甲烷氧化菌在填埋场覆盖层的工程应用 (Ⅰ):分离与筛选

选取了湖泊底泥、矿化垃圾、覆盖土和好氧污泥4种填埋场周边易得基质为分离源,采用驯化、传代培养、甲烷氧化能力及适应性等方法进行了适合于填埋场覆盖层应用的甲烷氧化菌的筛选研究.结果表明,从好氧污泥中分离得到的甲烷氧化菌较其它分离源得到的甲烷氧化菌具有更高的甲烷氧化活性(2461.29μg·h-1·g-1,以每g干污泥每小时氧化的CH4量(μg)计,下同)和甲烷氧化速率增幅(1045.56μg·h-1·g-1,以每g干污泥每小时氧化的CH4量(μg)计,下同),接种后能显著提高覆盖材料的甲烷氧化能力(p0.05),且不受CH4浓度的抑制.源自好氧污泥的甲烷氧化菌具有生长迟滞期短、生长速率高等特点,对填埋场的甲烷削减更具适应性,有利于工程扩大应用.     

Thermal and Electrical Analysis in a Solid Oxide Fuel Cell Stack Using a Curved Profile for the Inlet Flow Rate Along the Stacking Direction

This study analyzes the cell temperature and current density fields of a solid oxide fuel cell stack, in which the inlet flow rate along the stacking direction of the fuel is either a curved profile derived through hydraulics or a progressively decreasing profile. The results show that the temperature field was neglibibly affected by the non-uniform inlet profile of the fuel, but the current density distribution was apparently affected. The difference in current density distribution between the curved profile and the progressively decreasing profile was small in the case of an solid oxide fuel cell (SOFC) with 10 stacks, but became larger in an SOFC with 20 stacks. In the 10-stack SOFC, the difference of current density between the uniform inlet flow and the curved inlet flow was less than 3%, whereas the deviation in the curved profile was less than 12%. However, in a 20-stack SOFC, the difference of current density was over 20%, whereas the deviation in the curved profile was more than 50%. Comparing the results between the curved and the progressively decreasing inlet profile indicates that the current density difference was over 20% in the 20-stack SOFC, but below 1% in the 10-stack SOFC. Therefore, a progressively decreasing inlet profile can replace a curved profile for analyzing an SOFC stack when the number of stacks is less than 10.     

Treatment of Sulfate/Sulfide-Containing Wastewaters Using a Microbial Fuel Cell: Single and Two-Anode Systems

The microbial fuel cell (MFC) was employed to convert reductive potential in sulfate-laden wastewaters to electricity via reducing sulfate to sulfide by sulfate-reducing bacteria and then oxidizing sulfide to sulfur by exoelectrogens. The excess sulfide presented in the anodic solution inhibited the activities of functional strains in MFC. This study proposed the use of a two-anode system, with a sulfate-reducing bacteria anode and an exoelectrogen (C27) anode in the anodic cell, to efficiently convert reductive potential of sulfate into electricity. The microbial community of sulfate-reducing bacteria anode and the electrochemical characteristics of the studied MFCs were reported.     

Cu~(2+)离子与蛋白质混合体系相互作用机制研究

应用荧光光谱法研究Cu2+离子与血清蛋白质混合组份体系的结合反应机制,测定了反应体系的结合常数K、结合位点数n,探讨了荧光猝灭机理。同时探索了Cu2+与蛋白质混合组份体系及单一组份体系相互作用的差异。结果表明:混合组份体系中,牛血清白蛋白(Bovine serum albumin,BSA)与牛乳铁蛋白(Bovine lactoferrin,BLF)分子间也存在着相互作用,从而影响混合组份体系中BSA/BLF与Cu2+的相互作用,Cu2+与蛋白质混合组份体系相互作用并非蛋白质单组份体系作用之和。分析实验数据,首次发现当BSA/BLF达到临界比值时,金属离子与混合蛋白质组份相互作用过程中出现了蛋白质分子的"契合"现象。文章利用生物酶反应机制中的酶活性部位柔性假说合理解释了Cu2+与血清蛋白质混合组份体系相互作用中的"量敏效应"。     

微生物燃料电池在脱氮方面的研究进展

近年来微生物燃料电池(MFC)处理含氮废水的研究受到了越来越多的关注。文章对用于脱氮MFC的研究进行综述,总结了不同观点的MFC脱氮原理,并与传统生物脱氮技术相比,分析了碳氮比、溶解氧、pH值等因素对MFC脱氮性能的影响,阐述了存在的问题及今后发展前景。     

阴极电极面积和膜面积对H型MFCs产电能力的影响

以生活污水为底物,碳棒作电极,构建H型瓶式微生物燃料电池(microbial fuel cells,MFCs),研究了阴极电极面积和膜面积对电池产电能力的影响.阳极以厌氧污泥作接种体,两室分隔物使用阳离子交换膜(cation exchange membrane,CEM),阳极不使用中介体,阴极使用无催化剂的普通碳电极....     

