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1.
Environmental Science and Pollution Research - One of the main problems facing our planetary bodies is unexpected and sudden climate change due to continuously increasing global energy demand,...  相似文献   

2.
Environmental Science and Pollution Research - The need for power is rising on a daily basis all across the world. Due to the finite supply of fossil fuels, it is critical to develop innovative...  相似文献   

3.
微生物燃料电池在污水处理中的研究进展   总被引:1,自引:0,他引:1  
微生物燃料电池(microbial fuel cell,MFC)利用微生物催化剂将其代谢能直接转化为电能,具有原料广泛、反应条件温和、清洁高效等优点。简述了MFC的工作原理及分类,总结了用于污水处理的MFC的性能及其影响因素。探讨了MFC在实际应用中的瓶颈,并展望其在污水处理中的应用前景。  相似文献   

4.
微生物燃料电池(microbial fuel cell,MFC)利用微生物催化剂将其代谢能直接转化为电能,具有原料广泛、反应条件温和、清洁高效等优点.简述了MFC的工作原理及分类,总结了用于污水处理的MFC的性能及其影响因素.探讨了MFC在实际应用中的瓶颈,并展望其在污水处理中的应用前景.  相似文献   

5.
双室微生物燃料电池处理硝酸盐废水   总被引:2,自引:1,他引:2  
基于双室微生物燃料电池(microbial fuel cell,MFC),针对阴极分别接种活性污泥(A-MFC)和反硝化细菌(D-MFC),研究其产电情况和硝酸盐废水去除效果。结果表明,在产电的同时都可有效去除废水中的硝酸盐污染物。在外接电阻100Ω的情况下,2种MFC均具有良好的产电性能,A-MFC和D-MFC达到的最大输出电压分别为119.6 mV和117.2mV,最大功率密度分别为23.40 mW/m2和26.63 mW/m2;同时两者在阴极室的平均反硝化速率分别为1.86 mg/(L.d)和2.19 mg/(L.d),阳极室的平均COD去除率分别为81.9%和82.4%。另外,通过扫描电镜观察可知,A-MFC和D-MFC阴极碳布表面形貌存在差异,并且阳极与阴极碳布表面形貌差异显著。  相似文献   

6.
A coupled model of biological and settling phases aimed at optimal design of predenitrification systems is presented. Each unknown is obtained in explicit form, and is expressed as a function of the system's required performance. A model, taking into account both suspended and dissolved substrates, is adopted for the biological phase, while the limiting solid flux theory is assumed for the design of the settling phase. Finally, a relationship correlating the two phases is obtained expressing opportunely the sludge recycle flow and the sludge waste flow, without recourse to empirical parameters. The effect of different influent and effluent wastewater characteristics on the model's results is also analyzed.  相似文献   

7.
构建了双室微生物燃料电池(double microbial fuel cells,DMFC)型毒性传感器分别对Cr(Ⅵ)、Cd2+、Cu2+、Zn2+进行在线检测研究。通过对反应器进行优化,确定DMFC在外电阻为1 000 Ω时达到最大功率密度;外循环速率为0.933 4 mL·min-1时反应器运行较稳定。在最优条件下,通过监测铜离子来确定检测时间为60 min,清洗时间为10 min。在以上条件下进行重金属检测,结果表明4种重金属的检测范围分别为0.3~10、0.4~10、40~160、15~80 mg·L-1。抑制率可以用来验证反应器的可行性,检测范围内抑制率与重金属浓度呈现一定的线性关系,其相关系数分别为0.959 7、0.979 5、0.944 1、0.936 6。并可得到相应的线性方程,这些方程可用于验证DMFC-传感器的稳定性。选取检测范围内的浓度进行验证,结果表明4种重金属的相对误差均小于11%,传感器相对稳定并可长期运行。  相似文献   

8.
Environmental Science and Pollution Research - The microbial fuel cell (MFC) system is a promising environmental remediation technology due to its simple compact design, low cost, and renewable...  相似文献   

