0146-57241811090771--075020010
Radlat Phys Chem Vol 18, No 3--4, pp 771-777, 1981 Pnnted m Great Britain
Pergamon Press Ltd
C O M P O S T I N G OF G A M M A - R A D I A T I O N D I S I N F E C T E D S E W A G E S L U D G E W Kawakaml,
S.Hashlmoto,
H Watanabe,
H.Ito and M.Takehlsa
H.Watanabe,
K.Nlshlmura,
Takasakl Radlatlon Chemlstry Research Establishment, JAERI,
Takasakl,
Gunma
370-12,
Japan
The e x p a n s l o n of s e w a g e s e r v l c e s is o n e of the c u r r e n t m a l n d o m e s t i c p o l l c l e s of J a p a n
The f ~ f t h f l v e - y e a r - p l a n ( t h e M ~ n l s t r y of C o n s t r u c t i o n )
w l l l s t a r t n e x t year.
A c c o r d i n g to the plan, m o r e t h a n 7 m l l l l o n ton c a k e is
p r e s u m e d to be g e n e r a t e d ~n 1985.
M o s t p a r t of s l u d g e h a v e b e e n b u r i e d in the
ground directly or after burning.
But recently,
t h e s e m e t h o d s are u r g e d to be
r e e x a m l n e d f r o m v l e w p o l n t s of e n v l r o n m e n t a l or e n e r g y saving. On the o t h e r hand,
too m u c h d e p e n d l n g on c h e m l c a l
c u l t u r e h a v e led to h u m u s d e f i c i e n c y in sol1. i i z e r to f a r m l a n d h a v e b e e n d e s i r e d .
s l u d g e or r a p i d
fertl-
L a n d a p p l l c a t l o n of s e w a g e s l u d g e usu-
ally beneflts plant growth and crop productlon, t a r y p r o b l e m s to the n e ~ g h b o u r ,
f e r t l l l z e r S in the a g r l -
A p p l l c a t l o n of o r g a n l c
b u t it m a y c a u s e o d o r or sanl-
and p l a n t s m a y be h a r m e d d u e to b l l g h t s
In
f e r m e n t a t l o n of s l u d g e in soll
As the u r b a n l z a t l o n of r u r a l a r e a s h a s b e e n p r o g r e s s e d and the a g r i c u l ture is t r a d i t i o n a l l y ~ n t e n s l v e ~n Japan,
the d l r e c t a p p l l c a t l o n of r a w s l u d g e
m a y n o t be a c c e p t a b l e e v e n a f t e r d l s l n f e c t l o n .
A t r e a t m e n t for s t a b l l z a t l o n
of sludge,
to be e s s e n t i a l l y n e c e s s a r y
for e x a m p l e c o m p o s t l n g ,
is c o n s l d e r e d
as w e l l as d l s l n f e c t l o n for the land a p p l i c a t i o n . R C . C o o p e r and C ° G . G o l u e k e I) m e a s u r e d the c o u n t s of v i r u s e s ,
or c o l l f o r m s ,
fecal c o l l f o r m s and fecal s t r e p t o c o c c i in the c o m p o s t l n g m a s s f r o m w l n d r o w type compostlng,
and sald t h a t c o m p o s t l n g I t s e l f m i g h t not be as e f f e c t l v e a d l s l n as h l t h e r t o b e l i e v e d T . U s u l and A . S h o 3 1 2) e x a m l n e d c h a n g e s of
fectlon method
m l c r o f l o r a w l t h c o m D o s t l n g of s l u d g e u s l n g a p i l o t p l a n t o f e n c l o s e d v e s s e l type,
and r e D o r t e d t h a t c o l x f o r m s in p r o d u c t s w e r e
found to be a b o u t 105 per
g r a m of c o m p o s t In g e n e r a l , by the b a c t e r l a l
the g r o w t h of i n o c u l a t e d m l c r o o r g a n l s m s is a f f e c t e d s e r i o u s l y flora in a m l d l u m .
