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Accepted Manuscript
PVC degradation by Fenton reaction and biological decomposition
Tomáš Mackuľak, Alžbeta Takáčová, Miroslav Gál, Jozef Ryba
PII: S0141-3910(15)30036-7
DOI: 10.1016/j.polymdegradstab.2015.07.005
Reference: PDST 7693
To appear in: Polymer Degradation and Stability
Received Date: 20 March 2015
Revised Date: 30 June 2015
Accepted Date: 6 July 2015
Please cite this article as: Mackuľak T, Takáčová A, Gál M, Ryba J, PVC degradation by Fentonreaction and biological decomposition, Polymer Degradation and Stability (2015), doi: 10.1016/j.polymdegradstab.2015.07.005.
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PVC degradation by Fenton reaction and biological decomposition
Tomáš Mackuľaka, Alžbeta Takáčováa, Miroslav Gálb, Jozef Rybac
aDepartment of Environmental Engineering, Faculty of Chemical and Food Technology, Slovak
University of Technology, Radlinského 9, 812 37 Bratislava, Slovakia
bDepartment of Inorganic Technology, Faculty of Chemical and Food Technology, Slovak
University of Technology, Radlinského 9, 812 37 Bratislava, Slovakia
cDepartment of Fibres and Textile Chemistry, Faculty of Chemical and Food Technology, Slovak
University of Technology, Radlinského 9, 812 37 Bratislava, Slovak Republic.
Corresponding author. Tel.: +421 2 59325577
E-mail address: [email protected]
Abstract
The possibility of the degradation of the recalcitrant polymer polyvinylchloride (PVC) was the
object of our study. For this purpose the Fenton reaction with subsequent biodecomposition step
was successfully used. Molecular degradation fragments were determined by HPLC and GC-FID
method. After the first step - degradation of PVC by the Fenton reaction, the formation of trans-1,2-
dichloroethene, cis-1,2-dichloroethene, trichloroethene and tetrachloroethene was observed. Also
more complex molecules such as benzene, ethylbenzene and o-xylene were identified. Probably
these chemical compounds are the products of phthalates decomposition. The resulted mixture was
in the second step used as a substrate for anaerobic biogas production. Biological degradation of
used COD was α = 67.3% and F/I = 0.004 [gCOD g-1 VS]. The decomposition of other compounds
such as trans-1,2-dichlorethylene (60 %), cis -1,2-dichlorethylene (70 %) was also observed.
Moreover, benzene, ethylbenzene and o-xylene were completely removed during the biological
decomposition step. It is possible to assume that Fenton pretreatment improves the degradation of
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PVC and, by this way the low molecular weight fragments are formed. Subsequently degradation
products of PVC by GC-FID were identified. In next steps, the digestion of these fragments by
anaerobic microorganisms was observed. It was also found that in anaerobic sludge the degradation
of low molecular weight fragments is carried out. One can conclude that these small fragments are
used by microorganisms as biological substrate.
Keywords
Fenton reaction, polyvinylchloride, biodegradation, hydroxyl radicals, biogas
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1. INTRODUCTION
PVC belongs to group of synthetic polymers with wide industrial application. The properties
of these materials allowed them to substitute wood and concrete. PVC production is cheap, but
there is a concern about its effect on environment. This article is focused on the possibility of the
degradation of artificial substances such as polyvinylchloride (PVC), which belongs to slowly
degradable substances by natural processes; however the world production of these substances is
very high. Its combustion produces e.g. dioxins that belong to the most toxic compounds [1]. The
monomeric unit of PVC, vinyl chloride, is classified as a human carcinogen. Final polymer have
high stiffness because plasticizers such as di(2-ethylhexyl)phthalate (DEHP), di-isodecylphthalate
(DIDP) a di-isononyl phthalate (DINP) causing better flexibility are added [2]. The release of the
DEHP from PVC was proved. This could be dangerous because toys and medical products are made
also from PVC. Phthalates are suspicion to cause scleroderma, cholangiosarcoma, angiosarcoma,
brain carcinoma or acroosteolysis [3]. These compounds are serious environmental load because of
their presence in foodstuffs, surface waters or sludge [4]. The production of PVC is connected with
a formation of high carcinogenic intermediates such as ethyl dichlorine, vinylchlorine, and
hexachlorine benzene. During this process several types of hazardous additives e.g plasticizers,
stabilizers, and fire-retardants are also used [5, 6].
