Bioreduction of trichloroethene using a hydrogen-based membrane biofilm reactor

A H2-based, denitrifying membrane-biofilm reactor (MBfR) was effective for removing trichloroethene (TCE) by reductive dechlorination. When TCE was first added to the MBfR, reductive dechlorination took place immediately and then increased over 18 weeks, and TCE was completely dechlorinated to ethene by about 120 days. These results indicate that TCE-dechlorinating bacteria were present naturally in the H2-based biofilm, and that enrichment for TCE-dechlorinating bacteria occurred. Dehalococcoides were documented in the MBfR biofilm before and after TCE feeding. Their proportion, quantified using the 16S rRNA gene, increased from 2.9 to 12% after TCE addition. This is the first report in which Dehalococcoides are proven to be present as part of an autotrophic biofilm community active in reductive dechlorination of TCE to ethene in a laboratory controlled experiment. Based on the complete reduction of TCE to ethene, the 16S rRNA clone libraries results, and the amount of tceA and bvcA, it appears that at least two Dehalococcoides strains were present in the enriched biofilm. One of them seems to be a new strain that is unique for having tceA and bvcA reductive dehalogenases.     

Constitutive trichloroethylene degradation led by tac promoter chromosomally integrated upstream of phenol hydroxylase genes of Ralstonia sp. KN1 and its nucleotide sequence analysis

Ralstonia sp. KN1-10A is a strain capable of degrading trichloroethylene (TCE) constitutively due to the tac promoter (Ptac) integrated upstream of the phenol hydroxylase genes (phy) in its chromosome. The expression of Ptac was analyzed using luxAB of Vibrio harveyi as a reporter. After determining the nucleotide sequence of phyABCDE required for TCE degradation, a luxAB-encoding fragment was integrated downstream of phyE by homologous recombination in strain KN1-10A, obtaining strain KN1-10A-LX. In the same manner, the luxAB-encoding fragment was integrated into the chromosome of the wild-type strain, KN1. The resultant strain KN1-LX was used to analyze the gene expression caused by phenol induction. The expression induced by Ptac was compared to that by phenol induction. Although the level of luxAB expression led by Ptac was almost equal to that induced by phenol, the TCE degradation rate by the Ptac-carrying KN1-10A-LX was markedly slower than that by the phenol-induced KN1-LX. These results suggest that an important gene for TCE degradation was not transcribed by Ptac in KN1-10A-LX. The nucleotide sequence analysis showed the existence of a small gene, phyZ, upstream of phyA, and Ptac was found to be integrated into the middle of phyZ in KN1-10A-LX. The effect of phyZ on TCE degradation was examined by using recombinant strains expressing phyABCDE with or without phyZ in a plasmid. The coexistence of phyZ markedly accelerated TCE degradation. Through an exhaustive expression analysis, it was demonstrated that the chromosomal integration of Ptac was a very attractive method for high and stable production of phenol hydroxylase for TCE degradation.     

Trichloroethylene degradation by Ralstonia sp. KN1-10A constitutively expressing phenol hydroxylase: transformation products, NADH limitation, and product toxicity

Ralstonia sp. KN1-10A, which was constructed by inserting the tac promoter upstream of the phenol hydroxylase (PH) gene in the chromosomal DNA of the wild-type strain, Ralstonia sp. KN1, is a useful recombinant strain for eliminating trichloroethylene (TCE) from contaminated sites because it exhibits constitutive TCE oxidation activity. During TCE degradation by Ralstonia sp. KN1-10A, noxious chlorinated compounds, such as dichloroacetic acid, trichloroacetic acid, 2,2,2-trichloroethanol, and chloral, were not detected, and more than 95% of chlorine in TCE was released as chloride ions. Among the possible TCE transformation products, only carbon monoxide was detected, and its conversion percentage was 7 mol%. The addition of formate, which Ralstonia sp. KN1-10A could use as an exogenous electron donor, did not enhance the TCE degradation performance, suggesting that NADH depletion did not limit the degradation. The phenol degradation activity of Ralstonia sp. KN1-10A that previously degraded TCE was not markedly lower than that of cells not exposed to TCE, suggesting that Ralstonia sp. KN1-10A was not susceptible to product toxicity associated with TCE degradation. Furthermore, to clarify the mechanisms underlying TCE degradation by PH from Ralstonia sp. KN1, this enzyme was compared with another enzyme, a hybrid aromatic ring dioxygenase exhibiting a high TCE degradation activity in Escherichia coli and Pseudomonas sp. The initial TCE degradation rate of Ralstonia sp. KN1 (pKTP100), which produced PH, was 1 50 lower than that of Ralstonia sp. KN1 (pKTF200), which produced the hybrid aromatic ring dioxygenase. However, because of its lower product toxicity, the strain producing PH could degrade 2.3 times more TCE than that generated by the strain producing the hybrid aromatic ring dioxygenase.     

