Comparison of physical technologies for biomass control in biofilters treating gaseous toluene

Biofiltration of toluene in the presence of ethyl acetate or n-hexane: Performance and microbial community

This study describes the operation of two independent parallel laboratory-scale biotrickling filters (BTFs) to degrade different types of binary volatile organic compound (VOC) mixtures. Comparison experiments were conducted to evaluate the effects of two typical VOCs, i.e., ethyl acetate (a hydrophilic VOC) and n-hexane (a hydrophobic VOC) on the removal performance of toluene (a moderately hydrophobic VOC) in BTFs ''A" and ''B", respectively. Experiments were carried out by stabilizing the toluene concentration at 1.64 g m-3 and varying the concentrations of gas-phase ethyl acetate (0.85-2.8 g m-3) and n-hexane (0.85-2.8 g m-3) at an empty bed residence time (EBRT) of 30 s. In the presence of ethyl acetate (850 ± 55 mg m-3), toluene exhibited the highest removal efficiency (95.4 ± 2.2%) in BTF "A". However, the removal rate of toluene varied from 48.1 ± 6.9% to 70.1 ± 6.8% when 850 ± 123 mg m-3 to 2800 ± 136 mg m-3 of n-hexane was introduced into BTF "B". The high-throughput sequencing data revealed that the genera Pseudomonas and Comamonadaceae_unclassified are the core microorganisms responsible for the degradation of toluene. The intensity of the inhibitory or synergistic effects on toluene removal was influenced by the type and concentration of the introduced VOC, as well as the number and activity of the genera Pseudomonas and Comamonadaceae_unclassified. It provides insights into the interaction between binary VOCs during biofiltration from a microscopic perspective.

Microbial community regulation and performance enhancement in gas biofilters by interrupting bacterial communication

BACKGROUND

Controlling excess biomass accumulation and clogging is important for maintaining the performance of gas biofilters and reducing energy consumption. Interruption of bacterial communication (quorum quenching) can modulate gene expression and alter biofilm properties. However, whether the problem of excess biomass accumulation in gas biofilters can be addressed by interrupting bacterial communication remains unknown.

RESULTS

In this study, parallel laboratory-scale gas biofilters were operated with Rhodococcus sp. BH4 (QQBF) and without Rhodococcus sp. BH4 (BF) to explore the effects of quorum quenching (QQ) bacteria on biomass accumulation and clogging. QQBF showed lower biomass accumulation (109 kg/m³) and superior operational stability (85-96%) than BF (170 kg/m³; 63-92%) at the end of the operation. Compared to BF, the QQBF biofilm had lower adhesion strength and decreased extracellular polymeric substance production, leading to easier detachment of biomass from filler surface into the leachate. Meanwhile, the relative abundance of quorum sensing (QS)-related species was found to decrease from 67 (BF) to 56% (QQBF). The QS function genes were also found a lower relative abundance in QQBF, compared with BF. Moreover, although both biofilters presented aromatic compounds removal performance, the keystone species in QQBF played an important role in maintaining biofilm stability, while the keystone species in BF exhibited great potential for biofilm formation. Finally, the possible influencing mechanism of Rhodococcus sp. BH4 on biofilm adhesion was demonstrated. Overall, the results of this study achieved excess biomass control while maintaining stable biofiltration performance (without interrupting operation) and greatly promoted the use of QQ technology in bioreactors. Video Abstract.

Emissions, measurement, and control of odor in livestock farms: A review

Odor emissions from intensive livestock farms have attracted increased attention due to their adverse impacts on the environment and human health. Nevertheless, a systematic summary regarding the characteristics, sampling detection, and control technology for odor emissions from livestock farms is currently lacking. This paper compares the development of odor standards in different countries and summarizes the odor emission characteristics of livestock farms. Ammonia, the most common odor substance, can reach as high as 4100 ppm in the compost area. Sampling methods for point and area source odor emissions are introduced in this paper, and odor analysis methods are compared. Olfactometers, odorometers, and the triangle odor bag method are usually used to measure odor concentration. Odor control technologies are divided into three categories: physical (activated carbon adsorption, masking, and dilution diffusion), chemical (plant extract spraying, wet scrubbing, combustion, non-thermal plasma, and photocatalytic oxidation), and biological (biofiltration, biotrickling, and bioscrubbing). Each technology is elucidated, and the performance in the removal of different pollutants is summarized. The application scopes, costs, operational stability, and secondary pollution of the technologies are compared. The generation of secondary pollution and long-term operation stability are issues that should be considered in future technological development. Lastly, a case analysis for engineering application is conducted.

Simultaneous biodegradation of methane and styrene in biofilters packed with inorganic supports: Experimental and macrokinetic study

