Reduction of indicator and pathogenic microorganisms by psychrophilic anaerobic digestion in swine slurries

The objective of this study was to evaluate the efficiency of a low temperature anaerobic treatment to reduce viable populations of indicator microorganisms (total coliforms, Escherichia coli) and the presence of selected pathogens (Salmonella, Yersinia enterocolitica, Cryptosporidium and Giardia) in swine slurries from different sources. Experiments were carried out in 40 l Sequencing Batch Reactors (SBRs). Experimental results indicated that anaerobic digestion of swine manure slurry at 20 degrees C for 20 days in an intermittently fed SBR: (1) reduced indigenous populations of total coliforms by 97.94-100%; (2) reduced indigenous populations of E. coli by 99.67-100%; (3) resulted in undetectable levels of indigenous strains of Salmonella, Cryptosporidium, and Giardia. It can be considered as a promising method for reducing indigenous indicator and pathogenic microorganisms populations in liquid swine manure slurries.     

Mixing in anaerobic digestion

The mixing of the anaerobic digester contents significantly influences the efficiency of this operation; in particular, hydraulic dead zones are extremely detrimental to the reaction kinetics involved in anaerobic digestion. An analysis of the relative importance of thermal fluid movement in the digester to those caused by fluid inflow and outflow is presented. As an example, these principles are applied to a digester at the South Bend Wastewater Treatment Plant. Experimental measurements, which have general applicability for the measurement of digester mixing volume, confirm the theoretical conjectures. Various types of optimizations can be attempted on this mixing operation. One such optimization applied to gas lift mixers, as employed in the South Bend Treatment Plant, is illustrated.     

d-Hydantoinase from anaerobic microorganisms

Summary Of 373 anaerobic microbial isolates screened for the enzymatic conversion of dihydrouracil to N-carbamyl--alanine, several strains of Clostridium spp., C. glycolicum, C. subterminale and Peptococcus anaerobius were positive. These Clostridium and Peptococcus strains produced also N-carbamyl-d-amino acids from the respective 5-monosubstituted hydantoins. The d-hydantoinase activity from whole cell suspensions of P. anaerobius strain CRDA 303 was characterized with regard to pH and temperature stability and activity by using dihydrouracil (DHU) and isopropylhydantoin (IPH) as substrates. The d-hydantoinase from P. anaerobius was optimal at 60°C and at pH 6.5–9.5 for the substrate DHU. It was stable up to 55°C and at pH 5.0–9.5 and could be stored at 4°C under an aerobic atmosphere for at least 14 days. Offprint requests to: A. Morin     

微生物电解池耦合厌氧消化过程中产甲烷代谢通量与微生物的关系北大核心CSCD

为探究微生物电解池耦合厌氧消化(MEC-AD)产甲烷代谢通量与微生物的关系。实验以电压为扰动因子,采用代谢通量分析(MFA)的方法,得到微生物群落与产甲烷通量的响应关系。结果表明:电压扰动后产甲烷通量和产氢通量均发生显著变化,而电压扰动对产乙酸通量的影响较小,其中0.6 V扰动时产甲烷通量最大为0.522±0.051,较对照组1.0 V的0.295±0.013和1.4 V的0.395±0.029分别提高了77%和32%。另外,平均有15.7%±2.9%的H_(2)(通量)用于还原CO_(2)产甲烷和乙酸,平均有27.7%±6.9%的乙酸(通量)转化为CH_(4)。毛螺旋菌(Lachnospiraceae)的丰度对乙酸通量有显著影响,产CH_(4)通量与理研菌属(Petrimonas)、互营单胞菌属(Syntrophomonas)、拟杆菌属(Blvii28)、假单胞菌属(Acinetobacter)的丰度呈正相关,与梭菌属(Tuzzerella)、球形螺旋菌属(Sphaerochaeta)的丰度呈负相关。而影响产H2通量和产CH_(4)通量的物种具有相似性,多为拟杆菌、梭菌、假单胞菌和厚壁菌。此外,物种种间互作关系也是影响MEC-AD产甲烷通量的重要因素。     