Competition for sorption and degradation of chlorinated ethenes in batch zero-valent iron systems

The sorption and degradation of the chlorinated ethenes tetrachloroethene (PCE, 5 mg L(-1)) and trichloroethene (TCE, 10 mg L(-1)) were investigated in zero-valent iron systems (ZVI, 100 g L(-1)) in the presence of compounds common to contaminated groundwater with varying physicochemical properties. The potential competitors were chlorinated ethenes, monocyclic aromatic hydrocarbons, and humic acids. The effect of a complex matrix was tested with landfill contaminated groundwater. Nonlinear Freundlich isotherms adequately described chloroethene sorption to ZVI. In the presence of the more hydrophobic PCE (5 mg L(-1)), TCE sorption and degradation decreased by 33% and 30%, respectively, while TCE (10 mg L(-1)) decreased PCE degradation by 30%. In the presence of nonreactive hydrophobic hydrocarbons (i.e., benzene, toluene, and m-xylene at 100 mg L(-1)), TCE and PCE sorption decreased by 73% and 55%, respectively. The presence of the hydrocarbons had no effect on TCE degradation and increased PCE reduction rates by 50%, suggesting that the displacement of the chloroethenes from the sorption sites by the aromatic hydrocarbons enhanced the degradation rates. Humic acids did not interfere significantly with chloroethene sorption or with TCE degradation but lowered PCE degradation kinetics by 36% when present at high concentrations (100 mg L(-1)). The landfill groundwater with an organic carbon content of 109 mg L(-1) C had no effect on chloroethene sorption but inhibited TCE and PCE degradation by 60% and 70%, respectively.     

Variability in carbon isotopic fractionation during biodegradation of chlorinated ethenes: implications for field applications

Stable carbon isotopic analysis has the potential to assess biodegradation of chlorinated ethenes. Significant isotopic shifts, which can be described by Rayleigh enrichment factors, have been observed for the biodegradation of trichloroethlyene (TCE), cis-dichloroethylene (cDCE), and vinyl chloride (VC). However, until this time, no systematic investigation of isotopic fractionation during perchloroethylene (PCE) degradation has been undertaken. In addition, there has been no comparison of isotopic fractionation by different microbial consortia, nor has there been a comparison of isotopic fractionation by consortia generated from the same source, but growing under different conditions. This study characterized carbon isotopic fractionation during reductive dechlorination of the chlorinated ethenes, PCE in particular, for microbial consortia from two different sources growing under different environmental conditions in order to assess the extent to which different microbial consortia result in different fractionation factors. Rayleigh enrichment factors of -13.8@1000, -20.4@1000, and -22.4@1000 were observed for TCE, cDCE, and VC, respectively, for dechlorination by the KB-1 consortium. In contrast, isotopic fractionation during reductive dechlorination of perchloroethylene (PCE) could not always be approximated by a Rayleigh model. Dechlorination by one consortium followed Rayleigh behavior (epsilon = -5.2), while a systematic change in the enrichment factor was observed over the course of PCE degradation by two other consortia. Comparison of all reported enrichment factors for reductive dechlorination of the chlorinated ethenes shows significant variation between experiments. Despite this variability, these results demonstrate that carbon isotopic analysis can provide qualitative evidence of the occurrence and relative extent of microbial reductive dechlorination of the chlorinated ethenes.     