t h a t the g r o w t h p o t e n t i a l of Eschertch~a J r r a d l a t e d s l u d g e i n c r e a s e d w l t h dose. salmonellas grew rapidly
For e x a m p l e ,
D . N S h a h et al. 3) r e p o r t e d
col~ s t r a i n B w h i c h w a s i n o c u l a t e d in M E . M o r r l s et al. 4) f o u n d t h a t
in i r r a d i a t e d c o m p o s t ,
b u t that the g r o w t h c o u l d be
inhlblted by saturation of collforms bacteria after irradlatlon B a s e d on t h e s e r e s u l t s , h a v e two a d v a n t a g e s :
compostlng process using irradiated sludge may
the f z r s t is the c o m p o s t l n g p e r l o d m a y be s h o r t e n e d b y
seedlnq eefectlve compostlng bacteria flora,
into s l u d g e of c o n t r o l l e d b a c t e r i a l
the s e c o n d is the c o n t a m ~ n a t l o n b y p a t h o g e n s or t h e l r r e g r o w t h c a n be
p r e v e n t e d by i n o c u l a t l o n of s l u d g e w l t h i n n o c u o u s c o m p o s t l n g b a c t e r i a . We h a v e 1978,
s t u d l e d on c o m p o s t l n g of r a d l a t l o n d l s l n f e c t e d s e w a g e s l u d g e slnce
a ~ m l n g to p r e s e n t a n e w p r o c e s s of s l u d g e c o m p o s t x n g for a g r i c u l t u r a l
uses
Th~s process
sludge,
and c o m p o s t l n g step to r e m o v e o d o r and e a s l l y d e c o m p o s a b l e o r g a n i c s in
ls c o m p o s e d of two s t e p s
i r r a d ~ a t l o n s t e p to d l s l n f e c t
sludge In thls paper,
the g a m m a - l r r a d x a t ] o n e f f e c t on s l u d g e cake and c o m p o s t ~ n g
RPCVolIS, No 3/4---Y 771
772
W KAWAKA~liet al
condltlon
of I r r a d l a t e d
informatlons
Radlatlon
Dlslnfectlon
Seasonal sludge
and
sampled klnds
the o t h e r w a s Twenty The
McConkey's
sewage
a g a r was
1 shows
change
sludge
that
the
at
process
homogenlzed
was diluted
seasonal
changes
These
are
the
sludge
of s e w a g e
were
cltles.
Two
process,
and
sludge.
and
inoculated of
in s l u d g e counts
s h o w n to be
to g r o w t h
total
medla.
bacterla,
and
samples. of b a c t e r l a
and
2x10 s to 3x109
p e r g r a m of s l u d g e
of
cake,
and
by s e a s o n s .
survlval
curves
of the y - r a d l a t l o n
exponentially
cake
Sludges
in 200 mR of s t e r 1 1 1 z e d
~n t o t a l
counts
in s e w a g e
and T a k a s a k l
30 °C for e n u m e r a t l o n
37 °C for c o l l f o r m s
300 to 500 k r a d
dewatered means
2 shows
and n e a r l y
of M a e b a s h l
2x10 7 to 2x10 8 of c o l l f o r m s
as a f u n c t l o n
by
at
cake.
and
technological
examlned.
f r o m an a c t l v a t e d
dlgestlon
solutlon
so s l g n l f l c a n t l y
Figure
level
the
In s l u d g e
to o b t a l n
and c o l l f o r m s
on t h e m w e r e
plants
one w a s
cake w e r e
used
agar was used
total bacterla,
rapldly
treatment
sludge
of b a c t e r l a
effect
f r o m an a n a e r o b i c of
in o r d e r
Sludge
counts
examlned,
supernatant
Figure
sludge
in t o t a l
were
grams
D1fco-nutrlent
not
of S e w a g e
changes
f r o m the
collforms
are d l s c u s s e d
of the p r o c e s s .
