Microbial community in methanogenic packed-bed reactor successfully operating at short hydraulic retention time

The microbial community in a thermophilic anaerobic packed-bed reactor, which had been successfully operated to convert acetic and butyric acids to methane at a short hydraulic retention time (from 24 h to 1.9 h), was investigated. Archaea closely related to known methanogens were detected by 16S rRNA gene analyses of the effluents, together with diverse types of unidentified bacteria.     

l-Arabinose production from sugar beet arabinan by immobilized endo- and exo-arabinanases from Caldicellulosiruptor saccharolyticus in a packed-bed reactor

The immobilized endo- and exo-arabinanases from Caldicellulosiruptor saccharolyticus produced continuously an average of 16.5 gl(-1)l-arabinose from 20 gl(-1) sugar beet arabinan at pH 5.0 and 75°C for 216 h, with a productivity of 9.9 gl(-1)h(-1) and a conversion yield of 83%.     

Production and oxidative stability of a human milk fat substitute produced from lard by enzyme technology in a pilot packed-bed reactor

Residence time and time of production were investigated during the enzymatic production of a specific structured lipid/human milk fat substitute (SL-HMFS), on a kg scale, made from lard and soybean oil fatty acids, using a packed-bed reactor and short path distillation. There were no effects of residence time or time of production on C18:2 and C18:3 incorporation or on acyl migration in the sn-2 position. In addition, the SL-HMFS was compared to commercial human milk fat substitute (HMFS) regarding fatty acid composition, content of antioxidants and oxidative stability. Fats were stored at 60 °C for four days and the oxidative stability evaluated by analysis of peroxide value (PV) and volatile secondary oxidation products. SL-HMFS had a lower oxidative stability than did commercial HMFS products or lard, probably due to a lower level of tocopherol in SL-HMFS.     

Enzymatic synthesis of lard-based ascorbyl esters in a packed-bed reactor: Optimization by response surface methodology and evaluation of antioxidant properties

An optimal continuous production of lard-based ascorbyl esters (LBAEs) by transesterification of lard with l-ascorbic acid in a packed bed reactor (PBR) was developed using immobilized lipase (Novozym 435) as a catalyst in a tert-amyl alcohol solvent system. Response surface methodology (RSM) and central composite design (CCD) were employed to evaluate the effects of substrate flow rate, reaction temperature and substrate molar concentration ratio on the molar conversion of LBAEs. The optimum conditions were as follows: substrate flow rate 1.07 ml/min, reaction temperature 56.44 °C, and substrate molar concentration ratio 2.24:1. The optimum predicted LBAEs yield was 50.83% and the actual value was 50.50%. The above results shows that the RSM study based on CCD is adaptable for LBAEs yield studied for the current transesterification system. The antioxidant activities of LBAEs has also been studied. LBAEs represented positive antioxidant potential on superoxide anion radical and hydroxyl radicals and satisfactory antioxidant activity in lard and soybean oil. The results suggest that LBAEs has the potential to serve as natural antioxidant in food system.     

Kinetics of inulinase production by solid-state fermentation in a packed-bed bioreactor

In this work the cell growth and inulinase production by Kluyveromyces marxianus NRRL Y-7571 were investigated in a packed-bed bioreactor. For this purpose, seven experimental runs were carried out in order to verify the influence of the inlet air temperature and volumetric air flow rate on the process dynamics. The results showed that the manipulated variables affected significantly the process performance. The best condition for enzyme production was an inlet air temperature and volumetric flow rate of 30 °C and 3 m³ h⁻¹, respectively, reaching an activity of around 463 U gds⁻¹. The results obtained here can be useful in the scale-up and optimisation of packed-bed bioreactors configuration for inulinase production.     

