Effect of inoculation time on the bio-drying performance of combined hydrolytic-aerobic process

The study aimed at investigating the effects of inoculation time on the bio-drying performance of combined hydrolytic-aerobic process. Results showed that the addition of inoculating material at different time exhibited various effects not only on the degradation rate of total organics, but also on the performance of water removal and water content reduction. The beginning of aerobic stage (day 5) was suggested to be the optimal time for inoculation. Under this operational condition, 815 g/kg-W(0) (W(0)=initial water content) was removed and the water content reduced from the initial 72.0% to 48.5%. Adding inoculating material at the start of hydrolytic stage (day 0) reduced water removal and water content reduction rates. The addition of inoculating material at day 7 or 9 could not improve the bio-drying performance significantly. Additionally, the inoculation at days 0, 5, 7 and 9 enhanced lignocelluloses degradation rate by 3.8%, 11.6%, 7.9% and 7.7%, respectively.     

Effect of pH-neutralized leachate recirculation on a combined hydrolytic–aerobic biopretreatment for municipal solid waste

Four trials with different durations (1, 2, 3 and 4 days) of neutralized leachate recirculation and a control with distilled water recirculation for 4 days were set up to investigate the effect of recirculation duration on MSW biopretreatment by a combined hydrolytic–aerobic process. Results showed that recirculation could enhance water removal and organics degradation rates and thus lead to a lower water content of biopretreated materials, when compared with the control. Recirculation with duration of 4 days had the highest rates of water removal (83.7%) and organics degradation (62.1%) and lowest final water content (43.1%) due to the elimination of acid inhibition. As a result, recirculation with duration of 4 days had the highest sorting efficiency (75%) and heating value (10570 kJ/kg) and lowest respiration activity (98.6 mgO₂/g). Thereby, neutralized leachate recirculation with duration of 4 days was suggested to pretreat municipal solid waste with high water content.     

Modeling aerobic carbon source degradation processes using titrimetric data and combined respirometric-titrimetric data: experimental data and model structure

Experimental data are presented that resulted from aerobic batch degradation experiments in activated sludge with simple carbon sources (acetate and dextrose) as substrates. Data collection was done using combined respirometric-titrimetric measurements. The respirometer consists of an open aerated vessel and a closed non-aerated respiration chamber for monitoring the oxygen uptake rate related to substrate degradation. The respirometer is combined with a titrimetric unit that keeps the pH of the activated sludge sample at a constant value by addition of acid and/or base. The experimental data clearly showed that the activated sludge bacteria react with consumption or production of protons during aerobic degradation of the two carbon sources under study. Thus, the cumulative amount of added acid and/or base could serve as a complementary information source on the degradation processes. For acetate, protons were consumed during aerobic degradation, whereas for dextrose protons were produced. For both carbon sources, a linear relationship was found between the amount of carbon source added and the amount of protons consumed (in case of acetate: 0.38 meq/mmol) or produced (in case of dextrose: 1.33 meq/mmol) during substrate degradation. A model taking into account substrate uptake, CO(2) production, and NH(3) uptake for biomass growth is proposed to describe the aerobic degradation of a C(x)H(y)O(z)-type carbon source. Theoretical evaluation of this model for reference parameters showed that the proton effect due to aerobic substrate degradation is a function of the pH of the liquid phase. The proposed model could describe the experimental observations with both carbon sources.     

Aerobic treatment of black olive wastewater and the effect of an ozonation stage

The reduction of the pollutant organic matter present in wastewaters generated in the black olive production process is studied by an aerobic degradation, and by the combination of two successive steps: an ozonation pretreatment followed by an aerobic degradation. In the single aerobic process, in addition to the biomass evolution which is followed during each experiment, the removal of the pollutant load is evaluated by means of global parameters which are directly related with the organic matter, as the chemical oxygen demand and the total phenolic compounds content. A kinetic study is performed by using the Monod model, which applied to the experimental data, provides the specific kinetic parameters of this model: the kinetic constant for the substrate decomposition rate, the cellular yield coefficient and the kinetic constant for the biomass decrease during the death phase of microorganisms. In the combined process, an ozonation pretreatment is conducted with experiments where the ozone partial pressure is varied, and an important reduction in the phenolic compounds is achieved. The kinetic parameters of the following aerobic degradation stage are also evaluated, and the effect of the chemical oxidation pretreatment on this biological stage is discussed.     

