机构地区: 四川大学建筑与环境学院,四川成都610065
出 处: 《环境科学与技术》 2017年第7期126-130,共5页
摘 要: 试验采用厌氧流化床-生物阴极型双室微生物燃料电池(AFB-MFC)反应器,研究模拟废水的COD、NH3-N的去除效果和产电性能。结果表明,以葡萄糖为底物,在阳极室的COD容积负荷为5.0~10.0 kg/(m^3·d),HRT分别为16 h和24 h的条件下,AFB-MFC系统的厌氧流化床部分对COD的去除有很好的效果,COD去除率始终稳定在95%以上。阴极室对于NH3-N有很好的效果,平均去除率达到95%,阳极室对于NH3-N的去除在50%左右。系统在进水COD为5 000 mg/L,阳极室的COD容积负荷为5.0 kg/(m^3·d),阴极室为1.2 kg/(m^3·d)时产电效果最好。电压最高可达340 mV,能持续稳定产电70 h,功率密度为12.8 mW/m^2。另外,通过扫描电镜观察到厌氧生物颗粒中大部分为杆菌,其余为球形菌和丝状菌等。 A bench-scale experiment was conducted by using an apparatus of a biological-cathode-type double chamber microbial fuel cell (MFC) combined with an anaerobic fluidized bed (AFB) reactor, aiming at enhancing the MFC's power generation ability and removing pollutants (NH3-N, COD) from wastewater. As a result, the experiment showed that with glucose as a sort of substrate, under the operation condition: volume loading of COD in the anode chamber ranging from 5.0 to 10.0 kg/(m^3·d), and HRT of 16 h and 24 h, respectively, the system of AFB-MFC presented a very good effect of COD removal, and COD removal rate remained at more than 95%, a good removal of NH3-N (95%) also took place in cathode chamber while removal of NH3-N in the anode chamber is about 50%. Furthermore, when the system was operated under the condition as the influent COD concentration being 5 000 mg/L, the COD volume load in the anode chamber, 5.01 kg/(m^3· d), and in the cathode chamber, 1.19 kg/(m^3^d), the best power production effect could be achieved, the voltage being high up to 340 mV, which sustained for 70 h, and the power density reached 12.8 mW/m^2. In addition, most of the anaerobic granules were formed by bacillus in AFB reactor, and the rest were spherical bacteria and filamentous bacteria according to the scanning electron microscopy.