Microbial community structure in anaerobic degradation of terephthalate and phenol 3

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Microbial community structure in anaerobic degradation of terephthalate and phenol 3

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Introduction Chapter Introduction Introduction 1.1 Background With the advancement of technology in the 20th century, synthetic products such as petrochemical-related materials have gained their popularity due to their durability in physical properties and aesthetics in appearance. As a result, the demand of raw materials such as terephthalate and phenol for the manufacturing of plastic or petrochemical-related products has increased, and the production of terephthalate- and phenol-containing wastewaters has also increased over the years. Purified terephthalate (PTA, or 1,4-benzenedicarboxylic acid) is an important raw material used in the manufacture of various plastic products. The most well-known application of PTA is the production of polyethylene terephthalate (PET) bottles for carbonated drinks (Park & Sheehan, 1996). Other applications include polyester films, textile fibers, adhesive, coatings and packing materials (Franck & Stadelhofer, 1988). PTA is mainly produced in Asia (South Korea, Taiwan, China, Indonesia, Japan, Thailand and Malaysia), and the amount accounts for approximately 66% of total PTA production worldwide. The amount produced was approximately 35 million tons in 2006, and is increased at an annual rate of to 10% (Razo-Flores et al., 2006). During the production of PTA, high-strength wastewater containing terephthalate as the main component and other organic compounds like acetate, benzoate and p-toluate (para-toluate) is produced and discharged. Typically, one ton of PTA produced is accompanied by about 2.5−4.5 m3 of wastewater at a concentration equivalent to 20−40 kg chemical oxygen demand (COD)/m3 (Bushway & Gilman, 1986; Kleerebezem et al., 1999c; Shelley, 1991; Vanduffel, 1993). Introduction Like PTA, phenol is used as the raw material for the production of various resins like phenolic, epoxy, polycarbonate and polyamide for plywood adhesive, construction, automotive and appliance industries (Kirk-Othmer, 1978). The amount produced was estimated to be million tons in 2001 and is increased at an annual rate of 6%. Phenol is also a common constituent in the wastewaters generated from phenol manufacturing processes, petrochemical-related processes, coal gasification, coke ovens and oil refining processes. The concentration of phenol and phenolic compounds in wastewaters is approximately 1.0−1.7 x 104 mg/L, and the COD contributed by phenol and phenolic compounds ranges from 40 to 80% of the total COD in the wastewaters (Veeresh et al., 2005). With the advantages of cost-saving (low energy and nutrients requirements), effective removal, and energy recovery (methane), anaerobic biological treatments processes have gradually replaced aerobic processes as an attractive alternative for treating toxic and poorly biodegradable wastewaters. Since the late 1980s, various types of full-scale anaerobic reactors including the downflow stationary fixed film (DSFF), hybrid, anaerobic contact (AC), upflow anaerobic sludge bed (UASB), downflow anaerobic filter (DAF), internal circulation (IC), expanded granular sludge bed (EGSB) and upflow anaerobic filter (UAF) systems have been demonstrated to effectively treat PTA wastewater (Macarie, 2000). During these anaerobic treatment, degradation of terephthalate has been suggested as the rate limiting step (Kleerebezem et al., 1997; Kleerebezem et al., 2005). Phenol is highly toxic and a strong growth inhibitor for microorganisms, but it has been successfully treated by a full-scale and a number of Introduction laboratory-scale anaerobic reactors (Lao, 2002; Suidan et al., 1983a; Veeresh et al., 2005). During the anaerobic methanogenic treatment, terephthalate and phenol are degraded through methanogenic metabolism in the absence of alternative electron acceptors (e.g., sulfates, nitrates and oxidized forms metals). This process requires the interaction between syntrophic fermentative bacteria and methanogenic archaea (methanogens) so that the degradation of terephthalate and phenol can be coupled with the hydrogen- and acetate-consuming reactions to overcome the thermodynamic barrier in the initial step (positive Gibbs free energy, ∆Go') (Fig. 1.1), and the intermediates can be