Only a few publications dealt with the biological decomposition of PVC. The use of various
species of white rot fungi in PVC degradation was studied in this work [7]. In this paper the
usability of the enzymatic mixture is described. The results predict the possible biological ways of
artificial polymer degradation in natural environment. Utilization of degradation products as
biological substrates for aerobic and anaerobic microorganisms is also discussed. An analysis of
gases from waste dumps predicts the possibility of chlorinated polymers degradations in nature
environment [8]. Various chlorinated organic compounds are present in sediments and percolating
waters. Their source is probably the dissociative PVC waste. In the work of Hata et al. [9] the
degradation of cis-1,2-dichloroethene and vinylchloride in the landfill leachate by Clostridium
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saccarobutylicum was observed. The study of Leahy and Shreve [10] describes the presence of
dehalogenation of tetrachloroethylene (PCE) in landfill leachates by anaerobic microorganisms.
For the PVC elimination Advanced Oxidation Processes (AOP) resulting in low molecular
weight and, therefore, easier biologically degradable substances can be used [11]. Fenton reaction,
ozonization and ultrasonic treatment belong to the group of the most used AOPs. All of these
processes are able to degrade wide spectra of organic species namely chlorinated compounds,
antibiotics, endocrinic disruptors, and polymers that are present mainly in sediments and landfill
leachate [12-14].
Fenton reaction (H2O2/Fe2+) is a catalytic process based on the electron-transfer between metal
cation and H2O2 [12, 15]. This radical reaction is also a part of metabolic processes used by bio-
systems in Nature [15]. It may be used for degradation of different types of polymers (P-H).
Fe2+ + H2O2 → Fe3+ + HO– + HO• (1)
P-H + HO• → P• + H2O (2)
P• + O2 → POO• → PO• (3)
POO•(PO•) + PH → POOH (POH) + P• (4)
One of the examples is water soluble polyethyleneglycols degradation [16]. Feng at el. [17] dealt
with the photo-assisted Fenton reaction with UV irradiation for polystyrene splitting with efficiency
of 99 %. Authors assumed that cation-exchange mechanism of Fe3+ ions as a background of
heterogenic degradation process. Fenton reaction is also present in various biochemical and
biological processes; e.g. brown rot fungi use this reaction to split lignocellulose materials into
easier metabolizable compounds. These fungi use catechol-driven Fenton reaction instead of
enzymes for this purpose [18, 19]. An example, where these degradation processes can be observed
in a great scale are waste landfills where biotic and abiotic processes occur simultaneously in
aerobic and anaerobic conditions [12, 20].
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Similarly ozone can be used for the degradation of polymers, e.g. 1,4-trans-polychloroprene
or polyethylene [21]. In the work of Wang et al. [14] ultrasonic treatment was successfully used for
the degradation of ammonia pollution and COD. Gonze E et al. [22] described the decomposition of
chlorinated compounds via hydroxyl radicals produced by ultrasound. Ultrasound was also used for
polyvinylacetate (PVAC) and polyethyleneoxide (PEO) degradation [13]. Except chemical
procedures considerable part of scientific research is focused on the biodegradation of PCE, TCE
and DCE by genus Dehalococcoides [23, 24].
Our study is focused on the environmental aspects of raw PVC materials disintegration in
natural environments. This work is aimed on two-step PVC material degradation: the first one is
common Fenton reaction and in the next one degradation products by Fenton reaction are used as a
substrate for anaerobic fermentation. Our results will show the ability of anaerobic sludge to
decompose the degradation products of PVC (lower biogas production). The Fenton reaction and
subsequent bacterial digestion were chosen as possible biological processes of raw PVC materials
degradation that can occur in the landfills during anaerobic and anoxic conditions and produce low
molecular chlorinated compounds. Moreover, biogas production will be used to monitor the
digestion progress.