the g a m m a - l r r a d l a t l o n
of g l u d g e s
water
sludge
on d e v e l o p m e n t
wlth
dose,
It is n o t e d
is close
irradlatlon
for dose
bacterla,
Survlvlng and are
cake
reported leads
and c o l l f o r m s
col~forms
reduced
t h a t an a d e q u a t e
to the v a l u e s
of d e w a t e r e d
total
to u n d e t e c t a b l e
dlslnfectlon
for
in
dlmlnlsh
dose
s l u r r y ~ '5)
to s a v l n g
for
Thls
of r a d l a t l o n
energy. I
l
I
I
I
I
I
1
I
I
I
I
2:
31o
l
J
I
J
winter (Feb) 1
0 Maebash~ A Takasakl
~-, i lO
~-2 g_-3 ~ I
O Maebash, A Takasakt I
107!78
Dec
I
'79
I
I
I
I
I
I
Apn[ June Aug
Feb
% I
I
f
Total
cake
bacterlal Table
and t h e ± r
bacterla usually
were
counts
1 shows
radlatlon shown
radlatlon
also dlmlnlshed
sensltlvlty
to be m a l n l y but
rapldly
isolated
in p h o s p h a t e
composed they
I
IIO 115 Dose (Mrad)
20
Fig. 2 Gamma-radlatlon inactlvatlon of bacterla in sewage sludge
mlcroorganlsms
sensltlve,
05
Oct
Fig. i. Seasonal changes of counts of total bacterla and collforms
0.5 Mrad.
I
-50
wlth
from
dose,
2 Mrad
buffer.
The
of p s e u d o m o n a d s .
are p r o t e c t e d
but
in s e w a g e
slowly
irradlated
after sludge
remalnlng
Most
of t h e m are
sludge
The
Compostmg of gamma-radmUondisinfected sewage sludge
present
work
is t h e r e f o r e
deslgned
to s t u d y
the m e c h a n i s m
773
of p r o t e c t l o n .
T a b l e i. M z c r o o r g a n z s m s isolated from 2 Mrad irradlated sludge c a k e and t h e l r r a d l a t l o n s e n s l t l v l t y in p h o s p h a t e b u f f e r .
GRAM HORPHLOGYCOLOROF SURVIVALFRACTIONAT REACTION COLONIES 50 krad 500 krad HICROOOOOUS SPP(GR l)
+
COCCI
PINK/RED
6 x 10"I
2 x 10"I
HICROOOCCUS SPP(GR 2)
+
"
ORANGE
2 x 10"1
4 x 10-3
PSEUDOMONAS RADIORA
-
RODS
PSEUDOMO~VAS SPP(GR l )
"
YELLOW
6 x lO "S
........
YELLOW
2 x 10-7
........
of I r r a d i a t e d
of
3.
cake(water
4.
Mrad
uslng
ated
sludge
condltzon,
Thzs content
cake,
Co-60
was mzxed
actlvated
5-7
%) w e r e
apparatus
wlth were
has
80 %). whzch the
to r e d u c e
alumlna(30-60
used
ca.
does
not
for z s o t h e r m a l
The
other
In a e r o b l c
sludge
by I0 w t . %
was
fermentatlon.
zs a l a r g e r
One
ca.
wlth
of b a c t e r l a .
several
is s h o w n a dose The
in
of 3
irrada-
agents)
to m a l n t a l n
aeroblc
of s l u d g e
to i n i t i a t e
fermentatlon.
perllte
and the w a t e r
or d r l e d
content
compost(water
of t h e m z x t u r e
was
content 40-50
water bath
pump
zs
i0 g of
one uslng
volume
Irradlated
counts
condztlon,
fermentation.
of 50 mE u s l n g
is 13 £ zn e f f e c t a v e
the t o t a l
meshes),
as a d d l t l v e s ,
even
to i n z t l a t e
a reactor
~ddltzves(bulklng added
start
seed b a c t e r l a
apparatu=
experzments,
source
and s e e d s
The
sludge
the r e a c t o r
In these
Cake
zncludlng
of e x p e r l m e n t a l
in F l g u r e
kg of s l u d g e
Sludge
irradlated
starters
Two klnds
Flgure
1 x lO "8 ........
"
we a d d e d
sludge
I x lO "7
PS~./DOMO~AS SPP(GR 2)
Compostlng
shown
WIIITE
XIL4NTIIOMONAS SPP
Compostlng
hence
PINK/RED 2 x 10"I
"
humidfl=,er
reacter Fig. 3. Experzmental apparatus for zsothermal fermentatlon.
Fig. 4. Reactor system of the larger experlmental apparatus.
774
%.
W KAWAKAMIet al
T h e pH of t h e m z x t u r e w a s m e a s u r e d
water,
and found
humzdzfzed
to b e 7-8.
