Suspended Biomass Research Articles

Assessment of hybrid fixed and moving bed biofilm applications for wastewater treatment capacity increase – In situ tests in El-Gouna WWTP, Egypt

This paper provides a procedure for comparing the performance of different biofilm carrier medias and their surrounding suspended biomass through oxygen uptake rate (OUR) tests. For in situ (oxygen uptake rate (OUR) measurements, three identical lab scale biofilm reactors were set up at the El Gouna wastewater treatment plant (WWTP). In this setup, two options of media for moving-bed biofilm reactors (MBBR) and one media for fixed-bed biofilm reactors (FBBR) were compared. The WWTP also used the same carrier in a real scale hybrid application to analyze how the interactions between the carrier type and the suspended biomass influences the overall performance. The in situ OUR approach is recommended to measure the contribution of the biofilm fixed biomass under site specific conditions. Specifically, settleability and diffusion limitations are the two opposite poles that cannot be predicted adequately for mild climate conditions based on the literature. A biofilm carrier application can add but actually can also reduce the capacity in a hybrid activated sludge system: The added MBBR-media was able to grind down the sludge flocs forming a poorly settleable suspended biomass. The added FBBR-media can lead to extracellular polymeric substances (EPS) rich biofilms that contribute very little as substrate and oxygen are unavailable for the microorganisms present in the biofilm. In this application of the comparison procedure, Kaldnes K1 like MBBR media was compared with a recycling MBBR carrier option (poly propylene bottle caps) and Jäger Envirotech “BioCurlz™” FBBR media. The study showed higher average rates for the MBBR but decreased settleability. The FBBR showed higher peak rates when flushed to break up the biofilm and well settleable sludge. The determination of OUR per g of volatile solids (SOUR) showed comparable results for all the carriers and in warm conditions, only the capacity to accommodate biomass determines the contribution of the carrier.

Respirometric tests in a combined UASB-MBR system treating wastewater containing emerging contaminants at different OLRs and temperatures: Biokinetic analysis

This research focuses on the application of respirometric techniques to provide new insights into the biokinetic behaviour of bacterial species developed in an Upflow Anaerobic Sludge Blanked -UASB reactor combined with a membrane bioreactor -MBR, treating urban wastewater with emerging contaminants frequently found in this kind of effluents. The lab-scale pilot plant was operated at different metabolic and operational conditions by limiting the organic loading rate- OLR of the influent. In a first stage, the MBR was performed with suspended biomass, while in a second stage bio-supports were introduced to operate coexisting suspended and fixed biomass. From the results of the microscopic monitoring of sludge, it was concluded that the decrease in OLR resulted in a greater disintegration of the floc structure, more dispersed growth, and a low presence of inter-floccular bonds. However, no effect of toxicity or inhibition of microorganisms caused by the presence of emerging contaminants -ECs was determined. Kinetic modelling was carried out to study the behaviour of the system. The results showed a slowing down of biomass degradative capacity at low OLR stages and operating at low temperatures of mixed liquor. In addition, a decrease in oxygen consumption was observed with decreasing biodegradable substrate, resulting in lower degradation of organic matter. Mean values of specific oxygen uptake rate and heterotrophic biomass yield at low OLR were SOUR end = 1.49 and 1.15 mg O2· g MLVSS−1 h−1 and YH,MLSSV end = 0.48 and 0.28 mg MLVSS· mg COD−1substrate at stage 1 (suspended biomass) and stage 2 (suspended and supported biomass), respectively. From the analysis of the endogenous decomposition constant (kd), a higher cell lysis was determined operating with suspended biomass (kd = 0.03 d−1) in comparison to the operation coexisting suspended and supported biomass (kd = 0.01 d−1). Heterotrophic biomass yield values (YH, MLVSS = 0.48 ± 0.06, 0.40 ± 0.01 and 0.29 ± 0.01 mg MLVSS· mg COD−1substrate at high, medium and low OLR) showed lower sludge production at low OLR due to the influence of substrate limitation on cell growth.

