趋磁螺菌中磁小体链装配相关基因及其功能

趋磁细菌(MTB)依赖于体内磁小体结构在磁场中取向,多个磁小体以一定的组 织形式排列是形成菌体内生物磁罗盘的重要环节．多数趋磁细菌中磁小体成链排列,有效增加了细胞磁偶极矩,从而使菌体表现出在环境磁场中定向的能力．趋磁螺菌M. magneticum AMB－1和M. gryphiswaldense MSR－1中磁小体均沿细胞长轴形成一条磁 小体链．通过对相关基因突变体表型的研究,结合对磁小体链形成过程的实时动态观 察,人们已初步了解MamJ、MamK和MamA等基因在磁小体链装配和维护过程中的功能．本文介绍了近年来趋磁螺菌磁小体链装配过程中重要功能性基因的研究进展,并重点分析了AMB-1和MSR-1中磁小体链装配的差异．     

从铅锌矿渣中分离的微生物对重金属吸附特性的研究

从铅锌矿渣中分离到 16种菌 (包括 7株细菌和 9株真菌 ) ,并研究了它们对Zn2 + ,Pb2 + ,Cu2 + 的吸附特性。发现大多数菌株对Pb2 + 与Zn2 + 有不同程度的吸附 ,但对Cu2 + 的吸附能力较小。菌株对Zn2 + 的吸附率大于对Pb2 + 的吸附 ,能吸附Pb2 + 的菌株也能吸附Zn2 + 。pH 4～ 6是真菌吸附金属离子的较好范围 ,细菌仅在pH =5 .0条件下 ,对Pb2 + 与Zn2 + 有吸附。在测试的不同金属离子浓度范围内 (5 0mg/L 相似文献   

银离子抗性细菌质粒的分离与鉴定

通过对不同化工厂废水处理池的活性污泥进行富集、不同浓度银离子驯化后,分离得到30株银离子抗性细菌,最大硝酸银耐受量可达80 mg·ml^-1.对这些细菌进行质粒抽提与鉴定,质粒检出率为76.67％.40 mmol·L^-1的苯甲酸钠对HAg4细菌质粒的消除率可达98.75％;而350 μg· ml^-1的吖啶橙对HAg4细菌质粒的消除率只有77.78％.细菌质粒与银离子抗性密切相关.     

趋磁细菌及磁小体在肿瘤治疗中的应用

提高抗肿瘤药物的靶向性是肿瘤治疗、降低药物副作用的重要手段。在肿瘤组织内部由于癌细胞的快速增殖致使其形成低氧区,低氧区会对多种肿瘤治疗方案产生耐受。趋磁细菌 (Magnetotactic bacteria, MTB) 是一类能在细胞内产生外包生物膜、纳米尺寸、单磁畴磁铁矿 (Fe3O4) 或硫铁矿 (Fe3S4) 晶体颗粒-磁小体的微生物的统称。在磁场的作用下,趋磁细菌可凭借鞭毛运动至厌氧区。趋磁细菌在动物体内毒性较低且生物相容性良好,其磁小体与人工合成的磁性纳米材料相比优势显著。文中在介绍趋磁细菌及其磁小体生物学特点、理化性能的基础上,综述了趋磁细菌作为载体偶联药物进入肿瘤内部,并通过感受低氧信号定位于肿瘤低氧区,以及趋磁细菌竞争肿瘤细胞铁源的研究进展,总结了磁小体运载化疗药物、抗体、DNA疫苗靶向结合肿瘤的研究进展,分析了趋磁细菌及磁小体肿瘤治疗中面临的问题,并对趋磁细菌和磁小体在肿瘤治疗中的应用进行了展望。     

趋磁细菌生态学研究进展

趋磁细菌是一类革兰氏阴性的原核生物,广泛分布于淡水和海水环境中的有氧-无氧过渡区.趋磁细菌的分布与其环境中的氧、硫化物及铁等的浓度相关,不同种类分布在不同的物化梯度范围内.趋磁细菌的生长、磁小体的合成及磁小体的成分对环境有一定程度的指示作用.它们在生物地球化学循环中起着重要的作用.主要针对以上研究内容进行回顾,同时结合本实验室的一些研究结果做初步的分析,并对趋磁细菌生态学研究进行展望.     

