Wet oxidation pretreatment for the increase in anaerobic biodegradability of newspaper waste
-
Upload
martin-fox -
Category
Documents
-
view
214 -
download
0
Transcript of Wet oxidation pretreatment for the increase in anaerobic biodegradability of newspaper waste
Bioresource Technology 91 (2004) 273–281
Wet oxidation pretreatment for the increase in anaerobicbiodegradability of newspaper waste
Martin Fox, Tatsuya Noike *
Department of Civil Engineering, Graduate School of Engineering, Tohoku University, Aoba 6, Sendai 980-8579, Japan
Received 23 December 2002; received in revised form 10 May 2003; accepted 30 June 2003
Abstract
Wet oxidation was investigated for its process performance on methane fermentation of newspaper waste. The mechanisms of
solubilization of newspaper waste were investigated using the following criteria: destruction of total COD (TCOD), production of
soluble COD (SCOD), production of volatile fatty acids, production of soluble carbohydrates, production of soluble lignin de-
rivatives (SLD), production of furan (F) and destruction of lignin and cellulose. Wet oxidation was carried out at 170, 190, and 210
�C, with a retention time of 1 h. The highest removal efficiencies of TCOD and cellulose were achieved at 210 �C, approximately 40%
and 69% were destroyed, respectively. On the other hand, highest lignin removal efficiency was achieved at 190 �C in which ap-
proximately 65% was removed. Batch methane fermentation tests were performed in 2–l glass bottles filled with the wet oxidized
newspaper samples. Methane fermentation of newspaper pretreated at 190 �C gave the highest CH4 conversion efficiency (59% of the
initial TCOD was recovered as CH4 gas). Anaerobic cellulose removals varied from 74% to 88%.
� 2003 Elsevier Ltd. All rights reserved.
Keywords: Wet oxidation; Holocellulose and lignin solubilization; Methane conversion efficiency; Anaerobic cellulose degradation
1. Introduction
The amount of municipal and industrial waste is in-
creasing year by year. As a result, existing landfill sites
are rapidly running out of space and secondary pollu-tion is becoming a serious problem. Landfilling affects
the environment by leaching and emitting greenhouse
gases (Harf et al., 1999).
Recycling, incineration and other pre-treatment and
treatment processes are necessary to reduce the volume
of municipal and industrial solid wastes. Although, the
cost of recycling or zero waste operations is becoming
competitive with that of such traditional waste disposalmethods as landfilling and incineration, recycling must
be improved through technological developments and
for papers, by a social agreement to prefer paper made
with recycled papers. The utilization of recycled fibers in
Japan is about 53% and is expected to increase up to
55%. Almost 90% of raw materials for paperboard
production are derived from recycled fibers (Meshit-
*Corresponding author. Tel.: +81-22-217-7468; fax: +81-22-217-
7465.
E-mail address: [email protected] (T. Noike).
0960-8524/$ - see front matter � 2003 Elsevier Ltd. All rights reserved.
doi:10.1016/j.biortech.2003.06.001
suka, 1999). However, incineration processes as a dis-
posal route are applied to reduce those fractions of
discarded waste paper which are not recyclable any-
more. The ashes generated are then filled into a landfill
(Lay, 1997).In combustion processes, up to 50% of the known
dioxins may be derived from municipal waste incinera-
tors. Therefore, high processing technologies are indis-
pensable to avoid the production of such highly toxic
compounds (Sako, 1997).
New technological efforts are necessary to reduce the
volume of the organic fraction of solid waste. A variety
of biological and thermal processes are available for theconversion of biomass to energy resource (Jerger et al.,
1982), and research on mesophilic anaerobic bioconver-
sion of agricultural and wood residues has contributed to
much of the advancement in the understanding of ap-
plying bioconversion to lignocellulosic wastes (Clarkson
and Xiao, 1999). Crystallinity and lignification are by far
the most important factors of the susceptibility of cell-
ulosic materials to enzymatic and bacterial conversions(Cowling and Kirk, 1976). Therefore, enhancement of
the total accessible surface area of cellulosic substrates
can contribute to the creation of more effective pre-
treatments for lignocellulosic materials.
274 M. Fox, T. Noike / Bioresource Technology 91 (2004) 273–281
The process in which an organic material is oxidized
with gaseous oxygen in water is called �wet oxidation’
(Sorensen et al., 1990). In the case of lignocellulosic
materials, the wet oxidation process disrupts and oxi-
dizes cellulose and lignin to CO2, H2O, and carboxylic
acids (Bjerre et al., 1996).
This paper reports the effectiveness of wet oxidation
on the methane fermentation of newsprint and theevaluation of it as a new alternative treatment process.
2. Methods
2.1. Wet oxidation pretreatment experiment
Tests were conducted to study the reaction mecha-
nisms and to characterize the products of the wet oxi-
dation process. Ordinary newsprint was used as paperwaste material for the evaluation of wet oxidation. One
of the popular newspapers in Japan �Asahi’ was used.