Stable isotope evidence for biodegradation of chlorinated ethenes at a fractured bedrock site

Stable carbon isotope analysis of chlorinated ethenes and ethene was performed at a site contaminated with trichloroethene (TCE), a dense non-aqueous phase liquid (DNAPL). The site is located in fractured bedrock and had variable groundwater hydraulic gradients during the study due to a local excavation project. Previous attempts to biostimulate a pilot treatment area at the site resulted in the production of cis-1,2-dichloroethene (cis-DCE), the first product of reductive dechlorination of TCE. Cis-DCE concentrations accumulated however, and there was no appreciable production of the breakdown products from further reductive dechlorination, vinyl chloride (VC) and ethene (ETH). Consequently, the pilot treatment area was bioaugmented with a culture of KB-1, a natural microbial consortium known to completely reduce TCE to nontoxic ETH. Due to ongoing dissolution of TCE from DNAPL in the fractured bedrock, and to variable hydraulic gradients, concentration profiles of dissolved TCE and its degradation products cis-DCE, VC, and ETH could not convincingly confirm biodegradation of the chlorinated ethenes. Isotopic analysis of cis-DCE and VC, however, demonstrated that biodegradation was occurring in the pilot treatment area. The isotope values of cis-DCE and VC became significantly more enriched in 13C over the last two sampling dates (in one well from -17.6%o to -12.8%o and from -22.5%o to -18.2%o for cis-DCE and VC, respectively). Quantification of the extent of biodegradation in the pilot treatment area using the Rayleigh model indicated that, depending on the well, between 21.3% and 40.7% of the decrease in cis-DCE and between 15.2% and 36.7% of the decrease in VC concentrations can be attributed to the effects of biodegradation during this time period. Within each well, the isotope profile of TCE remained relatively constant due to the continuous input of undegraded TCE due to DNAPL dissolution.     

Trichloroethylene and tetrachloroethylene elimination from the air by means of a hybrid bioreactor with immobilized biomass

Two-phase bioreactors consisting of bacterial consortium in suspension and sorbents with immobilized biomass were used to treat waste air containing chlorinated ethenes, trichloroethylene (TCE) and tetrachloroethylene (PCE). Synthetic municipal sewage was used as the medium for bacterial growth. The system was operated with loadings in the range 1.48-4.76 gm(-3)h(-1) for TCE and 1.49-5.96 gm(-3)h(-1) for PCE. The efficiency of contaminant elimination was 55-86% in the bioreactor with wood chips and 33-89% in the bioreactor filled with zeolite. The best results were observed 1 week after the pollutant loading was increased. However, in these conditions, the stability of the process was not achieved. In the next 7 days the effectiveness of the system decreased. Contaminant removal efficiency, enzymatic activity and the biomass content were all diminished. The system was working without being supplied with additional hydrocarbons as the growth-supporting substrates. It is assumed that ammonia produced during the transformation of wastewater components induced enzymes for the cometabolic degradation of TCE and PCE. However, the evaluation of nitrogen compound transformations in the system is difficult due to the sorption on carriers and the combined processes of nitrification and the aerobic denitrification. An applied method of air treatment is advantageous from both economic and environmental point of views.     

Cometabolic degradation of TCE vapors in a foamed emulsion bioreactor

Effective cometabolic biodegradation of trichloroethylene (TCE) vapors in a novel gas-phase bioreactor called the foamed emulsion bioreactor (FEBR) was demonstrated. Toluene vapors were used as the primary growth substrate for Burkholderia cepacia G4 which cometabolically biodegraded TCE. Batch operation of the reactor with respect to the liquid feed showed a drastic decrease of TCE and toluene removal over time, consistent with a loss of metabolic activity caused by the exposure to TCE metabolites. Sustained TCE removal could be achieved when continuous feeding of mineral medium was implemented, which supported cell growth and compensated for the deactivation of cells. The FEBR exhibited its highest TCE removal efficiencies (82-96%) and elimination capacities (up to 28 gTCE m(-3) h(-1)) when TCE and toluene vapors were fed sequentially to circumvent the competitive inhibition by toluene. The TCE elimination capacity was 2-1000 times higher than reported in other gas-phase biotreatment reports. During the experiments, 85-101% of the degraded TCE chlorine was recovered as chloride. Overall, the results suggestthatthe FEBR can be a very effective system to treat TCE vapors cometabolically.     

