还原六价铬细菌及其还原酶的研究

从活性污泥中筛选出的C-2苏云金芽孢杆菌,能耐受250mg/L的六价铬,并具有较好的还原能力。研究表明木糖、果糖、玉米饼粉、苹果酸、琥珀酸、柠檬酸及Cu2+、Fe2+、Ca2+离子对C-2菌的还原有积极作用,菌体的接种量影响还原的速率。C-2菌还原的最适温度为37℃,最适pH为9.0;六价铬还原酶的最适pH为7.0、温度为37℃,Co2+、Cu2+、Fe2+、DTT、NADH对酶的还原有积极影响。     

硫酸盐还原菌及其还原解毒Cr(Ⅵ)的研究进展

硫酸盐还原菌是一类分布广泛, 能进行硫酸盐异化还原反应的严格厌氧菌。利用硫酸盐还原菌可去除环境中的许多污染物, 因而该类细菌在环境污染治理中具有广阔的应用前景。本文介绍了硫酸盐还原菌的生物学特性和代谢特征及其在环境污染治理中的应用, 并对硫酸盐还原菌还原解毒Cr(Ⅵ)及应用于含Cr(Ⅵ)废水处理的研究进展作了综述, 分析了其未来的研究方向。     

异化铁还原细菌LQ25还原重金属Cr (VI)的特性研究

[背景] 异化铁还原细菌能够在还原Fe （III）的同时将毒性较大的Cr （VI）还原成毒性较小的Cr （III）,解决铬污染的问题。[目的] 基于丁酸梭菌（Clostridium butyricum） LQ25异化铁还原过程制备生物磁铁矿,开展异化铁还原细菌还原Cr （VI）的特性研究。[方法] 构建以氢氧化铁为电子受体和葡萄糖为电子供体的异化铁培养体系。菌株LQ25培养结束时制备生物磁铁矿。设置不同初始Cr （VI）浓度（5、10、15、25和30 mg/L）,分别测定菌株LQ25对Cr （VI）还原效率以及生物磁铁矿对Cr （VI）的还原效率。[结果] 菌株LQ25在设置的Cr （VI）浓度范围内都能良好生长。当Cr （VI）浓度为15 mg/L时,在异化铁培养条件下,菌株LQ25对Cr （VI）的还原率为63.45%±5.13%,生物磁铁矿对Cr （VI）的还原率为87.73%±9.12%,相比菌株还原Cr （VI）的效率提高38%。pH变化能影响生物磁铁矿对Cr （VI）的还原率,当pH 2.0时,生物磁铁矿对Cr （VI）的还原率最高,几乎达到100%。电子显微镜观察发现生物磁铁矿表面有许多孔隙,X-射线衍射图谱显示生物磁铁矿中Fe （II）的存在形式是Fe （OH）₂。[结论] 基于异化铁还原细菌制备生物磁铁矿可用于还原Cr （VI）,这是一种有效去除Cr （VI）的途径。     

微生物还原Cr(VI)的研究进展

随着现代工业的发展, 水环境中的重金属对人类健康和环境带来严重的危害, 其中的Cr(VI)具有强烈的毒性。微生物在代谢过程中可以将Cr(VI)还原为Cr(III), 有效降低Cr(VI)的毒性。本文从可还原Cr(VI)的微生物、微生物还原Cr(VI)的机理、还原过程中存在的问题及发展方向等方面进行了综述。     