This material in a dry weight basis contains 54% cellu-
lose and 16% lignin (Fox, 2000). Hand shredded news-
print (20 g) was added individually to 1–l distilled water.
Subsequently, using a blender machine the preparation
was homogenized to form a slurry. Table 1 shows the
different slurry volumes filled into the autoclave. In or-der to improve the contact between gas and liquid
phase, mixing of the reactor was achieved by means of a
shaft impeller. Heating was performed using a heating
jacket. Pressurized air was supplied from a compressor
and during all the runs, the autoclave internal pressure
was maintained above the vapor pressure of the liquid in
order to ensure that the reaction would only occur in the
liquid phase. After the processing period, a sample wasremoved from the vessel and a portion was filtered in a
Kiriyama Roto apparatus using a 4 lm pore size filter.
The filtrate (liquor) was collected and kept for analysis
Table 1
Reaction temperature, autoclave total pressures, slurry volumes, stoichiometr
batch experiments
W.O. run label Newsprint
T (�C) a.t.p.a (kg/cm2) Slurries (ml) O
R-1 170 31.0 335 8
R-2 190 40.9 366 8
R-3 210 51.1 379 9
Batch label Initial pH TCOD (g/l) S
R-1 B-1 7.03 9.72 1
R-2 B-2 7.03 9.96 2
R-3 B-3 7.02 9.86 3
aAutoclave total pressure.bOxygen demand of the slurry (liquid phase).cGas phase volume of the autoclave.dOxygen supplied for oxidation (oxygen dose).e Stoichiometric oxygen factor.
of volatile fatty acids, sugars, and heterocyclic and sol-
uble lignin derivatives. The filtered cake (solid fraction)
was frozen with ethanol at )40 �C, freeze dried, and
dried in a vacuum oven at 40 �C–24 h for lignin and
cellulose determination.
2.2. Anaerobic biodegradability experiment
The anaerobic seed sludge for each batch reactor wastaken from a wastewater treatment plant located in
Yamagata City, Japan. The batch series was performed
in 2–l working volume glass bottles and incubated at
mesophilic condition (35 �C). A total of four batches
including the blank bottle was conducted using the wet
oxidation effluent as the sole substrate. Appropriate
quantities of seed sludge (300 ml) and wet oxidized
newsprint effluents (450 ml) were added to each vial, andsubsequently supplemented with 300 ml of phosphate–
vitamin–mineral solution (medium). Final volumes were
adjusted with distilled water to ensure equal initial total
COD concentration in each run (see Table 1). The
composition of the salt–vitamin mixture was adopted
from Khan (1977). To maintain anaerobic conditions
during the preparation of the batch assays, the bottles
were flushed with 20% CO2 and 80% N2 mixture for 2min. The pH of the vial contents was adjusted to 7. The
control vial was then supplemented with 300 ml digested
sludge and 700 ml distilled water and pH was adjusted
to 7. Following this, gas productions (by syringe mea-
surement) were monitored daily over 60 days until
methane production ceased.
2.3. Analytical methods
Lignin content in newsprint and filtered cakes ob-
tained from the filtration of newsprint wet oxidized ef-
fluents were determined by the Klason 72% sulfuric acid
ic oxygen conditions for newsprint slurries and initial conditions for the
2b (g) g.ph.c (l) O2
d (g) s.o.f.e (%)
.21 0.425 1.63 19.9
.97 0.394 1.76 19.6
.29 0.381 1.82 19.6
COD (g/l) Cellulose (g/l) Lignin (g/l)
.59 2.21 0.742
.34 1.89 0.478
.12 1.43 0.571
M. Fox, T. Noike / Bioresource Technology 91 (2004) 273–281 275
digestion procedure. Once methane fermentation tests
were concluded, bottles were opened and batch liquor
contents were kept for further chemical analysis. Before
the lignin content of batch liquors was determined,
samples were successively extracted using 80% aqueous
ethanol and water at 40 �C. This process removes low
molecular weight carbohydrates, soluble salts and pro-
teins were removed from these extractions (Iiyama et al.,1994). Cellulose concentrations were determined using a
colorimetric method (Updegraff, 1969). Chemical oxy-
gen demand (COD) by a closed reflux method and
suspended solids concentrations were determined ac-
cording to the procedures described in the Standard
Methods (APHA, 1995). Sugar composition of the wet
oxidation liquor was analyzed by high-performance
liquid chromatography (HPLC; Shimadzu, Kyoto,Japan) with refractive index detection (Shimadzu).
Separations were performed on a Biorad (Hercules, CA)
Aminex HPX-87P column (300 · 7.8 mm i.d.) at 85 �Cusing pure water as the mobile phase (0.6 ml/min). The
samples were filtered (0.22 lm) prior to HPLC analysis.