9.
Production of electricity from proteins using a microbial fuel cell.   总被引:4,自引:0,他引:4  
Electricity generation was examined from proteins and a protein-rich wastewater using a single chamber microbial fuel cell (MFC). The maximum power densities achieved were 354 +/- 10 mW/m2 using bovine serum albumin (BSA) and 269 +/- 14 mW/m2 using peptone (1100 mg/L BSA and 300 mg/L peptone). The recovery of organic matter as electricity, defined as the Coulombic efficiency (CE), was comparable to that obtained with other substrates with CE = 20.6% for BSA and CE = 6.0% for peptone. A meat packing wastewater (MPW), diluted to 1420 mg/L chemical oxygen demand, produced 80 +/- 1 mW/m2, and power was increased by 33% by adding salt (300 mg/L sodium chloride) to increase solution conductivity. A wastewater inoculum generated 33% less power than the MPW inoculum. The MFC was an effective method of wastewater treatment, demonstrated by >86% of biochemical oxygen demand and total organic carbon removal from wastewater.  相似文献   

10.
Eom H  Chung K  Kim I  Han JI 《Chemosphere》2011,85(4):672-676
In an effort to improve the efficiency and sustainability of microbial fuel cell (MFC) technology, a novel MFC reactor, the M2FC, was constructed by combining a ferric-based MFC with a ferrous-based fuel cell (FC). In this M2FC reactor, ferric ion, the catholyte in the MFC component, is regenerated by the FC system with the generation of additional electricity. When the MFC component was operated separately, the electricity generation was maintained for only 98 h due to the depletion of ferric ion in the catholyte. In combination with the fuel cell, however, the production of power was sustained because ferric ion was continually replenished from ferrous ion in the FC component. Moreover, the regeneration process of ferric ion by the FC produced additional energy. The M2FC reactor yielded a power density of up to 2 W m−2 (or time-averaged value of approximately 650 mW m−2), density up to 20 times (or approximately six times based on time-averaged value) higher than the corresponding MFC system.  相似文献   

11.
炼油废水微生物燃料电池启动及影响因素   总被引:1,自引:0,他引:1  
以炼油废水为碳源,构建双室填料型微生物燃料电池,考察接种液、外接电阻等电池启动条件,以及电导率、pH值和缓冲溶液强度等溶液性质对电池产电性能的影响。利用微生物燃料处理炼油废水,COD去除率(52±4)%,含油量去除率(81.8±3)%;利用废水中存在的原生菌即可启动电池,但启动期长,外加接种液可快速启动电池;启动时外接电阻的大小对电池稳定运行后的输出功率有明显影响,对电池内阻影响相对较小,当启动外接电阻为2 000Ω,电池输出功率最大,为288 mW/m3;随阳极溶液电导率电池增大,电池内阻降低,输出功率升高;pH值变化对电池阳极电势影响较大,进而影响电池输出,当溶液pH为9时,电池输出电压最大(388 mV),pH过高或过低均不利于电池产电;随着缓冲强度的增大,电池输出电压增大,且PBS缓冲强度的增大可从电导率增大和改善质子传递条件两方面提高电池的输出功率。  相似文献   

12.
为考察藻种类及阴极材料对藻阴极型微生物燃料电池性能的影响,以微藻及水绵为阴极生物,分别采用碳毡,碳纸,载铂碳纸为阴极材料,构建了微生物燃料电池。结果显示,以碳毡作为阴极材料时,2种藻阴极微生物燃料电池最大功率密度均高于以碳纸为阴极材料时相应的功率密度。采用载铂碳纸为阴极材料、天然湖水为阴极液,微生物燃料电池最大功率密度分别达到165.1 mW/m2(微藻阴极)和119.9 mW/m2(水绵阴极)。电化学测试表明,藻类生长形态影响了阴极的电化学特征,进而影响到了微生物燃料电池的性能。藻阴极MFC长期运行时,膜污染是藻阴极微生物燃料电池功率密度下降的关键因素之一。SEM-EDS分析显示,膜两侧污染主要原因分别是微生物生长和磷酸盐晶体沉积。  相似文献   

