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Review

Archaeal Diversity in Biofilm Technologies Applied to Treat Urban and Industrial Wastewater: Recent Advances and Future Prospects

by
Kadiya Calderón
1,*,†,
Alejandro González-Martínez
2,
Cinta Gómez-Silván
1,
Francisco Osorio
2,
Belén Rodelas
1 and
Jesús González-López
1
1
Environmental Microbiology Group, Department of Microbiology, Faculty of Pharmacy, and Institute of Water Research, University of Granada, Campus de Cartuja s/n, Granada 18071, Spain
2
Environmental Microbiology Group, Department of Civil Engineering, and Institute of Water Research, University of Granada, Campus de Cartuja s/n, Granada 18071, Spain
*
Author to whom correspondence should be addressed.
Present address: INRA, UMR 1347 Agroecology, 17 rue Sully, Dijon 21000, France.
Int. J. Mol. Sci. 2013, 14(9), 18572-18598; https://doi.org/10.3390/ijms140918572
Submission received: 18 July 2013 / Revised: 22 August 2013 / Accepted: 30 August 2013 / Published: 9 September 2013
(This article belongs to the Special Issue Biofilms: Extracellular Bastions of Bacteria)

Abstract

:
Biological wastewater treatment (WWT) frequently relies on biofilms for the removal of anthropogenic contaminants. The use of inert carrier materials to support biofilm development is often required, although under certain operating conditions microorganisms yield structures called granules, dense aggregates of self-immobilized cells with the characteristics of biofilms maintained in suspension. Molecular techniques have been successfully applied in recent years to identify the prokaryotic communities inhabiting biofilms in WWT plants. Although methanogenic Archaea are widely acknowledged as key players for the degradation of organic matter in anaerobic bioreactors, other biotechnological functions fulfilled by Archaea are less explored, and research on their significance and potential for WWT is largely needed. In addition, the occurrence of biofilms in WWT plants can sometimes be a source of operational problems. This is the case for membrane bioreactors (MBR), an advanced technology that combines conventional biological treatment with membrane filtration, which is strongly limited by biofouling, defined as the undesirable accumulation of microbial biofilms and other materials on membrane surfaces. The prevalence and spatial distribution of archaeal communities in biofilm-based WWT as well as their role in biofouling are reviewed here, in order to illustrate the significance of this prokaryotic cellular lineage in engineered environments devoted to WWT.

1. Archaea and Biofilms: An Introduction

Archaea is one of the three domains of life distinguished by Carl Woese by phylogenetic analysis based on 16S rRNA genes [1]. They are abundant and metabolically-diverse microorganisms which coexist with Bacteria and Eukarya in most Earth environments; however, they remain the least well known of the branches of the phylogenetic tree of life, despite the many efforts made to investigate their role in natural and engineered systems [2]. Their diversity remains rather unexplored, although it has been estimated to be comparable to that observed for Bacteria [2]. The physiological functions of the Archaea identified in mixed microbial communities suggest their significant role in the biogeochemical cycles of the planet, maintaining the flow and recycling of the nutrients in many environments [3]. In particular, the recent discovery of ammonia-oxidizing Archaea (AOA) changed the classical view of the nitrogen (N) cycle, as AOA are currently regarded as the main ammonia-oxidizing organisms in oceans and geothermal habitats [4].
Biofilms are complex, spatially-structured multicellular communities, formed on the surfaces or interfaces of materials of both organic and inorganic nature [5]. Biofilms are known to have existed since the discovery of microorganisms, as they were first visualized by van Leewenhoeck in the XVII century [6], and have become accepted as the dominant microbial life style in nature. Cell aggregation and surface adhesion provide a protected mode of growth, enabling survival in hostile environments. The nature of biofilm structure is dynamic, as the cells anchored to the surface eventually disperse and revert into the planktonic mode of living, which then enables the colonization of new niches [7].
The steps that lead to the formation of microbial biofilms have been extensively described by different authors [5,8,9]. It is generally accepted that the process starts when microbes associated with a surface change from a reversible to an irreversible mode of attachment to it, followed by the aggregation of cells and their subsequent proliferation. The cells in the biofilm are encased in a matrix of self-produced polymers of heterogeneous nature (lipids, polysaccharides, extracellular nucleic acids or proteins), referred to as the EPS (extracellular polymeric substances), which fulfill important functions [5]. The extraordinary tolerance of biofilms to antimicrobial compounds, heavy metals and other damaging agents derives from a complex mixture of physical, chemical and physiological factors: the metabolic heterogeneity of the community, the particular physiological state of the microorganisms in the different biofilm layers, the support of syntrophic and other mutualistic interactions, and the development of specialized subpopulations of resistant phenotypes and persister cells [10]. The relative contribution of each of these mechanisms (and possibly others) varies with the type of biofilm and the nature of the environment where they develop [3].
Since biofilms have been recorded in fossils more three billion years old, this lifestyle is acknowledged as an ancient feature of prokaryotes [7]. In past decades, the focus of researchers was centered mainly on bacterial biofilms; however, thanks to recent advances in monospecies cultures, it has been possible to demonstrate that Archaea are also capable of attaching to biotic and abiotic surfaces and developing biofilms [3]. Biofilm formation in the environment by members of the archaeal Phyla Euryarchaeaota, Crenarchaeota, Korarchaeota and Thaumarchaeota is well documented, particularly in extreme habitats [1114]. It is also well known that Archaea are present in biofilms of engineered habitats, such as acid-mine drainages, aquarium biofilters, or wastewater treatment (WWT) plants based on different technologies [1419]. This review aims to summarize the current knowledge on the characteristics of Archaea and the roles they play under the biofilm lifestyle in WWT systems, with particular emphasis on their occurrence, diversity and attributed functions.

2. Biofilm Systems Associated to WWT

Biological WWT technologies based on the use of biofilms are broadly applied for the removal of organic matter, nitrogen and other anthropogenic contaminants occurring in wastewater. Mixed-population biofilms develop in these systems, normally requiring the addition of carrier inert materials to provide a supporting surface. Although many configurations of biofilm-based WWT plants have been devised, they can be classified into two broad types: fixed-bed reactors, which regard all systems in which the biofilms develop on a static media; and expanded-bed reactors, which include carrier media subjected to continuous motion driven by stirring or an air flux [20]. Amongst other advantages compared to the more generally applied conventional activated sludge (CAS) technology, biofilm-based systems are simple to control and maintain, reduce space needs, lower cost, and minimize unwanted odors and noise [21].
Different WWT systems use granular sludge (GS), based on the aggregation of microbial biomass in structures named granules, which are regarded as suspended biofilm systems and dissimilar to flocs in their shape, structure and substrate diffusion properties [22,23]. Their typical morphology and inner structure is shown in Figure 1 [23]. Granules develop in the absence of a supporting surface by the auto-immobilization of the microorganisms, and are functionally described as concentric layers of densely-packed, near-spherical biofilms, each of which is inhabited by different microbial trophic groups [24,25]. Each granule is a functional unit in itself, comprising all the different microorganisms necessary for the degradation of wastewater, producing biomass and EPS [26].
GS has advantages over the conventional floc aggregates and biofilms developed on supporting media, with the main one being the wider surface area provided for the biofilm [27]. GS can develop in both aerobic and anaerobic systems, provided that certain conditions are given in bioreactor design [28]. The granulation process and granule stability are affected by many operating and external factors such as temperature, hydraulic retention time (HRT), organic loading rate (OLR), nutrient availability, and the presence of divalent cations and heavy metals [25,26,28,29]. In this review, only factors known to have an influence on archaeal diversity will be discussed.