一组Cr(Ⅵ)还原菌群YEM001的培养优化

铬（Cr）是一种广泛应用于钢铁、鞣革、印染等领域的重要工业原料，由此而带来的Cr(Ⅵ)污染已成为我国主要重金属污染之一。YEM001是一组能有效还原污泥和垃圾渗滤液中的Cr(Ⅵ)，实现Cr(Ⅵ)污染生物修复的微生物菌群。然而菌群的扩大培养成为YEM001进一步应用的障碍。以优化菌群YEM001培养工艺条件为目标，通过单因素实验、正交实验对YEM001菌群的培养基和发酵条件进行了优化。结果显示以淀粉为碳源，YEM001能实现快速稳定的生长。优化后的YEM001菌群培养基为淀粉10 g/L，氯化铵3 g/L，硫酸镁2 g/L，酵母浸粉1 g/L。通过对搅拌转速、pH、通气等的调控，获得最佳发酵工艺条件为28 ℃、pH值 7.5、不通入空气、搅拌转速50 r/min。在该条件下，YEM001的培养液OD₆₀₀值可达1.91，且在60 h内能够完全还原100 mg/L Cr(Ⅵ)。通过成本分析，优化后每100 L培养基价格降低了38.11元，较优化前成本降低51.85%。     

青霉吸附水体重金属铬条件与特性研究

目的:研究青霉(Penicillium lh-1)作为吸附剂去除水体中六价铬的吸附条件与吸附特性.方法:菌种摇瓶培养收获茵体,干燥粉碎分选,添加吸附剂到体积100ml浓度50mg/L六价铬溶液中,对最优吸附温度、pH、共存离子以及铬被吸附形式进行研究.结果:①温度28℃以及酸性环境(pH 3)为最优吸附条件,10 h内,Cr(Ⅵ)的生物吸附去除效率达99%.②铬的生物吸附主要以六价形式,约占80%,部分Cr(Ⅵ)被还原成Cr(Ⅲ),约占20%.③溶液中共存离子对六价铬吸附的影响不同,一价阴离子与Cu2+对Cr(Ⅵ)的吸附几乎没有影响,二价阴离子和Ni2+的存在却明显地影响了生物吸附剂对Cr(Ⅵ)的吸附.结论环境温度、溶液pH以及溶液中共存离子对铬的生物吸附有显著的影响.     

一株李氏禾内生细菌去除Cr(Ⅵ)的特性

李氏禾(Leersia hexandra)是中国境内发现的第一种铬超积累植物,该文对李氏禾内生菌及其除铬性能进行了研究。采用添加Cr(VI)的牛肉膏蛋白胨固体平板培养方法,从李氏禾根部分离筛选获得一株具有较强Cr(VI)抗性的内生细菌G04,分子生物学鉴定结果表明该菌株属于阴沟肠杆菌(Enterobacter cloacae)。采用摇瓶培养方法,以Cr(VI)去除率、总Cr(铬)的去除率以及菌体生物量为指标,考察了pH、温度、底物浓度、装液量、接种量、摇床转速以及反应时间等因素对Cr(VI)去除率、总铬去除率和菌株生长的影响。结果表明:在牛肉膏蛋白胨液体培养基中,菌株E. cloacae G04去除Cr(VI)的较优反应条件为初始pH5. 0、温度37℃、Cr(VI)浓度为100 mg·L~(-1)、装液量80 mL(250 mL三角瓶)、接种量15%、摇床转速为120r·min~(-1)、反应时间48 h。在此条件下,菌株E. cloacae G04对Cr(VI)和总铬的去除率分别为84%和8%。根据Cr(VI)去除率和总铬去除率的结果推测该菌株去除Cr(VI)的机制可能是以还原为主、吸附为辅。这表明李氏禾内生细菌E. cloacae G04菌株具有较好的应用潜力,既有可能直接用于土壤、水环境铬污染的修复,也有可能作为促植物修复铬污染的后备菌株,另外可为深入研究李氏禾的铬积累作用机制提供参考。     

细菌的Fe(Ⅲ)还原

细菌Fe(Ⅲ)还原是生物进化过程中最早出现的生物能量代谢途径,多种古细菌和真细菌具有Fe(Ⅲ)还原能力。在细菌Fe(Ⅲ)还原的过程中,需要多种膜蛋白的参与,且受到多途径的调控,特别是多血红素的细胞色素在电子传递过程中发挥重要作用。细菌Fe(Ⅲ)还原在生命的进化和整个生物地球化学循环中起到重要作用,具重要的环境学意义。     