填充床固态发酵生物反应器模拟研究进展

数学模型是固态发酵生物反应器设计、优化和操作的重要工具,它不仅可以指导SSF过程生物反应器的设计和操作,而且可以深入分析发酵系统内的各种现象从而控制整个发酵过程。文章分析近几年固态发酵填充床生物反应器的拟均相假设模拟模型、非均相假设模拟模型和间歇混合填充床生物反应器模拟模型,对模拟结果进行讨论,深入分析如何用数学方法描述SSF系统的传热传质模型。在分析填充床固态发酵底物床层的系统组成及其性质的基础上,提出利用多孔介质体积平均理论研究SSF系统传热传质过程的可能性。     

Effect of ammonium addition on methanogenic community in a fluidized bed anaerobic digestion

After immobilization of anaerobes on carbon felt in a fluidized-bed anaerobic digester at an ammonium concentration of 500 mg N/l, the results of real-time PCR analysis indicated that the cell densities of the immobilized methanogens and bacteria increased compared with those of the free-living methanogens and bacteria in the original anaerobically digested sewage sludge, respectively. The results of the clone analysis of the original sludge suggested that the major methanogens were Methanosaeta sp. and the members of the order Methanomicrobiales, and that after immobilization, these were changed to Methanobacterium and Methanosarcina sp. The results of real-time PCR analysis also showed that the ratio of the Methanosaeta sp. in the methanogenic archaea decreased from 58.2% to 0.3% after the immobilization. Methane production decreased at ammonium concentrations of greater than 6000 mg N/l. The results of real-time PCR analysis indicated that the cell density of the immobilized archaea decreased at ammonium concentrations of greater than 3000 mg N/l. On the other hand, the cell density of the immobilized bacteria did not decrease at an ammonium concentration of 6000 mg N/l, but decreased at that of 9000 mg N/l. The major methanogenic clones immobilized on the carbon felt at an ammonium concentration of 3000 or 6000 mg N/l were Methanobacterium sp. The present results indicated that methanogens were relatively more sensitive to ammonium than bacteria.     

Anaerobic treatment performance and microbial population of thermophilic upflow anaerobic filter reactor treating awamori distillery wastewater

Distillery wastewater from awamori making was anaerobically treated for one year using thermophilic upflow anaerobic filter (UAF) reactors packed with pyridinium group-containing nonwoven fabric material. The microbial structure and spatial distribution of microorganisms on the support material were characterized using molecular biological methods. The reactor steadily achieved a high TOC loading rate of 18 g/l/d with approximately 80% TOC removal efficiency when non-diluted wastewater was fed. The maximum TOC loading rate increased to 36 g/l/d when treating thrice-diluted wastewater. However, the TOC removal efficiency and gas evolution rate decreased compared with that when non-diluted wastewater was used. Methanogens closely related to Methanosarcina thermophila and Methanoculleus bourgensis and bacteria in the phyla Firmicutes and Bacteroidetes were predominant methanogens and bacteria in the thermophilic UFA reactor, as indicated by 16S rRNA gene clone analysis. Fluorescence in situ hybridization (FISH) results showed that a large quantity of bacterial cells adhered throughout the whole support, and Methanosarcina-like methanogens existed mainly in the relative outside region while Methanoculleus cells were located in the relative inner part of the support. The support material used proved to be an excellent carrier for microorganisms, and a UAF reactor using this kind of support can be used for high-rate treatment of awamori/shochu distillery wastewater.     

Gaseous hexane biodegradation by Fusarium solani in two liquid phase packed-bed and stirred-tank bioreactors

Biofiltration of hydrophobic volatile pollutants is intrinsically limited by poor transfer of the pollutants from the gaseous to the liquid biotic phase, where biodegradation occurs. This study was conducted to evaluate the potential of silicone oil for enhancing the transport and subsequent biodegradation of hexane by the fungus Fusarium solani in various bioreactor configurations. Silicone oil was first selected among various solvents for its biocompatibility, nonbiodegradability, and good partitioning properties toward hexane. In batch tests, the use of silicone oil improved hexane specific biodegradation by approximately 60%. Subsequent biodegradation experiments were conducted in stirred-tank (1.5 L) and packed-bed (2.5 L) bioreactors fed with a constant gaseous hexane load of 180 g x m(-3)(reactor) x h(-1) and operated for 12 and 40 days, respectively. In the stirred reactors, the maximum hexane elimination capacity (EC) increased from 50 g x m(-3)(reactor) x h(-1) (removal efficiency, RE of 28%) in the control not supplied with silicone oil to 120 g x m(-3)(reactor) x h(-1) in the biphasic system (67% RE). In the packed-bed bioreactors, the maximum EC ranged from 110 (50% RE) to 180 g x m(-3)(reactor) x h(-1) (> 90% RE) in the control and two-liquid-phase systems, respectively. These results represent, to the best of our knowledge, the first reported case of fungi use in a two-liquid-phase bioreactor and the highest hexane removal capacities so far reported in biofilters.     