Photocurable liquid biodegradable copolymers: in vitro hydrolytic degradation behaviors of photocured films of coumarin-endcapped poly(epsilon-caprolactone-co-trimethylene carbonate)

Coumarin-endcapped tetrabranched liquid copolymers composed of epsilon-caprolactone and trimethylene carbonate (TMC), prepared using pentaerythritol or four-branched poly(ethylene glycol) (PEG) as an initiator, were ultraviolet irradiated to produce photocured solid biodegradable copolymers. The hydrolytic degradation behaviors of photocured films were determined from the weight loss of the films. The initial hydrolysis rate (determined for up to 24 h using a quartz crystal microbalance) was enhanced with aqueous solutions of higher pH. The hydrolysis rate in the early period of immersion was increased with an increase in TMC content, whereas that in the later period (week order) decreased with a increase in TMC content. This inverse relation of composition dependence on the hydrolysis rate between the early and late periods was discussed. Topological measurements using scanning electron microscopy and atomic force microscopy as well as depth profiles of the fluorescein-stained hydrolyzed layer showed that for the pentaerythritol-initiated copolymer, irrespective of copolymer composition, hydrolysis occurred at surface regions and surface erosion proceeded with immersion time. For PEG-based copolymers, both surface erosion and bulk degradation occurred simultaneously. The hydrolyzed surfaces became highly wettable with water and exhibited noncell adhesivity.     

水分胁迫下丛枝菌根真菌对枳实生苗生长和渗透调节物质含量的影响

采用盆栽试验研究了水分胁迫下接种丛枝菌根真菌摩西球囊霉(Glomaus mosseae)对枳[Poncirustrifoliat(L.)Raf.]实生苗的生长和渗透调节物质含量的影响.结果表明,在土壤含水量为20%、16%和12%条件下,接种G.mosseae能够增加植株的生长(株高、茎粗、叶面积、地上部干重、地下部干重和植株干重),促进植株根系活跃吸收面积和根际土壤有效磷的吸收,提高叶片和根系可溶性糖含量的积累,降低叶片脯氨酸含量,增强植株的水分利用效率(达20%～40%),使枳实生苗的抗旱能力得到增强.土壤含水量为20%和16%条件下接种G.mosseae对植株的效果较土壤含水量为12%条件下更显著.12%的土壤含水量严重抑制Gmosseae的侵染,说明丛枝菌根侵染程度轻,其对植物的效果也差.     

Preparation, characterization, and microbial degradation of specifically radiolabeled [C]lignocelluloses from marine and freshwater macrophytes

Specifically radiolabeled [C-lignin]lignocelluloses were prepared from the aquatic macrophytes Spartina alterniflora, Juncus roemerianus, Rhizophora mangle, and Carex walteriana by using [C]phenylalanine, [C]tyrosine, and [C]cinnamic acid as precursors. Specifically radiolabeled [C-polysaccharide]lignocelluloses were prepared by using [C]glucose as precursor. The rates of microbial degradation varied among [C-lignin]lignocelluloses labeled with different lignin precursors within the same plant species. To determine the causes of these differential rates, [C-lignin]lignocelluloses were thoroughly characterized for the distribution of radioactivity in nonlignin contaminants and within the lignin macromolecule. In herbaceous plants, significant amounts (8 to 24%) of radioactivity from [C]phenylalanine and [C]tyrosine were found associated with protein, although very little (3%) radioactivity from [C]cinnamic acid was associated with protein. Microbial degradation of radiolabeled protein resulted in overestimation of lignin degradation rates in lignocelluloses derived from herbaceous aquatic plants. Other differences in degradation rates among [C-lignin]lignocelluloses from the same plant species were attributable to differences in the amount of label being associated with ester-linked subunits of peripheral lignin. After acid hydrolysis of [C-polysaccharide]lignocelluloses, radioactivity was detected in several sugars, although most of the radioactivity was distributed between glucose and xylose. After 576 h of incubation with salt marsh sediments, 38% of the polysaccharide component and between 6 and 16% of the lignin component (depending on the precursor) of J. roemerianus lignocellulose was mineralized to CO(2); during the same incubation period, 30% of the polysaccharide component and between 12 and 18% of the lignin component of S. alterniflora lignocellulose was mineralized.     