Furfural, 5-hydroxymethyl furfural (HMF) and soluble
lignin derivatives were analyzed at 55 �C using a Biorad
(Hercules, CA) Aminex HPX-87H column (60 �C).Furan is defined as the arithmetic sum of furfural and
HMF. These compounds were separated using a mobile
phase consisting of 0.005 M sulfuric acid (84% v/v) and
CH3CN (16% v/v) at an elution rate of 0.5 ml/min. Total
soluble lignin derivatives is defined as the sum of indi-
vidual peaks eluting in the regions corresponding to the
compounds being determined. These compounds were
separated using the same mobile phase as for furfuraland HMF at an elution rate of 0.35 ml/min. All peaks
were quantified using a variable-wavelength UV detec-
tor (210–300 nm). Methane and carbon dioxide were
measured using a gas chromatograph (GC, Shimadzu
8A) equipped with a thermal conductivity detector
(TCD) and 2 m stainless steel column packed with Po-
rapak T (50/80 mesh). Helium was used as the carrier
gas at a flow rate of 30 ml/min. Volatile fatty acid (VFA)concentrations were determined using gas chromato-
graphy (GC, Shimadzu 14B) with a flame ionization
detector (FID) and a 2 m glass column packed with
Unisole F-200 (30/60 mesh). Cellulose, lignin, total
COD, and soluble COD were determined in triplicate
samples.
3. Results and discussion
3.1. Wet oxidation performance
In order to understand the mechanisms and perfor-mance of the wet oxidation of newsprint, it was neces-
sary to observe (at the temperatures of 170, 190 and 210
�C) the following: destruction of the total chemical oxy-
gen demand (TCOD), production of soluble chemical
oxygen demand (SCOD), generation of organic acids
(volatile fatty acids), production of sugars derived from
holocellulose solubilization, production of soluble com-
pounds derived from lignin solubilization, heterocyclic
compounds like furfural and HMF, and cellulose and
lignin destruction.
In the wet oxidation tests a solution with 2% news-print and an initial TCOD concentration of 24.5 g/l was
used. The reduction of TCOD is shown in Fig. 1A. As
shown here, the gap between the dotted line and the
COD trend represents the destroyed fraction at each of
the respective temperatures. At 170 �C the oxidized
fraction reached approximately 13%; at 210 �C it
reached its highest––40% (see Table 2). Calculation of
the stoichiometric oxygen values for newsprint slurriesrevealed a maximum requirement of approximately 20%
O2. This requirement was given through compressed air,
which was injected into the wet oxidation vessel. As
shown in Table 1, stoichiometric oxygen conditions were
calculated taking into account the O2 available in the
gas phase of the reactor as well as the O2 in the slurry
necessary for complete oxidation (liquid phase). The
reason why the destruction of TCOD at 190 and 210 �Cappears with greater values than those of the stoichio-
metric requirements is perhaps due to the experimental
method of COD for phenolic compounds was underes-
timated. In other words, the potassium dichromate
COD method used in this analysis did not completely
oxidize the soluble monomers resulting in lower values
for the SCOD. Therefore, the contribution to TCOD of
the effluent is lower and therein the removal efficiency ofCOD appears to be overestimated. A solution of this
problem would be to make a balance in the carbon base
instead of the oxygen base.
Fig. 1A shows how newsprint was solubilized at the
tested temperatures (solubilization ratio %). The soluble
fraction at each temperature represents a group of sev-
eral soluble organic compounds produced through the
solubilization of lignin, hemicellulose and cellulose. Fig.1B–E shows organic acids (volatile fatty acids), sugars
(solubilization of the carbohydrate fraction of cellulose
and hemicellulose), soluble lignin derivatives (lignin
solubilization) and heterocyclic (thermal decomposition
of cellulose and hemicellulose). An increase in the sol-
ubilization ratio was expected to be a result of the rise of
the level of acidification of the newsprint slurry inside
the autoclave reactor. According to McGinnis et al.(1983) the softening of wood fiber in subcritical water
exposes lignin, hemicellulose and cellulose to acid reac-
tions. Acidification increases as the temperature rises
and produces more organic acids. As in this work,
Brauns (1952) revealed that a mild hydrolysis condition
of lignocellulose produces acetic and formic acids. These
acids may be formed from the acetyl and formyl groups
of lignin. At 170 �C the generated soluble COD reached
Table 2
Wet oxidation destruction efficiencies for newsprint
Destruction efficiencies (%)
170 �C 190 �C 210 �C
TCOD 13 33 40
Cellulose 38 57 69
Lignin 34 65 61
Fig. 1. Several trends for wet oxidized newsprint. (A) Total, soluble COD and solubilization rate; (B) acetic acid; (C) sugars; (D) lignin soluble
derivatives; (E) furans and (F) cellulose and lignin concentrations after wet oxidation (the results are means of three replicates and error bars
represent the standard deviation).
