聚乙烯醇高效降解菌的筛选及降解特性研究

以聚乙烯醇为唯一碳源从环境中筛选获得了高效降解聚乙烯醇的微生物菌株XT11,初步鉴定为假单胞菌属(Pseudomonas sp.).对菌株Pseudomonas XT11的生长过程及PVA降解过程进行了研究,发现该菌株在54 h内可将1 g/L的聚乙烯醇(PVA)降解.同时研究了温度、pH值及酵母膏浓度对该菌株降解PVA的影响,结果表明其最适温度、pH值和酵母膏浓度分别为30℃、7.0和0.5 g/L.研究了PVA浓度对PVA降解率的影响,发现随着PVA浓度的增大,PVA的降解率降低.     

聚乙烯醇高效降解菌的筛选及降解特性研究

以聚乙烯醇为唯一碳源从环境中筛选获得了高效降解聚乙烯醇的微生物菌株XT11, 初步鉴定为假单胞菌属(Pseudomonas sp.)。对菌株Pseudomonas XT11的生长过程及PVA降解过程进行了研究, 发现该菌株在54 h内可将1 g/L的聚乙烯醇(PVA)降解。同时研究了温度、pH值及酵母膏浓度对该菌株降解PVA的影响, 结果表明其最适温度、pH值和酵母膏浓度分别为30℃、7.0和0.5 g/L。研究了PVA浓度对PVA降解率的影响, 发现随着PVA浓度的增大, PVA的降解率降低。     

Production of antifungal saponins in an airlift bioreactor with a cell line transformed from Solanum chrysotrichum and its activity against strawberry phytopathogens

Abstract

Biotechnology through plant cell cultures in bioreactors is a tool that allows increasing the production of secondary metabolites of commercial interest. The hydrodynamic characterization, in addition to the transfer (OTR) and uptake (OUR) of oxygen through the dynamic method with different aeration rate, were used to see their influence on the production of biomass and saponins. The culture poisoning technique was used to determine the antifungal activity of the SC-2 and SC-3 saponins in vitro. Likewise, the shear or hydrodynamic stress of 273.6?mN/m² were calculated based on the Reynolds Number. The oxygen supply (OTR) was always greater than the demand (OUR) for all the aeration rate evaluated. Dry weight values of 8.6 gDW/L and a concentration of 2.7?mg/L and 187.3?mg/L of the saponins SC-2 and SC-3 respectively were obtained with an air flow of 0.1 vvm. In addition, it was possible to inhibit the growth of phytopathogenic fungi in vitro by up to 93%, while in vivo it was possible to reduce the infections of strawberry seeds inoculated with phytopathogens, obtaining up to 94% of germinated seeds. This information will facilitate the rational operation of the bioreactor culture system that produces secondary metabolites.     

Phenanthrene biodegradation by immobilized microbial consortium in polyvinyl alcohol cryogel beads

Removal of polycyclic aromatic hydrocarbons (PAHs), a group of widespread toxic compounds, has been one of the environmental issues in wastewater treatment systems for many years. In this study, biodegradation of phenanthrene (PHE), as a model contaminant, by a microbial consortium entrapped in polyvinyl alcohol (PVA) cryogel prepared by freeze-thaw method was investigated. The effect of inoculum size (300–900 mg of cell dry weight per liter) and initial PHE concentration (100–2000 ppm) as well as bead cell density (5 and 10 mg ml⁻¹) on PHE biodegradation by freely suspended cell (FC) and immobilized cell (IC) systems in aqueous phase was examined. Results showed that although both IC and FC systems were capable of complete removal of 100 and 250 ppm of initial PHE (as sole carbon and energy sources), incomplete PHE removals were observed at higher initial PHE concentrations up to 2000 ppm after 7 days. IC system resulted in the maximum PHE removal of 400 ppm at initial PHE concentration of 750 ppm and inoculum size of 600 mg l⁻¹, while under these conditions FC system removed 310 ppm of PHE. Moreover, bead cell density was shown to affect the performance of IC system, with the lower density of 5 mg ml⁻¹ leading to a higher PHE removal due to the enhanced transport phenomena in the culture. Additionally, a correlation was proposed to predict PHE biodegradation at a range of initial PHE concentrations.     