2. EXPERIMENTAL PART
2.1 Chemicals and reagents
In our experiments, all the reagents were analytical grade and used without further purification.
Hydrogen peroxide (H2O2, 30 %, w/w), sulfuric acid (H2SO4, 5 %, w/w ), sodium hydroxide
(NaOH, 20 %, w/w), ferrous sulfate hepta hydrate (FeSO4.7H2O, purity 98% min) were purchased
from Lachema (Brno, Czech Republic), The solutions were prepared using double-distilled
deionized water with resistivity above 18 MΩcm. All pH values were measured with pH meter
Model 215 (Denver Instrument, USA), which was calibrated with standard buffer solutions.
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2.2 Procedures
For a degradation study of PVC (SLOVIPLAST® TG 7008, ChZ Nováky, Slovakia; granulate with
diameter 4±2 mm, density 1430±50 kg m-3, thermal stability at 180 °C 180 min without mechanical
impurities) following procedure was used: Into Erlenmeyer flask 300 mL of deionized water and
0.5g of PVC material was added. Then pH of water was adjusted by 5 % solution of sulfuric acid to
pH = 3. Into a suspension calculated amount of 0.264 g of FeSO4.7 H2O and 0.80 mL (ratio 875:500
mg L-1, marked as X) or 1.60 mL (ratio 875:1000 mg L-1, marked as Y) of H2O2 was added [16].
Suspension was stirred for 20 minutes at 300 rpm and 16 °C and then was 5 minutes kept without
shaking. Subsequently, the suspension was neutralized with sodium hydroxide solution (30 %) to
stop the Fenton process and let to sediment for 15 minutes. Solution was analyzed by HPLC and
GC-FID method. Chemical oxygen demand (CODCr) was specified by spectrophotometric
dichromatic semimicro method. Released chlorine ions were determined by combined selective
chloride electrode (Sentek C1-ISE, UK).
2.3 Product analyses of PVC degradation by GC-FID instrumentation
Degradation products after the Fenton reaction were analyzed using Purge-and-trap technique
(Tekmar 3000, USA). A 5 mL of the sample was placed into a small vial and kept under a stream of
the nitrogen at a flow rate of 40 mL min-1. After that the nitrogen passed through a stainless steel
adsorption tube Carbopack C. The purge-and-trap device was coupled with a gas chromatograph
(Varian 3400 CX ,USA), column CP Select 624 CB (Varian USA) with dimensions D(30 m) x ID
(0,53 mm) x OD(30 m) and a temperature program: 50 ºC (hold 1 min), 5 ºC min−1 to 100 °C, 50 ºC
min−1 to 220 ºC (hold 2 min), injector (Varian) and detector (FID) temperature was 100 °C and
300 °C, respectively.
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2.4 Biological degradation of decomposition products of PVC in anaerobic sludge
In the second part of the experiment methane batch tests were realized. The reactor (0.65 L) for
biogas production was filled with anaerobic sludge from wastewater treatment plant unit in
Devínska Nová Ves (Slovakia) and was not adapted for decomposition of investigated compounds.
The initial values of sludge were: dry matter 16.5 g L-1, anneal loss 60 % and pH = 7.35. The
reactor temperature was 37-38 °C. Anaerobic semi-continual mixed reactors were filled with
300 mL of anaerobic stabilized sludge and 100 mL of mixture created by Fenton reaction (X,Y).
Biogas production was measured for 7 days by Micro-Oxymax device. The progress of the
degradation of PVC decomposition products was controlled by HPLC and GC-FID.
2.5 Samples analyses by HPLC method
Chemical analyses of sludge water were also performed by HPLC equipped with PDA detector
(Young Lin 9100). Mobile phase: 1 mL min-1 of methanol:water mixture, gradient 10:90 to 90:10,
16 minutes, temperature 25 °C, column GraceSmart, RP-18, length 150 mm, 4.6 mm ID, PDA
detector (wavelength used 200, 210, 222, and 235 nm).