Electrolysis-enhanced anaerobic digestion of wastewater

This study demonstrates enhanced methane production from wastewater in laboratory-scale anaerobic reactors equipped with electrodes for water electrolysis. The electrodes were installed in the reactor sludge bed and a voltage of 2.8-3.5 V was applied resulting in a continuous supply of oxygen and hydrogen. The oxygen created micro-aerobic conditions, which facilitated hydrolysis of synthetic wastewater and reduced the release of hydrogen sulfide to the biogas. A portion of the hydrogen produced electrolytically escaped to the biogas improving its combustion properties, while another part was converted to methane by hydrogenotrophic methanogens, increasing the net methane production. The presence of oxygen in the biogas was minimized by limiting the applied voltage. At a volumetric energy consumption of 0.2-0.3 Wh/L_R, successful treatment of both low and high strength synthetic wastewaters was demonstrated. Methane production was increased by 10-25% and reactor stability was improved in comparison to a conventional anaerobic reactor.     

Parametric sensitivity in modeling of anaerobic digestion

Summary A mathematical model for the anaerobic digestion process was analyzed by the parametric sensitivity method to determine the influence of individual model parameters on the selected output variables. The relative parametric sensitivity value indicated the most influential parameters in the process being yield coefficients and rate constants.     

Simulation study of anaerobic digestion control

A mixed culture anaerobic digestion model developed previously was applied to the evaluation of several digester control strategies. It was found that pH control by base addition or flow rate manipulation is inadequate. Based on an analysis of digester dynamics, a new control of the total suspended solids concentration at the feed was proposed through the manipulation of the underflow flow rate of the preceeding sedimentation unit. This control was tested in a variety of simulated runs and proved very effective in eliminating most of the usual causes of digester failure.     

A review of anaerobic digestion bio-kinetics

Anaerobic digestion is the key to sustainable wastewater management and bioenergy production. Kinetics plays an important role in the design of bioreactors, processes, and process scale-up in anaerobic digestion. This article focuses on a state-of-the-art literature review on the experimental kinetic studies of conventional anaerobic bioreactors and anaerobic membrane bioreactors. Various kinetic models that were used to fit the experimental data and derive the kinetic parameters are summarized and discussed in the literature. The values of the maximum specific growth rate µ_max, half saturation constant K_s, decay co-efficient k_d, sludge yield Y, and methane yield Y_CH4 from experimental studies are summarized for each model. This paper can serve as an updated comprehensive source of anaerobic bio-kinetic studies and digester design.     

Thermodynamic equilibrium model in anaerobic digestion process

Catabolic reactions provide the chemical energy necessary for the maintenance of living microorganisms. The catabolic reactions in anaerobic digestion process may progress close to the equilibrium state (ΔG = 0) depending strongly on the microorganisms in the digester. The thermodynamic equilibrium of catabolic reactions in the anaerobic digestion process was modelled under isothermal and isobaric conditions. Three thermodynamic models were considered; the ideal, the Debye-Hückel–Praunitz, and the Pitzer–Praunitz. The models in this paper concentrate on the methanogenic equilibrium of the anaerobic digestion process. The thermodynamic equilibrium model shows that the methanogenesis step requires thermal energy and electrons, so that anaerobic digestion may achieve high substrate degradation and high conversion to methane. Some thermodynamic recommendations are suggested for the future development of the methanogenic phase of anaerobic digestion.     

Origin of spores of anaerobic microorganisms in milk

Summary Samples from silage, hay, milk, air, and faeces were taken at 25 farms in mid-Sweden, farms with different hygienic standards of milk-production being chosen.The correlation between fodder and milk-quality was investigated. The investigation was limited to the transfer of spores of anaerobes to the milk during feeding with silage of various qualities.The role of grassland fodders other than silage in spore-infection of milk is discussed.These studies are still in progress. We are indebted to the Swedish Foundation: Fonden för främjande av forsknings- och försöksverksamheten på jordbrukets område for generous financial support. We also gratefully acknowledge the encouraging interest and support of Professor R. Nilsson.     