Use of glycerol for producing 1,3-dihydroxyacetone by Gluconobacter oxydans in an airlift bioreactor

1,3-Dihydroxyacetone can be produced by biotransformation of glycerol with glycerol dehydrogenase from Gluconobacter oxydans cells. Firstly, improvement the activity of glycerol dehydrogenase was carried out by medium optimization. The optimal medium for cell cultivation was composed of 5.6 g/l yeast extract, 4.7 g/l glycerol, 42.1 g/l mannitol, 0.5 g/l K₂HPO₄, 0.5 g/l KH₂PO₄, 0.1 g/l MgSO₄·7H₂O, and 2.0 g/l CaCO₃ with the initial pH of 4.9. Secondly, an internal loop airlift bioreactor was applied for DHA production from glycerol by resting cells of G. oxydans ZJB09113. Furthermore, the effects of pH, aeration rate and cell content on DHA production and glycerol feeding strategy were investigated. 156.3 ± 7.8 g/l of maximal DHA concentration with 89.8 ± 2.4% of conversion rate of glycerol to DHA was achieved after 72 h of biotransformation using 10 g/l resting cells at 30 °C, pH 5.0 and 1.5 vvm of aeration rate.     

Improved algal oil production from Botryococcus braunii by feeding nitrate and phosphate in an airlift bioreactor

To improve biomass and microalgal oil production of Botryococcus braunii, fed‐batch culture was investigated in an airlift photobioreactor. The optimal feeding time of the fed‐batch culture was after 15 days of cultivation, where 1.82 g/L of the microalgal biomass was obtained in the batch culture. Nitrate nutrient was the restrictive factor for the fed‐batch cultivation while phosphate nutrient with high concentration did not affect the microalgal growth. The optimal mole ratio of nitrate to phosphate was 34.7:1, where nitrate concentration reached the initial level and phosphate concentration was one quarter of its initial level. With one feeding, the biomass of B. braunii reached 2.56 g/L after 18 days. Two feedings in 2‐day interval enhanced the biomass production up to 2.87 g/L after 19 days of cultivation. The hydrocarbon content in dry biomass of B. braunii kept at high level of 64.3% w/w. Compared with the batch culture, biomass production and hydrocarbon productivity of B. braunii were greatly improved by the strategic fed‐batch cultivation.     

Analysis of petroleum biodesulfurization in an airlift bioreactor using response surface methodology

For the first time, growing cells of Gordonia alkanivorans RIPI90A were used for biodesulfurization (BDS) of diesel. This process was carried out in an internal airlift bioreactor. BDS parameters (oil/water phase ratio and initial sulfur concentration) were optimized in flasks using response surface methodology. Predicted results were found to be in good agreement with experimental results. Initial sulfur concentration had a remarkable effect on BDS process. Maximum removal of sulfur (21 mg/l) can be achieved at oil/water phase ratio of 25% (v/v) and initial sulfur concentration of 28 mg/l. Moreover, effect of superficial gas velocity (Ug) and working volume (v) on volumetric gas liquid mass transfer coefficient was studied in an airlift bioreactor for BDS of diesel. The best results were achieved at Ug and v of 2.5l/min and 6.6l, respectively. Subsequently, BDS of diesel was investigated in an airlift bioreactor under optimized conditions. Sulfur reduction after 30 h was 14 mg/l.     

聚乙烯醇生物降解研究进展

聚乙烯醇(PVA)是一种在纺织和化工行业中广泛使用的难降解的高分子聚合物。随着人们对纺织工业清洁生产的关注,如何在退浆工艺中就实现对PVA的生物降解、减少PVA废水的排放,并避免化学退浆过程中高温和氧化造成的棉纤维损伤,是近年来纺织生物技术领域的研究热点。由于PVA降解菌种类不多、培养周期长,PVA降解酶酶活不高、提取不容易等原因,使PVA的生化降解研究还局限在PVA降解菌的筛选、PVA降解酶的酶学性质研究等方面,PVA降解酶还未在纺织工业上得到应用。本文综述了近年来国内外在PVA降解菌筛选、PVA降解酶提取及酶学性质、PVA生化降解机理等方面的研究进展,并讨论了PVA生化降解研究中存在的问题及发展方向。     

Influence of sparger on energy dissipation, shear rate, and mass transfer to sea water in a concentric-tube airlift bioreactor

Data on volumetric mass-transfer coefficient, K_La_L, in a 12 × 10⁻³ m³ airlift bioreactor are reported. Measurements were made in sea water. The superficial gas velocity ranged up to 0.21 m/s. Four cylindrical spargers (60–1000 μm pore size) were tested. In bubbly flow, the sparger pore size strongly influenced the K_La_L; the highest K_La_L values were obtained with the smallest pore size. In contrast, in the transition and heterogeneous flow regimes, the pore size had little influence on K_La_L. The best correlation of the mass transfer data was obtained when both gas holdup and liquid superficial velocity were taken as independent variables. Shear rates were estimated in the different zones of the reactor. The highest values were found in the bottom zone of the reactor and in the gas-liquid separator. The penetration and isotropic turbulence models were used to develop a semi-theoretical equation relating the volumetric mass-transfer coefficient to shear rate; hence providing a better understanding of how the operational variables may be manipulated to attain a moderate shear rate and an appropriate level of mass transfer, two extremely important parameters for the growth of sensible microorganisms as those used in marine biotechnology.     