Advances in the Efficient Enrichment of Anammox Bacteria

Anaerobic ammonia oxidation (anammox) process is known as a low-energy and environmentally friendly process for treating nitrogen-rich wastewater. Anammox bacteria are the key microorganisms to achieve this biological process. However, the efficient enrichment of anammox bacteria has been a bottleneck for its practical application because of their slow growth and high sensitivity, and no pure culture has been found. Therefore, the development of efficient anammox bacterial enrichment techniques is of great theoretical and application value. Solving the problem of anammox bacterial activity and improving the process denitrification performance is one of the current research hotspots. In this paper, three aspects of anammox bacteria are described in terms of their physiological properties, environmental influencing factors, and short-term starvation tolerance; a systematic review of the latest research progress in accelerating the activity of anammox bacteria using enrichment strategies for process regulation, the construction of granulation models, suspended sludge biomass management, and strain preservation. Finally, the future frontier development of anammox bacteria was discussed and foreseen.

Electrode Material Optimization of Nitrous Oxide Recovery from Incineration Leachate in a ΔnosZ Pseudomonas aeruginosa/MEC System

Nitrous oxide (N2O) is not only recognized as a potent greenhouse gas, but it is also used in industry as a clean energy source. In this study, different electrode materials of carbon felt and graphite were equipped in the ΔnosZ P. aeruginosa/microbial electrolysis cell (MEC) systems to explore the optimization mechanism for long-term N2O recovery during incineration leachate treatment. The carbon felt group showed a better performance in N2O recovery across 45 days of operation. The N2O conversion efficiency was above 80% and the proportion of N2O in biogas accounted for 80.6% in the carbon felt group. qRT-PCR analysis was conducted to evaluate the expression of genes involved in denitrification (norB) and electroactivity (phzG, phzM, and phzH) of ΔnosZ P. aeruginosa. The results showed a significant upregulation in the suspended biomass (day 21) and the electron-attached biomass (day 45) from the carbon felt-equipped reactor, which was highly related to the opportunity of biomass exposed to the phenazine derivatives. By the carbon felt optimization in the system, 82.6% of the Pseudomonas genus survived after 45 days of operation. These results indicate that the carbon felt electrode has a more sustainable performance for N2O recovery in the ΔnosZ P. aeruginosa/MEC system.

Combined use of strictly anaerobic MBBR and aerobic MBR for municipal wastewater treatment and removal of pharmaceuticals

An integrated lab-scale wastewater treatment system consisting of an anaerobic Moving Bed Biofilm Reactor (AnMBBR) and an aerobic Membrane Bioreactor (AeMBR) in series was used to study the removal and fate of pharmaceuticals during wastewater treatment. Continuous-flow experiments were conducted applying different temperatures to the AnMBBR (Phase A: 35 °C; Phase B: 20 °C), while batch experiments were performed for calculating sorption and biotransformation kinetics. The total removal of major pollutants and target pharmaceuticals was not affected by the temperature of the AnMBBR. In Phase A, the average removal of dissolved chemical oxygen demand (COD), biological oxygen demand (BOD), and ammonium nitrogen (NH4–N) was 86%, 91% and 96% while in Phase B, 91%, 96% and 96%, respectively. Removal efficiencies ranging between 65% and 100% were observed for metronidazole (MTZ), trimethoprim (TMP), sulfamethoxazole (SMX), and valsartan (VAL), while slight (<30%) or no removal was observed for carbamazepine (CBZ) and diclofenac (DCF), respectively. Application of a mass balance model showed that the predominant mechanism for the removal of pharmaceuticals was biotransformation, while the role of sorption was of minor importance. The AeMBR was critical for VAL, SMX and TMP biodegradation; the elimination of MTZ was strongly enhanced by the AnMBBR. In both bioreactors, Bacteroidetes was the dominant phylum in both bioreactors over time. In the AnMBBR, Cloacibacterium and Bacteroides had a higher abundance in the biocarriers compared to the suspended biomass.