276 M. Fox, T. Noike / Bioresource Technology 91 (2004) 273–281
approximately 4.5 g/l and at 210 �C reached 6.5 g/l. A
solubilization ratio of 29% was attained at 210 �C (Fig.
1A). The final pH value at this temperature was 3. This
result coincides with that by McCarty et al. (1976) in
which organic refuse treated at 200 �C at pH 1 resulted
in 40% of soluble compounds. The result of a low pH
(acid condition) of refuse solubility was attributed to the
fact that the solubilization of cellulose and hemicellulosewas easier than lignin. With regards to the production of
organic acids like acetic, formic, propionic, butyric, iso-
butyric, valeric or iso-valeric, only acetic acid was
identified through the tested temperatures (Fig. 1B).
Concentrations varied from 0.21 g/l at 170 �C to 0.55 g/l
at 210 �C.Hemicellulose exists together with lignin and cellulose
in the fraction of municipal solid wastes through thefraction of paper wastes. The structure of hemicellulose
is thermally or chemically easier to hydrolyze than cel-
lulose (McCarty et al., 1976). Despite the fact that in this
work hemicellulose was not directly determined, it is
believed that the hemicellulose exists together with lig-
nin and cellulose as the main structural polymers of
ordinary newsprint.
From the soluble fraction some sugars were identified
(Fig. 1C). It clearly demonstrated that cellulose and
hemicellulose in low pH were solubilized to result insoluble compounds of lower molecular weight. Cellulose
was probably depolymerized to yield glucose. This is the
final compound of the cellulose hydrolysis. Glucose
forms the cellobiose structure which in turn forms the
cellulose polymer. Cellulose is a linear homopolymer of
several thousand DD-glucose units linked by b-1,4-glu-cosidic bonds (Chynoweth and Pullammanappallil,
1996). Glucose concentration increased from 0.05 g/l at170 �C to 0.5 g/l at 210 �C. It was observed that glucose
linearly increased as the temperature rose, indicating
that the production of this compound depended upon
the degree of acidity of the medium and instability of
cellulose. Hemicellulose could also serve as the source
for glucose production. Regarding the behavior of the
solubilization of the hemicellulose, its presence as a
structural polymer in newsprint was detected by theidentification of several monomers (xylose, arabinose,
and mannose). Bjerre et al. (1996) defined the hemicel-
lulose as a less stable lineal structure in subcritical
conditions than the cellulose. Hemicelluloses are com-
posed of both linear and branched heteropolymers of DD-
xylose, LL-arabinose, DD-mannose, DD-glucose, DD-galactose
and DD-glucuronic acid, and therefore, the products of
M. Fox, T. Noike / Bioresource Technology 91 (2004) 273–281 277
depolymerization are the monomers that make up the
hemicellulose polymer (Chynoweth and Pullammanap-
pallil, 1996). Despite that the instability of hemicellulose
at the tested temperatures was not studied, it seemed
that at 190 �C more solubility was achieved. At this
temperature, arabinose, xylose, and mannose reached
their maximum concentrations; 0.05, 0.1 and 0.3 g/l,
respectively.As described before, newsprint led evidence to the
production of heterocyclic compounds. Martinez et al.
(2000) indicated in their work that complex structures of
soluble compounds, which were partly inhibitory in
bacterial cultures, were produced during the acid hy-
drolysis of cellulose and hemicellulose at mild or low
temperatures. These compounds may include furfural
and 5-hydroxymethyl furfural. Yuan and Chen (1999)indicated that some furan compounds, which are kinds
of heterocyclic compounds, were found in several food
systems by thermal decomposition of sugars and
ascorbic acid. HMF and furfural are the main products
of the hydrolysis of hexoses and pentoses, respectively.
Fig. 1E shows these compounds detected at 280 nm. The
arithmetic sum of the concentration of HMF and furf-
ural represents the concentration of furan. This con-centration increased from 0.006 g/l at 170 �C to 0.065 g/l
at 210 �C. Contrary to the work of Bjerre et al. (1996) in
which experimental results showed that wet alkaline
oxidation of wheat straw did not produce furan, news-
print in acid conditions did produce it. This difference
may be due to Bjerre’s addition of alkalinity.
McCarty et al. (1976) pretreated lignocellulosic waste
at several temperatures with sodium hydroxide (pH 13)and chloridric acid (pH 1). The compounds produced at
pH 13 showed a higher solubilization ratio than those at
pH 1. Unfortunately, the nature of the soluble fractions
was not experimentally determined to understand the
behavior of holocellulose and lignin solubilization.
However, in general terms, it can be concluded that
holocellulose solubilization is enhanced at acid pH; on
the other hand, lignin solubilization is enhanced at al-kaline pH.