磁选育浸矿菌种新方法的研究--磁泳分离菌种

世界无处不有磁,磁场对整个世界产生着重大的影响。本文通过大量镜检工作,观察到从酸性矿坑水中初步分离培养得到的部分细菌对外加磁场均有微弱的趋磁性。基于菌种的这种特性,设计了磁泳装置用不同的磁场梯度分离细菌,磁泳分离的方法可以初步分离出近磁、远磁菌,这两个菌群的生理特性有着很大的差异,主要体现在其对亚铁氧化和对金属离子的浸出上,远磁菌亚铁氧化活性比近磁菌高将近50%,远磁菌对铜离子的浸出效果也比近磁菌好。近磁菌在强磁性矿物培养基中生长情况较好,而远磁菌在弱磁性矿物培养基中生长情况较好。而且,在近磁菌的纯培养菌体中分离到磁性颗粒。实验结果证明,采用磁泳用于分离体内含有磁性颗粒的细菌是可行并且有效的,这一分离技术和工艺的结合也将大大促进我国生物冶金的步伐。     

趋磁细菌概述及应用进展

趋磁细菌是一类具有趋磁行为的革兰氏阴性茵的统称,其趋磁特性是由于菌体内含有磁小体。磁小体是由膜包被的纳米尺寸单磁畴颗粒,在菌体内多呈链状排列。自被发现以来,趋磁细菌及磁小体已逐步成为新的生物资源被广泛研究于材料学、医学、生物学、物理学、地质学等多个学科领域,并在仿生学、生态学、医学、地质学、工业处理、卫生检验等多个领域得到应用。主要介绍了趋磁细菌的生物特征、研究发展进程,以及近年来在多个学科领域的研究与应用。     

趋磁细菌及其应用于生物导航的研究进展

趋磁性细菌是一种由于体内含有对磁场具有敏感性的磁小体,而能够沿着磁力线运动的特殊细菌,本文综述了趋磁细菌的分布、分类、特性、磁小体研究以及趋磁细菌在生物导航方面的研究进展。     

趋磁细菌及其应用于生物导航的研究进展

趋磁性细菌是一种由于体内含有对磁场具有敏感性的磁小体,而能够沿着磁力线运动的特殊细菌,本文综述了趋磁细菌的分布、分类、特性、磁小体研究以及趋磁细菌在生物导航方面的研究进展.     

趋磁细菌及磁小体的生物医学应用研究进展

近年来,趋磁细菌及其生物自身合成的磁小体由于良好的生物安全性逐渐被人们所认识,并被用于生物工程和医学应用研究。与人工化学合成磁性纳米颗粒相比,从趋磁细菌中提取的磁小体具有生物膜包被、生物相容性高、粒径均一及磁性高等优势。趋磁细菌因磁小体在其胞内呈链状排列,具有沿磁场方向泳动的能力,也被应用于各种应用研究。因此,综述了趋磁细菌及磁小体特性,并就最近的研究进展重点综述趋磁细菌和磁小体在生物工程及医学应用等领域的最新研究进展。     

The metal specificity and selectivity of ZntA from Escherichia coli using the acylphosphate intermediate

ZntA from Escherichia coli is a P-type ATPase that confers resistance to Pb(II), Zn(II), and Cd(II) in vivo. We had previously shown that purified ZntA shows ATP hydrolysis activity with the metal ions Pb(II), Zn(II), and Cd(II). In this study, we utilized the acylphosphate formation activity of ZntA to further investigate the substrate specificity of ZntA. The site of phosphorylation was Asp-436, as expected from sequence alignments. We show that in addition to Pb(II), Zn(II), and Cd(II), ZntA is active with Ni(II), Co(II), and Cu(II), but not with Cu(I) and Ag(I). Thus, ZntA is specific for a broad range of divalent soft metal ions. The activities with Ni(II), Co(II), and Cu(II) are extremely low; the activities with these non-physiological substrates are 10-20-fold lower compared with the values obtained with Pb(II), Zn(II), and Cd(II). Similar results were obtained with DeltaN-ZntA, a ZntA derivative lacking the amino-terminal metal binding domain. By characterizing the acylphosphate formation reaction in ZntA in detail, we show that a step prior to enzyme phosphorylation, most likely the metal ion binding step, is the slow step in the reaction mechanism in ZntA. The low activities with Ni(II), Co(II), and Cu(II) are because of a further decrease in the rate of binding of these metal ions. Thus, metal ion selectivity in ZntA and possibly other P1-type ATPases is based on the charge and the ligand preference of particular metal ions but not on their size.     