Recirculating packed-bed biofilm photobioreactor combined with membrane ultrafiltration as advanced wastewater treatment

Packed-bed biofilm photobioreactor combined with ultrafiltration membrane was investigated for intensifying the process for secondary wastewater effluent treatment. Cylindrical glass carriers were used as supporting material for the microalgal-bacterial biofilm, which developed from indigenous microbial consortium. Glass carriers allowed adequate growth of the biofilm with limited suspended biomass. Stable operation was achieved after a start-up period of 1000 h, where supernatant biopolymer clusters were minimized and complete nitrification was observed. After that time, biomass productivity was 54 ± 18 mg·L−1·day−1. Green microalgae Tetradesmus obliquus and several strains of heterotrophic nitrification–aerobic denitrification bacteria and fungi were identified. Combined process exhibited COD, nitrogen and phosphorus removal rates of 56 ± 5%, 12 ± 2% and 20 ± 6%, respectively. Membrane fouling was mainly caused by biofilm formation, which was not effectively mitigated by air-scouring aided backwashing.

Effects of biocarrier type and size on the performance of nitrification and simultaneous nitrification and denitrification

Four soft polyurethane biocarriers with different sizes and a hard polypropylene biocarrier were selected to evaluate the effects of material type and size on the nitrification and simultaneous nitrification and denitrification (SND) performance of the aerobic moving bed biofilm reactors (MBBR) in treating synthetic coking wastewater under different organic loading rates (OLR, 0.95, 0.65, 0.49 kg COD m−3 day−1). The attached biomass concentrations of the polyurethane biocarriers were 1.65 ± 0.15 g L−1, almost twice that of the polypropylene one (0.76 ± 0.05 g L−1), while the differences in the suspended biomass concentrations were relatively small (1.48 ± 0.18 g L−1 and 1.28 ± 0.06 g L−1, respectively). The SND efficiency of 32.43% ± 5.15% for all five MBBRs was achieved at an OLR of 0.95 kg COD m−3 d−1, which decreased to 8.48% ± 5.25% and 4.35% ± 2.99%, respectively, at lower OLRs. It was clear that OLR was an important factor affecting the SND performance. The MBBR using the smallest polyurethane biocarrier (10 mm × 10 mm × 10 mm) achieved complete nitrification at an OLR of 0.65 kg COD m−3 day−1, while the other ones achieved it at a lower OLR (0.49 kg COD m−3 day−1). The smallest polyurethane biocarrier exhibited a higher specific ammonium oxidizing rate (SAOR, 0.071 ± 0.007 g NH4+-N g−1 VSS day−1) than the other ones (0.045–0.050 g NH4+-N g−1 VSS day−1 for the larger size polyurethane ones and 0.023 ± 0.002 g NH4+-N g−1 VSS day−1 for the polypropylene one). Miseq analysis revealed that Nitrosomonas and Nitrospira were respectively the dominant AOB and NOB in all MBBRs. The polyurethane biocarriers enriched AOB and NOB in the biofilms as much as 14.6 and 9.7 times, while the polyethylene one only enriched them 3.8 and 2.2 times. Thus, the polyurethane biocarrier with smaller size was advantageous for improving nitrification capacity.

From hybrid process to pure biofilm anammox process: Suspended sludge biomass management contributing to high-level anammox enrichment in biofilms