3. Archaeal Communities in Anaerobic Bioreactors

Anaerobic bioreactors are used for the degradation of organic matter, generating methane as a value-added by-product [30]. The methanogenic metabolism is an exclusive feature of a group of prokaryotes classified in the Phylum Euryarchaeota, which is currently divided into six orders: Methanobacteriales, Methanococcales, Methanomicrobiales, Methanosarcinales, Methanopyrales and Methanocellales [31,32]. There are also a number of 16S rRNA gene types that are often retrieved from WWT which presumably belong to as yet uncultivated archaeal taxa with metabolic functions close to those of known methanogens [33]. This is the case of sequences assigned to the WSA2 (or ArcI) group, which is considered to be an archaeal taxon at the class level [34].
Despite their ample phylogenetic, morphological and physiological diversity, methanogens only use a limited number of substrates to obtain energy. Most methanogens are restricted to using H2 + CO2 or formate [31]. Some members of the Methanomicrobiales use secondary alcohols, and Methanosarcinales are the more metabolically versatile, being often able to use methyl group-containing compounds and also comprising the only acetoclastic methanogens, Methanosarcina spp. and Methanosaeta spp. [30,31].
Studies on the microbial diversity of anaerobic bioreactors have increased in the last 20 years, fuelled by the introduction of molecular cultivation independent methods. A wide array of primers and probes targeting phylogenetic markers of methanogens are currently available [34]. The archaeal diversity in this type of systems is limited when compared with bacterial diversity. The sequences retrieved from anaerobic reactors belong mostly to members of the Euryarchaeota phylum, although the occurrence of crenarchaeotal sequences has also been reported [33,3537]. Despite the many differences in wastewater nature, bioreactor design and operating conditions, an overall conclusion is that the dominant Archaea are the methanogens, which usually belong to the Methanobacteriaceae, Methanosarcinaceae and Methanosaetaceae [35,3743]. In most of the systems studied, both acetoclastic and hydrogenotrophic CO2-utilizing methanogenic Archaea coexist. It has been suggested that this configures the minimal archaeal microbiota required for stable anaerobic digestion [35].
Granular biomass formation by archaeal populations has been widely studied in anaerobic digestion processes [22,35,3741,4449]. From the technological point of view, these systems comprise mainly the UASB and expanded granular sludge bed (EGSB) reactors [28]. In 2003, McHugh et al. [50] proposed a layered structure for the anaerobic granules in which a central core of acetoclastic methanogens is surrounded by a layer of hydrogen- or formate-producing acetogens and hydrogen- or formate-consuming methanogens. The proposed granule structure provides an outside layer of microorganisms that hydrolyze and acidify complex organic matter [51] (Figure 2). Once the reactors have been seeded with anaerobic sludge and wastewater, the wastewater flows in the upward direction through the sludge and granule formation slowly occurs spontaneously under appropriate conditions of substrate and nutrient availability, pH, alkalinity, and upflow velocity [26].
Several other types of anaerobic reactors have been successfully designed and applied to a lesser extent for the treatment of a wide range of organic-rich wastewaters (reviewed by Tabatabaei et al. [41]). Anaerobic reactors comprising a fixed-bed or an expanded-bed phase for biofilm development have been widely evaluated for the treatment of urban and industrial wastewaters [35]. The bioreactors can be entirely designed as biofilm-based, or include a biofilm phase associated to a granular phase as part of an UASB or an anaerobic baffled reactor (ABR). Methanogenic Archaea adhere preferentially to packing support materials [52]; thus, the performance of methanogenesis is higher in bioreactors when such a surface is provided for biofilm development [42]. Besides, a biofilm phase helps to improve and maintain granulation in the associated granular phase [53]. Several packing materials, such as charcoal, gravel, brick pieces, pumice stones, coconut coir, carbon fiber, nylon fiber and plastic pieces have been tested [54,55].
Some efforts have been made to describe the core prokaryotic microorganisms essential for the anaerobic degradation of organic matter, providing evidence that the archaeal communities are indeed composed of a restricted number of operational taxonomic units (OTUs). Leclerc et al. [35] used molecular methods (16S rRNA-based single-strand conformation polymorphism fingerprints and clone libraries) to analyze and compare the diversity of Archaea in 44 anaerobic bioreactors based on different technologies and treating diverse types of wastes. Most frequently, a combination of sequences phylogenetically close to Methanobacterium spp. and Methanosaeta concilii was found. The authors also concluded that the distribution of the archaeal species was not strongly influenced by the nature of the wastewater, but depended in part on the type of bioreactor technology. The stirred-tank digesters were able to support a community of a higher diversity compared to the biofilm-based technologies. Some archaeal populations were often found to exclude each other, showing preference for a particular type of bioreactor design. For instance, Methanosarcina frisus was prevalent in stirred-tank and fixed-film digesters, but occurred in low levels in upflow anaerobic sludge bed (UASB) reactors, which in contrast favored the presence of Methanosaeta spp. Rivière et al. [33] compared seven mesophilic (29–37 °C) digesters used for sludge reduction in urban WWT plants across France, Germany and Chile, by analyzing large clone libraries of archaeal 16S rRNA gene fragments. In total, 69 different archaeal OTUs were found, with the majority of the sequences (62.4%) being affiliated to three OTUs shared among 4–7 of the analyzed digesters, and 24 other OTUs (34%) shared by 2–4 digesters. The last 42 OTUs were specific for one digester (3.6% of the sequences). In agreement with the study by Leclerc et al. [35], most of the recognized OTUs were affiliated to methanogenic Archaea (Methanosarcinales, Methanomicrobiales, Methanobacteriales and ArcI group) with Methanosaeta spp. as the main acetoclastic methanogen. Interestingly, the most represented OTU belonged to the ArcI lineage, and members of ArcI were the dominant archaeal populations (41%–69% of the sequences) in four of the analyzed anaerobic digesters.
The structure of archaeal communities in fixed-bed or expanded-bed biofilm systems has been scarcely investigated. In the study by Leclerc et al. [35], one fixed-bed reactor and seven fluidized-bed reactors treating diverse types of industrial wastewaters (brewery, winery, dairy) were evaluated, finding Methanobacterium, Methanosaeta and Methanosarcina as the prevalent genera. Comparing the results with those of GS systems, the authors concluded that all the fixed-bed and fluidized-bed reactors exhibited similar and distinctive archaeal diversity patterns, suggesting that the required attachment of cells to the supporting media strongly conditioned community structure. More recent studies indicate that Methanobacteriales and Methanomicrobiales coexist in fixed-film anaerobic reactors. Zhang et al. [42] explored the community dynamics in different compartments of two mesophilic fixed-bed anaerobic baffled reactors (FABRs) by the generation of archaeal clone libraries of the 16S rRNA gene and quantitative real-time PCR (qPCR). Although Methanobacteriales and Methanosaeta dominated the seed sludge used to inoculate the FABRs, Methanomicrobiales increased 30- to 42-fold after 32 days of operation. Methanolinea and Methanospirillum showed a preference to colonize the carbon fiber support during the start-up period, particularly in the last compartment of the system, where methanogenesis took place at the highest rate. Rademacher et al. [43] characterized the community structure of microbial biofilms developed in a thermophilic biogas system, by means of massive parallel sequencing (454-pyrosequencing). The bioreactor was a two-phase leach-bed process, with separate compartments for cellulolysis and methanogenesis on fixed-films supported by plastic carriers (Bioflow-40 media). 16S rRNA gene sequences and analysis of Pfam protein families were used to describe the structure of both the cellulolytic and methanogenic communities. Archaea represented 2% of the 16S rRNA sequences retrieved from the cellulolytic biofilm and a 12% of the methanogenic biofilm. Methanomicrobia dominated in the cellulolytic biofilm (2%), while both Methanomicrobia (7%) and Methanobacteria (4%) prevailed in the methanogenic biofilm, where the two most abundant genera detected were Methanosarcina and Methanobacterium (both 4%). The functional analysis supported the evidence of a clear spatial distribution of Archaea between both compartments. Four percent of the environmental genes belonged to Archaea in the cellulolytic biofilm, while the methanogenic biofilm revealed a higher contribution (22%).
The influence of operation conditions on the diversity of archaeal communities in GS, fixed-bed and expanded-bed reactors has been widely investigated in recent years. Two factors often regarded relevant are OLR and HRT. Several studies have been conducted under varying ORL and HRT in reactors treating municipal and industrial wastewaters of diverse nature and operated at different temperatures [37,39,40,44,56,57]. Analyzing the diversity of the prokaryotic communities by means of different molecular approaches, most of these studies concluded that Archaea were less sensitive than bacteria to changes in ORL and HRT [37,39,44,56]. The archaeal community in GS remained rather stable throughout operation, being mainly composed of members of Methanobacteriaceae, Methanosaetaceae and Methanosarcinaceae (Table 1). In contrast, in the packed-bed biofilm reactors the community was dominated by Methanobacteriaceae, Methanomicrobiaceae and Methanosarcinaceae, whose prevalence shifted along the experiments depending on the changes of both ORL and HRT [56,57].
Temperature is one factor that can affect the structure and dynamics of microbial communities in WWT plants; Archaea are not an exception. Several studies have evaluated the effect of temperature on the methanogenic communities in anaerobic bioreactors, comparing their diversity under thermophilic, mesophilic, or psycrophilic conditions. A pioneering work by Visser et al. [38] using immunochemical methods revealed differences in the composition of the methanogenic community after a temperature change from 38 to 55 °C, showing that diversity decreased at higher temperatures and that quantitative changes of the size of several subpopulations took place, including Methanobrevibacter smithii, Methanobrevibacter arboriphilus, Methanosarcina thermophila, Methanospirillum hungatei, Methanobacterium thermoautotrophicum, and Methanogenium cariaci. In contrast, Sekiguchi et al. [58] analyzed a clone library representing the archaeal community in granules of two UASB reactors fed synthetic wastewater and operated at 35 and 55 °C, and detected a similar composition of the methanogenic communities, composed mainly of Methanosaeta concilii, Methanosaeta thermophila and populations closely related to the Methanobacteriales. Using more sensitive molecular fingerprinting methods, Khemkhao et al. [47] evaluated the adaptation of microbial diversity from mesophilic to thermophilic conditions in five consecutive phases (37, 42, 47, 52 and 57 °C) in a UASB granular reactor treating palm oil mill effluent. The results of their study showed that in all cases the acetoclastic methanogens (Methanosaeta and Methanosarcina) were the dominant Archaea detected in the granules. Also, these authors reported that the dynamics of the archaeal populations were low at temperatures below 52 °C, while important microbial community shifts, particularly of the Methanosaeta species, occurred when temperature rose from 52 to 57 °C [47].
Many efforts have been focused to investigate the effect of low temperatures on archaeal diversity in GS anaerobic bioreactors, since the development of a well-functioning psychrophilic microbial consortium is a key factor to keep their operational stability. The results of several studies comparing parallel experiments in bioreactors operated at both psycrophilic and mesophilic conditions are summarized in Table 2, demonstrating temperature-dependent changes of the methanogenic community structure. A general conclusion is that the relative abundance of Methanosaeta spp. decreased at 15 °C, favoring the proliferation of Methanosarcina spp., and the dominance of the hydrogenotrophic methanogens, particularly the Methanomicrobiales. Other available studies reached similar conclusions regarding the diversity of methanogens in anaerobic GS operated at low temperature [5961]. Besides, O’Reilly et al. [45] concluded that the structure of the archaeal communities was drastically changed from that of the seed sludge under mesophilic conditions, while it remained considerably more stable under psychrophilic conditions.
In contrast, few studies have been directed to unravel how low temperatures influence methanogenic populations in anaerobic fixed-bed biofilm systems. 16S rRNA clone libraries and qPCR analyses demonstrated that Methanomicrobiales became enriched and displaced the Methanobacteriales in a packed-bed biofilm anaerobic reactor when temperature dropped from 18 to 5 °C, while the Methanosaetaceae remained at similar levels of abundance throughout the experiment [62]. Members of the Methanomicrobiales and Methanosaetaceae were able to proliferate and become stably adhered to the carbon fiber carrier; hence, the authors concluded that these archaeal groups had an important role for the efficiency of methanogenesis at low temperatures in this type of system.
The effect of the dissolved oxygen concentration (DO) on the archaeal populations in GS has been also evaluated. Hirisawa et al. [64] demonstrated that oxygen concentration did not affect significantly the performance or microbial diversity of UASB granular reactors when operated at different chemical oxygen demand (COD) to sulphate ratios (COD: SO42−). Archaea were the dominant domain inside the UASB reactor (68% of the cells) with a DO of 3.0 ± 0.7 mg/L. Under these operational conditions, Methanosaeta-like cells were the main methanogens detected by FISH and DGGE fingerprinting. The authors postulated the formation of consortia by the methanogens and facultative bacteria which were able to fast uptake the available O2, providing a mechanism of aerotolerance to the methanogens. Additionally, these results were obtained in granular sludge with a large size (2–3 mm diameter), which was found to be the majority of granular biomass inside the reactor (76%). The thickness of the granules and their concentric layered structure acted as a physical barrier to oxygen diffusion, and segregated niches of low-oxygen concentration were generated in their inner zones. Granular sludge of smaller diameter may thus yield different results. The tolerance of methanogenesis to oxygen in GS is of great interest, as this study demonstrated that the application of limited oxygen quantities did not inhibit methanogenesis or sulphate reduction in the UASB, while it allowed a low production of hydrogen sulphide, which is a toxic compound for the hydrogenotrophic methanogens.
The chemical composition of the treated water also affects the characteristics of the microbial communities in GS. Kobayashi et al. [65] reported that granulation was enhanced by the addition of certain concentrations of starch-containing waste to an UASB bioreactor treating methanol wastes, increasing the size of the granules formed in the bioreactor. Moreover, the addition of starch led to drastic changes of the structure of the archaeal populations, as revealed by DGGE and FISH. The authors observed that in the absence of starch the main archaeal species in the granular bioreactor were Methanomethylovorans hollandica, Methanobacterium aarhusense, Methanobacterium subterraneum and Methanolinea tarda. When starch was added to the UASB, methylotrophic Methanomethylovorans hollandica were still the most abundant methanogens, but an important shift of the rest of populations occurred, and Methanosaeta spp. (M. concilii and M. barkeri) became prevalent in the community. The authors pointed to the generation of acetate due to the degradation of the starch by fermentative bacteria as a possible factor influencing the proliferation of the acetoclastic Methanosaeta species.
Besides the metabolic role of methanogenic Archaea in anaerobic digestion, their contribution to the stability of GS has been widely reported. Many of the above-mentioned studies highlight that Methanosaeta spp. populations are abundant in stable, big-size granules, concluding that these organisms are required for the good performance of anaerobic bioreactors. Due to their filamentous-like morphology, these methanogens have been suggested to act as a backbone for granule initiation, becoming the basis for gathering other granule-forming microorganisms [66,67]. In particular, Methanosaeta concilii is believed to play a key role in setting up granulation [6870]. The initiation of granules by filamentous cells is followed by the subsequent colonization of acetogenic bacteria and hydrogenotrophic methanogens, leading to the layered granular biofilm structure [26].
The diversity or possible roles of Archaea in aerobic granular formation are completely unknown. Recent studies based on molecular tools have thoroughly analyzed the roles of bacteria, ciliated protozoa and fungi on the structuration of granules and their stability; however, the archaeal division was not explored [22,71]. Methanogenic Archaea seem not to be restricted to colonize and form biofilms in engineered systems operated under anaerobic conditions. Goméz-Silván et al. [16] analyzed the structure of the archaeal communities in samples of different pilot-scale bioreactors treating wastewater under aerobic conditions, including biofilm samples from submerged fixed-biofilters consisting of one aerated and one anoxic column, and using clayey schists as the biofilm support media. Temperature gradient gel electrophoresis (TGGE) of 16S rRNA gene fragments and phylogenetic analysis of the reamplified TGGE bands demonstrated that populations affiliated to the methanogenic Archaea (Methanosarcinales, Methanobacteriales and Methanomicrobiales) were present in all of the analyzed samples regardless of the aeration conditions, although the composition of the community varied depending of the characteristics of the treated water and the type of technology used. These authors also suggested that the methanogens found in the aerated WWT plants investigated in their study may simply survive under oxygen exposure and be restricted in their activity to the anoxic areas of the plants, or just play structural roles in cell-aggregate development as they are proposed to do in GS. Archaea have also been detected in other aerated WWT systems [7276].

