1./=
#/(/*.B 0A5B2(2?/ #AB?2(.*.B
(/" .* 1./=
#=2 A E= #A"/(/*.B
. #A5 B2B 0A5B/
5A.B .(.B / 0A" + #AB?2(.*.B
#ABM.(E=.B 2#A=. /2B.( 6(A5 / A(
5A0A= A /..B (.*.B 5A0A= A /..B
/.M. / 0A"
-4
4 ,
/
L 3 3
2 94 :4777
! E
12 ! 77
12 +
!
# )
+ 8
0
! !
# $ ' &
6 G = .
12 4777 Fixed Bed Reaktor !
87 < # %
0 6
12 '777
0 6
A 0 6 97 <
$
-:
4 4
/
3 /
12 -777 3 -77
E 12
> E 12
+
!
# )
+ 8
0
! !
# $ ' &
Fixed Bed Reaktor . 12 4777 Fixed Bed Reaktor !
97 <
# %
Trikling Filter
12 777
Trikling Filter
A Trikling Filter 97 <
$
-8
4 9
3
2
(
!
12 37 777 !
37
F %
3 37 5 12
37 777 !
3 777 fixed bed reactor C Fixed Bed
! %
) , $*=0& ! %
G 37 N 7 # 3-< %
%
C N % H %
C N 3
-E
2 %
8-< 9- < 3777
! 377
$ ! 0 ' 3& = #
47
0 ' 3 5 # 0 6
& "
3 2
= 7 - D 7
5 $ & 7 D 7
' * $ & 37 D '7
- 2 - 3 7 D 7
4
: " 5 )
8 6
9 # ) $ , 37 & 4 D 37
37 A 2 % $<& 8-
9-33 A ,
+ * B L , ) 0 0 .
43
0
'
$sustainable Development& !
E
!
end of pipe B metode end of pipe
# !
. #
%
! !
#
0 # ( 1 / " /
4
.
*
$
-3 . Ekspor Hasil Perikanan di Indonesia # !
" * # L # $399:&
. Polution Prevention for Fish and Shellfish Processing Industries " E A#. $3994&
/ Karakteristik Limbah dan Pemilihan Teknologi Limbah Cair #
B 0 # ( # 5
( L 3 L 3999
' . Pelatihan Penerapan Teknologi Produksi Bersih 0
( ##0 L 3; . 777
- * ! Biological Wastewater Treatment System Theory and Operation
L ) ( 3997
4 A , , Trackling Design and Performace, L A
4
*
? 3 / = # * #
4'
? ( # 5
4-? - E # ( 1 #
$# ( = # * ) D 1 L 0 &
? 4 0 # 0 #
44
? : 0 # ( . 5 '77
$ 6 G = &