The application of mainstream anammox is highly desirable for municipal wastewater treatment. However, enrichment of anammox bacteria (AnAOB) is challenging, particularly given the vicious competition from denitrifying bacteria (DB). Here, suspended sludge biomass management, a novel operational strategy for hybrid process (suspended sludge/biofilm), was investigated for 570 days based on a modified anaerobic–anoxic–oxic system treating municipal wastewater. By successively decreasing the suspended sludge concentration, the traditional hybrid process was successfully upgraded to a pure biofilm anammox process. During this process, both the nitrogen removal efficiency (NRE) and rate (NRR) were significantly improved (P < 0.001), from 62.1 ± 4.5% to 79.2 ± 3.9% and from 48.7 ± 9.7 to 62.3 ± 9.0 g N/(m3·d), respectively. Mainstream anammox was improved in the following: Candidatus Brocadia was enriched from 0.70% to 5.99% in anoxic biofilms [from (9.94 ± 0.99) × 108 to (1.16 ± 0.01) × 1010 copies/g VSS, P < 0.001]; the in situ anammox reaction rate increased from 8.8 ± 1.9 to 45.5 ± 3.2 g N/(m3·d) (P < 0.001); the anammox contribution to nitrogen removal rose from 9.2 ± 2.8% to 67.1 ± 8.3% (P < 0.001). Core bacterial microbiome analysis, functional gene quantification, and a series of ex situ batch experiments demonstrated that the stepwise decreases in suspended sludge concentration effectively mitigated the vicious competition of DB against AnAOB, enabling high-level AnAOB enrichment. This study presents a straightforward and effective strategy for enriching AnAOB in municipal wastewater, shedding fresh light on the application and upgradation of mainstream anammox.

Biological degradation and mineralization of tetracycline antibiotic using SBR equipped with a vertical axially rotating biological bed (SBR-VARB)

Tetracycline (TC) is a widely used antibiotic with a complex aromatic chemical structure and is highly resistant to biodegradation. In this study, an SBR equipped with a vertical axially rotating biological bed (SBR-VARB) was used for the biodegradation and mineralization of TC. SBR-VARB showed high efficiency in removing TC (97%), total phenolic compounds (TP) (95%), and COD (85%) under optimal operating conditions (TC = 50 mg/L, HRT = 1.75 d, and OLR = 36 g COD/m3 d). The SBR-VARB was able to treat higher concentrations of TC in shorter HRT than reported in previous studies. The contribution of VARB to improve SBR efficiency in removing TC, TP, and COD was 16, 36, and 48%, respectively. Intermediate compounds formed during the biodegradation of TC were identified using GC–MS under the optimal operating conditions of the bioreactor. These are mainly organic compounds with linear chemical structures. Based on the complete biodegradation of TC under the optimal operating conditions of the bioreactor, 93% and 36% of the chlorine and nitrogen atoms in the chemical structure of TC appeared in the wastewater, respectively. According to the sequence analysis of 16SrDNA, Pseudomonas sp., Kocuria Polaris, and Staphylococcus sp. were identified in the biofilm of VARB and the suspended biomass of the bioreactor. Therefore, SBR-VARB showed high efficiency in the biodegradation and mineralization of TC and can be used as a suitable option for treating wastewater containing antibiotics and other toxic compounds.

Deciphering community assembly and succession in sequencing batch moving bed biofilm reactor: Differentiation between attached and suspended communities

Elucidating community assembly and succession is crucial to understanding the ecosystem functioning. Herein, the ecological processes underpinning community assembly and succession were studied to uncover the respective ecological functions of attached biofilms and suspended biomass in a sequencing batch moving bed biofilm reactor. Compared with suspended biomass, attached biofilms presented higher relative abundances of Nitrospira (2.94 %) and Nitrosomonas (1.25 %), and contributed to 66.89 ± 11.37 % and 68.11 ± 12.72 % of nitrification and denitrification activities, respectively. The microbial source tracking result demonstrated that early formation of suspended biomass was dominated by the seeding effect of detached biofilms in the start-up period (days 0–30), while self-growth of previous suspended biomass was eventually outcompeted the seeding effect when the reactor stabilized (days 31–120). Null model and ecological network analysis further suggested distinctive ecological processes underpinning the differentiation between attached and suspended communities in the same reactor. Specifically, in the start-up period, positive interactions facilitated early formation of attached (73.84 %) and suspended communities (59.41 %), while homogenous selection (88.89 %) and homogenizing dispersal (65.71 %) governed assembly of attached and suspended communities, respectively. When the reactor stabilized, attached and suspended communities showed low composition turnover as reflected by dominant homogenizing dispersal, while they presented distinctive trends of interspecies interactions. This study sheds light on discrepant ecological processes governing community differentiation of attached biofilms and suspended biomass, which would provide ecological insights into the regulation of hybrid ecosystems.