4. Ammonia-Oxidizing Archaea (AOA) in WWT Plants: Occurrence and Significance

Since the first description of an aerobic Crenarchaeota group as potential ammonia-oxidizing organisms [77], the global N-cycle has been reconsidered. After isolation of the first AOA, Nitrosopumilus maritimus [78], only one other isolate—Candidatus Nitrososphaera viennensis—has been obtained so far [79], although many other AOA have been enriched from different environments (Table 3). In recent years, a vast number of studies based on molecular tools were performed in natural ecosystems such as soils, oceans or geothermal habitats and allowed the evaluation of the contribution of AOA to ammonia oxidation. In many cases, AOA were found to be dominant over ammonia-oxidizing bacteria (AOB), which were, until then, the only known organisms responsible for the limiting step of nitrification: ammonia oxidation [4,80]. However, with few exceptions [11] the vast majority of studies performed to date have been based on the detection of the archaeal amoA gene without demonstrating active ammonia oxidation by AOA, and the presence or high abundance of a functional gene does not mean that its associated function is actually operating. For this reason, some authors proposed the term amoA-encoding archaeon (AEA) to refer to these prokaryotic organisms [8183]. Recently, phylogenetic studies lead to the reclassification of the AOA and AEA as members of a new archaeal Phylum, the Thaumarchaeota [4,84,85], and highlighted this group as the potential ancestor of Archaea [85].
Considering that ammonia is the main N-species in urban wastewaters, its average concentration, and the fact that the application of the CAS technology under aerated conditions is the most widespread WWT, an important role of AOA in the N-removal from the water bodies in engineered systems was initially expected. Using clone libraries, Park et al. [95] detected for the first time the presence of AEA in five out of nine different CAS-based WWT plants. However, since then, few studies have proven the presence of AEA in WWT based on different kind of technologies. Many of the available studies also compared the abundance of AEA with that of AOB (Table 4). The results obtained have led to controversial conclusions, reporting either the complete absence of AEA [96], a minimal contribution of AEA to the ammonia-oxidizing community [97100], an equal contribution [101], or even AEA outcompeting AOB under certain conditions [96,102104].
AOB and AOA are phylogenetically distant, displaying significant differences in cell physiology and structure, and also demonstrating a significant level of ecological differentiation, as they are present in diverse niches [107,108]. For example, AEA appear to be more sensitive to drought, lysis, temperature and pH changes compared to AOB [107,108]. In the early studies conducted in WWT plants, Park et al. [95] pointed out that the AEA occurred in systems with alternation of aeration conditions, with low DO and long retention times (solids retention time, SRT > 15 days, and HRT > 24 h), outcompeting AOB in a system with very low DO (<0.2 mg/L). The kinetic parameter (Ks) for oxygen described for AOA is slightly lower than the values described for AOB [83], but studies in other WWT systems also detected a high abundance of AEA at higher DO, suggesting that AEA tolerate a wide range of oxygen concentrations [105].
The effect of operational parameters like SRT and HRT is also not clarified. It is well known that longer retention times favor the development of slow-growth microorganisms, as it is the case for both AOB and AOA. In this sense, the membrane bioreactor (MBR) technologies intensify this effect, due to the separation of solids by a filtration process [109]. However, the few studies conducted in WWT plants using this kind of technology did not clarify the positive effect of SRT over the abundance of the AEA community [98,106].
Recent studies described that the most important factor affecting AEA abundance in WWT plants is the available concentration of ammonia. Strong negative correlations are reported among ammonia levels in influent or effluent water and the abundance of archaeal amoA copies [104,105,110]. The Ks for ammonia of AOA is much lower than the values measured for AOB in WWT plants, but the growth rates of AOA are in range with those of the Nitrosospira/Nitrosomonas oligotropha cluster, with the AOB displaying the higher affinity for ammonia. These data suggest that the AOA are dominant under ammonia-limiting concentrations, whereas these AOB are not able to grow [83]. With ammonia levels closer to their Ks, Nitrosospira/Nitrosomonas oligotropha cluster and AEA co-dominate, while at higher ammonia concentrations, the AEA seem to be inhibited [83,105]. In general, AOB tend to dominate in systems receiving high direct additions of inorganic ammonia, whereas systems sustained by the mineralization of organic material (ammonification) select for AEA [4]. However, AEA have been recently detected in a CAS system with high influent ammonia concentration [100]. The flocs’ stratification could explain the detection of a sensitive microorganism under suboptimal conditions, but further analyses are required [83].

5. Archaea in Biofilms Formed in Membrane Bioreactors (MBR) and their Roles in Biofouling

MBR are an advanced technology that combines the classical biological treatment of wastewater with the use of micro- or ultrafiltration membranes to perform the liquid-solid separation, avoiding the use of the secondary clarifiers [111]. After some decades of existence, membrane bioreactors (MBR) are currently well established as WWT systems which directly compete with the CAS processes due to their many advantages, mostly the generation of pathogen-free treated water that can be directly reused [112]. Compared to CAS, MBR are characterized by a high SRT, which influences the biology of the system, lowering the microbial metabolic activity and growth rates due to the limitation of substrates [113], and favoring the development of slow-growing microorganisms [109]. In both CAS- and MBR-based WWT systems, different populations of microorganism grow together in cell aggregates (flocs), which are stratified structures that are less dense than granules but also hold different microhabitats along their depth [74,75,114].
Anaerobic Membrane Bioreactors (AnMBR) combine an anaerobic bioreactor with a membrane technology for advanced wastewater treatment. There are two main biological focuses of interest in terms of biofilms: the sludge bed of the bioreactor (typically an UASB) where the microbiota is attached to the sludge granules and treats the wastewater, and the biofilm formation on the coupled-membrane surfaces. Hence, the quality of the biofilms supported by the sludge particles and the intimacy of the sludge-wastewater contact are the factors which determine the success of treatment.
The bacterial diversity of MBR is well described; however, the archaeal community remains less explored, with most of the studies being focused on the methanogenic community in AnMBR and, most recently, to AEA in aerobic systems [98,102,110]. Despite their strictly anaerobic metabolism, it has been found that methanogenic Archaea are often part of the microbiota of aerated WWT systems [7276], and a few studies have also reported their presence in aerated MBR [16,102]. The presence of anaerobic Archaea under aerated conditions is explained by the anoxic microenvironments created by the flocs’ stratification, located in the core of the aggregates. In early studies [75], methanogenic Archaea were detected in activated sludge flocs, but it was not until a few years later that their ability to grow in aerated WWT plants was confirmed [74]. These studies also demonstrated the inactivation of the methanogenesis when the Archaea came into contact with oxygen, but showed that Archaea remained viable and rapidly became active when the anoxic conditions returned. In this sense, the methanogenic Archaea have been described as highly persistent under unfavorable nutritional conditions and tolerant to O2 [74,115].

5.1. Biofouling in MBR Systems

During the last decades, the interest for the application of the membrane technologies has emerged in WWT. However, one of the drawbacks limiting the use of these systems is biofouling, or the progressive accumulation of pore-blocking materials on the surface of the membranes, due to the growth of microbial biofilms and the subsequent gathering of different types of organic and inorganic materials [112]. The reduction of the permeate efflux and an increase in transmembrane pressure are the major signs of biofouling [116,117]. Consequently, higher energy use and an increase of the frequency of the required chemical cleaning operations of the membranes are needed, which means shorter membrane lifespans and membrane-replacement costs [9]. Hence, better understanding of membrane fouling is not only the key to solving the problem, but is also one of the main factors driving membrane technology forward.
Biofouling starts with the accumulation of microorganisms at the liquid-solid phase transition, occurring by the deposition, growth and metabolism of bacterial cells or flocs on the membranes [118]. Biofilms may or may not uniformly cover the substratum and minimally consist of one or more usually multiple layers of living and dead microorganisms and their associated extracellular products [17,118].
In MBR systems assisted by microfiltration (MF) or ultrafiltration (UF), membrane fouling is a major issue. Although there are various factors that affect membrane fouling on MBR, such as membrane and biomass properties, feed water characteristics and operating conditions, membrane biofouling via microbial products plays a critical role in determining the feasibility of utilizing MBR when compared with other biological processes. Organic colloids and soluble polysaccharides (a part of the bacterial EPS) were found to be the main contributors to membrane fouling and influence the membrane performance in wastewater filtration applications. Studies by Rosenberger et al. [119] demonstrated the involvement of fouling in the soluble and colloidal substances in effluents and in the water phase of activated sludge of MBR systems. Bound EPS has been noticed as a key foulant in these systems. Ramesh et al. [120,121] fractionated bound EPS into tightly-bound EPS and loosely-bound EPS. They stated that the tightly-bound EPS have the highest fouling potential, while the loosely-bound EPS contribute most of the filtration resistance of the sludge in the MBR.
Recent research has been dedicated to the study of biofouling under a multidisciplinary approach, although these efforts have been mostly focused on membrane technologies applied in aerobic WWT. Many of the available studies aimed for the characterization of the microbial populations responsible for biofouling in MBR and other membrane-based systems, but these have been mainly centered on Bacteria [122124], and little work is available which has analyzed the relevance of Archaea in biofouling. A recent study by Calderón et al. [17] examined the biodiversity of prokaryotic organisms in the fouling biofilms of an AnMBR, based on the UASB technology and coupled to UF membrane modules. They showed that chemical cleaning (NaClO) did not completely remove membrane biofouling, and the populations which remained attached after this operation supported the re-growth of the biofilm, leading to the regeneration of a community of similar structure. 16S rRNA-gene TGGE fingerprints targeting Archaea and sequencing of isolated TGGE bands revealed that the prevalent populations in the foulant layers were closely related to the Methanospirillaceae (63% of identified sequences), followed by populations related to Methanosaeta spp. Together with methanogenic Archaea, some bacterial populations phylogenetically close to the genus Sphingomonas spp. were detected as persistent components of the biofouling. Other authors have also pointed out the involvement of Sphingomonas spp. on biofilm formation in membrane systems. Miura et al. [122] analyzed for over three months the adhesion and formation of biofilms on the hollow-fiber MF membrane surfaces of a full-scale submerged MBR using real municipal wastewater delivered from the primary sedimentation basin of a municipal WWT facility. The characteristics of the fouling layers were monitored using scanning electron microscopy (SEM), and the composition of planktonic and biofilm microbial communities in the MBR were analyzed using culture-independent molecular-based methods (FISH, 16S rRNA gene clone libraries and phylogenetic analysis), concluding that sphingomonads had an important role in biofouling. These findings are consistent with the well-known ability of sphingomonads to colonize solid surfaces favored by their swarming and twitching motility, where they usually adhere strongly regardless of the surface nature, aided by the production of abundant exopolymers.
As the efficiency of backflushing and NaClO treatment as routine antifouling methods was proven to be limited, the use of alternative strategies was suggested, particularly those specifically directed towards microbial groups shown to be resistant to standard chemical cleaning methods (i.e., Sphingomonadaceae bacteria and methanogenic Archaea). Overall, the development of more appropriate strategies to control membrane biofouling requires a more thorough understanding of biofilm properties and behavior, especially the early steps in biofilm formation [9]. Currently, control measures for membrane biofouling include applying intermittent suction, improving module configurations, improving aeration, reducing the concentration of suspended solids in the bioreactor, applying a tangential surface shear force, backwashing the membrane module, and adding exogenous antibacterial agents [120,125]. In biological terms, quorum quenching has been developed as a new and prosperous strategy in antifouling [126].