Fermentatlon
zn t h e e x h a u s t gas.
condltlons
commerczal
analyzers
type
on eompostlng,
in t h e r e a c t o r ,
to k e e p the m z x t u r e
aerobzc and
CO 2 and NH 3 eoncentratzon
865 w e r e used.
t h e e f f e c t s of i r r a d z a t l o n ,
5 s h o w s r a t e s of C O
The
fermenting
lnztlal batch, k z n d s of
was placed
Experzments were
temperature
and other
a n d t h e f e r m e n t l n g a b i l i t y of v a r l o u s
seeds and composts produced.
Figure seeds.
flow rate
was observed by measurlng
Beckman
c a r r l e d o u t to e l u c l d a t e
in s l u r r y b y a d d l n g 5 t l m e s w e z g h t of
the mlxture
azr was blew at a constant
moistened.
reaction
After
seeds.
on
zn c o m p o s t l n g b y v a r l o u s
commerclal
are s h o w n to b e v e r y d l f f e r e n t
in t h e
20
Repeated use as s e e d s w a s
f o u n d to i m p r o v e as d e s c r l b e d
evolutlon
a b z l z t y of s e e d s
dependlng
of t h e p r o d u c t
2
the a b l l l t y
below. m
Flgure
6 shows
of t e m p e r a t u r e uszng
the
the effect
on compostlng
s e e d A.
~ 10
It is n o t e d o~
that the optlmum
temperature
for f e r m e n t a t i o n
is a r o u n d
°C
In o r d l n a r y
compostlng,
u
50
processes
for
it ~s e s s e n t l a l l y
necessary
to m a l n t a l n
the fer-
mentatlon
temperature
hlgher
0
0
10
20
30
I
I
I
i
I
I
40
50
60
70
80
90
Ttme(hr)
than about 65-70 certain period pathogens
in s l u d g e .
process using sludge,
°C for a
Fzg 5. Rates of CO 2 evolutzon zn compostzng by varlous cormnerclal seeds(A,B,C)
to r e d u c e
zrradlated
o n t h e o t h e r hand,
is n o t n e c e s s a r y dlslnfectlon
condltlons,
c a n be o p e r a t e d conditlon
irradiation
at
for f e r -
is e x p e c t e d
s h o r t e n the c o m p o s t l n g Figure
2o
hence
the optlmum
and
it
to c o n s l d e r
the p r o c e s s
mentatlon,
sludge(3 Mrad) i0 g, addltlve i0 g, seed 1 g, azr 50 mZ/mln, temperature 40 °C
In the
PC 15
to
tlme.
7 s h o w s e f f e c t s of and seed addltion
on compostlng.
As unlrradi-
o~
ated sludge contalns various 5 microorganisms, ferment
it s t a r t s to
lmmedlately
by
under aeroblc condltlon
]
itself and at 0
l o w e r t e m p e r a t u r e (curve I) . For hlgher
temperature
t a k e s t l m e to s t a r t tlon(curve
2).
Curves
3 and
4 s h o w t h e r a t e s of C O e v o 2
[
i
i
i
i
i
i
20
30
40
50
60
70
80
T=me(hr)
it
fermenta-
i 10
Fig
6
Effect of temperature on compostlng sludge(3 Mrad) i0 g, addltlve i0 g, seed A 1 g, air 50 m£/mln
90
100
Compostmg of gamma-radmtlond,slnfected sewage sludge
l u t l o n In c o m p o s t l n g
of u n l r r a d l a t e d
sludge ,
uslng
seeds(composts).
hlgher
775
i
,
l
i
i
I
I
30 40 TIME(hr)
50
60
T h e r a t e ~s m u c h
than that uslng
no seed.
3[
Irradl-
ated sludge does not ferment even underaerobic condltlon(curve
5).
seeds,
the fermentation
s t a r t s as s e e n in
curves
6 a n d 7.
there
As
shown by Figure
is n o r e m a r k a b l e
r a t e s of c o m p o s t l n g un~rradlated used.
By addlng
of
sludges,
d~fference
in t h e
irradlated
and
The other mlscellaneous
speclal
bacterla
for compost~ng,
wlth
and m~xlng
, !
thls process for obta~nlng
a small quantlty
a l a r g e a m o u n t of s l u d g e .
mentlng
can be used
experlments, tlme were sludge,
serlously
In o r d l n a r y
processes,
chaff,
increase.