In this study, the phenolic nature of the soluble
fraction of wet oxidized newsprint was characterized
and determined. These lignin derivatives were quantified
Table 3
Production of soluble lignin derivatives (SLD) and furan (F) detected at 210
g/l (210 nm)
T (�C) vOHa vCb 4-MTLc p-HYAD
170 0.215 0.000 0.020 0.048
190 0.486 0.000 0.016 0.024
210 0.312 0.010 0.021 0.030
aVanillyl alcohol.b Vanillic acid.c 4-Methylcatechol.d p-Hydroxybenzaldehyde.
with an UV-variable wavelength detector at 210 nm.
Fig. 1D shows the total concentration of SLD at the
tested temperatures. This total concentration is given by
the arithmetic sum of each determined compound at
the tested temperature. The following lignin mono-
mers were chosen to characterize the phenolic nature of
the wet oxidized newsprint: hydroquinone, vanillyl al-
cohol, p-hydroxybenzoic acid, vanillic acid, syringicacid, 4-methylcatechol, p-hydroxybenzaldehyde, guaia-
col, vanillin and syringaldehyde. Only four monomers
were identified. These concentrations are shown in Table
3. Vanillyl alcohol presented considerably higher con-
centrations compared with the other compounds, vary-
ing from 0.215 g/l at 170 �C to the maximum
concentration of 0.486 g/l at 190 �C and decreasing to
0.312 g/l at 210 �C. The pathways in which newsprint-lignin was solubilized (or degraded) from its structural
monomers to the phenolic compounds previously de-
termined were unknown. However, despite that these
mechanisms remained uninvestigated, the cause of sol-
ubilization was due to the fact that these soluble prod-
ucts were produced through a cascade of solubilization
reactions. This process gradually changed from neutral
pH towards acid conditions and produced the acid hy-drolysis. With regards to the lignin structure of news-
print, this should be similar to its precursors (i.e.
softwood). Newsprint in Japan is formed mainly by re-
cycled newsprint and when the fiber exhausts its internal
strength after 4 or 5 recycle operations, new fresh fibers
or pulp are replenished for newspaper making. Fresh
fibers are mainly made of thermomechanical pulps and
Kraft pulp (Iiyama, 1999). Lignin characterization isdifficult to accomplish because of the complexity of its
structure. Generally, lignin is formed by phenylpropane-
type groups including coniferyl units or similar units of
guaiacol-propane in the case of softwoods, and both
coniferyl and syringyl units in the case of hardwoods
(Sarkanen and Ludwig, 1971). Brauns (1952) indicated
that hot water played an important role in the behavior
of the solubilization of lignin. For example, an impor-tant degree of solubilization was generated with wood
heated at 100–120 �C. Coniferin, vanillin, methylfurf-
ural, and pyrocatechol were produced at more high
temperatures (180 �C).
and 280 nm
g/l (280 nm)
d SLD Furfural HMF F
0.283 0.003 0.003 0.006
0.551 0.007 0.006 0.013
0.402 0.018 0.047 0.065
278 M. Fox, T. Noike / Bioresource Technology 91 (2004) 273–281
The cellulose and lignin which were not hydrolyzed or
oxidized during wet oxidation were determined to cal-
culate the process removal (or destruction) efficiency of
cellulose and lignin (Table 2). Fig. 1F shows these
concentrations after wet oxidation. The dotted lines
represent the initial concentration of each compound
before pretreatment. Cellulose removal increased with
temperature; this agrees with the previous results whichindicated that cellulose solubilization increased in an
acid medium. Lignin removal, on the other hand, at-
tained its maximum value at 190 �C (65%) and later
decreased to 61% (210 �C). It seems reasonable to sup-
pose that the highest solubilization was obtained at 190
�C. Indeed, its maximum production of SLD was ac-
complished at this temperature (Fig. 1D).
The destructive action of wet oxidation on thenewsprint fiber was visualized through several scanning
electron microscope (SEM) plates (or photographs).
Fig. 2 shows the photos taken at different temperatures.
Photo A shows newsprint without wet oxidation. The
long and thin fibers which may be formed by cellulose,
hemicellulose and lignin can be observed here. Photo B
shows wet oxidized newsprint (170 �C). Here a partial
shell off of the outside layer of the fiber-wall is observedwithout major destruction in the fiber itself. Its oblong
form seems to keep untouched. In Photo C, the fiber
treated at 190 �C does not show a shell off like at 170 �C,
Fig. 2. Scanning electron microscope plates for wet oxidized newsprint. A: Ne
40.9 kg/cm2; D: 210 �C, 51.1 kg/cm2. For all pictures ·230, 15 kV, scale: 10
but a greater destruction occurred through segmentation
or if it is understood better, through the shortening of
the oblong fiber as shown in Photo A. In Photo D it is
clear that at 210 �C the fiber has lost almost completely
its oblong form leaving an amorphous remainder with-
out fibrous characteristics. Because the photos are in
black and white, it is not possible to appreciate the
change in color of the micro-fibers. The normal fibers ofnewspaper show a greyish color, whereas the fibers
treated at different temperatures (170, 190 and 210 �C)stain opaque and dark. The higher the temperature of
pretreatment, the darker is the color. Regarding Photo
D, it was necessary to give a gamma correction to be
able to identify it. The effluent presented an intense and
aromatic sweet scent very similar to vanillin. Also the
scent could have been like furfural. Martinez et al.(2000) indicated that syrups of the acid hydrolysis of
bagasse of sugarcane had a rich aroma. Also, solutions
showed a well-tanned color.