2.6 Measuring of biogas production via Micro-Oxymax device (Columbus Instruments, USA)
This equipment for measuring of biogas composition consists of detectors for methane, oxygen,
carbon dioxide, hydrogen, hydrosulphide and water. This equipment is fully automatized system for
continual measuring of gas concentration in hermetic flasks. It’s used for testing of material
biodegradeability under aerobic or anaerobic conditions. Obtained data are evaluated by Micro-
Oxymax software. Obtained results represent the cumulative production and consumption of CO2,
CH4.
2.7. Scanning electron microscopy
The influence of the Fenton reaction on the PVC in the heterogeneous mixture was also analyzed by
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SEM microscope JEOL 7500F operated at 5 or 10 kV with SEI detector. The sample was firstly
dried in the oven at 40 °C for at least two hours. Then the sample was stacked at Si plate and
analyzed in the vacuum (10-4 Pa).
3. RESULTS AND DISCUSSION
PVC itself is biologically resistant and the products of its degradation may be quite toxic.
Fig. 1. HPLC analysis of PVC degradation by the FR (Y).
Figure 1 shows the chromatogram of PVC degradation using the Fenton reaction (Y). Main, low
molecular degradation products are found between 1.7 and 2.5 min. Except low molecular
fragments more complex structures benzene (retention time 6.04 min) and ethylbenzene (retention
time 7.77 min.) were also observed. We assume that these compounds are the degradation products
of the present phthalates. Another interesting point is that at the beginning of the PVC degradation
by FR higher concentration of Cl- ions (22 mg L-1) compare to 4 mg L-1 at the end of the
degradation process was observed. We think that the decrease of Cl- ions concentration at the end of
the degradation process is caused by the presence of OH• radicals. Chlorine anions react with OH•
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radicals and formed Cl• radicals. This leads to the formation of different chlorinated compounds
(see Fig.2). Direct reaction between Cl- ions and OH• radicals during PVC degradation decreases
the Fenton reaction efficiency.
Fig. 2. GC-FID analysis of PVC degradation products by the Fenton reaction (Y)
The presence of chlorinated degradation products were proved by the gas chromatography. Trans-
1,2-dichlorethylene, cis-1,2-dichlorethylene, trichloroethylene, and tetrachlorethylene were
identified by GC-FID (see Table 1, Fig. 2). These products belong to persistent pollutants of
environment. Other degradation products such as ethylbenzene (9.06 min) and o-xylene (10.22 min)
were also observed. We assume that molecules with benzene core can be formed by the
decomposition of released phthalates from PVC. COD value can be considerably influenced by
decomposition of present stabilizers and fire retardants.
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Table 1 The concentration of PVC decomposition products by Fenton reaction (X,Y) after 20
minutes determined by GC-FID method.
compound c (mg L-1)
retention time (min) X Y
trans-1,2-dichlorethylene 0.112 0.277 2.41
cis -1,2-dichlorethylene 0.198 0.442 2.94
trichlorethylene 0.010 0.024 4.44
tetrachlorethylene 0.012 0.019 6.96
ethylbenzene 0.009 0.013 9.06
o-xylene 0.010 0.014 10.22
From Table 1 one can see that FR (X) exhibits lower degradation efficiency compare to the FR (Y).
Under anaerobic conditions the degradation of PVC products is realized mainly by abiotic ways.
The important factors are H2S, FeS and Fe2+ ions which dechlorinized these substances. Also the
presence of zinc and iron are able to speed up this process. In anaerobic sludge the biotic
degradation can be carried out with the help of sulphate-reduction bacteria [25].
In the next Fig. 3 SEM micrographs of PVC before and after the Fenton reaction Y can be seen.
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A
B
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Fig. 3. SEM micrographs of PVC material before the Fenton reaction Y (A), after the Fenton
reaction Y (B), zoom of the selected section of B (C).