油菜秸秆混合发酵降解菌的筛选

油菜秸秆含有大量木质纤维素,该类物质结构稳定,不易降解,限制了其工业化应用.通过对10株包括细菌、酵母菌和白腐真菌的菌株产酶能力和特性进行比较,并进行共同培养试验,筛选出5株可共同生长的木质纤维素降解菌BS09、BL、PC、TS和KS.通过对这5个菌株单独发酵降解油菜秸秆的能力考察,结果表明:PC对木质纤维素的降解能力...     

Modeling aerobic carbon oxidation and storage by integrating respirometric, titrimetric, and off-gas CO2 measurements

A method for detailed investigation of aerobic carbon degradation processes by microorganisms is presented. The method relies on an integrated use of the respirometric, titrimetric, and off-gas CO(2) measurements. The oxygen uptake rate (OUR), hydrogen ion production rate (HPR), and the carbon dioxide transfer rate (CTR) resulting from the biological as well as physicochemical processes, coupled with a metabolic model characterizing both the growth and carbon storage processes, enables the comprehensive study of the carbon degradation processes. The method allows the formation of carbon storage products and the biomass growth rates to be estimated without requiring any off-line biomass or liquid-phase measurements, although the practical identifiability of the system could be improved with additional measurements. Furthermore, the combined yield for biomass growth and carbon storage is identifiable, along with the affinity constant with respect to the carbon substrate. However, the individual yields for growth and carbon storage are not identifiable without further knowledge about the metabolic pathways employed by the microorganisms in the carbon conversion. This is true even when more process variables are measured. The method is applied to the aerobic carbon substrate degradation by a full-scale sludge using acetate as an example carbon source. The sludge was able to quickly take up the substrate and store it as poly-beta-hydroxybutyrate (PHB). The PHB formation rate was a few times faster than the biomass growth rate, which was confirmed by off-line liquid- and solid-phase analysis. The estimated combined yield for biomass growth and carbon storage compared closely to that determined from the theoretical yields reported in literature based on thermodynamics. This suggests that the theoretical yields may be used as default parameters for modeling purposes.     

降解纤维素的“超分子机器”研究进展

综述了目前关于纤维小体组装模式、纤维小体结构多样性及人工设计纤维小体等方面的研究进展.纤维小体是某些厌氧菌产生的由多个亚基共同组装而成的大分子机器,是致力于组织、协调多种酶组分协同高效催化降解木质纤维素的胞外蛋白质复合体.纤维小体是厌氧微生物水解纤维素的主体,具有非常高效的打破结晶纤维素的结晶结构和降解纤维素链的作用.纤维小体对木质纤维素降解的高效性来自于其自发组装而成的复杂的高级结构,其结构的复杂性因不同的厌氧微生物而有所不同.     

Sequential anaerobic/aerobic digestion of waste activated sludge: analysis of the process performance and kinetic study