Biodegradation of short-chain n-alkanes in oil sands tailings under methanogenic conditions

The biodegradation of a mixture of low molecular weight n-alkanes (C6, C7, C8, and C10) was assessed under methanogenic conditions using mature fine tailings (MFT) produced by the oil sands industry in Alberta, Canada. Microorganisms present in the MFT mineralized the added n-alkane mixture, producing 16.2 (+/- 0.3) or 20.5 (+/- 0.1) mmol of methane in the headspace of microcosms spiked with 0.2% or 0.5% w/v n-alkanes, respectively, during 29 weeks of incubation. The spiked n-alkanes biodegraded in the sequence C10 > C8 > C7 > C6. Degradation of 100% C10, 97% C8, 74% C7, and 44% C6 occurred in a mixture of n-alkanes in the MFT spiked at 0.2% after 25 weeks of incubation. The same pattern of biodegradation was also observed in the MFT spiked with 0.5% n-alkanes. Stoichiometric calculations confirmed the mineralization of the degraded n-alkanes to methane. This study showed that the short-chain n-alkanes, which comprise a significant portion of the unrecovered naphtha used in bitumen extraction and released into the settling basins, can be biodegraded into methane. These findings may influence decisions regarding extraction processes and long-term management of MFT, and they suggest that intrinsic, methanogenic metabolism of these n-alkanes may occur in other anoxic environments.     

Influence of growth phase on bacterial deposition: interaction mechanisms in packed-bed column and radial stagnation point flow systems

The influence of bacterial growth stage on cell deposition kinetics has been examined using a mutant of Escherichia coli K12. Two experimental techniques--a packed-bed column and a radial stagnation point flow (RSPF) system--were employed to determine bacterial deposition rates onto quartz surfaces over a wide range of solution ionic strengths. Stationary-phase cells were found to be more adhesive than mid-exponential phase cells in both experimental systems. The divergence in deposition behavior was notably more pronounced in the RSPF than in the packed-bed system. For instance, in the RSPF system, the deposition rate of the stationary-phase cells at 0.03 M ionic strength was 14 times greater than that of the mid-exponential cells. The divergence in the packed-bed system was most significant at 0.01 M, where the deposition rate for the stationary-phase cells was nearly 4 times greater than for the mid-exponential cells. To explain the observed adhesion behavior, the stationary and mid-exponential bacterial cells were characterized for their size, surface charge density, electrophoretic mobility, viability, and hydrophobicity. On the basis of this analysis, it is suggested that the stationary cells have a more heterogeneous distribution of charged functional groups on the bacterial surface than the mid-exponential cells, which results in higher deposition kinetics. Furthermore, because the RSPF system enumerates only bacterial cells retained in primary minima, whereas the packed column captures mostly cells deposited in secondary minima, the difference in the stationary and mid-exponential cell deposition kinetics is much more pronounced in the RSPF system.     