In Fig. 3 the differences in the structure (morphology) of PVC material before (A) and after (B) the
Fenton reaction Y are clearly visible. After the Fenton reaction Y is applied, PVC is fragmented
which is probably caused by the radicals formed during the Fenton process. Moreover, after the
attack of radicals defects in the PVC material structure are formed (C). Fragmentation of PVC
material observed by SEM microscopy was also confirmed by weight loss measurements of PVC
material before and after the Fenton processes. The highest weight losses of 10±2 % were detected
in the case of Fenton Y process.
Almost all above mention degradation products are potentially harmful for environment. Therefore
in the next part of our work we focused on utilization of these compounds as biological substrate in
anaerobic sludge[26]. The process of biodegradation in anaerobic sludge was controlled by HPLC
and GC-FID analyze. Production of biogas was also monitored.
During methane tests the decrease of organic compounds concentration formed during FR was
observed.
C
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Fig. 4. HPLC analyses of PVC degradation products by Fenton reaction in sludge 0 day.
Fig. 5. HPLC analyses of PVC degradation products by Fenton reaction in sludge after 7 days.
The significant decrease of the concentration of low molecular compounds released after PVC
degradation was observed in sludge water after seven days (Fig.4, Fig.5, Table 2).
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Table 2 Concentration of the selected compounds at the beginning (0 day) and at the end (7th day)
of the biological step determined by GC-FID method.
compound c (mg L-1)
retention time (min) 0 day 7th day
trans-1,2-dichlorethylene 0.088 0.035 2.41
cis -1,2-dichlorethylene 0.105 0.031 2.94
trichlorethylene 0.011 0.005 4.44
tetrachlorethylene 0.013 0.009 6.96
ethylbenzene 0.007 < DL 9.06
o-xylene 0.006 < DL 10.22
The concentration of the selected organic compounds at the beginning (0 day) and at the end (7th
day) of the biological step in anaerobic sludge condition is summarized in Table 2. Measured results
by GC-FID method exhibit partial decomposition of chlorinated low-molecular compounds. The
highest efficiency of the degradation was reached in the case of trans-1,2-dichlorethylene and cis -
1,2-dichlorethylene, respectively. The concentration of these compounds is influenced by the
decomposition of trichlorethylene and tetrachlorethylene during reductive dechlorination. Total
decomposition of benzene, etylbenzene, and o-xylene was observed at the end of the digestion
process. In general, the number of compounds with retention time under 2 minutes is lower at the
end of the anaerobic digestion (7th day) compare to the state immediately after the FR (0 day).
During the experiment the formation of oxalic (1.80 min) and formic acid (2.29 min) was also
observed. The first source of these compounds is probably the decomposition of chlorinated
compounds by enzymatic degradation by microorganisms and the second one is probably the
degradation of present phthalates. TCE can be degraded by reductive dechlorination and also by
aerobic and anaerobic degradation through the use of co-metabolism. Little et al. [27] describe the
process of the enzymatic degradation of TCE using various enzymatic substrates. Some
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microorganisms are able use TCE as a carbon and an energetic source. Some genuses of
methanotrophic organisms are able to degrade TCE by a nonspecific enzymatic activity (methane
monooxygenase) as a secondary substrate. These microorganisms consequently produce epoxide by
enzymatic degradation and exclude it from the cell. Epoxide is decomposed to dichloroacetic and
glyoxylic acids and one-carbon products.
To better control the progress of an anaerobic digestion of PVC decomposition products
after FR, biogas production was also monitored.
0 1 2 3 4 5 6 70
2
4
6
8
10
12
14
16
18
Pro
duct
ion
biog
as (
ml)
Time (day)
inocullum
pre-treated substrate PVC
Fig. 6. Cumulative biogas yield during the anaerobic digestion experiment.