Sequential anaerobic-aerobic digestion was applied to waste activated sludge (WAS) of a full scale wastewater treatment plant. The study was performed with the objective of testing the sequential digestion process on WAS, which is characterized by worse digestibility in comparison with the mixed sludge. Process performance was evaluated in terms of biogas production, volatile solids (VS) and COD reduction, and patterns of biopolymers (proteins and polysaccharides) in the subsequent digestion stages. VS removal efficiency of 40%, in the anaerobic phase, and an additional removal of 26%, in the aerobic one, were observed. For total COD removal efficiencies of 35% and 25% for anaerobic and aerobic stage respectively, were obtained. Kinetics of VS degradation process was analyzed by assuming a first order equation with respect to VS concentration. Evaluated kinetic parameters were 0.44 ± 0.20 d(-1) and 0.25 ± 0.15 d(-1) for the anaerobic stage and aerobic stage, respectively. With regard to biopolymers, in the anaerobic phase the content of proteins and polysaccharides increased to 50% and 69%, respectively, whereas in the subsequent aerobic phase, a decrease of 71% for proteins and 67% for polysaccharides was observed. The average specific biogas production 0.74 m(3)/(kg VS destroyed), was in the range of values reported in the specialized literature for conventional anaerobic mesophilic WAS digestion.     

Degradation of household biowaste in reactors.

Household derived biowaste was degraded by biological methods. The system involves the combined method of low-solids (up to 10% w/v of total solids (TS)) anaerobic digestion and aerobic degradation for the recovery of energy (biogas) and the production of fine humus-like material which can be used as a soil amender or a substrate for further thermal treatment (pyrolysis, gasification). The performance of batch and continuous processes carried out in bioreactors (stirred tank reactor, air-lift) of working volume 6 and 18 dm(3), at different temperatures (25-42 degrees C) was monitored by reduction of TS, volatile solids, chemical oxygen demand, total organic carbon, C/N in time. The application of continuous process with recirculation (33%) caused that for residence time of 8-16 h the obtained degree of organic load reduction was similar to that obtained after 72-96 h of the batch process. The experimental data of batch aerobic degradation was also subjected to kinetic analysis. The sequence of the two processes: aerobic and anaerobic or anaerobic and aerobic showed that the degree of organic load reduction was similar in both cases, while the amount of produced biogas was four times higher when the first stage was anaerobic. The final product after dewatering was subjected to pyrolysis and gasification. The gases obtained were characterised by a high heat of combustion of about 11-15 MJ Nm(-3).     

Degradation efficiency and molecular size alteration during the aerobic microbial treatment of lignite pyrolysis deposit water

 Investigations into aerobic biological degrada-tion were carried out as part of an extensive programme designed to facilitate the cheap remediation of a pyrolysis waste-water deposit. Attention was focused on the processes of carbon conversion by different populations. The susceptibility of a body of lignite-processing deposit water to microbiological degradation was examined in batch investigations in a Sapromat system and in continuous bench-scale fermenter cultivations, with respect to nutrient supply, inoculation culture and molecular size distribution. It was found that degradation best occurs with an adapted mixed culture. The autochthonous culture removes 30% less dissolved organic carbon (DOC) and has a 40% higher specific oxygen demand. A shortage of phosphorus, investigated with a view to avoiding additional eutrophication problems in the open water in the case of in situ remediation, causes reduced DOC degrada-tion and significantly higher specific oxygen demand. The biological process is overlapped by abiotic oxidation. During aerobic treatment, a concentration of colour-giving aromatic substances of between 0.5 kDa and 5 kDa was observed. This phenomenon is caused by the oxidation of low- and high-molecular-mass compounds. The removal of DOC is limited to 65% and mainly occurs in the range below 0.5 kDa (30%) and in the 0.5–1 kDa range (12%); the removal is negligible in the ranges 1–3 kDa (0.8%) and 3–5 kDa (2%) and a little higher in the ranges 5 kDa–0.3 μm (5%) and above 0.3 μm (6%). In the investigations it was discovered that DOC removal causes in the ranges below 0.5 kDa, 0.5–1 kDa and 5 kDa–0.3 μm mainly as a result of degradation, but the range above 0.3 μm is chiefly caused by bioadsorption. Aerobic microbiological treatment is able to remove most low-molecular-mass substances. In order to remove the macromolecular and colour-giving part of the deposit water, an additional treatment stage, e.g. flocculation, is required. Received: 10 October 1995/Received revision: 9 January 1996/Accepted: 15 January 1996     

Influence of Aloe vera on water absorption and enzymatic in vitro degradation of alginate hydrogel films