13.
生物电化学技术修复石油污染土壤并同步产出电能是一种新兴的污染土壤生态修复技术。对石油污染土壤通过其微生物燃料电池的构造,利用电化学阻抗谱分析了土壤的欧姆内阻,拟合估算了土壤的电导率,并考察了土壤微生物燃料电池的产电性能和修复效果。结果表明:采用丙酮清洗过的阳极并有水封的情况下,土壤微生物燃料电池的欧姆内阻下降了52%,电导率升高了1倍;在启动后的120 h内,最大电压和累计产出电量分别达189 mV和36 C,与对照相比分别增加了20和29倍。输出电压随着阴极与阳极之间距离的增大而减小。经过30 d的生物电化学处理,土壤中的总石油烃去除率是开路对照的3.3倍。该研究是石油污染盐碱土壤生物电化学修复的初步探索,以为污染土壤的生态修复提供新的思路。  相似文献   

14.
构建一种微生物燃料电池(MFC),首先将对氯酚在阴极室降解为苯酚,随后将阴极处理液在阳极室降解。研究了对氯酚废水经过阴阳双室分步处理后的去除效果和该MFC的产电性能,结果表明,在外电阻1 000 Ω时,阴极脱氯阶段最大输出电压为216 mV,产电周期为132 h;阳极降解阶段最大输出电压为277 mV,产电周期为48 h,对氯酚的总去除率为96.2%。实验结果表明该MFC能较好处理对氯酚废水,且与传统的生化处理技术相比,有较大的优势。  相似文献   

15.
微生物燃料电池(MFC)是一种将废水中化学能转化为电能的技术,近年来被证实可以用来同步脱氮。目前,NH4+-N的硝化与反硝化多是在MFC阴极室进行,其存在曝气条件下反硝化菌难以富集的问题,造成反硝化速度慢。为解决上述问题,本研究旨在构建一种基于阴离子交换膜的(AEM)MFC,即AEM-MFC,使阴极好氧硝化过程产生的NO2-与NO3-能通过阴离子交换膜迁移至厌氧阳极室,并在厌氧阳极室发生还原,使得反硝化不需在好氧阴极室进行。结果表明,当阴极投加200 mg/L NH4+-N时,AEM-MFC能在66 h完全去除总氮,而同样条件下基于阳离子交换膜(CEM)的MFC,即CEM-MFC,则需要26 d达到相同的脱氮效果。在阴极室投加不同浓度NH4+-N(从50到500 mg/L)条件下,AEM-MFC连续运行7个月,其产电与脱氮效果稳定。相比于传统生物脱氮方法,AEM-MFC不需要在运行过程中在加入酸或碱调节pH,所需COD/N较少,并能够同时回收电能。  相似文献   

16.
基于双室微生物燃料电池(microbial fuel cells,MFCs),以高盐榨菜废水为燃料,考察了电池的运行状况,同时探讨了盐度变化对电池产电性能影响,并通过投加甜菜碱研究其对MFCs系统抵抗盐度负荷冲击能力的影响。结果表明:MFCs稳定运行时(阳极室容积80 mL),最大功率密度、开路电压和电池内阻分别为3.55 W·m-3、0.698 V和427 Ω;底物中添加2 mmol·L-1甜菜碱后电池产电性能得到明显提升;当废水含盐量(增加到5 g·L-1 NaCl)为31.2 g·L-1时电池产电性能达到最佳,但是继续增高盐度后电池产电性能会急剧下降;投加甜菜碱有助于提高系统抵抗盐度负荷变化造成的冲击,维持电池的产电输出。  相似文献   