Purification and properties of polyvinyl alcohol oxidase with broad substrate range obtained from Pseudomonas vesicularis var. povalolyticus PH

Extracellular PVA oxidase produced by Pseudomonas vesicularis var. povalolyticus PH was purified to homogeneity by ammonium sulphate fractionation followed by successive column chromatography, and a study made of its characteristics. The molecular weight of the purified enzyme was estimated to be 75,000 by gel filtration and 85,000 by SDS-PAGE, suggesting that it consists of monomeric protein. Its isoelectric point was 5.7. The purified enzyme was colourless, and contained one atom of iron per molecule. It exhibited a broad pH activity profile with maximum activity at pH 10.0, and was stable between pH 6.0 and 10.0. The optimum temperature for enzyme activity was 40°C, with stability up to 45°C. The enzyme activity was inhibited strongly by Fe2+, Hg2+ and Sn2+, and weakly by Cu2+, EDTA, thiourea and IAA. The enzyme exhibited activity toward several secondary alcohols, suggesting that it was a secondary alcohol oxidase. In particular, the enzyme exhibited strong activity towards the larger secondary alcohols such as 2-octanol and 4-decanol, and relatively strong activity towards cyclohexanol and benzyl alcohol.     

PVA-Ca(NO3)2法包埋固定氧化亚铁硫杆菌研究

首次报道了把聚乙烯醇(PVA)、海藻酸钠混合水溶胶和氧化亚铁硫杆菌混合后滴入1%~5%(W/V)的Ca(NO3)2溶液中凝固成型,并把成型后的颗粒置-20℃条件下冷冻1d,从而形成固定化颗粒,把该颗粒在摇瓶中进行分批培养,对Fe2 最大氧化速率可达2.45g/(L.h)。而且整个固定化操作简单,颗粒不粘连、强度高、稳定性好,可以同时消除PVA-H3BO3法中PVA颗粒的粘连膨胀和H3BO3对微生物的毒性,具有很好的应用价值。     

A simple method for mass propagation of Spathiphyllum cannifolium using an airlift bioreactor

Summary A method for the micropropagation of Spathiphyllum cannifolium is presented using shoot tip proliferation onto Murashige and Skoog (MS) medium supplemented with different plant growth regulator concentrations and combinations. The proliferation responses were significantly influenced by the cytokinin type and concentrations. Supplementation of the medium with benzyladenine (BA; 4.44–13.32 μM) increased the shoot proliferation rate significantly as compared to other treatments. When cytokinins were used with auxin (indole-3-butyric acid, IBA and naphthalene acetic acid. NAA), the number of shoots per explant increased in comparison with treatments with BA alone. The largest number of shoots, 9.3 per explant, was obtained with 13.32 μM BA and 4.9 μM IBA. Different MS medium strengths and sucrose concentrations were used with the aim to stimulate in vitro shoot proliferation. Full MS medium with 30 gl⁻¹ sucrose was found to be suitable for shoot tip culture of Spathiphyllum. Comparative studies between gelled medium and bioreactor culture [continuous immersion (with or without net) and temporary immersion in liquid media using ebb and flood] revealed that shoot multiplication and growth were more efficient in continuous immersion (with net) bioreactor with low cytokinin-supplemented media. Plantlets from the bioreactor were cultured hydroponically for 30 d and 100% of plants were rooted and acelimatized successfully. Rapid and efficient multiplication rate in bioreactor and successful transfer to greenhouse makes this protocol suitable for large-scale multiplication of this important foliage plant.     

Comparison of stirred tank and airlift bioreactors in the production of polygalacturonases by Aspergillus oryzae

The production of endo and exo-polygalacturonase (PG) by Aspergillus oryzae IPT 301 was studied in a stirred tank bioreactor (STR) and an internal circulation airlift bioreactor. Using a factorial experimental design, a soluble culture medium was defined which allowed the production of exo- and endo-PG comparable to that obtained in a medium containing suspended wheat bran. The soluble medium was used in tests to compare the production of these enzymes in the STR and airlift bioreactor. In these tests, after 96 h, maximum enzymatic activity values achieved for exo- and endo-PG were 65.2 units (U) per mL and 91.3 U mL⁻¹, in the STR, with similar activity values of 60.6 U mL⁻¹ and 86.2 U mL⁻¹, respectively, being achieved in the airlift bioreactor. The airlift bioreactor also showed satisfactory results regarding the oxygen transfer rate in this process, indicating its potential to be used in an eventual larger scale production of exo- and endo-PG, with lower costs for both installation and operation.     