Combined removal of chlorinated ethenes and heavy metals by zerovalent iron in batch and continuous flow column systems

The combined removal of chlorinated ethenes and heavy metals from a simulated groundwater matrix by zerovalent iron (ZVI) was investigated. In batch, Ni (5-100 mg L(-1)) enhanced trichloroethene (TCE, 10 mg L(-1)) reduction by ZVI (100 g L(-1)) due to catalytic hydrodechlorination by bimetallic Fe0/Ni0. Cr(VI) or Zn (5-100 mg L(-1)) lowered TCE degradation rates by a factor of 2 to 13. Cr(VI) (100 mg L(-1)) in combination with Zn or Ni (50-100 mg L(-1)) inhibited TCE degradation. Addition of 20% H2(g) in the headspace, or of Zn (50-100 mg L(-1)), enhanced TCE removal in the presence of Ni and Cr(VI). Sorption of Zn to ZVI alleviated the Cr(VI) induced inhibition of bimetallic Fe0/Ni0 apparently due to release of protons necessary for TCE hydrodechlorination. In continuous ZVI columns treating tetrachloroethene (PCE, 1-2 mg L(-1)) and TCE (10 mg L(-1)), and a mixture of the metals Cr(VI), Zn(II), and Ni(II) (5 mg (L-1)), the PCE removal efficiency decreased from 100% to 90% in columns operated without heavy metals. The PCE degradation efficiency remained above 99% in columns receiving heavy metals as long as Ni was present. The findings of this study indicate the feasibility and limitations of the combined treatment of mixtures of organic and inorganic pollutants by ZVI.     

Dechlorination of trichloroethene in a continuous-flow bioelectrochemical reactor: effect of cathode potential on rate, selectivity, and electron transfer mechanisms

The exciting discovery that dechlorinating bacteria can use polarized graphite cathodes as direct electron donors in the reductive dechlorination has prompted investigations on the development of novel bioelectrochemical remediation approaches. In this work, we investigated the performance of a bioelectrochemical reactor for the treatment of trichloroethene (TCE). The reactor was continuously operated for about 570 days, at different potentiostatically controlled cathode potentials, ranging from -250 mV to -750 mV vs standard hydrogen electrode. The rate and extent of TCE dechlorination, as well as the competition for the available electrons, were highly dependent on the set cathode potential. When the cathode was controlled at -250 mV, no abiotic hydrogen production occurred and TCE dechlorination (predominantly to cis-DCE and VC), most probably sustained via direct extracellular electron transfer, proceeded at an average rate of 15.5 ± 1.2 μmol e(-)/L d. At this cathode, potential methanogenesis was almost completely suppressed and dechlorination accounted for 94.7 ± 0.1% of the electric current (15.0 ± 0.8 μA) flowing in the system. A higher rate of TCE dechlorination (up to 64 ± 2 μmol e(-)/L d) was achieved at cathode potentials lower than -450 mV, though in the presence of a very active methanogenesis which accounted for over 60% of the electric current. Remarkably, the bioelectrochemical reactor displayed a stable and reproducible performance even without the supply of organic carbon sources with the feed, confirming long-term viability.     

Reduction of nickel and uranium toxicity and enhanced trichloroethylene degradation to Burkholderia vietnamiensis PR1301 with hydroxyapatite amendment

The use of hydroxyapatite (HA) to sequester metals at mixed waste sites may reduce metal toxicity and facilitate microbial degradation of cocontaminant organics. The constitutive trichloroethylene (TCE) degrader, Burkholderia vietnamiensis PR1301, grew at 34.1 and 1.7 mM Ni at pH 5 and 7, respectively, with 0.01 g mL(-1) HA compared to 17 and 0.85 mM Ni without HA. PR1 grew at 4.2 mM U at pH 5 and 7 with 0.01 g mL(-1) HA compared to 1.1 mM U without HA. A similar decrease in the toxicity of Ni and U in combination was observed with HA. The ability of PR1 to degrade TCE at 0.85, 1.7, and 3.4 mM Ni and at 0.42 and 1.1 mM U was examined. The presence of TCE resulted in a decreased tolerance of PR1 to Ni and U; however, HA facilitated TCE degradation in the presence of Ni and U, effectively doubling the metal concentrations at which TCE degradation proceeded. These studies suggest that metal sequestration via HA amendments may offer a feasible approach to reducing metal toxicity to microorganisms at mixed waste sites, thereby enhancing the degradation of cocontaminant organics.     