This study investigates the influence of Aloe vera on water absorption and the in vitro degradation rate of Aloe vera-Ca-alginate hydrogel films, for wound healing and drug delivery applications. The influence of A. vera content (5%, 15% and 25%, v/v) on water absorption was evaluated by the incubation of the films into a 0.1 M HCl solution (pH 1.0), acetate buffer (pH 5.5) and simulated body fluid solution (pH 7.4) during 24 h. Results show that the water absorption is significantly higher for films containing high A. vera contents (15% and 25%), while no significant differences are observed between the alginate neat film and the film with 5% of A. vera. The in vitro enzymatic degradation tests indicate that an increase in the A. vera content significantly enhances the degradation rate of the films. Control films, incubated in a simulated body fluid solution without enzymes, are resistant to the hydrolytic degradation, exhibiting reduced weight loss and maintaining its structural integrity. Results also show that the water absorption and the in vitro degradation rate of the films can be tailored by changing the A. vera content.     

Kinetics of Oxygen Release from ORC

Oxygen release compounds (ORC) are one possibility to enhance aerobic degradation in contaminated aquifers. However, some applications have been reported where oxygen concentrations did not meet expectations, this was attributed to ground water composition, e.g., high pH. Column experiments have been performed and the measurements were interpreted using a numerical model to investigate oxygen release kinetics from ORC in more detail. Because the zero-order rate law recommended by the manufacturer did not reflect the measurements, a more complex kinetic scheme was developed. The simulations show a minor influence of inorganic ground water constituents on oxygen release from ORC in the columns due to buffering by mineral precipitation, but an enhanced oxygen release if aerobic degradation takes place. If ORC is applied as socks, the impact of inorganic ground water composition increases compared to the application in column experiments. A simple quadratic equation is provided to estimate oxygen release rate from the buffer capacity of the ground water versus increasing pH—a parameter easily determinable in the laboratory. For slightly mineralized waters with high pH, this equation forecasts decreased oxygen release, but no total inhibition of oxygen release.     

Kinetics of Oxygen Release from ORC

Oxygen release compounds (ORC) are one possibility to enhance aerobic degradation in contaminated aquifers. However, some applications have been reported where oxygen concentrations did not meet expectations, this was attributed to ground water composition, e.g., high pH. Column experiments have been performed and the measurements were interpreted using a numerical model to investigate oxygen release kinetics from ORC in more detail. Because the zero-order rate law recommended by the manufacturer did not reflect the measurements, a more complex kinetic scheme was developed. The simulations show a minor influence of inorganic ground water constituents on oxygen release from ORC in the columns due to buffering by mineral precipitation, but an enhanced oxygen release if aerobic degradation takes place. If ORC is applied as socks, the impact of inorganic ground water composition increases compared to the application in column experiments. A simple quadratic equation is provided to estimate oxygen release rate from the buffer capacity of the ground water versus increasing pH—a parameter easily determinable in the laboratory. For slightly mineralized waters with high pH, this equation forecasts decreased oxygen release, but no total inhibition of oxygen release.     

Biological degradation of Ascophyllum nodosum

The alginate forms the major structural component of the cell wall and the intercellular matrix of the brown alga Ascophyllum nodosum. Successful biological degradation of A. nodosum would largely depend on the dissolution of the alginate, but reactive compounds in the alga such as polyphenols may also have toxic effects on the microbial population involved. Aerobic and anaerobic batch reactors, operated at 35°C and pH 7, were fed milled A. nodosum, nutrients and inocula adapted to seaweed degradation. The dominant factor for conversion of organic matter during anaerobic digestion was the inhibitory effect of the polyphenols on alginate lyases and methane production. Probably, the relative large fraction of high molecular weight polyphenols (>10 kDa) in this alga gave efficient binding of proteins during digestion. The anaerobic degradation was greatly stimulated when the polyphenols were fixed with low amounts of formaldehyde. An accumulated content of guluronate in the remaining alginate indicated that Ca-crosslinking also limited the guluronate lyase access to the polymer. In contrast, the aerobic digestion of alga gave no increase in the guluronate content of the residual alginate. Compared to anaerobic conditions, the phenols had a much lower influence on the hydrolytic rate of organic matter during aerobic conditions. This revised version was published online in August 2006 with corrections to the Cover Date.     