Resource recovery using enriched purple phototrophic bacteria in an outdoor flat plate photobioreactor: Suspended vs. attached growth

Purple phototrophic bacteria (PPB) can produce single-cell protein from wastewater at high yields. Growing in a biofilm vs suspended can improve product quality and consistency. This study compares suspended and attached growths of enriched PPB cultures in an outdoor flat plate photobioreactor treating poultry-processing wastewater. Attached growth had lower VFA removal efficiencies (95 ± 2.7 vs 84 ± 6.4 %) due to light limitations and low substrate diffusion rates. Nevertheless, similar overall treatment performances and productivities were achieved (16 ± 2.2 and 18 ± 2.4 gCOD·m−2·d−1 for attached and suspended) at loading rates of 1.2–1.5 gCOD·L−1·d−1. Biofilms had higher quality than suspended biomass, with lower ash contents (6.9(0.6)% vs 57(16)%) and higher PPB abundances (0.45–0.67 vs 0.30–0.45). The biofilm (20–50 % of the total biomass) might be used as feed and the suspended fraction as fertiliser, improving the economics of the process. Semi-continuous PPB growth outdoors as biofilm is technically feasible, obtaining a superior product without jeopardising performance.

Understanding the role of polyurethane sponges on rapid formation of aerobic granular sludge and enhanced nitrogen removal

Long formation time and limited simultaneous nitrification–denitrification (SND) are still the problems for aerobic granular sludge (AGS) application. This study presents a novel strategy to simultaneously promote sludge granulation and enhance nitrogen removal. This new approach consists of adding polyurethane sponges (PUS) and applying intensive aeration periodically. To demonstrate the effectiveness of this strategy and understand the role of PUS, two sequencing batch reactors (R1: without PUS; R2: PUS addition) were used. The results show that the granulation time in R2 (14 days) was much shorter and the nitrogen removal (80.7 %) was much higher when compared to the R1 (75 days and 64.8 %). Biofilm was rapidly formed on PUS because of the porous network structure, resulting in the low suspended biomass concentration. Thus, a close to discrete non-flocculent settling type was created, which promoted the selection of well-settling aggregates rapidly and efficiently. Meanwhile, biofilm was detached from PUS by intensive aeration, providing the nucleus (fragments of biofilm) in-suit for microbial adhesion. Under the combined effects, the aerobic granulation process was significantly accelerated. The total biomass amount was maintained during initial granulation because of the rapid biofilm formation, resulting in the stable removal of NH4+-N at a rapid start-up period. The rapid formation of biofilm and fast granulation created more anoxic zones during aeration and thereby enhanced SND. The biofilm formation also increased the relative abundances of aerobic denitrifiers (Dokdonella and Denitratisoma), autotrophic denitrifiers (Sulfuritalea), and hydrolytic/fermentativebacteria (Ferruginibacter, Opitutus, and Lactobacillus), which enhanced the SND performance and endogenous denitrification.