6. Future Prospects

The knowledge of archaeal diversity, abundance and functions has considerably increased in the last decades. In particular, their unique role as methanogenic organisms has been a central subject of investigation, and their significance in many ecological niches is currently well understood. Regarding the importance of these organisms in WWT, the structure and dynamics of archaeal communities in granular systems are thoroughly investigated, and the information on the influence of operating conditions on their diversity and performance is extensive. However, analogous research focused on fixed-film and expanded-bed reactors is limited in comparison, even though the benefits of providing a support material for biofilm formation are well acknowledged to improve methanogenesis and the general performance of anaerobic bioreactors. The reasons for the widespread presence of methanogenic Archaea in aerobic WWT, the understanding of their survival strategies in a theoretically hostile environment, the roles they may fulfill in organic matter degradation under aerobic conditions, or their suggested contribution to structural stability of suspended cell aggregates and biofilms, are also challenges for future research on the subject.
The wide distribution of AEA in the environment is well recognized at present. There is ample confirmation of their prevalence over AOB in habitats such as oceans, sprigs, soils or estuarine sediments [11,107,127129]. However, the abundance of AEA in engineered habitats is reported to be highly variable, and the reasons determining this random distribution remain obscure. In particular, the influence of geography on AEA occurrence is striking. To the best of the authors’ knowledge, there are still no reports of AEA detection in urban WWT plants based in Europe [96], while their presence in WWT systems examined in America and Asia is frequently reported [83]. The adaptation of AOA to low-ammonia levels is suggested by several studies, but other factors such as low carbon substrate availability, low pH, low DO concentration and sulphide content characterize niches where AEA are reported abundant [129]. The survey of AEA occurrence in WWT is still fairly limited, and the information gathered to date is often contradictory; thus, the factors determining the occurrence and abundance of AEA need to be further addressed.
The real contribution of AEA to ammonia oxidation in engineered habitats also needs to be assessed. Mußmann et al. [96] found that AEA outnumbered AOB up to 10-fold in a WWT plant treating refinery wastewater, but the application of a nitrification mathematical model, the detection of poor archaeal assimilation of labeled 13CO2, and FISH-microautoradiography (FISH-MAR) studies performed with 14C-inorganic carbon strongly evidenced that AEA were not acting as true chemolithoautotrophic ammonia-oxidizing microbes despite carrying and transcribing the amoA gene. The authors failed to find the possible source of carbon used by the AEA, even though they made a great effort applying FISH-MAR using a variety of radiolabeled substrates (amino acids, pyruvate, acetate, benzoate, and phenol). Further research is thus required to reveal the roles and importance of these organisms when expressing a heterotrophic mode of living in WWT, as well as the nature of the substrates that support their growth.
The use of MBR in wastewater treatment is steadily growing due to their many advantages over the CAS process; however, biofouling is a major issue restraining the broad application of this technology. Consequently, control of biofouling has become the main topic in MBR research. Conventional methods applied to minimize or eliminate biofouling often fail, because particular members of the biofilm community are intrinsically resistant to such chemical and physical treatments [17,130]. Alternative antifouling strategies are thus welcomed to efficiently eliminate the persistent components of the fouling biofilms. Methanogenic Archaea have been detected as recalcitrant components of the biofilms fouling membranes in MBR systems [17]. Studies analyzing de novo biofilm development inside an UASB reactor conclude that Archaea are absent during the initial phases of biofilm formation, but proliferate during the consolidation stage [131]. The reasons why Archaea are particularly persistent to antifouling strategies remain to be clarified. The unique characteristics of the archaeal cell envelope [132] may contribute to the persistence of these organisms on membrane surfaces.
Information about the mechanisms which control biofilm formation by Archaea is scattered. An endopolysaccharidase (disaggregatase) was isolated from a strain of Methanosarcina mazei, which efficiently dispersed the aggregates of M. mazei cells and was only secreted at certain stages of their life cycle [133]. The gene encoding the enzyme has been isolated and characterized [134]; however, the regulation of its expression and the possible role of disaggregatase under the biofilm life style have not been yet clarified. The roles of transcriptional regulators of the Lrs14 family in surface attachment and biofilm development have been just recently described in the Crenarchaeota [135]. Future studies should bring forth new insights into the regulation of biofilm formation and dispersal in Archaea.
In recent years, several authors have proposed advanced antifouling methods, focused to the particular biological characteristics of the microorganisms that made them able to develop very persistent biofilms. Enzymatic disruption of EPS, addition of chemical uncouplers, quorum-quenchers, or bacterial polysaccharides with antibiofilm activity are some of the methods which have proven effective for the dispersal of bacterial biofilms [136,137]. However, there is virtually no information available on the effectiveness of these approaches on biofilm-forming Archaea, although these prokaryotic organisms have been commonly identified in mixed-population biofilms in both aerated and anaerobic WWT plants.
Inhibition of quorum sensing (QS) by quorum quenchers is one of the more promising biological tools recently introduced to control microbial attachment and membrane fouling [126,137]. QS mechanisms in Archaea are still poorly known. However, the implication of acyl-homoserine lactones (AHLs) as QS signals in methanogenic Archaea has been recently revealed [62]. The luxI and luxR homologues, filI and filR, were located in the genome of a Methanosaeta harundinacea strain and were confirmed as the determinants of the production of long-chain (C10–C14) AHLs. The filIR genes actively regulate cell assembly by determining the morphology change of M. harundinacea from short cells to long filaments, hence controlling the role of these organisms in cell aggregation. The production of AHL-like compounds has been observed in pure cultures of Methanosarcina mazei and Methanothermobacter thermoautotrophicus, and orthologues of the filI-filR genes were also detected in the genomes of several methanogens (Methanosaeta concilii, Methanosaeta thermophila, M. mazei and Methanospirillum hungatei). These data suggest that QS mediated by AHLs is widespread in this archaeal clade. Consequently, methanogenic AHLs are promising tools for the promotion of granulation of sludge; at the same time, knowledge of the QS mechanism of these organisms provides new targets for the control of archaeal-related biofouling by means of quorum-quenching.

Acknowledgements

This research was supported by the Spanish Ministerio de Economía y Competitividad (MINECO) in collaboration with Fondo Europeo de Desarrollo Regional (FEDER) (project reference CTM2010-17609/TECNO), and by Junta de Andalucía (project reference P09-RNM-5412). MINECO (FPI program) and Universidad de Granada (Plan Propio) are also acknowledged for personal grants to C.G.S.

Conflicts of Interest

The authors declare no conflict of interest.