The adsorption of copper(II) ions on to dehydrated wheat bran (DWB): determination of the equilibrium and thermodynamic parameters

The adsorption of copper(II) ions on to dehydrated wheat bran (DWB), a by-product of the flour process, was investigated as a function of initial pH, temperature, initial metal ion concentration and adsorbent dosage. The optimum adsorption conditions were initial pH 5.0, initial copper concentration 100 mg l⁻¹, temperature 60 °C and adsorbent dosage 0.1 g. The adsorption equilibrium was described well by the Langmuir isotherm model with maximum adsorption capacity of 51.5 mg g⁻¹ of copper(II) ions on DWB. The observation of an increase in adsorption with increasing temperature leads to the result that the adsorption of copper(II) ions on DWB is endothermic in nature. The thermodynamic parameters such as enthalpy, free energy and entropy changes were calculated and these values show that the copper(II)-DWB adsorption process was favoured at high temperatures.     

Application of Freundlich and Langmuir models to multistage purification process to remove heavy metal ions by using Schizomeris leibleinii

The adsorption of iron(III), lead(II) and cadmium(II) ions onto Schizomeris leibleinii, a green alga, was studied with respect to initial pH, temperature, initial metal ion and biomass concentration to determine the optimum adsorption conditions. Optimum initial pH for iron(III), lead(II) and cadmium(II) ions were 2.5, 4.5 and 5.0 at optimum temperature 30°C, respectively. The initial adsorption rates increased with increasing initial iron(III), lead(II) and cadmium(II) ion concentrations up to 100, 100 and 150 mg l⁻¹, respectively. The Freundlich and Langmuir adsorption isotherms were developed at various initial pH and temperature values. The adsorption of these metal ions to S. leibleinii was investigated in a two-stage mixed batch reactor. The residual metal ion concentrations (C_eq) at equilibrium at each stage for a given ‘quantity of dried algae (X₀)/volume of solution containing heavy metal ion (V₀)’ ratio were calculated using Freundlich and Langmuir isotherm constants. The experimental biosorption equilibrium data for iron(III), lead(II) and cadmium(II) ions were in good agreement with those calculated by both Freundlich and Langmuir models. The adsorbed iron(III), lead(II) and cadmium(II) ion concentrations increased with increasing X₀/V₀ ratios while the adsorbed metal quantities per unit mass of dried algae decreased.     

Adsorption of Cu(II) and Pb(II) onto diethylenetriamine-bacterial cellulose

Diethylenetriamine-bacterial cellulose (EABC) was synthesized by amination with diethylenetriamine on bacterial cellulose (BC). Its adsorption properties for Cu(II) and Pb(II) were investigated. The parameters affecting the metal ions adsorption, such as contact time, solution pH, and initial metal ions concentration have been investigated. The adsorption kinetics and adsorption isotherms were further studied. The results show that the adsorption rate could be well fitted by pseudo-second-order rate model, and adsorption isotherm could be described by the Langmuir model. The regeneration of EABC was also studied. This study provides the relatively comprehensive data for the EABC application to the removal of metal ion in the wastewater.     

Biosorption behaviors of biosorbents based on microorganisms immobilized by Ca-alginate for removing lead (II) from aqueous solution

Multiple microorganisms directly or treated with NaOH were immobilized by using Ca-alginate embedding to form biosorbents I and II, successively. The biosorption behaviors of biosorbents I and II for Pb(II) from aqueous solution were investigated in a batch system. Effects of solution pH, initial metal concentration, biosorbent dosage, contact time, temperature, and ionic strength on the adsorption process were considered to study the biosorption equilibrium, kinetics, thermodynamics, and mechanism of Pb(II) ion adsorption on the 2 types of biosorbents. The results showed that the adsorption capacity of biosorbent II for Pb(II) was higher than that of biosorbent I, and biosorbent II had a faster adsorption rate for Pb(II) ions. According to FTIR spectra, the carboxyl, amine, and hydroxyl groups on the biomass surface were involved in the biosorption of Pb(II). EDX analysis showed that ion exchange may be involved in the biosorption process, and the morphology observed by SEM micrograph of biosorbent I was completely different from that of biosorbent II. Desorption and regeneration experiments showed that the 2 types of biosorbents could be reused for 3 biosorption-desorption cycles without significant loss of their initial biosorption capacities.     