六价铬还原细菌Bacillus cereus S5.4的筛选鉴定及还原特性研究

六价铬生物毒性极大,是造成环境污染的主要重金属之一,其生物治理策略已引起了广泛关注。已经发现许多微生物具有六价铬抗性和还原性,但能工业应用的还十分有限。从宝钢电镀污泥中分离得到一系列高六价铬抗性菌株,其中一株S5.4显示出高六价铬还原性,经形态和生理生化特征及16s rDNA序列比对,鉴定为Bacillus cereus。该菌株好氧生长,在固体LB培养基上培养48h能耐受40mmol/L Cr6 ,并对Mn2 、Ba2 和Mo6 也显出高抗性;在液体LB培养基中培养72h完全还原2mmol/L Cr6 ,并能在补充培养基和六价铬的条件下连续还原。该菌株还原六价铬时,最适浓度为2mmol/L Cr6 ,最适温度范围30~37℃,最适pH 7~9。     

细菌吸附Pd2+的研究

从不同来源的细菌菌株中筛选获得一株吸附Ｐｄ＾２＋能力较强的菌株Ｒ０８,经鉴定为地衣芽孢杆菌（Ｂａｃｉｌｌｕｓ ｌｉｃｈｅｎｉｆｏｒｍｉｓ）Ｒ０８。Ｒ０８死菌体吸附Ｐｄ＾２＋的最适ｐＨ值３．５,其吸附作用是一种快速而非依赖温度的过程。吸附作用受菌体浓度和Ｐｄ＾２＋浓度影响。在起始Ｐｄ＾２＋浓度２００ｍｇ／Ｌ、菌浓度０．４ｇ／Ｌ、ｐＨ３．５和３０℃条件下,吸附４５ｍｉｎ,吸附量为２２４．８ｍｇ／ｇ。透     

Bacterial reduction of hexavalent chromium

Summary Cr(VI)-reducing bacteria are widespread and Cr(VI) reduction occurs under both aerobic and anaerobic conditions. Under aerobic conditions, both NADH and endogenous cell reserves may serve as the electron donor for Cr(VI) reduction. Under anaerobic conditions, electron transport systems containing cytochromes appear to be involved in Cr(VI) reduction. High cell densities are necessary to obtain a significant rate of Cr(VI) reduction. Cr(VI) reduction by bacteria may be inhibited by Cr(VI), oxygen, heavy metals, and phenolic compounds. The optimum pH and temperature observed for Cr(VI) reduction generally coincide with the optimal growth conditions of cells. The optimum redox potential for Cr(VI) reduction has not yet been established.     

Modeling hexavalent chromium reduction in Escherichia coli 33456

A model based on te analysis of the mechanism of enzymatic reactions was developed to characterize the rate and extent of microbial reduction of hexavalent chromium in Escherichia coli 33456. A finite reduction capacity (R(c)) was proposed and incorporated into the enzymatic model to regulate the toxicity effect on cells due to the oxidizing power of Cr(VI). The parameter values were determined by nonlinear least-square analysis using experimental data of anaerobic cultures. The obtained parameters were then used to predict Cr(VI) reduction in aerobic cultures along with a modification term of uncompetitive inhibition from molecular oxygen. The applicability of the developed model was demonstrated through excellent prediction of the results of batch studies conducted over range of initial Cr(VI) concentrations, initial cell densities, and DO levels. A sensitivity analysis revealed that the parameters obtained using the experimental data were unique, and neither change in K(c), the half-velocity constant, at high initial Cr(VI) concentrations nor change in R(c), the reduction capacity, at low initial Cr(VI) concentrations was sensitive to model prediction. (c) 1994 John Wiley & Sons, Inc.     