3.2. Anaerobic biodegradability performance
In general terms, to degrade anaerobically lignocell-
ulosic materials, these have to be partially delignified or
the microorganisms have the capacity to degrade the
holocellulose and lignin or to break at least their
structural link (Cowling and Kirk, 1976). Khan (1977)
wsprint fiber without wet oxidation, B: 170 �C, 31.0 kg/cm2; C: 190 �C,0 lm.
Table 4
Incubation time, total methane production and conversion efficiencies
(%)
Batch label Incubation
time (days)
CH4 (S.T.P.) (liter) Ce (%)a
Ncb Toc
B-1 60 2.4 4.7 51.0 (51)
B-2 60 2.3 3.9 58.9 (59)
B-3 62 1.8 3.6 50.0 (50)
aConversion efficiency (Nc=To � 100).bNet cumulated volume was corrected for the methane production
attributable to the seed.c Theoretical maximum methane production.
M. Fox, T. Noike / Bioresource Technology 91 (2004) 273–281 279
investigated the degradation of cellulosic materials using
mixed culture of bacteria. Newsprint was one of the
tested materials in this study. In a period of 4 weeks, less
than 45% of the cellulose was degraded. According to
the suggestion by the author, an important part of the
holocellulose present in the newspaper was not de-
graded. Moreover, the presence of the lignin affected
negatively the ability of the mixed culture to degradecellulose.
The main objectives to pretreat newspaper by the wet
oxidation process were to improve the biodegradability
of the holocellulose in solubilizing or destroying the
greater amount of lignin leaving the fraction of carbo-
hydrates as intact as possible, and to determine the
optimal pretreatment temperature for the best methane
conversion efficiency. The biodegradable nature of theeffluent of the wet oxidation process was evaluated
through the recovery of its total COD as methane gas.
Likewise, the improvement in the bioavailability of cel-
lulose after wet oxidation was evaluated through re-
moval efficiencies in the batch experiments.
Wet oxidized newspaper at 170, 190 and 210 �C were
used to fill the batch reactors enumerated B-1, B-2 and
B-3, respectively. Based on the total COD of each batchreactor (see Table 1), the maximum theoretical potential
of methane production was calculated from the relation
that indicates that 0.35 liter of methane at standard
temperature and pressure (S.T.P.) is generated from 1 g
of COD (McCarty, 1964). The total cumulated volume
of methane and the methane conversion efficiency for
each batch reactor are shown in Table 4. The cumulated
methane curves were constructed on the basis of dailyvalues until the maximum period of 65 days. Table 5
summarizes the final conditions after 65 days of incu-
bation. The effluents reached relatively high convert-
ibilities of COD. The newsprint treated at 190 �Creached the highest methane conversion. Approximately
59% of the initial COD was recovered as methane gas.
As shown in Fig. 3, net cumulated methane production
curves reached very similar potentials, giving B-3 asmaller one. If lag phases are observed, a retardation
period can be seen 10–15 days before the beginning of
the phase of methane production. The phenolic and
Table 5
Anaerobic removal efficiencies for TCOD, cellulose, lignin, furan and solubl
Run of W.O. Batch label Final pH TCOD (g/l) (%)
R-1 B-1 6.7 5.2 46
R-2 B-2 6.9 5.1 49
R-3 B-3 6.6 5.5 44
SLD (g/l) (%)
Initial Final
R-1 B-1 0.441 0.002 99.5
R-2 B-2 0.552 0.032 94.2
R-3 B-3 0.404 0.066 83.7
heterocyclic nature of the soluble fraction probably
caused this delay in the methane production. Young and
Frazer (1987) indicated that monomers in lignin such as
vanillic acid, vanillin, syringic acid, syringaldehyde,
ferulic acid and cinnamic acid are degraded almost
completely under methanogenic conditions in enrich-
ment cultures of digester sludge. In the studies of ac-
climatization of organisms to phenolic compounds,McCarty et al. (1976) mentioned that the methane fer-
mentation of simple ring structures formed by the heat
treatment of cellulose, hemicellulose and lignin had to
be difficult. Acclimatized cultures were incubated with
different soluble compounds which were supposedly
generated from the heat treatment of lignocellulose.