Construction a hybrid biosorbent using Scenedesmus quadricauda and Ca-alginate for biosorption of Cu(II), Zn(II) and Ni(II): kinetics and equilibrium studies

The potential use of the immobilized fresh water algae (in Ca-alginate) of Scenedesmus quadricauda to remove Cu(II), Zn(II) and Ni(II) ions from aqueous solutions was evaluated using Ca-alginate beads as a control system. Ca-alginate beads containing immobilized algae were incubated for the uniform growth at 22 degrees C for 5d ays. Adsorption of Cu(II), Zn(II) and Ni(II) ions on the immobilized algae showed highest values at around pH 5.0. Adsorption of Cu(II), Zn(II) and Ni(II) ions on the immobilized algae increased as the initial concentration of metal ions increased in the medium. The maximum adsorption capacities of the immobilized algal biosorbents for Cu(II), Zn(II) and Ni(II) were 75.6, 55.2 and 30.4 mg/g (or 1.155, 0.933 and 0.465 mmol/g) biosorbent, respectively. When the heavy metal ions were in competition, the amounts of adsorbed metal ions were found to be 0.84 mol/g for Cu(II), 0.59 mol/g for Ni(II) and 0.08 mol/g for Zn(II), the immobilised algal biomass was significantly selective for Cu(II) ions. The adsorption-equilibrium was also represented with Langmuir, Freundlich and Dubinin-Radushkevich adsorption isotherms. The adsorption of Cu(II), Zn(II) and Ni(II) ions on the immobilized algae followed second-order kinetic.     

Independence of the domains of metallothionein in metal binding

Mammalian metallothionein is a low molecular weight protein with two metal-binding domains. To determine if metal binding in one domain affects binding in the other, we prepared peptides corresponding to the regions that enfold the two metal-thiolate clusters. Metal reconstitution studies of these peptides revealed stoichiometries of metal binding similar to those observed within the intact molecule. Thus, the alpha domain coordinates 4 Cd(II), 6 Cu(I), or 6 Ag(I) ions regardless of whether the domain is part of the total protein or is studied as a separate peptide. Likewise, the beta domain binds 3 Cd(II), 6 Cu(I), or 6 Ag(I) ions in both the intact protein and as a separate peptide. If cluster B in intact metallothionein is preformed with Cu(I) or Ag(I), cluster A saturates with either 4 mol eq of Cd(II) or 6 mol eq of Ag(I). Similarly, preformation of the A cluster with Cd(II) does not affect the binding of 6 Cu(I) ions in the B cluster. Therefore, the metal-dependent folding of the protein to create one cluster occurs independent of constraints or influences from the other domain. Formation of the protein with a tetrahedrally coordinated metal in one cluster and a trigonally coordinated metal in the other center is possible.     

Sorption of Cu(II) and Cd(II) by extracellular polymeric substances (EPS) from Aspergillus fumigatus

Sorption of Cu(II) and Cd(II) onto the extracellular polymeric substances (EPS) produced by Aspergillus fumigatus was investigated for the initial pH of the solution, EPS concentrations, contact time, NaCl concentration, initial metal ion concentration and the presence of other ions in the solution. The results showed that the adsorption of metal ions was significantly affected by pH, EPS concentrations, initial metal concentration, NaCl concentration and co-ions. The sorption of Cu(II) and Cd(II) increased with increasing pH and initial metal ion concentration but decreased with an increase in the NaCl concentration. The maximum sorption capacities of A. fumigatus EPS calculated from the Langmuir model were 40 mg g⁻¹ EPS and 85.5 mg g⁻¹ EPS for Cu(II) and Cd(II), respectively. The binary metal sorption experiments showed a selective metal binding affinity in the order of Cu(II) > Pb(II) > Cd(II). Both the Freundlich and Langmuir adsorption models described the sorption of Cu(II) and Cd(II) by the EPS of A. fumigatus adequately. Fourier transform infrared spectroscopy (FTIR) analysis revealed that carboxyl, amide and hydroxyl functional groups were mainly correlated with the sorption of Cu(II) and Cd(II). Energy dispersive X-ray (EDX) system analysis revealed that the ion-exchange was an important mechanism involved in the Cu(II) and Cd(II) sorption process taking place on EPS.     

Activated carbon prepared from biomass as adsorbent: elimination of Ni(II) from aqueous solution.

Activated carbon (AC) prepared from waste Parthenium was used to eliminate Ni(lI) from aqueous solution by adsorption. Batch mode adsorption experiments are carried out, by varying contact time, metal ion concentration, carbon concentration, pH and desorption to assess kinetic and equilibrium parameters. They allowed initial adsorption coefficient, adsorption rate constant and maximum adsorption capacities to be computed. The adsorption data were modeled by using both Langmuir and Freundlich classical adsorption isotherms. The adsorption capacity (Q0) calculated from the Langmuir isotherm was 54.35 mg Ni(II)/g of AC at initial pH of 5.0 and 20 degrees C, for the particle size 250-500 microm. Increase in pH from 2 to 10 increased percent removal of metal ion. The regeneration by HCl of Ni(II)-saturated carbon by HCl, allowed suggestion of an adsorption mechanism by ion-exchange between metal ion and H+ ions on the AC surfaces. Quantitative recovery of Ni(II) was possible with HCl.