A strategy for fast anammox biofilm formation under mainstream conditions

One of the bottlenecks to applying anaerobic ammonium oxidation (Anammox) is the long start-up time, especially under mainstream conditions. This study proposed a strategy for fast anammox biofilm formation under mainstream conditions. By first cultivating an aerobic heterotrophic biofilm, and then transferring to anoxic conditions, a pre-cultivated heterotrophic biofilm can be formed in 12 days. The pre-cultivated heterotrophic biofilm then functions as a “glue” to accelerate anammox bacteria adhesion and biofilm formation. Secondary settled effluent with externally added 15–30 mg-N·L−1 ammonium and nitrite was applied as reactor influent. With a single inoculation of suspended growth anammox-laden biomass and no bioaugmentation, an anammox-enriched biofilm formed after 5 months of operation under uncontrolled temperature of 15–20 °C. Both the nitrogen removal rate and specific anammox activity exponentially increased over the course of study, corresponding to an estimated anammox doubling time of 10.8 days. The biofilm thickness on primed carriers was 2–3 times higher than on the non-primed carriers over the first 5 months of operation, and the hszA gene copy number in primed biofilms revealed was consistently 1 to 2 times higher than the non-primed carrier biofilm, indicating that biofil m carrier priming via selection for a pre-cultivated heterotrophic biofilm base can effectively improve the anammox enrichment rate at early stages of reactor operation. Time, rather than the type of biofilm (primed versus non-primed), had a stronger influence on microbial community structure over the full 230 days of reactor operation. Candidatus Brocadia was the only detected anammox bacteria genus. Overall, pre-cultivation of heterotrophs on biofilm carriers provides a simple route to accelerate anammox-enriched biofilm formation under mainstream conditions.

Synergistic effects of powdered activated carbon (PAC) during initial biofilm formation of the methanogenic consortium on polyurethane foam

AbstractBACKGROUNDIn the unfavorable conditions of anaerobic digestion systems, the attached or immobilized microbial communities used as biofilm are more resistant to being washed out than the suspended biomass. The biofilm formation was determined by the carrier characteristics, considering their physicochemical properties and high availability. This study presented an approach for improving the use of polyurethane (PU) foam as a biofilm carrier for methanogenic consortium.RESULTSThe effect of powdered activated carbon (PAC) on the reactor performance and biofilm formation was apparent during days 0–30. The average chemical oxygen demand (COD) removal, methane (CH4) composition, and CH4 yield of PAC‐supplemented reactor (R2) in this period were 71.40%, 82.0%, and 0.3 L CH4 g−1 COD removed, respectively; these values were higher than those of the control reactor (R1). In addition, a greater amount of biomass was observed on the PU foam of R2 (1.47 g VSS), indicating a higher biofilm formation. Scanning electron microscopy (SEM) analysis revealed that microbial biofilm on the PAC‐supplemented PU was also denser than that on the control PU. In addition, fluorescence in situ hybridization (FISH) detected layers of Methanosarcinales and Smithella sp.CONCLUSIONThis study demonstrated that PAC supplementation had synergistic effects during initial biofilm formation of the methanogenic consortium by accelerating microbial attachment, preserving biofilm structure, and enhancing methanogenic activity. © 2023 Society of Chemical Industry (SCI).

Effect of nutrients deficiency on biofilm formation and single cell protein production with a purple non-sulphur bacteria enriched culture

Purple non-sulphur bacteria (PNSB) are of interest for biorefinery applications to create biomolecules, but their production cost is expensive due to substrate and biomass separation costs. This research has utilized fuel synthesis wastewater (FSW) as a low-cost carbon-rich substrate to produce single-cell protein (SCP) and examines PNSB biofilm formation using this substrate to achieve a more efficient biomass-liquid separation. In this study, PNSB were grown in Ca, Mg, S, P, and N-deficient media using green shade as biofilm support material. Among these nutrient conditions, only N-deficient and control (nutrient-sufficient) conditions showed biofilm formation. Although total biomass growth of the control was 1.5 times that of the N-deficient condition and highest overall, the total biofilm-biomass in the N-deficient condition was 2.5 times greater than the control, comprising 49% of total biomass produced. Total protein content was similar between these four biomass samples, ranging from 35.0 ± 0.2% to 37.2 ± 0.0%. The highest protein content of 44.7 ± 1.3% occurred in the Mg-deficient condition (suspended biomass only) but suffered from a low growth rate. Overall, nutrient sufficient conditions are optimal for overall protein productivity and dominated by suspended growth, but where fixed growth systems are desired for cost-effective harvesting, N-deficient conditions provide an effective means to maximize biofilm production without sacrificing protein content.