Further,
densltles
c a r r l e d o u t at 50 °C.
affected by fermentatlon
aeroblc condltion
are very
as t h e s e c a n b e o b t a l n e d
small,
8 s h o w s t h e r a t e s of C O
carbon
the amount
are deslrable
so c o u n t s o f b a c t e r i a
5 to 7, a n d t h e r a t e s
in s l u d g e to c a r b o n d i o x i d e
a r e v e r y hlgh.
is c a l c u l a t e d
added are
Repeated
The converslon to be
of
20 to 30 % f r o m
carbon dloxlde.
s h o w n in F i g u r e
5.
f o u n d to b e
seriously
or physical
s l m l l a r as t h e p a t t e r n
~n i s o t h e r m a l
compost-
T h e r a t e of C O 2 e v o l u t l o n
to t h a t of t h e s m a l l e x p e r i m e n t s .
temperature
So compostlng
f r o m p o l n t of s l u d g e t r e a t -
~s s h o w n to i m p r o v e i t s s e e d a c t i v i t y .
the large reactor
evolutlon was
to b e a d d e d f o r
o n l y in s e a s o n a n d t h e b u l k
9 s h o w s t h e r a t e s of C O 2 a n d N H 3 e v o l u t l o n
nearly equal
t h a n 20 h o u r s of
certaln seed actlvlty.
b u t t h e s e m a k e w e l g h t of p r o d u c t
as s l u d g e cake,
In F i g u r e s
of e v o l u t e d
Figure
aeration,
7 3 B 2
e v o l u t l o n In c o m p o s t l n g u s i n g d r i e d 2 to k e e p t h e s l u d g e a e r o b l c . The drled compost
added by the same amount
larger than cases
very
such addltlves
as s e e d s a n d a d d i t i v e s
u s e of t h e p r o d u c t
and more
large area for storage are needed.
ment.
Figure
tlme,
s t r a w or b a r k a r e p r o p o s e d
uslng
• ng u s l n g
70
T h e r a t e of C O 2 e v o l u -
for obtaznlng
in t h e r e a c t o r ,
method wlthout
organlc
sludge I0 g, addltlve i0 g, alr 50 mZ/mln, temperature 50 °C (curve 1 40 °C), curves 1 2 3 4 5 6 dose (Mrad) 0 0 0 0 3 3 seed(compost A,B) A B - A (g) 0 0 2 2 0 2
for varlous
f o u n d to b e n e c e s s a r y
malntalnlng
was
|
a d d e d as s e e d s to t h e i r r a d l a t e d
fermentation was
composts
!
Fag 7. Effects of irradlatlon and seed (compost A or B) addltlon on compostzng
of s e e d s
In t h e s e
and fermentatlon were
tlon was
i
20
those
also exam-
fermented
,'~ 10
O0
the compost pro-
as s e e d s .
sludges
suffers
The fer-
a b 1 1 1 t y of c o m p o s t w a s
I n e d to c l a r l f y w h e t h e r duced
",.
seeds are always re-
serlous dlsadvantages seeds
on compost-
seeds.
If n e w s p e c i a l qulred
~-2C
so l o n g as s e e d s a r e
in s l u d g e h a v e no b a d i n f l u e n c e ing u s l n g
30
7,
In t h e s e e x p e r i m e n t s ,
affected by physlcal
s t a t e of s l u d g e ,
of C O 2 e v o l u t l o n u n d e r
condltlon
is
NH 3
s u c h as
a n d a l s o f o u n d to b e c o m e good condltlons,
differently
hltherto reported. Experlments was
of a d l a b a t l c
s m a l l e r t h a n in i s o t h e r m a l
fermentatlon were fermentation
that both CO 2 and NH 3 evolutlon,
measures
a l s o c a r r l e d out,
at 50
°C.
of degradation
but the rate
Those results mean of e a s i l y d e c o m p o s -
W KAWAKAMI et al
776
able organics
and deodorlzatlon
the o p e r a t l o n
condltion
The perlod
compostlng
of i r r a d l a t e d
and lower temperature
examine
respectlvely,
is k e p t g o o d
the q u a l i t y
sludge
,3o
tst
~ ~
as m e n t i o n e d
for a g r l c u l t u r a l
repeat
2~ ..... 3rd
after about
3 days,
when
compostlng.
c a n be p e r f o r m e d
in t h l s p r o c e s s
of product
cease
in i s o t h e r m a l
in r a t h e r above,
short
p o t t e s t s to
u s e s are p l a n n e d .
t
:
|
,
O4
i
,,
-----
,
I
i
i
03
02z
l8 2o
e,o /
0
0
I
I
i
I
I
i
10
20
30
40
50
60
70
"'"
o,
30 40 50 60 70 TIME(hr) F i g . 9. Rates of CO2 and NH3 e v o l u t i o n i n 10
Fig. 8. Effect of repeated use of drled compost as seed and addlt~ve on compostlng.
