Radiat. Phys. Chem. Vol. "/2 No 8-5 pp. 901-906 1988
/88/09901-06508.00/0 ~) 1988 Pergamon press Ltd
Printed in Great Britain
Effects
of
Enzymatic
Irradiation Hydrolysis
K.Kojima sumitomo
as a P r e t r e a t m e n t
of C e l l u l o s e
S.Miyake
Electric
in
Materials
I.Uda
industries,
Ltd.
Osaka,
Japan
Introduction
The w o r l d ' s fuels,
diminishing
forcing
required
energy
industrial
supply
fuels.
various Under
kinds
these
and
circumstances,
Development(RAPAD)
the M i n i s t r y
of
International
as a m e m b e r
as a p r e t r e a t m e n t some of
the
in t h e i r
of a l t e r n a t i v e
Alternatives
Electric
created
countries including
q u a n t i t i e s of energy,
to d e v e l o p
has
of R A P A D
qrowing
efforts
sources
Industry
the
of c e l l u l o s e
this
to r e p l a c e
(MITI).The
to e x a m i n e
hydrolysis
for
1980,
about
to o b t a i n
Association
e s t a b l i s h e d in May and
anxiety
to s t r i v e
all-out
energy
has b e e n
in e n z y m a t i c
Japan
the R e s e a r c h
was
Trade
a
with
effects
purpose,
petroleum
for
role
their
Petroleum support
from
of S u m i t o m o
of i r r a d i a t i o n
materials-In
this
report,
r e s u l t s are d e s c r i b e d .
Experiment
Figure c haff with
1 shows
as the m a t e r i a l s , 2 MeV
and o t h e r enzyme.
samples
Other
called
samples we used
"Onozuka".
a sugar
be a f f e c t e d
were
processes
of
10mA.
treated were
carried
After
by alkali,
and
a commercially
of g l u c o s e
for each
by the d i f f e r e n t
process.
rice
samples
generated
straw beam
and h y d r o l y z e d
the a m o u n t
acceleratoz
by an
by enzyme. cellulase
by s a c c h a r i f i c a t i o n
We e x p e c t e d
and
were milled
hydrolyzed
trichoderma viride
t y p e s of p r e t r e a t m e n t . 90]
some
then they w e r e
milled
available
Using
out by an e l e c t r o n
irradiation,
simultaneously
The a m o u n t
analyzer
we i n v e s t i g a t e d .
i r r a d i a t i o n was
and a c u r r e n t
As the enzyme,
with
the v a r i o u s
was m e a s u r e d
of g l u c o s e
to
902
K. KOJIMA, S. MIYAKE AND I. UDA
l ,..irradiation~ ' alkali I
]
treatmen~
I
milling and I saccharificat!on J
1
Fig.
l
1 Flowchart Enzymatic
of E x p e r i m e n t a l Hydrolysis
Processes
Results One
effect
milled
to small
rice
straw
save
energy
Then,
milled
the
cellulose
irradiation.
milled
for reducing the
in F i g u r e
energy
We also
into
straw
to small
tested
1 shows
simultaneous increases,
3, c o m p a r e d
to o b t a i n the
Saccharification Table
after
be e a s i l y
being
that
small
to small
materials
Figure
2 shows
particles. particles
particles,
the
could
rice
be e a s i l y
that
the
irradiated
In other words,
we
by u s i n g
this method.
s t r a w was
hydrolyzed
could
by the enzyme.
shown
less
was
particles
could
after
easily As
of i r r a d i a t i o n
effects
was
that
about
the of
carried
generating
same
out
irrdiationand
milling
in a ball mill completely
saccharification. speed
only,
milling
needed
g l u c o s e yield.
simultaneous
we can a l m o s t
m i l l i n g and the
with milling
of g l u c o s e
and enzymatic h y d r o l y s i s .
inside
change
rice
Furthermore, becomes
an air oven. straw
as the
faster.
