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负荷对膜曝气生物反应器去除有机物和硝化的影响 总被引:1,自引:0,他引:1
讨论了在模拟生活废水的浓度阶段性变化的情况下,有机物负荷以及氮负荷对膜曝气生物反应器的有机物去除和硝化的影响。结果表明,TOC负荷和TN负荷分别从6.6 g/(m2.d)和3.2 g/(m2.d)到26g/(m2.d)和5.8g/(m2.d)变化,碳氮质量比从2.1到4.6变化时,得到94%~97%的TOC去除率。碳氮质量比从2.1到3.7变化时,硝化率约为90%;当碳氮质量比增加到4.6时,硝化率降到81%。在第一阶段,碳氮质量比为2.85,TN负荷从2.5到9.5 g/(m2.d)变化时,TOC去除率为95%。最大硝化速率和硝化率分别为7.5 g/(m2.d)和90%。和传统的生物膜比较,用膜曝气生物反应器处理废水,可同时提高有机物去除速率和硝化速率。 相似文献
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为探究膜生物反应器(MBR)进行厌氧氨氧化的可行性及性能,通过逐渐提高进水NH_4~+-N、NO_2~--N的含量和降低HRT,成功启动了自流出水式MBR厌氧氨氧化过程,分析了反应器脱氮效果和厌氧氨氧化污泥特性,并采用扫描电镜和X射线光电子能谱中空纤维膜表面进行分析。结果表明,经过60 d的启动,NH_4~+-N、NO_2~--N和TN的去除率分别达到96.22%、99.91%和81.66%,TN去除负荷最大可达到330 g/(m~3·d)。在启动过程中,污泥颜色逐渐变为红褐色;中空纤维膜表面厌氧氨氧化菌呈不规则的椭球状,结构紧凑;MBR运行稳定阶段末期中空纤维膜表面C、N和Ca特征峰增多,是膜污染化学组分的主要构成元素。 相似文献
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无泡式中空纤维膜生物反应器(Membrane-aerated biofilm reactor,MABR)有效地将生物膜法污水处理技术和膜分离技术结合在一起,其具有无泡曝气和硝化反硝化一体的优点。回顾了MABR的发展历程,分析了MABR的基本结构和原理,介绍了MABR常用的膜材料及氧传质系数模型,阐述了MABR的影响因素,综述了国内外MABR的研究与应用现状,指出了MABR需要解决的问题并展望了该技术的未来发展。 相似文献
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Jiawei Zhu Shaobin Guo Gongping Liu Zhengkun Liu Zhicheng Zhang Wanqin Jin 《American Institute of Chemical Engineers》2015,61(8):2592-2599
To accelerate the commercial application of mixed‐conducting membrane reactor for catalytic reaction processes, a robust mixed‐conducting multichannel hollow fiber (MCMHF) membrane reactor was constructed and characterized in this work. The MCMHF membrane based on reduction‐tolerant and CO2‐stable SrFe0.8Nb0.2O3‐δ (SFN) oxide not only possesses a good mechanical strength but also has a high oxygen permeation flux under air/He gradient, which is about four times that of SFN disk membrane. When partial oxidation of methane (POM) was performed in the MCMHF membrane reactor, excellent reaction performance (oxygen flux of 19.2 mL min?1 cm?2, hydrogen production rate of 54.7 mL min?1 cm?2, methane conversion of 94.6% and the CO selectivity of 99%) was achieved at 1173 K. And also, the MCMHF membrane reactor for POM reaction was operated stably for 120 h without obvious degradation of reaction performance. © 2015 American Institute of Chemical Engineers AIChE J, 61: 2592–2599, 2015 相似文献
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Zhentao Wu Irfan M.D. Hatim Benjamin F.K. Kingsbury Ejiro Gbenedio K. Li 《American Institute of Chemical Engineers》2009,55(9):2389-2398
A novel inorganic hollow fiber membrane reactor (iHFMR) has been developed and applied to the catalytic dehydrogenation of propane to propene. Alumina hollow fiber substrates, prepared by a phase inversion/sintering method, possess a unique asymmetric structure that can be characterized by a very porous inner surface from which finger-like voids extend across ∼80% of the fiber cross-section with the remaining 20% consisting of a denser sponge-like outer layer. In contrast to other existing Pd/Ag composite membranes, where an intermediate γ-Al2O3 layer is often used to bridge the Pd/Ag layer and the substrate, the Pd/Ag composite membrane prepared in this study was achieved by coating the Pd/Ag layer directly onto the outer surface of the asymmetric substrate. After depositing submicron-sized Pt (0.5 wt %)/γ-alumina catalysts in the finger-like voids of the substrates, a highly compact multifunctional iHFMR was developed. Propane conversion as high as 42% was achieved at the initial stage of the reaction at 723 K. In addition, the space-time yields of the iHFMR were ∼60 times higher than that of a fixed bed reactor, demonstrating advantages of using iHFMR for dehydrogenation reactions. © 2009 American Institute of Chemical Engineers AIChE J, 2009 相似文献
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Yuan Li Mingzhi Zhang Yuanyuan Chu Xiaoyao Tan Jun Gao Shaobin Wang Shaomin Liu 《American Institute of Chemical Engineers》2018,64(10):3662-3670
Cost‐effective and robust nickel (Ni) membrane for H2 separation is a promising technology to upgrade the conventional H2 industries with improved economics and environmental benignity. In this work, Ni hollow fibers (HFs) with one closed end were fabricated and assembled into a membrane module for pure H2 separation by applying vacuum to the permeate side. The separation behavior of the HF module was investigated both experimentally and theoretically. Results indicate that H2 recovery can be improved significantly by changing the operation conditions (temperature or feed pressure). Ni HF is a promising membrane geometry, but the negative effect of pressure drop when H2 passes through the lumen cannot be ignored. Under the vacuum operation mode, there is little difference in term of H2 recovery efficiency whether the feed gas flow is controlled in countercurrent or recurrent operation. This work provides important insight to the development of superior membrane H2 separation system. © 2018 American Institute of Chemical Engineers AIChE J, 64: 3662–3670, 2018 相似文献
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