Abiotic degradation of trichloroethylene under thermal remediation conditions

The degradation of trichloroethylene (TCE) to carbon dioxide (CO2) and chloride (Cl-) has been reported to occur during thermal remediation of subsurface environments. The effects of solid-phase composition and oxygen content on the chemical reactivity of TCE were evaluated in sealed ampules that were incubated at 22 and 120 degrees C for periods ranging from 4 to 40 days. For all treatments, no more than 15% of the initial amount of TCE was degraded, resulting in the formation of several non-chlorinated products including Cl-, CO2, carbon monoxide, glycolate, and formate. First-order rate coefficients for TCE disappearance ranged from 1.2 to 6.2 x 10(-3) day(-1) at 120 degrees C and were not dependent upon oxygen content orthe presence of Ottawa sand. However, the rate of TCE disappearance at 120 degrees C increased by more than 1 order-of-magnitude (1.6 to 5.3 x 10(-2) day(-1)), corresponding to a half-life of 13-44 days in ampules containing 1% (wt) goethite and Ottawa sand. These results indicate that the rate of TCE degradation in heated, three-phase systems is relatively insensitive to oxygen content, but may increase substantially in the presence of iron bearing minerals.     

Trichloroethylene transformation by natural mineral pyrite: the deciding role of oxygen

The transformation of trichloroethylene (TCE) in natural mineral iron disulfide (pyrite) aqueous suspension under different oxygen conditions was investigated in laboratory batch experiments. TCE transformation was pursued by monitoring its disappearance and products released with time. The effect of oxygen was studied by varying the initial dissolved oxygen concentration (DO(i)) inside each reactor. Transformation rates depended strongly on DO(i) in the system. In anaerobic pyrite suspension, TCE did not transform as it did under aerobic conditions. The transformation rate increased with an increase in DO(i). The TCE transformation kinetics was fitted to a pseudo-first-order reaction with a rate constant k (h(-1)) varying from 0.004 to 0.013 for closed systems with DO(i) varying from 0.017 to 0.268 mmol/L under the experimental conditions. In the aerobic systems, TCE transformed to several organic acids including dichloroacetic acid, glyoxylic acid, oxalic acid, formic acid, and finally to CO2 and chloride ion. Dichloroacetic acid was the only chlorinated intermediate found. Both TCE and the pyrite surface were oxidized in the presence of O2. Oxygen consumption profiles showed O2 was the common oxidant in both TCE and pyrite oxidation reactions. Ferric ion cannot be used as an alternative oxidant to oxygen for TCE transformation.     

Evaluation of the intrinsic photocatalytic oxidation kinetics of indoor air pollutants

This paper presents a methodology for the evaluation of the intrinsic photocatalytic oxidation (PCO) kinetics of indoor air pollutants. It combines computational fluid dynamics (CFD) modeling of the fluid flow in the reactor with radiation field modeling and photocatalytic reaction kinetics to yield a rigorous model of a flat-plate, single-pass, flow-through photocatalytic reactor for indoor air purification. This method was applied to model the PCO of trichloroethylene (TCE) in humidified air and to derive kinetic parameters directly from kinetic data in an integral flow reactor. Steady-state PCO experiments of TCE over irradiated TiO2 (Degussa P25) thin films immobilized on glass supports were carried out at different radiation intensities, flow rates, and inlet substrate concentrations. The oxidation rate of TCE was found to be first-order on the incident photon flux and to follow a Langmuir-Hinshelwood type reaction kinetics rate law. Mass transfer resistances were observed at Reynolds numbers less than 46. Apparent quantum yields were found to be up to 0.97 mol Einstein(-1). A comparison of the model prediction with the experimental results in an integral reactor yielded pollutant-specific kinetic rate parameters which were independent of reactor geometry, radiation field, and fluid-dynamics. The kinetic parameters would,therefore, be more universally applicable to the design and scale-up of photocatalytic reactors for indoor air purification.     