Granular activated carbon stimulated microbial extracellular secretions in anaerobic digesters: An egalitarian act and beyond

Granular activated carbon (GAC) has been widely studied for its roles in improving anaerobic digestion (AD) through its conductive properties in stimulating direct interspecies electron transfer or its surface functional groups in altering redox conditions in AD. In the present study, the impacts of GAC on the biosynthesis of extracellular microbial secretions (e.g., amino acids and vitamins), and the roles of these secretions in AD were investigated. Four continuous laboratory reactors were operated under ambient temperature (20 ± 0.5 °C) conditions, including two up-flow anaerobic sludge blanket (UASB) bioreactors with GAC addition to one of the UASBs; and two anaerobic sequencing batch reactors (ASBRs) each fed with the centrifuged supernatants (to remove suspended biomass and GAC debris) of UASB effluents supplemented with additional carbon source (glucose). Our finding shows that GAC addition stimulated extracellular microbial secretions in UASB, and these secretions, which can work as essential nutrients, enhanced COD removal (from 48 ± 3 % to 60 ± 1 %) and methane production (31 ± 3 % to 47 ± 5 %) in its downstream ASBR. Interestingly, microbial kinetics test showed that extracellular microbial secretions from the GAC-amended UASB improved methane production rate from 72.5 ± 1.5 to 105.6 ± 1.2 mg CH4-COD/g VSS/d without dramatic microbial community shift. We conclude that the impact of GAC on AD does not only rely on the direct contact of microorganisms and GAC materials, and the GAC-stimulated microbial extracellular secretions represent an important mechanism in conductive material amended AD.

Nitrogen influence on suspended vs biofilm growth and resource recovery potential of purple non-sulfur bacteria treating fuel synthesis wastewater

Purple non-sulfur bacteria (PNSB) have a strong potential for various bioproduct avenues including single-cell protein (SCP), and production of pigments and polyhydroxybutyrate. However, high substrate and separation costs are major barriers to commercialization. Therefore, this research investigates the integration of PNSB biomass production with treatment of fuel synthesis wastewater (FSW) for a low-cost substrate and formation of biofilm for improved harvesting. An enriched PNSB culture was cultivated in two different biofilm photobioreactors (nitrogen sufficient, N+, and nitrogen-deficient, N-) with a piece of woven agricultural shade cloth as biofilm support material. Higher chemical oxygen demand (COD) removal and PNSB biofilm were obtained in the N- condition. The maximum bacteriochlorophylls occurred in the N+ suspended culture (2.65 ± 0.3 µg/g), and maximum carotenoids in the N- suspended culture (3.75 ± 1 µg/g). The cellular protein content in both conditions and biomass types was between 40 % and 44 %. The polyhydroxybutyrate content was 10–12 %, except for the N+ suspended biomass condition, which was only 3.5 %. To conclude, a nitrogen-deficient biofilm-based system showed a similar bioproduct performance to other operational modes, indicating its potential to reduce costs of PNSB-produced high value-added resources, including carotenoids, SCP, and polyhydroxybutyrate while removing organics from wastewater.

Syntrophic acetate oxidation having a key role in thermophilic phenol conversion in anaerobic membrane bioreactor under saline conditions