20
compost~ng uslng the larger reactor sludge(3 Mrad) 4 kg, addltlve (perl~te) 1 kg, seed(compost) 400 g, alr 4 5 Z/mln, temperature 50 °C
sludge(3 Mrad) i0 g, compost i0 g, alr 50 m£/mln, temperature 50 °C
Conclusions
Sewage is m a i n l y plant
sludge disposal
composed
growth
sludge compatible
is m o s t thls
environmental,
promlslng
study,
condition
of
irradlated
application
to a g r i c u l t u r a l
and sanitary problems.
In o d e r to
a n d to u s e it as a s a f e s o l l c o n d i t i o n e r ,
it b y a e r o b i c c o m p o s t l n g
the g a m m a - r a d l a t l o n
Sludge
of sludge usually benefits
B u t the d l r e c t
agricultural
to p l a n t s
to c o n v e r t
in u r g e n t n e e d o f r e s o l u t i o n .
and appllcatlon
and crop production.
land may cause make
is a p r o b l e m
of organics,
dlslnfectlon
sludge were
of
examined.
into
sludge cake The
it
living humus.
In
and c o m p o s t l n g
following conclusions
were
obtained (I) A n a d e q u a t e d l s l n f e c t l o n value
is c l o s e
leads
to s a v l n g o f t o t a l
(2) W h e n
to t h a t
seeds are
dlfference
is
radlatlon
used
300 to 500 k r a d
for s l u d g e cake,
The irradlatlon
of dewatered
to i n i t i a t e
fermentation,
of unlrradlated
sludge does not ferment by itself,
Compost
produced
c a n a c t as
seed~.
and bulking
(4) T h e o p t i m u m
compostlng evolution
is a b o u t
condltlon
50
°C.
in the p r o c e s s
can be carried out in the i s o t h e r m a l
(5) N H 3 e v o l u t l o n
cake
is no r e m a r k a b l e
and lrradlated
sludges.
as a s t a r t e r
are
Repeated use of the product The drled
compost can be
agents.
temperature
sider dlslnfection
there
and s e e d s
seeds has no bad influence on the seed actlvlty u s e d as s e e d s
and thls
sludge
energy.
in t h e r a t e s o f c o m p o s t l n g
(3) I r r a d i a t e d needed
dose
for s l u r r y .
at t h e o p t i m u m
fermentation
is c o n s l d e r e d
As
it is n o t n e c e s s a r y
uslng irradiated temperature.
Is h i g h e r
to o c c u r at a l m o s t
than the
sludge, The
to c o n the
rate of CO 2
in t h e a d l a b a t l c . s a m e t l m e as C O 2, a n d
as
Compostmg of gamma-radiation disinfected sewage sludge
777
both CO 2 and NH 3 evolutlon cease after about 3 days at the o p t l m u m condtlons. References (i) R.C.Cooper and C.G.Golueke,
Compost S c l e n c e / L a n d Ut111zatlon,
20(2),
29
(1978). (2) T.Usul and A,Sho31 , presented at the 17th annual m e e t l n g of the Japan Sewage Works Assoclatlon, (3) D.N.Shah, Foundatlon,
Tokyo(1980).
A.J.Slnsky and J.G.Trump.
a report to the U.S.Natzonal
Sclence
NSF Grant E N V 77-10199(1979).
(4) M.E.Morrls,
J.S.Slvlnskl,
J.R.Brandon,
K . S . N e u h a u s e r and R.L.Ward,
the
Proceedlngs of the 3rd Internatlonal C o n f e r e n c e of ESNA W o r k l n g Group on "Waste Irradlatlon",
Brno(1978).
(5) A Suess and T.Lessel,
Radlat. Phys. Chem., 2, 357(1977).