Degradation of carbendazim and 2,4-dichlorophenoxyacetic acid by immobilized consortium on loofa sponge

A fungicide, carbendazim (methyl-2-benzimidazole carbamate; MBC), and a herbicide, 2,4-dichlorophenoxyacetic acid (2,4-D), could be simultaneously degraded by a microbial consortium obtained from several soil samples in Japanese paddy fields with enrichment continuous culture. The degradation ability of the consortium was increased by immobilization on loofa (Luffa cylindrica) sponge in comparison with that of free-living consortium. MBC and 2,4-D were completely degraded within 5.5 d and 1.5 d, respectively. The toxicity of these pesticides in culture medium to Daphnia magna was reduced by treatment with the consortium corresponding to their degradation. The degradation ability of the immobilized consortium at pHs in the range from 6 to 9, at temperatures from 15 degrees C to 37 degrees C, and at low NH(4)(+)-N concentrations (1-10 mg/l) was not very different from that under the basal condition (pH 7, 30 degrees C, 424 mg/l NH(4)(+)-N and 472 mg/l PO(4)(3)(-)-P). At low pHs 4 and 5, the ability was significantly lower than that of the basal condition. Moreover, incubation at low PO(4)(3)(-)-P concentrations (1-10 mg/l) caused a decrease in pH at which the degradation ability also became lower. However, the ability in this culture completely recovered when pH was adjusted to 7 or the phosphate concentration was increased to the basal level. Analysis by denaturing gradient gel electrophoresis (DGGE) showed the whole population of the consortium became faint at low pH or low phosphate concentrations but became distinct again as much as those under the basal conditions, indicating that the decrease in the degradation ability caused by low pH was due to that whole population of the consortium underwent serious damage but could survive and recover. These results suggest the immobilized consortium on loofa sponge is a promising material for bioremediation of polluted water with these pesticides in paddy fields.     

Distinguishing abiotic and biotic transformation of tetrachloroethylene and trichloroethylene by stable carbon isotope fractionation

Significant carbon isotope fractionation was observed during FeS-mediated reductive dechlorination of tetrachloroethylene (PCE) and trichloroethylene (TCE). Bulk enrichment factors (E(bulk)) for PCE were -30.2 +/- 4.3 per thousand (pH 7), -29.54 +/- 0.83 per thousand (pH 8), and -24.6 +/- 1.1 per thousand (pH 9). For TCE, E(bulk) values were -33.4 +/- 1.5 per thousand (pH 8) and -27.9 +/- 1.3 per thousand (pH 9). A smaller magnitude of carbon isotope fractionation resulted from microbial reductive dechlorination by two isolated pure cultures (Desulfuromonas michiganensis strain BB1 (BB1) and Sulfurospirillum multivorans (Sm)) and a bacterial consortium (BioDechlor INOCULUM (BDI)). The E(bulk) values for biological PCE microbial dechlorination were -1.39 +/- 0.21 per thousand (BB1), -1.33 +/- 0.13 per thousand (Sm), and -7.12 +/- 0.72 per thousand (BDI), while those for TCE were -4.07 +/- 0.48 per thousand (BB1), -12.8 +/- 1.6 per thousand (Sm), and -15.27 +/- 0.79 per thousand (BDI). Reactions were investigated by calculation of the apparent kinetic isotope effect for carbon (AKIEc), and the results suggest that differences in isotope fractionation for abiotic and microbial dechlorination resulted from the differences in rate-limiting steps during the dechlorination reaction. Measurement of more negative E(bulk) values at sites contaminated with PCE and TCE may suggest the occurrence of abiotic reductive dechlorination by FeS.     