Hydrodynamic characteristics of immobilized cell beads in a liquid-solid fluidized-bed bioreactor

This study examined the hydrodynamic characteristics of a liquid-solid fluidized-bed bioreactor using elastic particles (PVA gel beads) of various diameters as carriers. The drag coefficient-Reynolds number, velocity-voidage, and expansion index-Reynolds number relationships observed during fluidization of PVA gel beads in a fluidized bed in our experiments were compared with the published results. Predictions made from previous correlations were examined with our new experimental findings, revealing the inadequacy of most of these correlations. Thus, new correlations describing the above-mentioned relationships are suggested. The drag coefficient of immobilized cell beads is larger than that of free cell ones at the same Reynolds number because the surface of the immobilized cell beads is rougher. For multiparticle systems, the correction factor, f(epsilon), is a function of the falling gel bead properties (Reynolds number) as well as the fluidized gel bead properties (Archimedes number), and depend strongly on the bed voidage (epsilon). A new simple relation was developed to predict easily the epsilon value from 0.5-0.9 at 4,986 < A(r) < 40,745 or 34 < Re(t) < 186. For all the immobilized cell beads used in this study, the prediction error of the bed voidage was less than 5% at epsilon > 0.5. The prediction equations in this study can be further applied to analyzing the hydrodynamic characteristics of a fluidized-bed reactor using similar entrapped elastic particles as carriers.     

Hydrogenotrophic denitrification of synthetic aquaculture wastewater using membrane bioreactor

A hydrogenotrophic denitrification system was evaluated in removing nitrate from synthetic aquaculture wastewater for recirculation purposes. Two membrane bioreactor (MBR) systems, namely, aeration–denitrification system (ADS) and denitrification–aeration system (DAS) were studied with 50 mg/L of influent concentrations for both organic matter and nitrate nitrogen. The DAS achieved better removal efficiency of 91.4% total nitrogen (T-N) and denitrification rate of 363.7 mg/L.day at a HRT of 3 h compared to ADS. Further, there was no nitrite accumulation in the DAS effluent. The nitrite accumulation in ADS effluent was lesser when CO₂ was used as buffer rather than K₂HPO₄ and KH₂PO₄. Estimation of kinetic parameters of hydrogenotrophic bacteria indicated lesser sludge production compared to heterotrophic denitrification. In the DAS, membrane fouling was nonexistent in the aeration reactor that was used to produce the recirculating effluent. On the contrary, membrane fouling was observed in the denitrification reactor that supplied hydrogen to the mixed liquor. Thus, this study demonstrated DAS capability in maintaining the acceptable water quality appropriate for aquaculture, in which a closed recirculating system is typically used.     

Biodegradation of polyvinyl alcohol by a mixed microbial culture

A mixed culture capable of degrading 1 g l⁻¹ polyvinyl alcohol (PVA) completely was screened from sludge samples at Pacific Textile Factory, Wuxi, China. This mixed culture had stronger capability of degrading PVA with low polymerization and high saponification than degrading PVA with high polymerization and low saponification. Inorganic nitrogen source was more suitable for the mixed culture to grow and degrade PVA than organic nitrogen source. Microorganisms and relative abundance of this mixed culture were explored by terminal restriction fragment length polymorphism (T-RFLP). Small PVA molecules were detected in cell extracts of the mixed culture. This indicated that PVA degradation in the mixed culture was in fact a combined action of extracellular and intracellular enzymes. Two strains producing extracellular PVA-degrading enzyme were isolated from the mixed culture. They could individually degrade PVA1799 with polymerization of 1700 from initial average molecular weight 112,981 to 98,827 Da and 84,803 Da, respectively. However, only small amount of PVA124 in polymerization of 400 could be degraded by these two strains.     