17.
Chèvre N  Brazzale AR 《Chemosphere》2008,72(5):803-810
Modeling concentration-response function became extremely popular in ecotoxicology during the last decade. Indeed, modeling allows determining the total response pattern of a given substance. However, reliable modeling is consuming in term of data, which is in contradiction with the current trend in ecotoxicology, which aims to reduce, for cost and ethical reasons, the number of data produced during an experiment. It is therefore crucial to determine experimental design in a cost-effective manner. In this paper, we propose to use the theory of locally D-optimal designs to determine the set of concentrations to be tested so that the parameters of the concentration-response function can be estimated with high precision. We illustrated this approach by determining the locally D-optimal designs to estimate the toxicity of the herbicide dinoseb on daphnids and algae. The results show that the number of concentrations to be tested is often equal to the number of parameters and often related to the their meaning, i.e. they are located close to the parameters. Furthermore, the results show that the locally D-optimal design often has the minimal number of support points and is not much sensitive to small changes in nominal values of the parameters. In order to reduce the experimental cost and the use of test organisms, especially in case of long-term studies, reliable nominal values may therefore be fixed based on prior knowledge and literature research instead of on preliminary experiments.  相似文献   

18.
Changes in the characteristics of algae-derived organic matter (AOM) were examined upon the operation of a microbial fuel cell (MFC) using multiple analytical methods. Temporal variations in the UV absorption and fluorescence excitation–emission matrix of the AOM revealed that less condensed humic-like components and large-sized protein-like fluorescent compounds were preferentially decomposed over the period of electricity generation. They also showed that low UV-absorbing extracellular organic matters (EOM) were produced at the end of the operation. SEC chromatograms demonstrated that smaller-sized UV-absorbing components were initially decomposed, followed by the net production of EOM with an intermediate molecular weight. Fourier transform infrared (FT-IR) spectra showed that proteins and polysaccharides were the two most dominant structures of the AOM in the MFC. Two-dimensional correlation spectroscopy combined with FT-IR provided additional valuable information on the sequential changes of the AOM, which occurred in the order of proteins → acidic functional groups → polysaccharides → amino acids/proteins.  相似文献   

19.
膜生物反应器(MBR)是一种高效的污水处理工艺,而微生物燃料电池(MFC)能利用NO-3作为电子受体进行脱氮。为解决膜生物反应器(MBR)脱氮效率低和膜污染问题,建立了一套能够进行脱氮、有效抑制膜污染的一体式MFC-好氧MBR新工艺。以开路MFC-MBR反应器为对照,对耦合系统中污水处理效果、膜污染情况进行研究。研究表明,2套系统的COD去除率均超过88%,对NH4-N的去除均达到99%。闭路MFC-MBR系统TN去除率达到69.4%,高于开路系统的55.3%。混合液的MLVSS/MLSS稳定在88%左右,同时耦合系统能够改善污泥混合液的性质,zeta电位的绝对值和粘度较开路系统有所减少,污泥颗粒平均体积粒径(233.482μm)较开路系统(94.877μm)有明显增加,膜清洗周期延长了41.17%。  相似文献   

20.
一体式MFC-好氧MBR运行效果及膜污染特性   总被引:1,自引:0,他引:1  
膜生物反应器(MBR)是一种高效的污水处理工艺,而微生物燃料电池(MFC)能利用N0i作为电子受体进行脱氮。为解决膜生物反应器(MBR)脱氮效率低和膜污染问题,建立了一套能够进行脱氮、有效抑制膜污染的一体式MFC-好氧MBR新工艺。以开路MFC—MBR反应器为对照,对耦合系统中污水处理效果、膜污染情况进行研究。研究表明,2套系统的COD去除率均超过88%,对NH4-N的去除均达到99%。闭路MFC—MBR系统TN去除率达到69.4%,高于开路系统的55.3%。混合液的MLVSS/MLSS稳定在88%左右,同时耦合系统能够改善污泥混合液的性质,zeta电位的绝对值和粘度较开路系统有所减少,污泥颗粒平均体积粒径(233.482μm)较开路系统(94.877μm)有明显增加,膜清洗周期延长了41.17%。  相似文献   

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