References

  1. Woese, C.R.; Fox, G.E. Phylogenetic structure of the prokaryotic domain: The primary kingdoms. Proc. Natl. Acad. Sci. USA 1977, 74, 5088–5090. [Google Scholar]
  2. Gribaldo, S.; Brochier-Armanet, C. The origin and evolution of Archaea: A state of the art. Philos. Trans. R. Soc. Lond. Ser. B 2006, 361, 1007–1022. [Google Scholar]
  3. Fröls, S. Archaeal biofilms: Widespread and complex. Biochem. Soc. Trans 2013, 41, 393–398. [Google Scholar]
  4. Stahl, D.A.; de la Torre, J.R. Physiology and diversity of ammonia-oxidizing archaea. Annu. Rev. Microbiol 2012, 66, 83–101. [Google Scholar]
  5. Stoodley, P.; Sauer, K.; Davies, D.G.; Costerton, J.W. Biofilms as complex differentiated communities. Annu. Rev. Microbiol 2002, 56, 187–209. [Google Scholar]
  6. Van Leewenhoeck, A. An abstract of a letter from Mr. Anthony Leewenhoeck at Delft, Dated Sep. 17. 1683. Containing some microscopical observations, about animals in the scurf of the teeth, the substance call’d worms in the nose, the cuticula consisting of scales. Philos. Trans. R Soc. Lond. Ser. B 1683, 166, 568–574. [Google Scholar]
  7. Hall-Stoodley, L.; Costerton, J.W.; Stoodley, P. Bacterial biofilms: From the natural environment to infectious diseases. Nat. Rev. Microbiol 2004, 2, 95–108. [Google Scholar]
  8. Watnick, P.; Kolter, R. Biofilm, city of microbes. J. Bacteriol 2000, 182, 2675–2679. [Google Scholar]
  9. Guo, W.; Ngo, H.-H.; Li, J. A mini-review on membrane fouling. Bioresour. Technol 2012, 122, 27–34. [Google Scholar]
  10. Harrison, J.J.; Ceri, H.; Turner, R.J. Multimetal resistance and tolerance in microbial biofilms. Nat. Rev. Microbiol 2007, 5, 928–938. [Google Scholar]
  11. Weidler, G.W.; Gerbl, F.W.; Stan-Lotter, H. Crenarchaeota and their role in the nitrogen cycle in a subsurface radioactive thermal spring in the Austrian Central Alps. Appl. Environ. Microbiol 2008, 74, 5934–5942. [Google Scholar]
  12. Reysenbach, A.L.; Ehringer, M.; Hershberger, K. Microbial diversity at 83 degrees C in Calcite Springs, Yellowstone National Park: Another environment where the Aquificales and “Korarchaeota” coexist. Extremophiles 2000, 4, 61–67. [Google Scholar]
  13. Jones, D.S.; Albrecht, H.L.; Dawson, K.S.; Schaperdoth, I.; Freeman, K.H.; Pi, Y.; Pearson, A.; Macalady, J.L. Community genomic analysis of an extremely acidophilic sulfur-oxidizing biofilm. ISME J 2012, 6, 158–170. [Google Scholar]
  14. Sauder, L.A.; Engel, K.; Stearns, J.C.; Masella, A.P.; Pawliszyn, R.; Neufeld, J.D. Aquarium nitrification revisited: Thaumarchaeota are the dominant ammonia oxidizers in freshwater aquarium biofilters. PLoS One 2011, 6, e23281. [Google Scholar]
  15. Edwards, K.J.; Bond, P.L.; Gihring, T.M.; Banfield, J.F. An archaeal iron-oxidizing extreme acidophile important in acid mine drainage. Science 2000, 287, 1796–1799. [Google Scholar]
  16. Gómez-Silván, C.; Molina-Munoz, M.; Poyatos, J.M.; Ramos, A.; Hontoria, E.; Rodelas, B.; González-López, J. Structure of archaeal communities in membrane-bioreactor and submerged-biofilter wastewater treatment plants. Bioresour. Technol 2010, 101, 2096–2105. [Google Scholar]
  17. Calderon, K.; Rodelas, B.; Cabirol, N.; Gonzalez-Lopez, J.; Noyola, A. Analysis of microbial communities developed on the fouling layers of a membrane-coupled anaerobic bioreactor applied to wastewater treatment. Bioresour. Technol 2011, 102, 4618–4627. [Google Scholar]
  18. Morales, M.; Arancibia, J.; Lemus, M.; Silva, J.; Gentina, J.; Aroca, G. Bio-oxidation of H2S by Sulfolobus metallicus. Biotechnol. Lett 2011, 33, 2141–2145. [Google Scholar]
  19. Justice, N.B.; Pan, C.; Mueller, R.; Spaulding, S.E.; Shah, V.; Sun, C.L.; Yelton, A.P.; Miller, C.S.; Thomas, B.C.; Shah, M.; et al. Heterotrophic archaea contribute to carbon cycling in low-pH, suboxic biofilm communities. Appl. Environ. Microbiol 2012, 78, 8321–8330. [Google Scholar]
  20. Cheng, K.-C.; Demirci, A.; Catchmark, J. Advances in biofilm reactors for production of value-added products. Appl. Microbiol. Biotechnol 2010, 87, 445–456. [Google Scholar]
  21. Gómez-Villalba, B.; Calvo, C.; Vilchez, R.; González-López, J.; Rodelas, B. TGGE analysis of the diversity of ammonia-oxidizing and denitrifying bacteria in submerged filter biofilms for the treatment of urban wastewater. Appl. Microbiol. Biotechnol 2006, 72, 393–400. [Google Scholar]
  22. Winkler, M.K.; Kleerebezem, R.; de Bruin, L.M.; Verheijen, P.J.; Abbas, B.; Habermacher, J.; Van Loosdrecht, M.C. Microbial diversity differences within aerobic granular sludge and activated sludge flocs. Appl. Microbiol. Biotechnol 2013, 97, 7447–7458. [Google Scholar]
  23. Wang, J.; Kang, J. The characteristics of anaerobic ammonium oxidation (ANAMMOX) by granular sludge from an EGSB reactor. Process Biochem 2005, 40, 1973–1978. [Google Scholar]
  24. Lettinga, G. Anaerobic digestion and wastewater treatment systems. Antonie Leeuwenhoek 1995, 67, 3–28. [Google Scholar]
  25. Tiwari, M.K.; Guha, S.; Harendranath, C.S.; Tripathi, S. Influence of extrinsic factors on granulation in UASB reactor. Appl. Microbiol. Biotechnol 2006, 71, 145–154. [Google Scholar]
  26. Abbasi, T.; Abbasi, S.A. Formation and impact of granules in fostering clean energy production and wastewater treatment in upflow anaerobic sludge blanket (UASB) reactors. Renew. Sustain. Energy Rev 2012, 16, 1696–1708. [Google Scholar]
  27. Van der Star, W.R.L.; Abma, W.R.; Blommers, D.; Mulder, J.-W.; Tokutomi, T.; Strous, M.; Picioreanu, C.; Van Loosdrecht, M.C.M. Startup of reactors for anoxic ammonium oxidation: Experiences from the first full-scale anammox reactor in Rotterdam. Water Res 2007, 41, 4149–4163. [Google Scholar]
  28. Skiadas, I.V.; Gavala, H.N.; Schmidt, J.E.; Ahring, B.K. Anaerobic granular sludge and biofilm reactors. Adv. Biochem. Eng. Biotechnol 2003, 82, 35–67. [Google Scholar]
  29. Adav, S.S.; Lee, D.-J.; Show, K.-Y.; Tay, J.-H. Aerobic granular sludge: Recent advances. Biotechnol. Adv 2008, 26, 411–423. [Google Scholar]
  30. Angelidaki, I.; Karakashev, D.; Batstone, D.J.; Plugge, C.M.; Stams, A.J.M. Biomethanation and its potential. Methods Enzymol 2011, 494, 327–351. [Google Scholar]
  31. Liu, Y.; Whitman, W.B. Metabolic, phylogenetic, and ecological diversity of the methanogenic archaea. Ann. N. Y. Acad. Sci 2008, 1125, 171–189. [Google Scholar]
  32. Sakai, S.; Imachi, H.; Hanada, S.; Ohashi, A.; Harada, H.; Kamagata, Y. Methanocella paludicola gen. nov., sp. nov., a methane-producing archaeon, the first isolate of the lineage “Rice Cluster I”, and proposal of the new archaeal order Methanocellales ord. nov. Int. J. Syst. Evol. Microbiol 2008, 58, 929–936. [Google Scholar]
  33. Rivière, D.; Desvignes, V.; Pelletier, E.; Chaussonnerie, S.; Guermazi, S.; Weissenbach, J.; Li, T.; Camacho, P.; Sghir, A. Towards the definition of a core of microorganisms involved in anaerobic digestion of sludge. ISME J 2009, 3, 700–714. [Google Scholar]
  34. Narihiro, T.; Sekiguchi, Y. Oligonucleotide primers, probes and molecular methods for the environmental monitoring of methanogenic archaea. Microb. Biotechnol 2011, 4, 585–602. [Google Scholar]
  35. Leclerc, M.; Delgènes, J.-P.; Godon, J.-J. Diversity of the archaeal community in 44 anaerobic digesters as determined by single strand conformation polymorphism analysis and 16S rDNA sequencing. Environ. Microbiol 2004, 6, 809–819. [Google Scholar]
  36. Collins, G.; Kavanagh, S.; McHugh, S.; Connaughton, S.; Kearney, A.; Rice, O.; Carrigg, C.; Scully, C.; Bhreathnach, N.; Mahony, T.; et al. Accessing the black box of microbial diversity and ecophysiology: Recent advances through polyphasic experiments. J. Environ. Sci. Health Part A 2006, 41, 897–922. [Google Scholar]
  37. Dang, Y.; Ye, J.; Mu, Y.; Qiu, B.; Sun, D. Effective anaerobic treatment of fresh leachate from MSW incineration plant and dynamic characteristics of microbial community in granular sludge. Appl. Microbiol. Biotechnol 2013, 1–12. [Google Scholar]
  38. Visser, F.A.; Van Lier, J.B.; Macario, A.J.; Conway de Macario, E. Diversity and population dynamics of methanogenic bacteria in a granular consortium. Appl. Environ. Microbiol 1991, 57, 1728–1734. [Google Scholar]
  39. Buzzini, A.P.; Sakamoto, I.K.; Varesche, M.B.; Pires, E.C. Evaluation of the microbial diversity in an UASB reactor treating wastewater from an unbleached pulp plant. Process Biochem 2006, 41, 168–176. [Google Scholar]
  40. Del Nery, V.; Pozzi, E.; Damianovic, M.H.R.Z.; Domingues, M.R.; Zaiat, M. Granules characteristics in the vertical profile of a full-scale upflow anaerobic sludge blanket reactor treating poultry slaughterhouse wastewater. Bioresour. Technol 2008, 99, 2018–2024. [Google Scholar]
  41. Tabatabaei, M.; Rahim, R.A.; Abdullah, N.; Wright, A.-D.G.; Shirai, Y.; Sakai, K.; Sulaiman, A.; Hassan, M.A. Importance of the methanogenic archaea populations in anaerobic wastewater treatments. Process Biochem 2010, 45, 1214–1225. [Google Scholar]
  42. Zhang, D.; Li, J.; Guo, P.; Li, P.; Suo, Y.; Wang, X.; Cui, Z. Dynamic transition of microbial communities in response to acidification in fixed-bed anaerobic baffled reactors (FABR) of two different flow directions. Bioresour. Technol 2011, 102, 4703–4711. [Google Scholar]
  43. Rademacher, A.; Zakrzewski, M.; Schluter, A.; Schonberg, M.; Szczepanowski, R.; Goesmann, A.; Puhler, A.; Klocke, M. Characterization of microbial biofilms in a thermophilic biogas system by high-throughput metagenome sequencing. FEMS Microbiol. Ecol 2012, 79, 785–799. [Google Scholar]
  44. Pereira, M.A.; Roest, K.; Stams, A.J.; Mota, M.; Alves, M.; Akkermans, A.D. Molecular monitoring of microbial diversity in expanded granular sludge bed (EGSB) reactors treating oleic acid. FEMS Microbiol. Ecol 2002, 41, 95–103. [Google Scholar] [Green Version]