converted to the final gaseous products (CH4 and CO2). Figure 1.1 conditions. Proposed terephthalate and phenol degradation under methanogenic 1.2 Problem statements Due to the recent awareness of environmental protection, more stringent environmental legislation has been implemented to control the discharge of potentially harmful compounds in many countries. Phenol is a carcinogenic compound, and can affect Introduction aquatic life at concentrations >1 mg/L (Autenrieth et al., 1991), whereas the toxicity of terephthalate remains unclear. Thus, the release of these compounds in environments has attracted great environmental and public health concerns in recent years, and there is a strong need to effectively treat these terephthalate- and phenol-containing wastewaters before discharge. Over the last 20 years, although empirical know-how of anaerobic treatment technologies utilimately reaches the good performance on the treatments of these wastewaters, these still face a number of challenges, as described below, for improvement. (A) Limited application of treatment processes for PTA wastewater at temperatures above 37°C Anaerobic processes for treating PTA wastewater have been successfully achieved under mesophilic (30−37ºC) conditions. As the production of PTA is carried out under high pressure and temperature, the PTA wastewaters are usually generated at high temperatures (40−60ºC). Therefore, additional time to store them in an equalization tank to cool down the wastewater before the mesophilic anaerobic treatment processes is necessary. It further suggests that anaerobic treatment processes under high temperatures (>37ºC) conditions can be an attractive alternative. So far, the development of thermophilic anaerobic treatment is relatively limited. Thermophilic treatments are reported to generally have much higher specific organic removal rates than the mesophilic treatments (van Lier et al., 1997), but it is relatively difficult to establish a stable microbial consortium in the thermophilic (55°C) terephthalate-degrading reactor (Kleerebezem et al., 1999c). This is attributed to a low number of thermophilic Introduction terephthalate-degrading microorganisms in the original seed sludge, and inappropriate operational conditions to enrich the microbial consortia (Kleerebezem et al., 1999c). Until now, the biodegradability of terephthalate and the responsible microorganisms at temperatures above 37°C is poorly known and further studies are necessary. (B) Limited information on phenol-degrading microbial consortia Anaerobic biological processes have been demonstrated to efficiently treat phenol-containing wastewaters at organic loadings (6−8 kg COD/m3 • day) in the laboratory-scale bioreactors (Veeresh et al., 2005). Prior to reaching the extraordinary performance (>90% removal of phenol), it requires a long start-up time (~300 days) to acclimatize the suitable microbial populations from seed sludge, to develop efficient phenol-degrading capability as well as particular microbial interaction and spatial orientation that can facilitate the rapid exchange of nutrients and products (Veeresh et al., 2005). Like the terephthalate-degrading methanogenic consortium, phenol degradation under thermophilic conditions is reported to be relatively difficult and unstable as compared to that under mesophilic conditions (Fang et al., 2006; Karlsson et al., 1999). As a result, the development of thermophilic techniques to treat phenol-containing wastewater is relatively limited. A better understanding of the phenol-degrading microbial community could provide crucial information for better selection of seeding sludge to shorten the start-up time in the mesophilic processes, and facilitate the development of thermophilic processes. So far, the phenol-degrading methanogenic microbial consortia was only characterized for biomass samples taken from a laboratory reactor operated at a temperature at 26°C (Fang et al., 2004; Zhang et al., 2005). The Introduction microbial populations responsible for phenol degradation under mesophilic and thermophilic conditions have not been fully identified and characterized. (C) Limited information on full-scale reactor to treat phenol-containing wastewater Many anaerobic laboratory-scale bioreactors have been successfully used to treat phenol-containing wastewaters. However, most of them were fed with synthetic wastewater and had better control of the operational parmeters (e.g., loading