In situ methane enrichment in anaerobic digestion

A major cost consideration in the use of anaerobic digestion to convert biomass and waste to utility-grade gas is the expense of separating CO(2) from the product gas. Anaerobic digestion has a number of inherent properties that can be exploited to increase the methane content of the gas directly produced by the digester, the most important of which is the high solubility of CO(2)(40-60 times that of methane) in water under digestion conditions. The methane enrichment concept examined in this study involved the recirculation of a liquid stream from the digester through a CO(2) desorption process and the return of the liquid stream back to the digester for absorption of additional CO(2) produced by the conversion of organic materials. A steady-state equilibrium model predicted that a digester gas methane content exceeding 94% could be achieved with this scheme using modest recirculation rates provided a desorption process could be designed to achieve a 60+% CO(2) removal efficiency in the degassing of the liquid recycle stream. Using fixed-film laboratory digesters operated on synthetic feedstocks, the technique of methane enrichment was tested under pressurized and unpressurized conditions. A 93 + 2% methane gas stream was produced from a volatile-acid-fed bench-scale digester simulating the methanogenic stage of two-phase digestion under conditions of (1) a pH swing achieved without caustic addition that allowed digestion at pH 7. 5 and air stripping at pH 6. 5-7. 0, (2) digester pressurization to 30 psig, and (3) a recycle rate of 0. 33 L/L reactor/day. Significant but lower levels of methane enrichment were achieved with the single-stage digester at the low experimental recycle rate. However, the narrow range among all experiments of CO(2) desorption efficiencies achieved in air stripping the recycle stream (35-60% CO(2) removal) suggests that comparable methane enrichment-may be achieved with unpressurized single-stage digestion using greater recycle rates. A materials balance analysis of data from an unpressurized, single-stage digester employing no chemical addition and using laboratory degassing efficiencies indicated that 94% methane could be produced at recycle rates of less than 1. 4 L/L reactor/day with a methane loss of less than 2%.     

Semi-continuous anaerobic digestion of a food industry wastewater in an anaerobic filter

The experimental results of semi-continuous tests of anaerobic digestion of confectionery industry wastewater, carried out at different residence times and organic loads in an upflow anaerobic filter, are presented and discussed. Giving COD removals higher than 80% under the whole range of conditions tested, the anaerobic filter demonstrated not only a great ability of biomass to adapt itself to a new carbon source but also an excellent capability to deal with organic load fluctuations and to utilise dilute feeds. Sampling at different filter heights demonstrated that the biogas development ensured mixing within the filter and that most of the organic substances were utilised at the bottom of the reactor, especially when very dilute wastewater was fed. The results of this work could be taken as a starting basis for scaling-up the process to the industrial scale.     

Long-term storage of obligate anaerobic microorganisms in glycerol

We evaluated the possibility of storing the cultures of obligate anaerobic microorganisms (clostridia, acetogenic and sulfate-reducing bacteria, and methanogenic archaea) in 25% glycerol at ?70°C for a long time (up to 3 years). This method of storage is adequate for preserving cell viability in the majority of obligate anaerobes.     

Detection and quantification of microorganisms in anaerobic bioreactors

The presence of sulfate in anaerobic reactors can trigger competitive and syntrophic interactions between various groups of microorganisms, such as sulfate reducers, methanogens and acetogens. In order to steer the reactor process in the direction of sulfidogenesis or methanogenesis, it is essential to get insight into the population dynamics of these groups of microorganisms upon changes in the reactor operating conditions. Several methods exist to characterize and quantify the microbial sludge composition. Combining classical microbiological and modern molecular-based sludge characterization methods has proven to be a powerful approach to study the microbial composition of the anaerobic sludge.     

Long-term storage of obligate anaerobic microorganisms in glycerol

We evaluated the possibility of storing the cultures of obligate anaerobic microorganisms (clostridia. acetogenic and sulfate-reducing bacteria, and methanogenic archaea) in 25% glycerol at -70 degrees C for a long time (up to 3 years). This method of storage is adequate to preserve cell viability in most obligate anaerobes.