  45. O’Reilly, J.; Lee, C.; Collins, G.; Chinalia, F.; Mahony, T.; O’Flaherty, V. Quantitative and qualitative analysis of methanogenic communities in mesophilically and psychrophilically cultivated anaerobic granular biofilims. Water Res 2009, 43, 3365–3374. [Google Scholar] [Green Version]
  46. Li, J.; Wang, J.; Luan, Z.; Deng, Y.; Chen, L. Evaluation of performance and microbial community in a two-stage UASB reactor pretreating acrylic fiber manufacturing wastewater. Bioresour. Technol 2011, 102, 5709–5716. [Google Scholar]
  47. Khemkhao, M.; Nuntakumjorn, B.; Techkarnjanaruk, S.; Phalakornkule, C. UASB performance and microbial adaptation during a transition from mesophilic to thermophilic treatment of palm oil mill effluent. J. Environ. Manag 2012, 103, 74–82. [Google Scholar]
  48. Nelson, M.C.; Morrison, M.; Schanbacher, F.; Yu, Z. Shifts in microbial community structure of granular and liquid biomass in response to changes to infeed and digester design in anaerobic digesters receiving food-processing wastes. Bioresour. Technol 2012, 107, 135–143. [Google Scholar]
  49. Xing, W.; Zuo, J.E.; Dai, N.; Cheng, J.; Li, J. Reactor performance and microbial community of an EGSB reactor operated at 20 and 15 °C. J. Appl. Microbiol 2009, 107, 848–857. [Google Scholar]
  50. McHugh, S.; Carton, M.; Mahony, T.; O’Flaherty, V. Methanogenic population structure in a variety of anaerobic bioreactors. FEMS Microbiol. Lett 2003, 219, 297–304. [Google Scholar]
  51. Liu, Y.; Xu, H.-L.; Yang, S.-F.; Tay, J.-H. Mechanisms and models for anaerobic granulation in upflow anaerobic sludge blanket reactor. Water Res 2003, 37, 661–673. [Google Scholar]
  52. Sasaki, K.; Morita, M.; Hirano, S.; Ohmura, N.; Igarashi, Y. Effect of adding carbon fiber textiles to methanogenic bioreactors used to treat an artificial garbage slurry. J. Biosci. Bioeng 2009, 108, 130–135. [Google Scholar]
  53. Najafpour, G.D.; Zinatizadeh, A.A.L.; Mohamed, A.R.; Hasnain Isa, M.; Nasrollahzadeh, H. High-rate anaerobic digestion of palm oil mill effluent in an upflow anaerobic sludge-fixed film bioreactor. Process Biochem 2006, 41, 370–379. [Google Scholar]
  54. Patel, P.; Patel, C.; Madamwar, D. Anaerobic upflow fixed-film bioreactor for biomethanation of salty cheese whey. Appl. Biochem. Biotechnol 1999, 76, 193–201. [Google Scholar]
  55. Acharya, B.K.; Mohana, S.; Madamwar, D. Anaerobic treatment of distillery spent wash—A study on upflow anaerobic fixed film bioreactor. Bioresour. Technol 2008, 99, 4621–4626. [Google Scholar]
  56. Sasaki, K.; Haruta, S.; Tatara, M.; Yamazawa, A.; Ueno, Y.; Ishii, M.; Igarashi, Y. Microbial community in methanogenic packed-bed reactor successfully operating at short hydraulic retention time. J. Biosci. Bioeng 2006, 101, 271–273. [Google Scholar]
  57. Sasaki, K.; Haruta, S.; Ueno, Y.; Ishii, M.; Igarashi, Y. Archaeal population on supporting material in methanogenic packed-bed reactor. J. Biosci. Bioeng 2006, 102, 244–246. [Google Scholar]
  58. Sekiguchi, Y.; Kamagata, Y.; Syutsubo, K.; Ohashi, A.; Harada, H.; Nakamura, K. Phylogenetic diversity of mesophilic and thermophilic granular sludges determined by 16S rRNA gene analysis. J. Microbiol 1998, 144, 2655–2665. [Google Scholar]
  59. McHugh, S.; Carton, M.; Collins, G.; O’Flaherty, V. Reactor performance and microbial community dynamics during anaerobic biological treatment of wastewaters at 16–37 degrees C. FEMS Microbiol. Ecol 2004, 48, 369–378. [Google Scholar]
  60. Connaughton, S.; Collins, G.; O’Flaherty, V. Development of microbial community structure and actvity in a high-rate anaerobic bioreactor at 18 °C. Water Res 2006, 40, 1009–1017. [Google Scholar]
  61. Bandara, W.M.K.R.T.W.; Kindaichi, T.; Satoh, H.; Sasakawa, M.; Nakahara, Y.; Takahashi, M.; Okabe, S. Anaerobic treatment of municipal wastewater at ambient temperature: Analysis of archaeal community structure and recovery of dissolved methane. Water Res. 2012, 46, 5756–5764. [Google Scholar]
  62. Zhang, G.; Zhang, F.; Ding, G.; Li, J.; Guo, X.; Zhu, J.; Zhou, L.; Cai, S.; Liu, X.; Luo, Y.; et al. Acyl homoserine lactone-based quorum sensing in a methanogenic archaeon. ISME J 2012, 6, 1336–1344. [Google Scholar]
  63. Siggins, A.; Enright, A.M.; O’Flaherty, V. Methanogenic community development in anaerobic granular bioreactors treating trichloroethylene (TCE)-contaminated wastewater at 37 degrees C and 15 degrees C. Water Res 2011, 45, 2452–2462. [Google Scholar]
  64. Hirasawa, J.S.; Sarti, A.; Del Aguila, N.K.; Varesche, M.B. Application of molecular techniques to evaluate the methanogenic archaea and anaerobic bacteria in the presence of oxygen with different COD: Sulfate ratios in a UASB reactor. Anaerobe 2008, 14, 209–218. [Google Scholar]
  65. Kobayashi, T.; Yan, F.; Takahashi, S.; Li, Y.Y. Effect of starch addition on the biological conversion and microbial community in a methanol-fed UASB reactor during long-term continuous operation. Bioresour. Technol 2011, 102, 7713–7719. [Google Scholar]
  66. Sallis, P.J.; Uyanik, S. Granule development in a split-feed anaerobic baffled reactor. Bioresour. Technol 2003, 89, 255–265. [Google Scholar]
  67. Song, M.; Shin, S.G.; Hwang, S. Methanogenic population dynamics assessed by real-time quantitative PCR in sludge granule in upflow anaerobic sludge blanket treating swine wastewater. Bioresour. Technol 2010, 101, S23–S28. [Google Scholar]
  68. Angenent, L.T.; Sung, S.; Raskin, L. Formation of granules and Methanosaeta fibres in an anaerobic migrating blanket reactor (AMBR). Environ. Microbiol 2004, 6, 315–322. [Google Scholar]
  69. Fernandez, N.; Sierra-Alvarez, R.; Amils, R.; Field, J.A.; Sanz, J.L. Compared microbiology of granular sludge under autotrophic, mixotrophic and heterotrophic denitrification conditions. Water Sci. Technol 2009, 59, 1227–1236. [Google Scholar]
  70. Zheng, D.; Angenent, L.T.; Raskin, L. Monitoring granule formation in anaerobic upflow bioreactors using oligonucleotide hybridization probes. Biotechnol. Bioeng 2006, 94, 458–472. [Google Scholar]
  71. Weber, S.D.; Ludwig, W.; Schleifer, K.H.; Fried, J. Microbial composition and structure of aerobic granular sewage biofilms. Appl. Environ. Microbiol 2007, 73, 6233–6240. [Google Scholar]
  72. Czepiel, P.M.; Crill, P.M.; Harriss, R.C. Methane emissions from municipal wastewater treatment processes. Environ. Sci. Technol 1993, 27, 2472–2477. [Google Scholar]
  73. Daelman, M.R.J.; Van Voorthuizen, E.M.; Van Dongen, U.G.J.M.; Volcke, E.I.P.; Van Loosdrecht, M.C.M. Methane emission during municipal wastewater treatment. Water Res 2012, 46, 3657–3670. [Google Scholar]
  74. Gray, N.D.; Miskin, I.P.; Kornilova, O.; Curtis, T.P.; Head, I.M. Occurrence and activity of Archaea in aerated activated sludge wastewater treatment plants. Environ. Microbiol 2002, 4, 158–168. [Google Scholar]
  75. Lens, P.N.; De Poorter, M.P.; Cronenberg, C.C.; Verstraete, W.H. Sulfate reducing and methane producing bacteria in aerobic wastewater treatment systems. Water Res 1995, 29, 871–880. [Google Scholar]
  76. Ren, Y.; Wang, J.; Li, H.; Zhang, J.; Qi, P.; Hu, Z. Nitrous oxide and methane emissions from different treatment processes in full-scale municipal wastewater treatment plants. Environ. Technol 2012. [Google Scholar] [CrossRef]
  77. Treusch, A.H.; Leininger, S.; Kletzin, A.; Schuster, S.C.; Klenk, H.P.; Schleper, C. Novel genes for nitrite reductase and Amo-related proteins indicate a role of uncultivated mesophilic crenarchaeota in nitrogen cycling. Environ. Microbiol 2005, 7, 1985–1995. [Google Scholar]
  78. Könneke, M.; Bernhard, A.E.; De La Torre, J.R.; Walker, C.B.; Waterbury, J.B.; Stahl, D.A. Isolation of an autotrophic ammonia-oxidizing marine archaeon. Nature 2005, 437, 543–546. [Google Scholar]
  79. Tourna, M.; Stieglmeier, M.; Spang, A.; Konneke, M.; Schintlmeister, A.; Urich, T.; Engel, M.; Schloter, M.; Wagner, M.; Richter, A.; et al. Nitrososphaera viennensis, an ammonia oxidizing archaeon from soil. Proc. Natl. Acad. Sci. USA 2011, 108, 8420–8425. [Google Scholar]
  80. Beman, J.M.; Francis, C.A. Diversity of ammonia-oxidizing archaea and bacteria in the sediments of a hypernutrified subtropical estuary: Bahia del Tobari, Mexico. Appl. Environ. Microbiol 2006, 72, 7767–7777. [Google Scholar]
  81. Dang, H.; Li, J.; Zhang, X.; Li, T.; Tian, F.; Jin, W. Diversity and spatial distribution of amoA-encoding archaea in the deep-sea sediments of the tropical West Pacific Continental Margin. J. Appl. Microbiol 2009, 106, 1482–1493. [Google Scholar]
  82. Hatzenpichler, R. Diversity, physiology, and niche differentiation of ammonia-oxidizing Archaea. Appl. Environ. Microbiol 2012, 78, 7501–7510. [Google Scholar]
  83. Limpiyakorn, T.; Fürhacker, M.; Haberl, R.; Chodanon, T.; Srithep, P.; Sonthiphand, P. amoA-encoding archaea in wastewater treatment plants: A review. Appl. Microbiol. Biotechnol 2013, 97, 1425–1439. [Google Scholar]
  84. Brochier-Armanet, C.; Boussau, B.; Gribaldo, S.; Forterre, P. Mesophilic crenarchaeota: Proposal for a third archaeal phylum, the Thaumarchaeota. Nat. Rev. Microbiol 2008, 6, 245–252. [Google Scholar]
  85. Spang, A.; Hatzenpichler, R.; Brochier-Armanet, C.; Rattei, T.; Tischler, P.; Spieck, E.; Streit, W.; Stahl, D.A.; Wagner, M.; Schleper, C. Distinct gene set in two different lineages of ammonia-oxidizing archaea supports the phylum Thaumarchaeota. Trends Microbiol 2010, 18, 331–340. [Google Scholar]
  86. Park, S.J.; Kim, J.G.; Jung, M.Y.; Kim, S.J.; Cha, I.T.; Kwon, K.; Lee, J.H.; Rhee, S.K. Draft genome sequence of an ammonia-oxidizing archaeon, “Candidatus Nitrosopumilus koreensis” AR1, from marine sediment. J. Bacteriol 2012, 194, 6940–6941. [Google Scholar]