聚焦原料皮

无论对于BLC的研究项目还是商务活动而言 ,有关原料皮的工作一直扮演着重要的角色 ,而且 ,这方面的工作也越来越受到政府的特别关注。现今 ,我们一直研究的是有关畜牧业对皮革质量、数量和肉食安全卫生的影响 ,并研究在屠宰场受到污染的动物皮与公共健康之间的密切关系。2 0 0 0年 4月由UK的食品标准机构(FSA)发起 ,由环境、食品和农业事务(DEFRA)部门共同协作提出 ,食品安全卫生的改善是各行业共同努力的中心问题。对于皮革行业来讲 ,以安全为中心的条款进一步推动了清洁饲养的发展 ,更加强调了肉食安全研究并在行业内普及的重要性 ,这项工作的深入进行 ,预示着皮革质量的长期稳定和持续性改善。本论文的中心是肉食安全问题 ,同时探讨不洁家畜对皮革质量的影响以及FSA将采取怎样的行动来实现即定目标     

Influence of Ni and Co on methanogenic activity and the amounts of coenzymes involved in methanogenesis

The requirement of Ni²⁺ and Co²⁺ addition on methanogenic activity and the coenzymes involved in methanogenesis were investigated in anaerobic continuous cultivation with synthetic wastewater using acetate as the sole carbon source. Addition of Ni²⁺ and Co²⁺ to the synthetic wastewater drastically increased the maximum dilution rate of the cultivation. The concentrations of coenzymes F₄₃₀ and corrinoids in the biomass increased to 0.62 μmol-Ni/g-VSS and 0.67 μmol-Co/g-VSS, respectively with the increase of the dilution rate. Methanogenic activity of the culture broth also increased with an increase of dilution rate. However, without addition of Ni²⁺ and Co²⁺, F₄₃₀ and corrinoids were not detected in the biomass and methanogenic activity was only a trace level at a dilution rate of 0.025 d⁻¹. When the amounts of Ni²⁺ and Co²⁺ added at a dilution rate of 0.6 d⁻¹ were lowered in steps, the concentrations of F₄₃₀ and corrinoids in the biomass and methanogenic activity decreased with decreasing amounts of Ni²⁺ and Co²⁺ added. These results suggest that Ni²⁺ and Co²⁺ were required for the methane-producing reactions via increases of coenzymes F₄₃₀ and corrinoids.     

Effect of temperature on microbial community of a glucose-degrading methanogenic consortium under hyperthermophilic chemostat cultivation

We continuously fed an anaerobic chemostat with synthetic wastewater containing glucose as the sole source of carbon and energy to study the effects of temperature on the microbial community under hyperthermophilic (65-80 degrees C) conditions. Methane was produced normally up to 77.5 degrees C at a dilution rate of 0.025 d(-1). However, the concentration of microorganisms and the rate of gas production decreased with increasing operation temperature. The microbial community in the chemostat at various temperatures was analyzed based on the 16S rRNA gene using molecular biological techniques including clone library analysis and denaturing gradient gel electrophoresis (DGGE). Aceticlastic methanogens related to Methanosarcina thermophila were detected at 65 degrees C and hydrogenotrophilic methanogens related to Methanothermobacter thermautotrophicus were the dominant methanogens between 70 degrees C to 77.5 degrees C. Bacteria related to Clostridium stercorarium and Thermoanaerobacter subterraneus comprised the dominant glucose-fermenting bacteria at temperatures of 65 degrees C and above, respectively. Bacteria related to Thermacetogenium phaeum and to Tepidiphilus margaritifer and Petrobacter succinatimandens were the dominant acetate-oxidizing bacteria at 70 degrees C and at 75-77.5 degrees C, respectively. The results suggested that, at temperatures of 70 degrees C and above, methane production via the aceticlastic pathway was negligible and indirect methanogenesis from acetate was dominant. Since acetate oxidation is a rate limiting step and a higher temperature favors the hydrolysis and acid formation, a two stage fermentation process, acidogenic and methanogenic fermentation stages operated under different temperatures, should be more suitable for the thermophilic anaerobic treatment at temperatures above 65 degrees C.     