真菌还原Cr（VI）的研究

从不同来源的样品中分离筛选出几株抗Ｃｒ（ＶＩ）的真菌,他们能在含３００￣５００ｍｇ／ＬＫ２Ｃｒ２Ｏ７的蔗糖合成培养基中生长,其中ＢＳ－１菌株抗Ｋ２Ｃｒ２Ｏ７达９００ｍｇ／Ｌ．ＢＳ－１等４株真菌在含２００ｍｇ／Ｌ Ｋ２Ｃｒ２Ｏ７的培养基中生长４￣６ｄ后,培养液中的Ｃｒ（ＶＩ）已全部消失。这些真菌经鉴定为青霉菌ＢＳ－１和ＢＳ－３,黑曲霉ＢＲ－４和黄曲霉ＢＸ－１。经紫外可见光扫描及化学分析证实,高毒的Ｃ     

Kinetics and modeling of hexavalent chromium reduction in Enterobacter cloacae

Kinetics of bacterial reduction of toxic hexavalent chromium (chromate: CrO(4) (2-)) was investigated using batch and fedbatch cultures of Enterobacter cloacae strain HO1. In fedbatch cultures, the CrO(4) (2-) feed was controlled on the basis of the rate of pH change. This control strategy has proven to be useful for avoiding toxic CrO(4) (2-) overload. A simple mathematical model was developed to describe the bacterial process of CrO(4) (2-) reduction. In this model, two types of bacterial cells were considered: induced, CrO(4) (2-)-resistant cells and uninduced, sensitive ones. Only resistant cells were assumed to be able to reduce CrO(4) (2-). These fundamental ideas were supported by the model predictions which well approximated all experimental data. In a simulation study, the model was also used to optimize fed-batch cultures, instead of lengthy and expensive laboratory experiments. (c) 1993 John Wiley & Sons, Inc.     

A novel technology for biosorption and recovery hexavalent chromium in wastewater by bio-functional magnetic beads

The goal of this study was to develop an applied technique for the removal and recovery of heavy metal in wastewater. It is novel that the Cr(VI) could be adsorbed and recovered by bio-functional magnetic beads. Furthermore, the magnetic separation technology would make their separation more convenient. The beads were constituted by the powder of Rhizopus cohnii and Fe(3)O(4) particles coated with alginate and polyvinyl alcohol (PVA). The parameters effecting Cr(VI) removal were obtained: the optimum pH 1.0 and optimum temperature 28 degrees C. The biosorption took place mainly in form of Cr(VI) and R. cohnii biomass played a key role in Cr(VI) adsorption. The model of Langmuir isotherm and Lagergren could be better used to fit the sorption process and kinetics, respectively. The beads still maintained predominant characteristics of adsorption, recovery and magnetism after five cycles for adsorption-desorption. The mechanism of adsorption was gained by Fourier transform infrared spectroscopy (FTIR), raman spectroscopy (RS) and scanning electron microscopy (SEM). The groups of -NH(3)(+), -NH(2)(+)-, and NH- played an important role in the Cr(VI) adsorption. Consequently, the beads exhibited the superior performances in Cr(VI) cleanup, separation and recovery and the perspective potential in application.     

Effects of combining biological treatment and activated carbon on hexavalent chromium reduction

The objectives of the present work were: (a) to analyze the Cr(VI) removal by combining activated sludge (AS) with powdered activated carbon (PAC), (b) to analyze the effect of PAC and Cr(VI) on the growth kinetics of activated sludge, and (c) to determine if the combined method (AS-PAC) for Cr(VI) removal can be considered additive or synergistic with respect to the individual processes. Chromate removal was improved by increasing PAC concentrations in both PAC and AS-PAC systems. Cr(VI) removal using the AS-PAC system was higher than using AS or PAC. The increase of Cr(VI) caused longer lag phase and lower observed specific growth rate (μ_obs), biomass yield (Y_X/S), and specific growth substrate consumption rate (q_S) of activated sludge; additionally, PAC did not enhance the growth kinetic parameters (μ_obs, Y_X/S, q_S). Cr(VI) reduction in AS-PAC system was the result of the additive effect of each individual Cr(VI) removal process.     