  87. Mosier, A.C.; Allen, E.E.; Kim, M.; Ferriera, S.; Francis, C.A. Genome sequence of “Candidatus Nitrosopumilus salaria” BD31, an ammonia-oxidizing archaeon from the San Francisco Bay estuary. J. Bacteriol 2012, 194, 2121–2122. [Google Scholar]
  88. Park, S.J.; Kim, J.G.; Jung, M.Y.; Kim, S.J.; Cha, I.T.; Ghai, R.; Martin-Cuadrado, A.B.; Rodriguez-Valera, F.; Rhee, S.K. Draft genome sequence of an ammonia-oxidizing archaeon, “Candidatus Nitrosopumilus sediminis” AR2, from Svalbard in the Arctic Circle. J. Bacteriol 2012, 194, 6948–6949. [Google Scholar]
  89. Kim, B.K.; Jung, M.Y.; Yu, D.S.; Park, S.J.; Oh, T.K.; Rhee, S.K.; Kim, J.F. Genome sequence of an ammonia-oxidizing soil archaeon, “Candidatus Nitrosoarchaeum koreensis” MY1. J. Bacteriol 2011, 193, 5539–5540. [Google Scholar]
  90. Blainey, P.C.; Mosier, A.C.; Potanina, A.; Francis, C.A.; Quake, S.R. Genome of a low-salinity ammonia-oxidizing archaeon determined by single-cell and metagenomic analysis. PLoS One 2011, 6, e16626. [Google Scholar]
  91. Preston, C.M.; Wu, K.Y.; Molinski, T.F.; DeLong, E.F. A psychrophilic crenarchaeon inhabits a marine sponge: Cenarchaeum symbiosum gen. nov., sp. nov. Proc. Natl. Acad. Sci. USA 1996, 93, 6241–6246. [Google Scholar]
  92. Lehtovirta-Morley, L.E.; Stoecker, K.; Vilcinskas, A.; Prosser, J.I.; Nicol, G.W. Cultivation of an obligate acidophilic ammonia oxidizer from a nitrifying acid soil. Proc. Natl. Acad. Sci. USA 2011, 108, 15892–15897. [Google Scholar]
  93. Hatzenpichler, R.; Lebedeva, E.V.; Spieck, E.; Stoecker, K.; Richter, A.; Daims, H.; Wagner, M. A moderately thermophilic ammonia-oxidizing crenarchaeote from a hot spring. Proc. Natl. Acad. Sci. USA 2008, 105, 2134–2139. [Google Scholar]
  94. De La Torre, J.R.; Walker, C.B.; Ingalls, A.E.; Könneke, M.; Stahl, D.A. Cultivation of a thermophilic ammonia oxidizing archaeon synthesizing crenarchaeol. Environ. Microbiol 2008, 10, 810–818. [Google Scholar]
  95. Park, H.D.; Wells, G.F.; Bae, H.; Criddle, C.S.; Francis, C.A. Occurrence of ammonia-oxidizing archaea in wastewater treatment plant bioreactors. Appl. Environ. Microbiol 2006, 72, 5643–5647. [Google Scholar]
  96. Mußmann, M.; Brito, I.; Pitcher, A.; Sinninghe Damsté, J.S.; Hatzenpichler, R.; Richter, A.; Nielsen, J.L.; Nielsen, P.H.; Müller, A.; Daims, H.; et al. Thaumarchaeotes abundant in refinery nitrifying sludges express amoA but are not obligate autotrophic ammonia oxidizers. Proc. Natl. Acad. Sci. USA 2011, 108, 16771–16776. [Google Scholar]
  97. Jin, T.; Zhang, T.; Yan, Q. Characterization and quantification of ammonia-oxidizing archaea (AOA) and bacteria (AOB) in a nitrogen-removing reactor using T-RFLP and qPCR. Appl. Microbiol. Biotechnol 2010, 87, 1167–1176. [Google Scholar] [Green Version]
  98. Ozdemir, B.; Mertoglu, B.; Yapsakli, K.; Aliyazicioglu, C.; Saatci, A.; Yenigun, O. Investigation of nitrogen converters in membrane bioreactor. J. Environ. Sci. Health Part A 2011, 46, 500–508. [Google Scholar]
  99. Wells, G.F.; Park, H.D.; Yeung, C.H.; Eggleston, B.; Francis, C.A.; Criddle, C.S. Ammonia-oxidizing communities in a highly aerated full-scale activated sludge bioreactor: Betaproteobacterial dynamics and low relative abundance of Crenarchaea. Environ. Microbiol 2009, 11, 2310–2328. [Google Scholar]
  100. Yapsakli, K.; Aliyazicioglu, C.; Mertoglu, B. Identification and quantitative evaluation of nitrogen-converting organisms in a full-scale leachate treatment plant. J. Environ. Manag 2011, 92, 714–723. [Google Scholar]
  101. Sonthiphand, P.; Limpiyakorn, T. Change in ammonia-oxidizing microorganisms in enriched nitrifying activated sludge. Appl. Microbiol. Biotechnol 2011, 89, 843–853. [Google Scholar]
  102. Bai, Y.; Sun, Q.; Wen, D.; Tang, X. Abundance of ammonia-oxidizing bacteria and archaea in industrial and domestic wastewater treatment systems. FEMS Microbiol. Ecol 2012, 80, 323–330. [Google Scholar]
  103. Kayee, P.; Sonthiphand, P.; Rongsayamanont, C.; Limpiyakorn, T. Archaeal amoA genes outnumber bacterial amoA genes in municipal wastewater treatment plants in Bangkok. Microb. Ecol 2011, 62, 776–788. [Google Scholar]
  104. Sauder, L.A.; Peterse, F.; Schouten, S.; Neufeld, J.D. Low-ammonia niche of ammonia-oxidizing archaea in rotating biological contactors of a municipal wastewater treatment plant. Environ. Microbiol 2012, 14, 2589–2600. [Google Scholar]
  105. Limpiyakorn, T.; Sonthiphand, P.; Rongsayamanont, C.; Polprasert, C. Abundance of amoA genes of ammonia-oxidizing archaea and bacteria in activated sludge of full-scale wastewater treatment plants. Bioresour. Technol 2011, 102, 3694–3701. [Google Scholar]
  106. Yu, T.; Li, D.; Qi, R.; Li, S.T.; Xu, S.W.; Yang, M. Structure and dynamics of nitrifier populations in a full-scale submerged membrane bioreactor during start-up. Appl. Microbiol. Biotechnol 2011, 90, 369–376. [Google Scholar]
  107. Adair, K.; Schwartz, E. Evidence that ammonia-oxidizing archaea are more abundant than ammonia-oxidizing bacteria in semiarid soils of northern Arizona, USA. Microb. Ecol 2008, 56, 420–426. [Google Scholar]
  108. Prosser, J.I.; Nicol, G.W. Relative contributions of archaea and bacteria to aerobic ammonia oxidation in the environment. Environ. Microbiol 2008, 10, 2931–2941. [Google Scholar]
  109. Witzig, R.; Manz, W.; Rosenbergerb, S.; Krugerb, U.; Kraumeb, M.; Szewzyk, U. Microbiological aspects of a bioreactor with submerged membranes for aerobic treatment of municipal wastewater. Water Res 2002, 36, 394–402. [Google Scholar]
  110. Ye, L.; Zhang, T. Bacterial communities in different sections of a municipal wastewater treatment plant revealed by 16S rDNA 454 pyrosequencing. Appl. Microbiol. Biotechnol 2013, 97, 2681–2690. [Google Scholar]
  111. Judd, S. The status of membrane bioreactor technology. Trends Biotechnol 2008, 26, 109–116. [Google Scholar]
  112. Le-Clech, P. Membrane bioreactors and their uses in wastewater treatments. Appl. Microbiol. Biotechnol 2010, 88, 1253–1260. [Google Scholar]
  113. LaPara, T.M.; Klatt, C.G.; Chen, R. Adaptations in bacterial catabolic enzyme activity and community structure in membrane-coupled bioreactors fed simple synthetic wastewater. J. Biotechnol 2006, 121, 368–380. [Google Scholar]
  114. He, S.B.; Xue, G.; Wang, B.Z. Factors affecting simultaneous nitrification and de-nitrification (SND) and its kinetics model in membrane bioreactor. J. Hazard Mater 2009, 168, 704–710. [Google Scholar]
  115. Santegoeds, C.M.; Damgaard, L.R.; Hesselink, G.; Zopfi, J.; Lens, P.; Muyzer, G.; De Beer, D. Distribution of sulfate-reducing and methanogenic bacteria in anaerobic aggregates determined by microsensor and molecular analyses. Appl. Environ. Microbiol 1999, 65, 4618–4629. [Google Scholar]
  116. Ridgway, H.F.; Flemming, H.-C. Biofouling of Membranes. In Water Treatment Membrane Processes, 1st ed.; Mallevialle, J., Odendaal, P.E., Eds.; McGraw-Hill: New York, NY, USA, 1996; pp. 6.1–6.62. [Google Scholar]
  117. Herrera-Robledo, M.; Morgan-Sagastume, J.M.; Noyola, A. Biofouling and pollutant removal during long-term operation of an anaerobic membrane bioreactor treating municipal wastewater. Biofouling 2010, 26, 23–30. [Google Scholar]
  118. Ivnitsky, H.; Katz, I.; Minz, D.; Volvovic, G.; Shimoni, E.; Kesselman, E.; Semiat, R.; Dosoretz, C.G. Bacterial community composition and structure of biofilms developing on nanofiltration membranes applied to wastewater treatment. Water Res 2007, 41, 3924–3935. [Google Scholar]
  119. Rosenberger, S.; Evenblij, H.; Te Poele, S.; Wintgens, T.; Laabs, C. The importance of liquid phase analyses to understand fouling in membrane assisted activated sludge processes—Six case studies of different European research groups. J. Membr. Sci 2005, 263, 113–126. [Google Scholar]
  120. Ramesh, A.; Lee, D.J.; Wang, M.L.; Hsu, J.P.; Juang, R.S.; Hwang, K.J.; Liu, J.C.; Tseng, S.J. Biofouling in membrane bioreactor. Sep. Sci. Technol 2006, 41, 1345–1370. [Google Scholar]
  121. Ramesh, A.; Lee, D.J.; Lai, J.Y. Membrane biofouling by extracellular polymeric substances or soluble microbial products from membrane bioreactor sludge. Appl. Microbiol. Biotechnol 2007, 74, 699–707. [Google Scholar]
  122. Miura, Y.; Watanabe, Y.; Okabe, S. Membrane biofouling in pilot-scale membrane bioreactors (MBRs) treating municipal wastewater: Impact of biofilm formation. Environ. Sci. Technol 2007, 41, 632–638. [Google Scholar]
  123. Gao, D.-W.; Zhang, T.; Tang, C.-Y.Y.; Wu, W.-M.; Wong, C.-Y.; Lee, Y.H.; Yeh, D.H.; Criddle, C.S. Membrane fouling in an anaerobic membrane bioreactor: Differences in relative abundance of bacterial species in the membrane foulant layer and in suspension. J. Membr. Sci 2010, 364, 331–338. [Google Scholar]
  124. Lin, H.; Liao, B.-Q.; Chen, J.; Gao, W.; Wang, L.; Wang, F.; Lu, X. New insights into membrane fouling in a submerged anaerobic membrane bioreactor based on characterization of cake sludge and bulk sludge. Bioresour. Technol 2011, 102, 2373–2379. [Google Scholar]
  125. Chang, I.; Le Clech, P.; Jefferson, B.; Judd, S. Membrane fouling in membrane bioreactors for wastewater treatment. J. Environ. Eng 2002, 128, 1018–1029. [Google Scholar]
  126. Yeon, K.M.; Cheong, W.S.; Oh, H.S.; Lee, W.N.; Hwang, B.K.; Lee, C.H.; Beyenal, H.; Lewandowski, Z. Quorum sensing: A new biofouling control paradigm in a membrane bioreactor for advanced wastewater treatment. Environ. Sci. Technol 2009, 43, 380–385. [Google Scholar]
  127. Leininger, S.; Urich, T.; Schloter, M.; Schwark, L.; Qi, J.; Nicol, G.W.; Prosser, J.I.; Schuster, S.C.; Schleper, C. Archaea predominate among ammonia-oxidizing prokaryotes in soils. Nature 2006, 442, 806–809. [Google Scholar]