Effect of dilution rate on structure of a mesophilic acetate-degrading methanogenic community during continuous cultivation

The community structures of two mesophilic acetate-degrading methanogenic consortia enriched at dilution rates of 0.025 and 0.6 d(-1) were analyzed by fluorescence in situ hybridization (FISH) and phylogenetic analyses based on 16S rDNA clonal sequences and quantitative real-time polymerase chain reaction (PCR). FISH experiments with archaeal and bacterial domain-specific probes showed that archaeal cells were predominant and only a small number of bacterial cells were detected at both dilution rates. In the domain Archaea, the number of cells closely related to Methanosarcina barkeri was shown to be greater at the high dilution rate using FISH with species-specific probes. Taxonomic analyses based on rDNA clonal sequences obtained at the low and high dilution rates showed that 43% of 100 clones and 72% of 92 clones, respectively, were affiliated with the domain Archaea and the remainders at each dilution rate were affiliated with the domain Bacteria. Within the domain Archaea, all rDNA clones at both dilution rates were affiliated with the genera Methanosaeta or Methanosarcina of the aceticlastic methanogens. Within the domain Bacteria, the rDNA clones obtained at the low dilution rate were affiliated with four phyla, Firmicutes (36%), Bacteroidetes (9%), Chloroflexi (6%) and candidate division OP12 (5%). The rDNA clones obtained at the high dilution rate were affiliated with four phyla, Firmicutes (16%), Bacteroidetes (8%), Proteobacteria (1%) and candidate division OP12 (3%). Real-time quantitative PCR experiments showed that the number of rDNA sequences affiliated with the genus Methanosarcina was greater at the high dilution rate. In addition, a significant number of rDNA sequences affiliated with the genus Methanoculleus were detected only at the low dilution rate. Detection of a hydrogenotrophic methanogen at the low dilution rate suggests that the syntrophic acetate oxidation by hydrogenotrophic methanogens and acetate-oxidizing bacteria could occur at the low dilution rate.     

想到哪里 说到哪里——对超硬材料行业一些问题的看法

文章叙述了目前超硬材料行业中所面临的无序发展以及人才、发展水平定位等问题,并引用事实和数据进行了回答,认为应该充分发挥行业专家和技术委员会的作用,提高论文水平,并对行业在“十五”中的发展提出了看法。     

生化反应器的传质性能

利用因次分析法建立了生化反应器通风发酵罐体积溶氧系数K1α与设备参数及操作变量的关联式,利用亚硫酸钠氧化法测定K1α,通过所得实验数据采用最小二乘法回归出K1α与各操作变量及设备参数间的关系式。     

Difference in the nature of tannins on in vitro ruminal methane and volatile fatty acid production and on methanogenic archaea and protozoal populations

Six plant sources of hydrolyzable tannins (HT) or HT and condensed tannins (CT; designated as HT1, HT2, HT3, HT + CT1, HT + CT2, and HT + CT3) were evaluated to determine their effects in vitro on CH₄ production and on ruminal archaeal and protozoa populations, and to assess potential differences in biological activities between sources containing HT only or HT and CT. Samples HT1, HT2, and HT3 contained only HT, whereas samples HT + CT1, HT + CT2, and HT + CT3 contained HT and CT. In experiment 1, in vitro incubations with samples containing HT or HT + CT resulted in a decrease in CH₄ production of 0.6 and 5.5%, respectively, compared with that produced by incubations containing the added tannin binder polyethylene glycol-6000. Tannin also suppressed the population of methanogenic archaea in all incubations except those with HT2, with an average decrease of 11.6% in HT incubations (15.8, 7.09, and 12.0 in HT1, HT2, and HT3) and 28.6% in incubations containing HT + CT (35.0, 40.1, and 10.8 in HT + CT1, HT + CT2, and HT + CT3) when compared with incubations containing added polyethylene glycol-6000. The mean decrease in protozoal counts was 12.3% in HT and 36.2% in HT + CT incubations. Tannins increased in vitro pH, reduced total VFA concentrations, increased propionate concentrations, and decreased concentrations of iso-acids. In experiment 2, when a basal diet was incubated with graded levels of HT + CT1, HT + CT2, and HT + CT3, the total gas and CH₄ production and archaeal and protozoal populations decreased as the concentration of tannins increased. Our results confirm that tannins suppress methanogenesis by reducing methanogenic populations in the rumen either directly or by reducing the protozoal population, thereby reducing methanogens symbiotically associated with the protozoal population. In addition, tannin sources containing both HT and CT were more potent in suppressing methanogenesis than those containing only HT.