rate, recycle rate, temperature and hydraulic retention time [HRT]). These laboratory-scale bioreactors may not provide the same environmental conditions as the full-scale bioreators. As a result, the microbial populations found in the laboratory-scale bioreactors or enrichment cultures may not fully represent those in full-scale bioreactors treating wastewaters containing phenol. So far, only one full-scale UASB reactor has been constructed and operated to treat the wastewater from phenol production under mesophilic conditions since 1986 (Macarie, 2000). To facilitate the development of full-scale processes, a better understanding of the phenol-degrading microbial community in a full-scale plant is necessary. (D) Limitation of conventional culture-dependent approaches The bioreactor where the degradation of organic pollutants takes place traditonally referred to as a “black box”. In the past 10 years, microbial populations inside wastewater treatment plants have been extensively studied in order to correlate their identity, abundance and dynamics to the reactor performance. In anaerobic wastewater treatment systems for treating terephthalate- or phenol-containing wastewaters, microorganisms Introduction play as the catalysts to degrade the substances. However, owing to the limitations associated with the conventional techniques (time-consuming and low culturability of environmental microorganisms) and the difficulty of isolating syntrophic bacteria, only two mesophilic terephthalate-degrading bacteria (Pelotomaculum terephthalicum and Pelotomaculum isophthalicum) (Qiu et al., 2004; Qiu et al., 2006) and one phenol-transforming bacteria (Cryptanaerobacter phenolicus) (Juteau et al., 2005) have been isolated. The presence of these isolates P. isophthalicum, P. terephthalicum and C. phenolicus in the laboratory-, pilot- and full-scale terephthalate- or phenol-degrading reactors remains unknown. It is almost impossible to describe microbial community in the reactors based on the information of limited isolate strains available so far, and the isolates may not even represent as the main population involved in terephthalate or phenol degradation. Therefore, the microbial community structures in anaerobic degradation of terephthalate and phenol remain to be further characterized. Recently, microbial populations inside wastewater treatment plants have been extensively investigated using 16S rRNA-based culture-independent molecular techniques with an attempt to identify the key players and understand their abundance, dynamics, and distribution within the “black box” in relation to the reactor performance. These in-depth understandings are important to optimize biological processes. 1.3 Objectives The overall objective of this research is to study the microbial community structures responsible for anaerobic terephthalate and phenol degradation using 16S rRNA gene-based molecular approaches. Specific objectives are: Introduction a. To characterize the microbial community structure and dynamics in a thermophilic (55°C) anaerobic laboratory-scale hybrid reactor degrading terephthalate-containing wastewater, b. To study the microbial community structure in a terephthalate-degrading anaerobic hybrid bioreactor operated at 46−50°C, c. To identify the important microbial populations in the methanogenic phenol-degrading enrichments under mesophilic (37°C) and thermophilic (55°C) conditions, and d. To investigate the microbial community structure in a mesophilic full-scale phenol-degrading anaerobic fluidized bed reactor. The results will provide evidence that terephthalate can be degraded under 46−50ºC and 55ºC conditions; improve our understanding of syntrophic microorganisms in the terephthalate and phenol degradation systems; identify microorganisms that are important to the degradation; and provide additional knowledge for future development of methanogenic treatment technologies for terephalate- and phenol-containing wastewaters. 1.4 Organization of the thesis The thesis consists of eight chapters. Chapter provides a general introduction, the problem statements and objectives. 