to glucose by irradiation dose
Effects of irradiation as a pretreatment
1
~
903
O0
E
0 ";-
0
•
0
0
48 Mrod ~- ..12
g-
t
0
0
I
I
5
10
> Milling time with boll mill Fig.2
Effect
of
Irradiation
on Particle
Size
• 100
8O j[~,J
-060
A/
/,"
>., e 0
40
milling only A
~
irrodiotion end milling
O
o20
0
I
I
I
0.1
0.2
0.3
I
0.4
I
I
I
0.5
0.6
0.7
> Energy for pretrestment ( K w h / k g ) Fig.3 Table.l
Effect
of
Irradiation
Simultaneous
Irradiation
(Mrad)
dose
Milling
on G l u c o s e
and
Yield
Saccharification
Time
needed
Percent
till
I% g l u c o s e
conversion
generated
glucose 168
(Hrs)
of
hours (%)
0
24
92
24
14
89
48
Ii
95
96
7
93
of
after
904
K. KOJIMA, S. MIYAKE AND I. UDA
Another
effect
easily for
removed
rice
Figure
The
the
that
5 shows We
the
tested
find
the
lignin
of c e l l u l o s e
irradiation.
The e x t r a c t e d
of rice
straw
of
in F i g u r e
6. The
7 shows
chaff.
In the
In the
case
the
Figure
amount
was e a s i l y
materials
4 shows
increased
removed
was
the r e s u l t
by i r r a d i a t i o n ,
by a l k a l i t r e a t m e n t
the case
extracted amount
of rice
of our
than
chaff, of
the g l u c o s e
the g l u c o s e 120°C.
for
make
and e n z y m a t i c
yield
But a f t e r treatment
it c l e a r
enzymatic
yield
that
0
1.1J
I
5O -->
I0(
Irradiation dose (Mrad)
Effect
of
on L i g n i n Alkali
Irradiation Extraction
Dose by
Treatment
(IN N a O H
aq.30°C,
about
of c e l l u l o s e
3oi
0
only
irradiation
hydrolysis
at all
4.1%
15min)
are of
of rice
20% a f t e r
irradiation,
is very
the
.
at a low t e m p e r a t u r e
ID
Fig.4
at all
hydrolysis
48 M r a d ' s
0
L0
was
was
o
S ~
by i r r a d i a t i o n
by i r r a d i a t i o n
5o
E o
concentrations
at v a r i o u s t e m p e r a t u r e s
increased
20% by alkali
experiments
of p r e t r e a t m e n t
by v a r i o u s
increased
treatment
chaff,
at a h i g h t e m p e r a t u r e
results
amount
of a l k a l i
of u n t r e a t e d
was m o r e
straw
s t r a w by a l k a l i
extracted
results
of rice
of NaOH.
of n o n - i r r a d i a t e d
yield
as a f o r m
that
treatment
Figure
treatment
of t r e a t m e n t
concentrations
temperatures.
The
by alkali.
results
tested
glucose
that
treatment after
lignin
the
can
results
sho w n
treated
was
irradiation.
of NaOH. of
irradiation
by a l k a l i
straw
indicating aft e r
of
of
alkali the 30°C.
effective
materials.
Effects of irradiation as a pretreatment
60
--
96
905
Mrod i ~
50
O
E o
40
"0
0 Mrod
"6 S 3O /
x
I.iJ
o
oT0
I
0.5
1.0
---> Concenlrolion Fig.5
Effects and
of N o O H IN)
of N a O H
Concentration
Irradiation Dose
Lignin
Extraction
on
(NaOH,
70
60°C
s
48 ~.d..f :
v
6O e-
E
50 o
40
~
30 I
0
5O >
Fig.
Temperature
6 Effects
I00 (°C)
of T e m p e r a t u r e
Irradiation Extraction
Dose
and
on L i g n i n
(IN N a O H
15min)
15min)
906
K. KOJIMA~ S. MIYAKE AND I. UDA
1 Dose Temp. Time Gluco ll~yield Extroded" amount IMrod) (°C) [h) ~ ~(%) %0 {% )<
Untreated 0
e0 ~2 0
2~
30 ~0
I[ I 4"1 35.6 IIIItlllllllse ~L8.O IIIIIIIIIIIIIIIIIIIII,~.6 2~ IIIIIIIIIIIII!IIIIIIII[22~ 25.3 i llllllllllIl~62 lllll ~L2.3 Ill~9~ ,
I
•57.0
.
IIIII
p
~52.1
/! 22.9 Fig.7 G l u c o s e Yields
46.8 and Lignin
Extraction Amounts Alkali-treated
for
Rice Chaff
(IN NaOH aq)
Acknowledgment This r e s e a r c h was c a r r i e d out as a part of a c t i v i t i e s from MITI.
of RAPAD,
under a s u b s i d y
We wish to thank R A P A D for g r a n t i n g p e r m i s s i o n to p u b l i s h
this report