Four upflow 0.018 m³ biofilters (3 beds), B-ME, B-200, B-500 and B-700, all packed with inorganic materials, were operated at a constant air flow rate of 0.18 m³ h^-1 to eliminate methane (CH₄), a harmful greenhouse gas (GHG), and styrene (C₈H₈), a carcinogenic volatile organic compound (VOC). The biofilters were irrigated with 0.001 m³ of recycled nutrient solution (NS) every day (flow rate of 60 × 10^-3 m³ h^-1). Styrene inlet load (IL) was kept constant in each biofilter. Different CH₄-ILs varying in the range of 7-60 gCH₄ m^-3 h^-1 were examined in B-ME (IL of 0 gC₈H₈ m^-3 h^-1), B-200 (IL of 9 gC₈H₈ m^-3 h^-1), B-500 (IL of 22 gC₈H₈ m^-3 h^-1) and B-700 (IL of 32 gC₈H₈ m^-3 h^-1). Finally, the effect of C₈H₈ on the macrokinetic parameters of CH₄ biofiltration was studied based on the Michaelis-Menten model. Average C₈H₈ removal efficiencies (RE) varying between 64 and 100% were obtained at CH₄-ILs increasing from 7 to 60 gCH₄ m^-3 h^-1 and for C₈H₈-ILs range of 0-32 gC₈H₈ m^-3 h^-1. More than 90% of C₈H₈ was removed in the bottom and middle beds of the biofilters. By increasing C₈H₈-IL from 0 to 32 gC₈H₈ m^-3 h^-1, maximal EC in Michaelis-Menten model and macrokinetic saturation constant declined from 311 to 39 g m^-3 h^-1 and from 19 to 2.3 g m^-3, respectively, which confirmed that an uncompetitive inhibition occurred during CH₄ biofiltration in the presence of C₈H₈.

Performance enhancement of a biofilter with pH buffering and filter bed supporting material in removal of chlorobenzene

Acidic substances, which produced during chlorinated volatile organic compounds, will corrode the commonly used packing materials, and then affect the removal performance of biofiltration. In this study, three biofilters with different filter bed structure were established to treat gaseous chlorobenzene. CaCO₃ and 3D matrix material was added in filter bed as pH buffering material and filter bed supporting material, respectively. A comprehensive investigation of removal performance, biomass accumulation, microbial community, filter bed height, voidage, pressure drops, and specific surface area of the three biofilters was compared. The biofilter with CaCO₃ and 3D matrix material addition presented stable removal performance and microbial community, and greater biomass density (209.9 kg biomass/m³ filter bed) and growth rate (0.033 d^-1) were obtained by using logistic equation. After 200 days operation, the height, voidage, pressure drop, specific surface area of the filter bed consisted of perlite was 27.4 cm, 0.39, 32.8 Pa/m, 974,89 m²/m³, while those of the filter bed with CaCO₃ addition was 28.2 cm, 0.43, 21.3 Pa/m, and 1021.03 m²/m³, and those of the filter bed with CaCO₃ and 3D matrix material addition was 28.7 cm, 0.55, 17.4 Pa/m, and 1041.60 m²/m³. All the results verified the biofilter with CaCO₃ and 3D matrix material addition is capable of sustaining the long-term performance of biofilters. CaCO₃ could limit the changes of removal efficiency, microbial community and filter bed structure by buffering the pH variation. And 3D matrix material could maintain the filter bed structure by supporting the filter bed, regardless of the buffering effect.

Comparative Evaluation of Selected Biological Methods for the Removal of Hydrophilic and Hydrophobic Odorous VOCs from Air

Due to increasingly stringent legal regulations as well as increasing social awareness, the removal of odorous volatile organic compounds (VOCs) from air is gaining importance. This paper presents the strategy to compare selected biological methods intended for the removal of different air pollutants, especially of odorous character. Biofiltration, biotrickling filtration and bioscrubbing technologies are evaluated in terms of their suitability for the effective removal of either hydrophilic or hydrophobic VOCs as well as typical inorganic odorous compounds. A pairwise comparison model was used to assess the performance of selected biological processes of air treatment. Process efficiency, economic, technical and environmental aspects of the treatment methods are taken into consideration. The results of the calculations reveal that biotrickling filtration is the most efficient method for the removal of hydrophilic VOCs while biofilters enable the most efficient removal of hydrophobic VOCs. Additionally, a simple approach for preliminary method selection based on a decision tree is proposed. The presented evaluation strategies may be especially helpful when considering the treatment strategy for air polluted with various types of odorous compounds.

Treatment of hydrophobic volatile organic compounds using two-liquid phase biofilters

The traditional one-liquid phase biofilter (OLPB), with water as the selected liquid phase, demonstrated low performance to volatile hydrophobic organic compounds. In this study, a novel two-liquid phase biofilter (TLPB) using silicone oil and water was established to treat gaseous dichloromethane (DCM). A comprehensive investigation of removal performance, kinetic analysis, biomass accumulations, pressure drops, CO₂ productions, and microbial communities of the two biofilters was compared. Results showed that TLPB presented an average removal efficiency of 85% during 200 days of operation, which was higher than that of OLPB (63%). Owing to the buffering effects caused by silicone oil, TLPB demonstrated a superior fluctuation resistance capability than OLPB. TLPB was determined at a higher actual mass distribution coefficient of 6.00 than that of the OLPB (3.99), thereby suggesting a significantly more effective mass transfer process inside TLPB compared with that in OLPB. Furthermore, a rapid biomass accumulation process was observed in TLPB. The specific growth rates of biomass in OLPB and TLPB were calculated as 0.035 and 0.026 g of dry biomass/g of dry filter per day, respectively. The carbon balances were analyzed in the two biofilters. The yield coefficients (Y) were determined at 1.449 and 1.143 g of dry biomass/g of removed VOC for OLPB and TLPB, respectively. However, the corresponding CO₂ production fraction was 0.263 g and 0.316 g per 1 g of DCM for OLPB and TLPB, respectively. The variations in fraction of carbon in DCM transformation to biomass and to CO₂ suggested distinct microbial transformation pathways of utilizing DCM in the two biofilters, which were mainly caused by the different microbial communities and metabolic activities.