Figure 6 shows production of biogas during 7 days test in anaerobic conditions. An elevated amount
of produced biogas in comparison with production of biogas from the sludge without substrate was
observed. Single sludge cumulates 7.7 mL of biogas with composition of 29 wt. % of methane and
71 wt. % of carbon dioxide during 7 days. This production is caused by decomposition processes in
the sludge. The sludge with concentration of 11.5 mg of COD of substrate and feed/inoculum ratio
F/I = 0 004 [gCOD g-1VS] accumulate ca twice more biogas with content of 26 wt. % of methane and
74 wt. % of carbon dioxide. Efficiency of used COD of biological decomposition is α = 67.3 %. It is
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possible to assume that biological decomposable after adaptation will be higher. Production of
methane after the addition of decomposition products of PVC after FR is influenced by many
factors. Decomposition of organic compounds to carbon dioxide is caused by the inhibition of
methanogenic germs in presence of TCE and VC. These compounds can inhibit the growth of
methanogenic germs and, consequently, the production of biogas itself. Young et al. [28] investigate
biodegradation of trichloroethene (TCE) and hexahydro-1,3,5-trinitro-1,3,5-triazine (RDX) by anaerobic
sludge. They observed that anaerobic sludge itself was not able to degrade TCE. Therefore, germs cultures
adapted for TCE were used. Higher efficiency of the degradation was reached and decomposition products
were identified as cis-dichloroethene and other chlorinated metabolites. Increased concentration of CO2 in
produced biogas can be also influenced by mechanism of decomposition of TCE and DCE [29].
Some dehalorespiring organisms are able to efficiently degrade PCE, TCE, DCE, VC to less toxic
compounds. Subsequently TCE can be degraded under anaerobic condition by reductive
dechlorination to carbon dioxide[28, 29].
Because the Fenton reaction is widely spread in natural environment, the measured PVC
degradation results show the possibility of its decomposition in natural environments not only by
chemical ways but also by biological processes in aerobic and anaerobic conditions. Decomposed
PVC materials can be a source of small chlorinated molecules like trans-1,2-dichloroethene, cis-1,2-
dichloroethene, trichloroethene and tetrachloroethene [8, 10]. These products were already
identified in landfill gas and sediment leachate [8, 9] what supports the assumption, that the Fenton
reaction is able to degrade chlorinated polymer materials in an environment and like this, partly
supports the self-cleaning of an environment. A very important fact that come out of our
experiments and greatly influences the efficiency of the degradation processes in the environment is
a combination of biotic and abiotic processes in aerobic and anaerobic conditions [10]. It should be
stressed that the processes that lead to the presence of these toxic chlorinated compounds and their
presence in landfill gas and sediment leachate it is not yet fully understood.
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4. CONCLUSION
The aim of this work was to prove the possibility of the degradation of commercially
available synthetic polymer PVC by the Fenton reaction and subsequent anaerobic digestion in the
sludge water. Results obtained by HPLC and GC-FID confirm the formation of low molecular
organic compounds. During degradation process of PVC chlorinated products such as trans-1,2-
dichlorethylene, cis -1,2-dichlorethylene, trichlorethylene and tetrachlorethylene were identified.
Benzene, etylbenzene, and o-xylene were also found. Various ratios between Fenton reagents
FeSO4.7 H2O and H2O2 was tested. In the next step, under the anaerobic conditions, these
compounds undergo a dechlorination and further decomposition. We observed that the products of
the FR degradation serve as a source of carbon for anaerobic bacteria. After addition of 11.5 mg
COD anaerobic sludge F/I = 0.004 [gCOD g-1 VS] produced ca 14 mL of biogas with content of
26 wt. % of methane and 74 wt. % of carbon dioxide with efficiency of α = 67.3 %. Also high
efficiency of the decomposition of selected organic compounds such as trans-1,2-dichlorethylene
60 %, and cis-1,2-dichlorethylene 70 % was observed. On the other side, trichlorethylene and
tetrachlorethylene were degraded with lower efficiency. It is possible to assume that Fenton
pretreatment improves the degradation of PVC and, by this way the low molecular weight
fragments are formed. Subsequently we identified degradation products of PVC by GC-FID. In next
steps, the degradation of these fragments by anaerobic microorganisms was observed. It was also
found that in anaerobic sludge the degradation of low molecular weight fragments is carried out.
One can conclude that these small fragments are used by microorganisms as biological substrate.
We also proved that investigated reactions are able to participate on processes of degradation of
waste from chlorinated polymers in the environment.
Acknowledgement
This work was supported by the Slovak Research and Development Agency under the contract No.
APVV-0122-12.
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