Tuning the polylactide hydrolysis rate by plasticizer architecture and hydrophilicity without introducing new migrants

The possibility to tune the hydrolytic degradation rate of polylactide by plasticizer architecture and hydrophilicity without introduction of new degradation products was investigated by subjecting polylactide with cyclic oligolactide and linear oligolactic acid additives to hydrolytic degradation at 37 and 60 °C for up to 39 weeks. The more hydrophilic oligolactic acid plasticizer led to larger water uptake and rapid migration of plasticizer from the films into the aging water. This resulted in a porous material more susceptible to further hydrolysis. During hydrolysis at 37 °C the mass loss was generally 10-20% higher for the material containing linear oligolactic acid plasticizers. The hydrolysis accelerating effect of the linear oligolactic acid is probably counteracted by the higher degree of crystallinity in the films containing oligolactic acid additives. The degradation process was monitored by measurements of mass loss, water uptake, molar mass changes, material composition changes, surface changes, and thermal properties. The water-soluble degradation products were analyzed by following pH changes and identified by electrospray ionization-mass spectrometry (ESI-MS). The time frame for formation of water-soluble products was influenced by the architecture and hydrophilicity of the plasticizer. Furthermore, the advantage with oligolactide and oligolactic acid plasticizers was clearly demonstrated as they do not introduce any new migrants into the degradation product patterns.     

Treatment of high strength distillery wastewater (cherry stillage) by integrated aerobic biological oxidation and ozonation

The performance of integrated aerobic digestion and ozonation for the treatment of high strength distillery wastewater (i.e., cherry stillage) is reported. Experiments were conducted in laboratory batch systems operating in draw and fill mode. For the biological step, activated sludge from a municipal wastewater treatment facility was used as inoculum, showing a high degree of activity to distillery wastewater. Thus, BOD and COD overall conversions of 95% and 82% were achieved, respectively. However, polyphenol content and absorbance at 254 nm (A(254)) could not be reduced more than 35% and 15%, respectively, by means of single biological oxidation. By considering COD as substrate, the aerobic digestion process followed a Contois' model kinetics, from which the maximum specific growth rate of microorganisms (mu(max)) and the inhibition factor, beta, were then evaluated at different conditions of temperature and pH. In the combined process, the effect of a post-ozonation stage was studied. The main goals achieved by the ozonation step were the removal of polyphenols and A(254). Therefore, ozonation was shown to be an appropriate technology to aid aerobic biological oxidation in the treatment of cherry stillage.     

Microbial degradation of hydrocarbons in soil during aerobic/anaerobic changes and under purely aerobic conditions

Microbial hydrocarbon degradation in soil was studied during periodical aerobic/anaerobic switching and under purely aerobic conditions by using a pilot-scale plant with diesel-fuel-contaminated sand. The system worked according to the percolation principle with controlled circulation of process water and aeration. Periodical switching between 4 h of aerobic and 2 h of anaerobic conditions was achieved by repeated saturation of the soil with water. Whatever the cultivation mode, less than 50% of the diesel was degraded after 650 h because the hydrocarbons were adsorbed. Contrary to expectations, aerobic/anaerobic changes neither accelerated the rate of degradation nor reduced the residual hydrocarbon content of the soil. Obviously the pollutant degradation rate was determined mainly by transport phenomena and less by the efficiency of microbial metabolism. The total mass of oxygen consumed and carbon dioxide produced was greater under aerobic/anaerobic changing than under aerobic conditions, although the mass of hydrocarbons degraded was nearly the same. As shown by an overall balance of microbial growth and by a carbon balance, the growth yield coefficient was smaller during aerobic/anaerobic changes than under aerobic conditions. Received: 25 November 1997 /  Received revision: 15 January 1998 / Accepted: 18 January 1998