Phenol conversion under saline thermophilic anaerobic conditions requires the development and sustenance of a highly specialized microbial community. In the present research, an anaerobic membrane bioreactor (AnMBR) fed with an influent containing 0.5 g·L−1 phenol and 6.5 gNa+·L−1 was operated at 55 °C for 300 days. Phenol degradation was limited when phenol was the sole substrate. However, the phenol removal efficiency significantly (p < 0.001) increased to 80 % corresponding to a conversion rate of 29 mgPhenol·gVSS−1d−1 when acetate (0.5 gCOD·L−1) was simultaneously provided. Isotopic analysis using 1–13C labeled acetate and measuring 13CH4 revealed that acetate was first oxidized to hydrogen and CO2, prior to methanogenesis, resulting in an increased abundance of hydrogenotrophic methanogens. It is hypothesized that the latter is of crucial importance for achieving effective anaerobic oxidation of phenol and its metabolites. Remarkably, the phenol conversion rate in the membrane-associated biomass was three times higher than in the suspended biomass. The observed difference in the conversion rate could be explained by the presence of an increased abundance of hydrogenotrophic methanogens in the membrane-associated biomass confirmed by a microbial community analysis of Archaea. Benzoate was measured in the permeate suggesting that phenol degradation occurred via the benzoyl-CoA pathway. The results of the current study suggest that syntrophic acetate oxidation coupled with hydrogenotrophic methanogenesis, which results in the presence of an abundant electron sink, plays a key role in enhancing thermophilic phenol degradation. The obtained insights widen the application of anaerobic digestion to treat saline phenolic-rich wastewater at high temperatures.

Integration of coagulation-flocculation process for improved solid–liquid separation of anaerobically treated textile effluent

ABSTRACT Anaerobic process is a promising technique for textile effluent treatment. However, poor solid–liquid separation and residual chemical oxygen demand (COD) in the treated effluent limit its scope for industrial applications. The study analyzed the nature of suspended microbial biomass in the anaerobically treated effluent and further targeted its feasible separation process. The size of the majority of suspended biomass (82%) particles ranged from 500 to 1000 nm. The suspended biomass showed 37.13% hydrophobicity and −15.4 mV zeta potential. The optimization of the coagulation-flocculation (CF) process showed 93% turbidity removal at 400 mg/L of alum, 8 mg/L of a cationic polymer and acidic pH 4, through one variable at a time approach. The optimized results using Central Composite Design (CCD) were experimentally validated, and 97% turbidity removal was recorded at 400 mg/L alum concentration, 12 mg/L of the cationic polymer, and pH 3.2. The results obtained were statistically significant, with a high regression coefficient (R2 = 0.97) at 95% confidence limits. The final treated effluent after CF showed 67% COD removal (from 862 ± 40 to 280 ± 14 mg/L) with 83% color removal (from 740 to 124 Hazen). Hence, the integration of the CF process with the anaerobic process could be a promising approach for textile effluent treatment.

Treatment of high-strength saline bilge wastewater by four pilot-scale aerobic moving bed biofilm reactors and comparison of the microbial communities

ABSTRACT Four Pilot-scale Moving Bed Biofilm Reactors (MBBRs) were operated for the treatment of real, saline, bilge wastewater. The MBBRs were connected in pairs to create two system configurations with different filling ratios (20%, 40%) and were operated in parallel. The inflow organic loading rate (OLR) varied from 3.6 ± 0.2 to 7.8 ± 0.6 g COD L−1 d−1, salinity was >15 ppt and three hydraulic residence times (HRTs) were tested 48, 30 and 24 h. In both systems, the first-stage bioreactors (R1 and R3) eliminated the higher part of the organic load (57%–65%). The second-stage bioreactors (R2 and R4) removed an additional fraction (18%–31%) of the organic load received by the effluent of R1 and R3, respectively. The microbial communities of the influent wastewater, suspended, and attached biomass were determined using 16S rRNA gene amplicon sequencing analysis. The evolution of the microbial communities was investigated and compared over the different operational phases. The microbial communities of the biofilm presented higher diversity and greater stability in composition over time, while the suspended biomass exhibited intense and rapid changes in the dominance of genera. Proteobacteria, Bacteroidetes and Firmicutes were highly present in the biofilm. The genera Celeribacter, Novispirillum, Roseovarius (class: Alphaproteobacteria) and Formosa (class: Flavobacteriia) were highly present during all operational phases. Principal Component Analysis (PCA) was used to identify similarities between samples, exhibiting high relation of samples according to the series of the bioreactor (1st, 2nd).