Modeling simultaneous hexavalent chromium reduction and phenol degradation by a defined coculture of bacteria

Based on the kinetics of Cr(VI) reduction by Escherichia coli ATCC 33456 and phenol degradation by Pseudomonas putida DMP-1, a mathematical model is developed to describe simultaneous Cr(VI) reduction and phenol degradation in the coculture of the two species. The developed model incorporates the toxicity effects of Cr(VI) and phenol on phenol degradation and Cr(VI) reduction in the coculture. The model illustrates the inhibitory effects of phenol on Cr(VI) reduction and Cr(VI) toxicity toward phenol degradation. The model also reveals the recoveries of the activities of the repressed bacterial cells with continuous Cr(VI) reduction and phenol degradation in the coculture. The model is capable of predicting simultaneous Cr(VI) reduction and phenol degradation within a broad range of Cr(VI) and phenol concentrations and under an appropriate composition of populations. However, the model simulates lower concentrations of phenol than experimental observations once Cr(VI) is reduced to a low level (<7 mg/L). The model simulation for Cr(VI) also deviates from experimental data when P. putida is outnumbered by E. coli by a ratio of 1:5. (c) 1995 John Wiley & Sons, Inc.     

Enhancement of hexavalent chromium reduction and electricity production from a biocathode microbial fuel cell

Enhancement of Cr (VI) reduction rate and power production from biocathode microbial fuel cells (MFCs) was achieved using indigenous bacteria from Cr (VI)-contaminated site as inoculum and MFC architecture with a relatively large cathode-specific surface area of 340–900 m² m⁻³. A specific Cr (VI) reduction rate of 2.4 ± 0.2 mg g⁻¹VSS h⁻¹ and a power production of 2.4 ± 0.1 W m⁻³ at a current density of 6.9 A m⁻³ were simultaneously achieved at an initial Cr (VI) concentration of 39.2 mg L⁻¹. Initial Cr (VI) concentration and solution conductivity affected Cr (VI) reduction rate, power production and coulombic efficiency. These findings demonstrate the importance of inoculation and MFC architecture in the enhancement of Cr (VI) reduction rate and power production. This study is a beneficial attempt to improve the efficiency of biocathode MFCs and provide a good candidate of bioremediation process for Cr (VI)-contaminated sites.     

Characterization of enzymatic reduction of hexavalent chromium by Escherichia coli ATCC 33456.

Chromium reduction by Escherichia coli ATCC 33456 quantitatively transferred hexavalent chromium, Cr(VI), to trivalent chromium, Cr(III). The reduced chromium was predominantly present in the external medium. Supernatant fluids of cell extract, obtained by centrifugation at 12,000 and 150,000 x g, showed almost the same Cr(VI) reduction activity, indicating that Cr(VI) reduction by E. coli ATCC 33456 was a largely soluble reductase activity. In studies with respiratory inhibitors, no inhibitory effects on aerobic and anaerobic Cr(VI) reduction were demonstrated by addition of cyanide, azide, and rotenone into both intact cell cultures and supernatant fluids of E. coli ATCC 33456. Although cytochromes b and d were identified in the membrane fraction of cell extracts, Cr(VI) was not reduced by the membrane fraction alone. The cytochrome difference spectra analysis also indicated that these cytochromes of the respiratory chain require the presence of the soluble Cr(VI) reductase to mediate electron transport to Cr(VI). Stimulation of Cr(VI) reduction by an uncoupler, 2,4-dinitrophenol, indicated that the respiratory-chain-linked electron transport to Cr(VI) was limited by the rate of dissipation of the proton motive force.