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111.
Dawei LIANG Yanyan LIU Sikan PENG Fei LAN Shanfu LU Yan XIANG 《Frontiers of Environmental Science & Engineering》2014,8(4):624-630
A biocathode with microbial catalyst in place of a noble metal was successfully developed for hydrogen evolution in a microbial electrolysis cell (MEC). The strategy for fast biocathode cultivation was demonstrated. An exoelectrogenic reaction was initially extended with an H2-full atmosphere to enrich Ha-utilizing bacteria in a MEC bioanode. This bioanode was then inversely polarized with an applied voltage in a half-cell to enrich the hydrogen-evolving biocathode. The electrocatalytic hydrogen evolution reaction (HER) kinetics of the biocathode MEC could be enhanced by increasing the bicarbonate buffer concentration from 0.05 mol·L-1 to 0.5 mol· L-1 and/or by decreasing the cathode potential from -0.9 V to - 1.3 V vs. a saturated calomel electrode (SCE). Within the tested potential region in this study, the HER rate of the biocathode MEC was primarily influenced by the microbial catalytic capability. In addition, increasing bicarbonate concentration enhances the electric migration rate of proton carriers. As a consequence, more mass H+ can be released to accelerate the biocathode-catalyzed HER rate. A hydrogen production rate of 8.44 m3. m 3. d1 with a current density of 951.6 A. m-3 was obtained using the biocathode MEC under a cathode potential of - 1.3 V vs. SCE and 0.4 mol· L-1 bicarbonate. This study provided information on the optimization of hydrogen production in biocathode MEC and expanded the practical applications thereof. 相似文献
112.
曝气条件下采用微电解-Fenton工艺处理模拟染料废水。在最佳微电解工艺即铁炭比为45 g∶45 g,pH=3,反应时间为60 min;在Fenton工艺pH值为3,H2O2投加量0.7 mL,反应时间为120 min时,染料废水总脱色率达92%,其色度去除率高于单独微电解工艺时的63%和单独Fenton工艺时的67%。模拟染料废水经微电解及Fenton工艺处理后,废水pH值、Fe2+浓度和色度均发生变化。 相似文献
113.
114.
Jiqin Wang Xiaoxia Yi Xiangfei Zeng Shuyuan Chen Rui Wang Jiancheng Shu Mengjun Chen Zhengxue Xiao 《Frontiers of Environmental Science & Engineering》2021,15(6):117
115.
Ling Wang Chunxue Yang Sangeetha Thangavel Zechong Guo Chuan Chen Aijie Wang Wenzong Liu 《Frontiers of Environmental Science & Engineering》2021,15(4):56
116.
Jingya SHEN Yuliang SUN Liping HUANG Jinhui YANG 《Frontiers of Environmental Science & Engineering》2015,9(6):1084-1095
Cobalt and copper recovery from aqueous Co(II) and Cu(II) is one critical step for cobalt and copper wastewaters treatment. Previous tests have primarily examined Cu(II) and Co(II) removal in microbial electrolysis cells (MECs) with abiotic cathodes and driven by microbial fuel cell (MFCs). However, Cu(II) and Co(II) removal rates were still slow. Here we report MECs with biocathodes and driven by MFCs where enhanced removal rates of 6.0±0.2 mg?L−1?h−1 for Cu(II) at an initial concentration of 50 mg?L−1 and 5.3±0.4 mg?L−1 h−1 for Co(II) at an initial 40 mg?L−1 were achieved, 1.7 times and 3.3 times as high as those in MECs with abiotic cathodes and driven by MFCs. Species of Cu(II) was reduced to pure copper on the cathodes of MFCs whereas Co(II) was removed associated with microorganisms on the cathodes of the connected MECs. Higher Cu(II) concentrations and smaller working volumes in the cathode chambers of MFCs further improved removal rates of Cu(II) (115.7 mg?L−1?h−1) and Co(II) (6.4 mg?L−1?h−1) with concomitantly achieving hydrogen generation (0.05±0.00 mol?mol−1 COD). Phylogenetic analysis on the biocathodes indicates Proteobacteria dominantly accounted for 67.9% of the total reads, followed by Firmicutes (14.0%), Bacteroidetes (6.1%), Tenericutes (2.5%), Lentisphaerae (1.4%), and Synergistetes (1.0%). This study provides a beneficial attempt to achieve simultaneous enhanced Cu(II) and Co(II) removal, and efficient Cu(II) and Co(II) wastewaters treatment without any external energy consumption. 相似文献
117.
铁炭微电解法降解1-丁基-3-甲基咪唑六氟磷酸盐 总被引:2,自引:0,他引:2
使用铁炭微电解法降解1-丁基-3-甲基咪唑六氟磷酸盐([BMIM]PF6),并探讨了铁炭微电解法降解[BMIM]PF6的影响因素、工艺条件及其反应动力学.结果表明,影响铁炭微电解降解[BMIM]PF6的因素按从大到小的顺序为:炭铁比、pH、反应时间;铁炭微电解降解[BMIM]PF6的最佳工艺条件是:铁粉用量3g.l-1、水样pH2.5、炭铁比2、反应时间为60—90min;在此条件下,[BMIM]PF6的去除效率可以达到90%以上且该降解反应为三级反应. 相似文献
118.
电解法处理废料贵铅的电极极化研究 总被引:1,自引:1,他引:0
以含金银铅废料制成贵铅为原料,利用电化学热力学和动力学理论,对贵铅电解法实现金银与铅的分离和得到纯铅的电极过程极化行为与工艺条件的关系进行了研究。从而确定了贵铅电解时的电解液组成为[pb2+]70g/L,温度为40℃,β-萘酚/胶联合添加剂等工艺条件.同时根据动力学的研究证明了贵铅电解的电极反应速度受扩散控制,其扩散速度常数K扩=1.917×10-3cm/s。扩散层厚度为0.0051cm,在ηk=75mV时的阴极过程活化能为16.10kJ/mol,为贵铅电解工业分离回收金银铅提供了可靠的理论依据和设计参数。 相似文献
119.
曝气催化铁内电解法预处理混合化工废水 总被引:8,自引:0,他引:8
采用曝气催化铁内电解法对上海某工业污水场的进水进行预处理,降低了后续生化处理中难降解有机物的负荷,并较大程度地去除了正磷酸盐。废水中的有机物及正磷酸盐在两周的稳定运行中平均去除率分别达到52%和70%。废水经预处理后,pH平均上升0.5。 相似文献
120.