Biodegradation results indicated that with a suitable
acclimatization all the soluble compounds are anaero-bically degraded and transformed to methane. Between
the tested compounds appeared HMF, furfural, phenol,
catechol, benzoate, benzaldehyde, cinnamic acid and
vanillin. In the present work, a previously conditioned
culture was not used, which could have been one of the
reasons to understand the delay in the production of
methane. Appropriate acclimatization should serve to
enhance the development of particular enzymes of acertain mixed culture to ferment organic molecules to
methane. Table 5 shows the efficiencies of removal of the
phenolic and heterocyclic compounds produced during
wet oxidation. Removal efficiencies varied from 84% (B-
3) to 100% (B-1) for SLD and from 87% (B-3) to 96%
(B-2) for furan.
e lignin derivatives
Cellulose (g/l) (%) Lignin (g/l) (%)
0.58 74 0.67 10
0.24 88 0.42 12
0.33 77 0.49 14
Furan (mg/l) (%)
Initial Final
5.55 0.545 90.2
13.0 0.586 95.5
65.1 8.79 86.5
Fig. 3. Net cumulated methane production for the batch experiments.
280 M. Fox, T. Noike / Bioresource Technology 91 (2004) 273–281
The anaerobic degradation of newspaper without an
effective pretreatment leaves an important fraction of
cellulose without degrading. Other studies on anaerobic
bioconversion of paper waste made by Clarkson and
Xiao (1999) indicated that the supposed factor thatlimited a suitable anaerobic conversion of newsprint was
the physical structural association between lignin and
cellulose. In reactors treating paper waste in a period of
300 days, 80% of the available cellulose was degraded. It
seemed that wet oxidation of newspaper changed and
improved the structural relationship between lignin and
cellulose. It most likely made the anaerobic degradation
of holocellulose more vulnerable. As shown in Table 5,cellulose had the greater bacterial degradation in B-2,
where approximately 88% of cellulose was degraded; B-3
and B-1 had 77% and 74%, respectively. With regards to
the percentages of anaerobic removal of lignin, these
results were considered to be inconsistent. Indeed, re-
covered lignin concentrations after methane fermenta-
tion could be inexact due to the quantity of biomass of
the batch reactors for solvent extractions were restrictedto small amounts. If the previous reasons are taken into
account it can be concluded that lignin was not de-
graded anaerobically.
4. Conclusions
Due to a complex lignin–holocellulose structural as-
sociation, the biodegradability of newsprint is especially
low compared with other organic wastes used for
methane recovery. As an attractive renewable source of
energy, its low biodegradability had to be improved witheffective thermal pretreatments in the reduction of lignin
without destroying or degrading the fraction of sugars
(carbohydrates) present in the paper fiber. The following
conclusions can be drawn from this study:
Wet oxidation was a pretreatment technically viable
for the fragmentation and solubilization of newsprint.
The solubilization process on the fibers of paper gener-
ated volatile fatty acids, monosaccharides, heterocyclicand soluble lignin compounds.
Analyzing the pretreatment process from the point of
view of the effectiveness (if conserved much or less intact
the fraction of holocellulose for the later anaerobiolog-
ical process) it can be concluded that the solubilization
of the fiber was enhanced through the natural acidifi-
cation of the wet oxidation process (maximum solubi-
lization ratio was 29% at 210 �C). With regards to the
cellulose removal in the pretreatment process, relatively
high removals at 190 and 210 �C were achieved (57%
and 69%, respectively). Therefore, the remaining cellu-lose for the biological process is low and the requirement
for effectiveness is not totally fulfilled. Nevertheless, it is
thought that due to the thermal and acid effect of sub-
critical water, the fiber changed in some degree its
physical dependency with the lignin and made it bio-
logically more susceptible to be degraded.
The biodegradable nature of newsprint treated in
subcritical water was evaluated through the conversionof the COD to methane using a mixed culture. The
highest methane conversion was obtained with the
fraction of paper pretreated at 190 �C. Fifty nine percentwas converted to methane gas in an approximated pe-
riod of 60 days. The cellulose which was not removed in
the oxidation process served as substrate for the mixed
cultures. Removal efficiencies of cellulose varied be-
tween 74% and 88%. With regards to the lignin, it wasnot degraded anaerobically.
Anaerobic reduction of total lignin derivatives and
furans were accomplished with high efficiencies. Remo-
vals varied between 84% and almost 100% for total
lignin derivatives. Furan removals varied between 87%
and 96%.
Further research is needed in order to optimize the
process for methane fermentation. Adding buffer duringwet oxidation should be an essential solution to prevent
the natural acidification of the process. This should
improve methane fermentation efficiency of wet oxidized
newsprint by leaving more free-holocellulose and solu-
bilizing more lignin.