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(ºC) Reactor volume (L) Full − 1280 m3 Lab 37 0.66 Lab 37 2.8 Lab 37 2.8 Lab 37 2.8 Sucrose ( 134 ) 0 .33 0.5 Phenol/ p -cresol: 800 /30 0 − Lab 35 2.0 0.5 37 2.0 Lab 30 0.16 Lab 26 2.8 Phenol: 1260 Phenol: 1260 Phenol/ p -cresol: 280/ 132 Phenol: 1260 6 Lab Glucose (260) Glucose (120) Acetate (55) Glucose (−) 0.5 1 0.5 0.50.6 0.5 8 7 6 Phenol: 98±1 Phenol: 100 p-cresol: 93 Phenol: 98 References (Borghans & van... matters and the standard Gibbs free-energy Fermentative reaction ∆Go' (kJ/reaction) Terephthalate + 8 H2O → 3 acetate- + 2 HCO3- + 3 H+ + 3 H2 +38 .9 Phenol + 5 H2O → 3 acetate- + 3 H+ + 2 H2 +10.2 Hydrogenotrophic methanogenesis 4 H2 + HCO3- + H+ → CH4 + 3 H2O − 131 .2 Acetotrophic methanogensis Acetate- + H2O → CH4 + HCO3- 2.2.2 32 .6 Proposed terephthalate degradation pathway Anaerobic degradation of terephthalate. .. terms “phenols”, “total phenols” or “phenolics” used for wastewaters or contaminated sites denote simple phenol or a mixture of phenolic compounds, such as phenol, cresol isomers (ortho-, meta- and para-), resorcinol, hydriquinone and dimethyl phenol Phenols are often found in wastewaters generated from coal gasification, coke ovens, and petroleum-related manufacturing processes (e.g., phenolic resin,... studies Using microscopy, Kleerebezem and co-workers (1999a, b) observed that spore-forming rods (3 to 4 µm) were associated with Methanosaeta- and Methanospirillum-like cells in a terephthalate- degrading consortium degrading bacteria was 7−28 days The doubling time of these terephthalate- Wu and co-workers (2001) studied the microbial community structure in a mesophilic terephthalate- degrading granular... dominant microbial populations could be identified However, they observed that the microbial populations under thermophilic conditions were different from those observed in the bioreactor operated under ambient temperature The microbial communities involving in thermophilic phenol degradation remain to be characterized 32 Materials and Methods Chapter 3 Materials and Methods 33 Materials and Methods 3. 1... extremely slow in the media containg isophthalate in the presence of Methanospirillum hungatei cells A defined “pure co-culture” of strain JIT was obtained by co-cultured with M hungatei with 3- hydroxybenzoate (5 mM) and yeast extract (0.02%) as the carbon substrate The cells are 0.8−1.0 µm wide and 2.0 3. 0 µm long, occurring singly or in pairs The spores are spherical and at central of the cell Tiny colonies,... 2.1 Anaerobic treatment of terephthalate- and phenol- containing wastewaters During the past 20 years, anaerobic digestion processes have become an attractive biological approach to treat toxic and poorly biodegradable wastewaters (e.g., petrochemical wastewaters) (Lettinga, 1995) In these processes, organic compounds are degraded and converted into methane and carbon dioxide in the absence of oxygen and. .. populations in this UASB system Like anaerobic degradation of terephthalate, the initial conversion of phenol has been identified as the rate-limiting step As a result, non-layered structure of phenol- degrading granules was observed in the UASB reactors operated at 26°C (Fang et al., 1996; Zhang et al., 2005) 31 Literature Review Fang and co-workers (2006) also enriched a phenol- degrading methanogenic... with that reported by Evans (1977) Thus, the degradation pathway of phenol via caproate needs to be further confirmed 2 .3 Microbial communities for terephthalate and phenol degradation 2 .3. 1 Microorganisms involved in terephthalate degradation 2 .3. 1.1 Culture-dependent studies Two mesophilic terephthalate- degrading bacteria, Pelotomaculum terephthalicum and Pelotomaculum isophthalicum have been isolated... and Methods 3. 1 Terephthalate- and phenol- degrading microbial consortia 3. 1.1 Thermophilic anaerobic terephthalate- degrading reactor A 1.2-liter laboratory-scale hybrid reactor, packed with 69 polypropylene Pall rings (Flexiring®, Koch Inc.) (total volume = 400 mL), was used to enrich anaerobic microbial consortia degrading terephthalate under thermophilic conditions (Fig 3. 1) was inoculated with seed . represent as the main population involved in terephthalate or phenol degradation. Therefore, the microbial community structures in anaerobic degradation of terephthalate and phenol remain to be further. coke ovens and oil refining processes. The concentration of phenol and phenolic compounds in wastewaters is approximately 1.0−1.7 x 10 4 mg/L, and the COD contributed by phenol and phenolic. development of thermophilic techniques to treat phenol- containing wastewater is relatively limited. A better understanding of the phenol- degrading microbial community could provide crucial information

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