外加酶强化剩余污泥微生物燃料电池产电特性的研究

以剩余污泥作为接种液和基质,探讨了外加酶(中性蛋白酶、α-淀粉酶)强化单室型剩余污泥微生物燃料电池产电效率的可行性,研究了酶投加量对微生物燃料电池的产电特性及剩余污泥减量的影响.结果表明,在相同条件下,实验组产生的最大功率密度远远高于对照组;当酶的总投加量为10 mg.g-1时,最大输出功率密度及污泥水解效率达到最大,即中性蛋白酶组的最大功率密度、库仑效率、TCOD去除率、TSS去除率、VSS去除率分别为507 mW.m-2、3.98%、88.31%、83.18%、89.03%,而α-淀粉酶组则分别为700 mW.m-2、5.11%、94.09%、98.02%、98.80%.本实验采用向剩余污泥中投加酶的方法,成功增强了微生物燃料电池的产电效率,同时对剩余污泥有效地进行了处理,为微生物燃料电池的实际应用提供了新途径.     

Sulfide oxidation in fluidized bed bioreactor using nylon support material

A continuous fluidized bed bioreactor (FBBR) with nylon support particles was used to treat synthetic sulfide wastewater at different hydraulic retention time of 25, 50 and 75 min and upflow velocity of 14, 17 and 20 m/hr. The effects of upflow velocity, hydraulic retention time and reactor operation time on sulfide oxidation rate were studied using statistical model. Mixed culture obtained from the activated sludge, taken from tannery effluent treatment plant, was used as a source for microorganisms. The diameter and density of the nylon particles were 2-3 mm and 1140 kg/m³, respectively. Experiments were carried out in the reactor at a temperature of (30 ± 2)℃, at a fixed bed height of 16 cm after the formation of biofilm on the surface of support particles. Biofilm thickness reached (42 ± 3) μupm after 15 days from reactor start-up. The sulfide oxidation, sulfate and sulfur formation is examined at all hydraulic retention times and upflow velocities. The results indicated that almost 90%-92% sulfide oxidation was achieved at all hydraulic retention times. Statistical model could explain 94% of the variability and analysis of variance showed that upflow velocity and hydraulic retention time slightly affected the sulfide oxidation rate. The highest sulfide oxidation of 92% with 70% sulfur was obtained at hydraulic retention time of 75 min and upflow velocity of 14 m/hr.     

温拌沥青混合料环境与经济效益分析

为了研究温拌沥青混合料相比热拌沥青混合料产生的环境与经济效益,不仅对它们在拌和与摊铺过程中产生的有害气体排放量的检测数据进行了对比分析,还引用计算CO2排放量的回归方程对沥青混合料在不同生产温度时的CO2排放量进行了计算分析。结果表明:在沥青路面工程中应用温拌沥青混合料具有明显的环境与经济效益。在对我国2009年用于公路建设的沥青消耗量带来的燃料消耗与废气排放量进行计算分析后,认为推广应用温拌沥青混合料对国家公路的绿色建设以及经济的可持续发展都有着重要意义。     

流化床微生物燃料电池基质降解动力学研究

研究了在30℃左右条件下,流化床微生物燃料电池(FBMFC)处理有机废水的基质降解动力学。在空气阴极、单室、无膜液固流化床微生物燃料电池中,以污水和椰壳活性炭为液相和固相,通过实验考察不同水力停留时间的污水COD变化。选取Monod模型和简单动力学模型,通过合理的假设推导出流化床微生物燃料电池处理模拟有机废水时的基质降解动力学模型。将实验数据代入到理论推导得到的动力学模型中,进行线性拟合和对比分析,得到Monod模型和一级反应动力学模型表达式。结果表明流化床微生物燃料电池基质降解为一级反应;Monod模型表达式为:t/s0-st=4.769 7/st+15.885,一级动力学模型为:lnCA=-0.025 32t+8.109 15,理论推导模型与实验数据具有较好的吻合性。