Acknowledgements
The authors wish to express their profound thanks to
Mr. Takamasa Ohki, Hitachi Zosen Co. Ltd. for the
technical support they offered for the wet oxidation of
paper wastes. They also wish to extend their grate-
ful thanks to Professor Kenji Iiyama, Asian Natu-
ral Environmental Science Center, the University of
Tokyo.
References
APHA, 1995. Standard Methods for the Examination of Water and
Wastewater, 19th ed. American Public Health Association, Wash-
ington, DC.
Brauns, F.E., 1952. The Chemistry of Lignin. Academic Press, New
York. pp. 543–549.
M. Fox, T. Noike / Bioresource Technology 91 (2004) 273–281 281
Bjerre, A.B., Olesen, A.B., Fernquist, T., Ploger, A., Schmidt, S.A.,
1996. Pretreatment of wheat straw using combined wet oxidation
and alkaline hydrolysis resulting in convertible cellulose and
hemicellulose. Biotech. Bioeng. 49, 568–577.
Chynoweth, D.P., Pullammanappallil, P., 1996. Anaerobic digestion of
municipal solid wastes. In: Barlaz, M.A., Palmisano, A.C. (Eds.),
Microbiology of Solid Waste. CRC Press, Boca Raton, FL, pp. 71–
113.
Clarkson, W., Xiao, W., 1999. Anaerobic bioconversion of paper
waste. In: Proceedings of the II International Symposium on
Anaerobic Digestion of Solid Waste, Barcelona, pp. 75–82.
Cowling, E.B., Kirk, T.K., 1976. Properties of cellulose and lignocell-
ulosic materials substrate for enzymatic conversion processes.
Biotech. Bioeng. 6, 95–123.
Fox, M.H., 2000. Methane fermentation of cellulosic wastes pre-
treated with the wet oxidation process. M.Sc. thesis, Tohoku
University.
Harf, J., Hug, A., Vogel, F., Von Rohr, P.R., 1999. Scale-up of
catalytic wet oxidation under moderate conditions. Environ. Progr.
18, 14–20.
Iiyama, K., Stone, B., Macauley, B., 1994. Compositional changes in
compost during composting and growth of Agaricus bisporus.
Appl. Environ. Microbiol. 5 (60), 1538–1546.
Iiyama, K., 1999. Personal communication.
Jerger, D., Dolenc, D., Chynoweth, D., 1982. Bioconversion of woody
biomass as a renewable source of energy. Biotech. Bioeng. 12, 233–
248.
Khan, A.W., 1977. Anaerobic degradation of cellulose by mixed
culture. Can. J. Microbiol. 23, 1700–1705.
Lay, J.J., 1997. Analysis of methane production from different
anaerobic environments. Ph.D. thesis, Tohoku University.
Martinez, A., Rodriguez, M., York, S., Preston, J., Ingram, L., 2000.
Effects of Ca(OH)2 treatments (‘‘overliming’’) on the composition
and toxicity of bagasse hemicellulose hydrosylates. Biotechn.
Bioeng. 69 (5), 526–536.
McCarty, P.L., 1964. Anaerobic waste treatment fundamentals, Part
One, Chemistry and microbiology. Public Works, 107–112.
McCarty, P.L., Young, L.Y., Gossett, J.M., Stuckey, D.C., Healy, Jr.,
J.B., 1976. Heat treatment for increasing methane yields from
organic materials. In: Microbial Energy Conversion Seminar,
Gottingen, pp. 179–199.
McGinnis, G.D., Wilson, W.W., Mullen, C.E., 1983. Biomass
pretreatment with water and high-pressure oxygen. The wet
oxidation process. Ind. Eng. Chem. Prod. Res. Dev. 22, 352–357.
Meshitsuka, G., 1999. Comprehensive processes for pollution free
pulping. In: Proceedings of the Workshop: Targeting Zero Emis-
sions for the Utilization of Renewable Resources (Biorefinery,
Chemical Risk Reduction, and Lignocellulosics Economy). United
Nations University, Tokyo, pp. 34–38.
Sarkanen, K.V., Ludwig, C.H., 1971. Lignins: Occurrence, Formation,
Structure, and Reaction. Wiley-Interscience, New York.
Sako, T., 1997. Supercritical solutions. Look Japan 42 (492), 24–25.
Sorensen, E., Bjerre, A.B., Rasmussen, E., 1990. Soil recovery by wet
oxidation. Environ. Tech. 11, 429–436.
Updegraff, M.D., 1969. Semimicro determination of cellulose in
biological materials. Anal. Biochem. 32, 420–424.
Young, L.Y., Frazer, A.C., 1987. The fate of lignin and lignin-derived
compounds in anaerobic environments. Geomicrobiology 5 (3/4),
261–293.
Yuan, J.P., Chen, F., 1999. Simultaneous separation and determina-
tion of sugars, ascorbic acid and furanic compounds by HPLC-
dual column detection. Food Chem. 64, 423–427.