30L生物反应器连续灌注培养重组CHO—C28细胞表达HBsAg的研究

应用３０ Ｌ生物反应器和微载体悬浮 培养技术,通过电脑全自动控制,连续灌注培养分泌ＨＢｓＡｇ 的重组ＣＨＯ－Ｃ２８细胞。试验了培养方式、连续灌流速度,反应器转速和细胞对葡萄糖消耗等工艺条件。观察培养６０ 天,细胞的生长形态、ＨＢｓＡｇ 分泌动态和染色体数。研究结果表明,连续培养６０ 天,细胞密度可达７．０×１０６ｃｅｌｌｓ／ｍ ｌ,平均维持在（５．０～６．０）×１０６ｃｅｌｌｓ／ｍ ｌ,收液的ＲＰＨＡ 滴度可达１∶５１２,ＨＢｓＡｇ 每天平均产量为３０ ｍ ｇ。     

A two-step procedure for in vitro multiplication of cloudberry (<Emphasis Type=Italic>Rubus chamaemorus</Emphasis> L.) shoots using bioreactor

Cultures of three cloudberry (Rubus chamaemorus L.) clones collected from natural stands in Newfoundland and Labrador, Canada were established in vitro on a modified cranberry (Vaccinium macrocarpon Ait.) tissue culture medium containing 8.9 μM 6-benzylaminopurine (BAP). Clones were compared for in vitro shoot proliferation on gelled medium supplemented with varying levels of BAP and thidiazuron (TDZ). Addition of 5.8 μM gibberellic acid (GA₃) in 8.9 μM BAP-contained medium improved shoot proliferation. TDZ supported rapid shoot proliferation at low concentration (1.1 μM) but induced 20–30% hyperhydricity in a plastic airlift bioreactor system containing liquid medium. Bioreactor-multiplied hyperhydric shoots were transferred to gelled medium containing 8.9 μM BAP and 5.8 μM GA₃ and produced normal shoots within 4 weeks of culture. Genotypes differed significantly with respect to multiplication rate with ‘C1’ producing the most shoots per explant. Proliferated shoots were rooted on a potting medium with 65–75% of survivability of rooted plants. Present results suggested the possibility of large-scale multiplication of cloudberry shoots in bioreactors.     

Biotransformation of glucose to gluconic acid by Aspergillus niger—study of mass transfer in an airlift bioreactor

A glucose–gluconic acid biotransformation system was suggested for the experimental study of oxygen transfer in bioreactors. This biosystem was used for the investigation of the effect of the flow rate and biomass concentration on the volumetric oxygen transfer coefficient k_La in a 10 dm³ internal-loop airlift bioreactor. For this purpose, the fermentation broth of the mycelial strain Aspergillus niger was employed, representing a three-phase system, where bubbles come into contact with dense rigid pellets. The results showed that the presented biotransformation system can be successfully utilised for the determination of the oxygen transfer rate in airlift bioreactors. The experiments showed a strong positive influence of the air flow rate on the rate (r_Glu), specific rate of gluconic acid production (k_Glu/X) as well as on the volumetric oxygen transfer coefficient (k_La). This confirmed an expected limitation of production rate by the oxygen transport from the gas to the liquid phase in the whole range of air flow rates applied. Moreover, consistent curves of the production rate r_Glu and k_La values vs. biomass concentration c_X (amount of enzymes) were observed. These exhibited a local maximum for c_X equal to 6.68 g dm⁻³. On the other hand, the specific production rate monotonously decreased with increasing biomass concentration. A decline of k_La values at higher c_X values was attributed to a bubble coalescence promoting effect of mycelial pellets.     

Removal of carbonaceous and nitrogenous pollutants from a synthetic wastewater using a membrane-coupled bioreactor

Two modified Ludzack-Ettinger (MLE)-type membrane-coupled bioreactors (MBRs) were investigated in this study for the purpose of removing both nitrogenous and carbonaceous pollutants from a synthetic wastewater. During the first MBR experiment, removal efficiencies were high (>90%) for chemical oxygen demand (COD) and ammonia, but total nitrogenous pollutant removal efficiency was poor (~25%). Bacterial community analysis of ammonia oxidizing bacteria (AOB) by a nested PCR-DGGE approach detected two Nitrosomonas-like populations and one Nitrosospira-like population. During the initial portion of the second MBR experiment, COD and ammonia removal efficiencies were similar to the first MBR experiment until the COD of the influent wastewater was increased to provide additional electron donors to support denitrification. Total nitrogen removal efficiencies eventually exceeded 90%, with a hydraulic residence time (HRT) of 24 h and a recirculation ratio of 8. When the HRT of the MBR experiment was decreased to 12 h, however, ammonia removal efficiency was adversely affected. A subsequent increase in the HRT to 18 h helped improve removal efficiencies for both ammonia (>85%) and total nitrogenous compounds (~70%). Our research demonstrates that MBRs can be effectively designed to remove both carbonaceous and nitrogenous pollutants. The ability of the microbial community to switch between anoxic (denitrifying) and oxic (nitrifying) conditions, however, represents a critical process constraint for the application of MLE-type MBR systems, such that little benefit is gained compared to conventional designs.