  128. Wuchter, C.; Abbas, B.; Coolen, M.J.; Herfort, L.; Van Bleijswijk, J.; Timmers, P.; Strous, M.; Teira, E.; Herndl, G.J.; Middelburg, J.J. Archaeal nitrification in the ocean. Proc. Natl. Acad. Sci. USA 2006, 103, 12317–12322. [Google Scholar]
  129. Erguder, T.H.; Boon, N.; Wittebolle, L.; Marzorati, M.; Verstraete, W. Environmental factors shaping the ecological niches of ammonia-oxidizing archaea. FEMS Microbiol. Rev 2009, 33, 855–869. [Google Scholar]
  130. Lequette, Y.; Boels, G.; Clarisse, M.; Faille, C. Using enzymes to remove biofilms of bacterial isolates sampled in the food-industry. Biofouling 2010, 26, 421–431. [Google Scholar]
  131. Fernandez, N.; Diaz, E.E.; Amils, R.; Sanz, J.L. Analysis of microbial community during biofilm development in an anaerobic wastewater treatment reactor. Microb. Ecol 2008, 56, 121–132. [Google Scholar]
  132. Mathai, J.C.; Sprott, G.D.; Zeidel, M.L. Molecular mechanisms of water and solute transport across archaebacterial lipid membranes. J. Biol. Chem 2001, 276, 27266–27271. [Google Scholar]
  133. Xun, L.Y.; Mah, R.A.; Boone, D.R. Isolation and characterization of disaggregatase from Methanosarcina mazei LYC. Appl. Environ. Microbiol 1990, 56, 3693–3698. [Google Scholar]
  134. Osumi, N.; Kakehashi, Y.; Matsumoto, S.; Nagaoka, K.; Sakai, J.; Miyashita, K.; Kimura, M.; Asakawa, S. Identification of the gene for disaggregatase from Methanosarcina mazei. Archaea 2008, 2, 185–191. [Google Scholar]
  135. Orell, A.; Peeters, E.; Vassen, V.; Jachlewski, S.; Schalles, S.; Siebers, B.; Albers, S.V. Lrs14 transcriptional regulators influence biofilm formation and cell motility of Crenarchaea. ISME J 2013. [Google Scholar] [CrossRef]
  136. Bernal, P.; Llamas, M.A. Promising biotechnological applications of antibiofilm exopolysaccharides. Microb. Biotechnol 2012, 5, 670–673. [Google Scholar]
  137. Xiong, Y.; Liu, Y. Biological control of microbial attachment: A promising alternative for mitigating membrane biofouling. Appl. Microbiol. Biotechnol 2010, 86, 825–837. [Google Scholar]
Figure 1. Scanning electron micrographs of anaerobic granular sludge cultivated in an Expanded Granular Sludge Bed (EGSB) reactor. (A) Morphology of anaerobic granules used (40× magnification); (B,C,D) Inner structure of anaerobic granules (6000× magnification). Reprinted from [23], Process Biochemistry, Vol. 40, Wang, J. and Kang, J., The characteristics of anaerobic ammonium oxidation (ANAMMOX) by granular sludge from an EGSB reactor, Pages 1973–1978, Copyright (2005), with permission from Elsevier.
Figure 1. Scanning electron micrographs of anaerobic granular sludge cultivated in an Expanded Granular Sludge Bed (EGSB) reactor. (A) Morphology of anaerobic granules used (40× magnification); (B,C,D) Inner structure of anaerobic granules (6000× magnification). Reprinted from [23], Process Biochemistry, Vol. 40, Wang, J. and Kang, J., The characteristics of anaerobic ammonium oxidation (ANAMMOX) by granular sludge from an EGSB reactor, Pages 1973–1978, Copyright (2005), with permission from Elsevier.
Ijms 14 18572f1
Figure 2. Anaerobic granule formation, according to the model of McHugh et al. [50].
Figure 2. Anaerobic granule formation, according to the model of McHugh et al. [50].
Ijms 14 18572f2
Table 1. Effect of Organic Loading Rate (OLR) and Hydraulic Retention Time (HRT) on the diversity of methanogenic Archaea in anaerobic bioreactors.
Table 1. Effect of Organic Loading Rate (OLR) and Hydraulic Retention Time (HRT) on the diversity of methanogenic Archaea in anaerobic bioreactors.
Reference[37][39][44][56][57]
Type of bioreactorEGSBUASBEGSBPacked-bed biofilm
Nature of wastewaterLeachate from municipal sewage sludge incineration plantUnbleached cellulose pulpOleic acidShort-chain fatty acids
Temperature (°C)33 ± 130 ± 33755
ORL (kg COD/m3/day)3.0 to 18.40.53 to 1.402 to 810 to 1292.9 to 12.2
HRT (h)2.5 to 4.036 to 242424 to 1.415 to 3.6
Method of study of prokaryotic diversityDGGE, qPCRSEM, DGGEDGGE, FISHClone libraryDGGE
Prevalent Archaea detectedMethanosaeta (68.4%) shifting to Methanosarcina (62.3%) at the end of the experimentMethanosarcina
Methanosaeta
Methanobacterium
Methanosaeta
Methanoculleus
Methanothermobacter
Methanosarcina
COD: chemical oxygen demand; SEM: scanning electron microscopy; DGGE: denaturing gradient gel electrophoresis; FISH: fluorescence in situ hybridization; qPCR: quantitative real-time PCR.
Table 2. Effect of temperature on the diversity of methanogenic Archaea in anaerobic bioreactors operated under psycrophilic or mesophilic conditions. See Table 1 footnote for abbreviations.
Table 2. Effect of temperature on the diversity of methanogenic Archaea in anaerobic bioreactors operated under psycrophilic or mesophilic conditions. See Table 1 footnote for abbreviations.
Reference[45][49][63]
Type of bioreactorEGSBEGSBEGSB
Nature of wastewaterSynthetic glucose wastewaterSynthetic brewery wastewaterSynthetic wastewaterSynthetic wastewater added with trichloroethylene (10–60 mg/L)
Temperature (°C)15 and 3715 and 2015 and 37
ORL (kg COD/m3/day)5.8-3
HRT (h)121824
Method of study of prokaryotic diversityDGGE, qPCRClone library, DGGEqPCR
Archaea detected at both temperaturesMethanobacterium beijingense
Methanosaeta concilii
Methanobacterium
Methanosaeta
Methanobacteriales
Methanosaetaceae
Archaea favored by psycrophilic conditionsMethanocorpusculum
Methanosarcinaceae
Methanospirillum
Methanosphaerula
Methanometylovorans
Methanosarcina
Methanomicrobiales
Archaea favored by mesophilic conditionsMethanospirillum hungatei--
Relevant effects of temperatureqPCR demonstrated important shifts of Methanosaeta abundance at 15 °C
Hydrogenotrophic methanogens prevailed at 15 °C, particularly Methanomicrobiales
Lower temperature decreased the abundance of Methanosaeta and led to a higher diversity of methanogensStart up was slower at 15 °C
Methanomicrobiales emerged earlier at 15 °C
Methanosaetaceae response to trichloroethylene toxicity differed with temperature
Table 3. Current status of proposed classification of ammonia-oxidizing Thaumarchaeota. Please note that not all the taxonomic names are published validly.
Table 3. Current status of proposed classification of ammonia-oxidizing Thaumarchaeota. Please note that not all the taxonomic names are published validly.
OrdersGeneraSpeciesOriginReference
Nitrosopumilales (Group I.1a, marine)NitrosopumilusN. maritimusAquarium in Seattle (USA)[78]
Candidatus N. koreensis78-m-deep marine sediment off Svalbard (Arctic Circle)[86]
Candidatus N. salariaSediments in the San Francisco Bay estuary (USA)[87]
Candidatus N. sediminisMarine sediment off Svalbard (Arctic Circle)[88]
Candidatus NitrosoarchaeumCandidatus N. koreensisSoil sample from the rhizosphere of Caragana sinica[89]
Candidatus N. limniaLow-salinity sediments in San Francisco Bay (USA)[90]
Cenarchaeales (Group I.1a associated)CenarchaeumC. symbiosumMarine sponge[91]
Candidatus NitrosotaleaCandidatus N. devanaterraAcidic soil (pH 4.5)[92]
Nitrososphaerales (Group I.1b, soil)Candidatus NitrososphaeraCandidatus N. viennensisGarden soil in Vienna (Austria)[79]
Candidatus N. gargensisMicrobial mats of the Siberian Garga hot spring[93]
Unclassified Thaumarchaeota (Group ThAOA)Candidatus NitrosocaldusCandidatus N. yellowstoniSediment from hydrothermal spring in Yellowstone (USA)[94]
Table 4. Occurrence and abundance of amoA-encoding archaeon (AEA) and ammonia-oxidizing bacteria (AOB) in wastewater treatment (WWT) plants.
Table 4. Occurrence and abundance of amoA-encoding archaeon (AEA) and ammonia-oxidizing bacteria (AOB) in wastewater treatment (WWT) plants.
Reference[95][99][105][98][106][102]
Method of studyClone libraryqPCRqPCRqPCRClone libraryqPCR
No. and type of WWT plants5 AS4 AS1 AS4 urban AS3 industrial ASMBRMBR3 urban3 industrial
SRT (days)17.41117.7512Complete retention15–20
HRT (h)4022.56.24.554.38
COD540177179465596266.31334.67
BOD271.525439.69984.83249333
Average influent NH4+ (mg/L)28.5424.4718.98.23180.84.834.23121.53
Average effluent NH4+ (mg/L)0.160.380.861.217.050.31
% NH4+ removal99.3097.9095.4579.6083.5072.00
DO (mg/L)3.383.803.87
TSS sludge (mg/L)3335281541771,17104600
AEA *+104–106108–1011ND (<102)103–104+105–106103–104
AOB *+ (except 1)+108–109108–1010109–1010105–106+103–105107–109
AS: activated sludge; MBR: membrane bioreactor; SRT: solids retention time; HRT: hydraulic retention time; COD: chemical oxygen demand; BOD: biological oxygen demand at 5 days; DO: dissolved oxygen; TSS: total suspended solids; ND: not detected.
*clone library: positive (+) or negative (−) detection; qPCR: number of amoA gene copies/l activated sludge.

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Calderón, K.; González-Martínez, A.; Gómez-Silván, C.; Osorio, F.; Rodelas, B.; González-López, J. Archaeal Diversity in Biofilm Technologies Applied to Treat Urban and Industrial Wastewater: Recent Advances and Future Prospects. Int. J. Mol. Sci. 2013, 14, 18572-18598. https://doi.org/10.3390/ijms140918572

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Calderón K, González-Martínez A, Gómez-Silván C, Osorio F, Rodelas B, González-López J. Archaeal Diversity in Biofilm Technologies Applied to Treat Urban and Industrial Wastewater: Recent Advances and Future Prospects. International Journal of Molecular Sciences. 2013; 14(9):18572-18598. https://doi.org/10.3390/ijms140918572

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Calderón, Kadiya, Alejandro González-Martínez, Cinta Gómez-Silván, Francisco Osorio, Belén Rodelas, and Jesús González-López. 2013. "Archaeal Diversity in Biofilm Technologies Applied to Treat Urban and Industrial Wastewater: Recent Advances and Future Prospects" International Journal of Molecular Sciences 14, no. 9: 18572-18598. https://doi.org/10.3390/ijms140918572

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