Iron nanoparticles coated with amphiphilic polysiloxane graft copolymers: dispersibility and contaminant treatability

Amphiphilic polysiloxane graft copolymers (APGCs) were used as a delivery vehicle for nanoscale zerovalent iron (NZVI). The APGCs were designed to enable adsorption onto NZVI surfaces via carboxylic acid anchoring groups and polyethylene glycol (PEG) grafts were used to provide dispersibility in water. Degradation studies were conducted with trichloroethylene (TCE) as the model contaminant. TCE degradation rate with APGC-coated NZVI (CNZVI) was determined to be higher as compared to bare NZVI. The surface normalized degradation rate constants, k(SA) (Lm(2-) h(-1)), for TCE removal by CNZVI and bare NZVI ranged from 0.008 to 0.0760 to 007-0.016, respectively. Shelf life studies conducted over 12 months to access colloidal stability and 6 months to access TCE degradation indicated that colloidal stability and chemical reactivity of CNZVI remained more or less unchanged. The sedimentation characteristics of CNZVI under different ionic strength conditions (0-10 mM) did not change significantly. The steric nature of particle stabilization is expected to improve aquifer injection efficiency of the coated NZVI for groundwater remediation.     

茶菌人工复合菌剂构建和发酵性能分析

利用从茶菌中分离纯化的4个优势菌株构建人工复合菌剂。通过单独培养和不同复合方式培养的比较，确定菌株在茶菌发酵和菌膜形成中的作用；采用高效液相色谱、顶空固相微萃取和气相色谱-质谱联用等方法分析茶菌发酵过程中主要生化成分变化；经历多次传代接种后，采用人工分离和宏基因组分析相结合分析菌群组成和稳定性。结果表明：供试的4个菌株中，葡糖醋杆菌J5(Gluconacetobacter sp. J5)是产生纤维素和菌膜的核心菌株。混合菌株组合C3C5C6J5发酵后在菌体生长、糖利用、发酵液pH值、总酸度和茶多酚含量等指标与自然发酵相似。经历6代转接后菌群稳定，复配的菌株在人工菌群中均为优势菌株。表明从天然茶菌饮料中分离纯化功能菌株，通过菌株复配构建稳定的人工发酵剂可行，为茶菌的标准化工业生产打下基础。     

Continuous treatment of gas-phase trichloroethylene by Burkholderia cepacia G4 in a two-stage continuous stirred tank reactor/trickling biofilter system

A two-stage continuous stirred tank reactor/trickling biofilter system was developed and operated for continuous treatment of gas-phase trichloroethylene (TCE) by Burkholderia cepacia. The maximum TCE elimination capacity was 28.0 mg TCE/l.d, and complete removal of TCE was obtained for inlet loading below 25.3 mg TCE/l.d. The reactor system was stably operated for more than 3 months.     

Nitrogen removal characteristics and biofilm analysis of a membrane-aerated biofilm reactor applicable to high-strength nitrogenous wastewater treatment

A membrane-aerated biofilm reactor (MABR) capable of simultaneous nitrification and denitrification in a single reactor vessel was developed to investigate the characteristics of nitrogen removal from high-strength nitrogenous wastewater, and biofilm analysis using microelectrodes and the fluorescence in situ hybridization (FISH) technique was performed. Mean removal percentages of total organic carbon (TOC) and nitrogen were 96% and 83% at removal rates of 5.76 g-C m(-2) d(-1) and 4.48 g-N m(-2) d(-1), respectively. For stable removal efficiency, constant washing of the biofilm was needed. Dissolved oxygen microelectrode measurement revealed that the biofilm thickness was about 1600 microm, and that oxygen penetrated about 300 to 700 microm, from the outer surface of the membrane. Furthermore, FISH analysis revealed that ammonia-oxidizing bacteria (AOB) were located near the outer surface of the membrane, whereas other bacteria were located from the inner to the outer part of the biofilm. Combining these results demonstrated that simultaneous nitrification and denitrification occurred in the biofilm of the MABR system. In addition, stoichiometric analysis revealed that after 130 d(-1), the free ammonia (FA) concentration ranged within the concentration causing inhibition of the growth of nitrite oxidizing bacteria (NOB) and that AOB consumed 86% of the oxygen supplied through the intra-membrane. These results indicate that nitrogen removal not via nitrate but via nitrite was mainly achieved in the MABR system.