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三相复合生物流化床反应器处理废水性能研究 总被引:8,自引:0,他引:8
提出和设计了一种新型的自充氧式复合生物流化床反应器,将该反应器应用于合成废水的处理,考察了反应器的挂膜以及停留时间、气水比,容积负荷等对COD去除率的影响,研究结果表明,该反应器在处理废水时,停留时间可达2h和1.5h,COD容积负荷提高到8.56和12.63kg/d.m^3,效率比同类反应器高1倍以上,气水比也有所下降,仅为32-34,具有停留时间短,能耗低,是一种高效的新型生物流化床反应器。 相似文献
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Claudio Garibay‐Orijel Elvira Ríos‐Leal Jaime García‐Mena Hctor Mario Poggi‐Varaldo 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》2005,80(10):1180-1187
A fluidized bed bioreactor (FBBR) was operated for more than 575 days to remove 2,4,6‐trichlorophenol (TCP) and phenol (Phe) from a synthetic toxic wastewater containing 80 mg L?1 of TCP and 20 mg L?1 of Phe under two regimes: Methanogenic (M) and Partially‐Aerated Methanogenic (PAM). The mesophilic, laboratory‐scale FBBR consisted of a glass column (3 L capacity) loaded with 1 L of 1 mm diameter granular activated carbon colonized by an anaerobic consortium. Sucrose (1 g COD L?1) was used as co‐substrate in the two conditions. The hydraulic residence time was kept constant at 1 day. Both conditions showed similar TCP and Phe removal (99.9 + %); nevertheless, in the Methanogenic regime, the accumulation of 4‐chlorophenol (4CP) up to 16 mg L?1 and phenol up to 4 mg L?1 was observed, whereas in PAM conditions 4CP and other intermediates were not detected. The specific methanogenic activity of biomass decreased from 1.01 ± 0.14 in M conditions to 0.19 ± 0.06 mmolCH4 h?1 gTKN?1 in PAM conditions whereas the specific oxygen uptake rate increased from 0.039 ± 0.008 in M conditions to 0.054 ± 0.012 mmolO2 h?1 gTKN?1, which suggested the co‐existence of both methanogenic archaea and aerobic bacteria in the undefined consortium. The advantage of the PAM condition over the M regime is that it provides for the thorough removal of less‐substituted chlorophenols produced by the reductive dehalogenation of TCP rather than the removal of the parent compound itself. Copyright © 2005 Society of Chemical Industry 相似文献
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The effects of oxygen supply conditions and specific biofilm interfacial area on the phenol removal rate in a three‐phase fluidized bed bioreactor were evaluated. The experimental data were well‐explained by the semi‐theoretical equation based on the assumption that the reaction rate follows first‐order reaction kinetics with respect to oxygen and zero‐order one with respect to phenol. Two cases, biological reaction as rate‐controlling step and oxygen absorption as rate‐controlling step, were both explicable by this semi‐theoretical equation. The maximum volumetric phenol removal rate was 27.4 kg·m?3·d?1. 相似文献
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作者介绍了采用三相生物流经床工艺处理苎麻污水的实例,处理后水中的COD和BOD浓度均低于《污水综合排标准》GB8978-88。该工艺流程简单,投资规模小,无二次污染。实践证明:这一方法用于苎麻污水处理是非常成功的,有很主的实用价值。 相似文献
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Jun Li Jing Kong Qingshan Zhu Hongzhong Li 《American Institute of Chemical Engineers》2017,63(2):459-468
A two‐stage, fluidized reduction route is proposed to synthesize iron nanoparticles (NPs), with the aim of enhancing the quality of fluidization and preventing sintering activity. At both low and high temperatures, the degree of metallization η is approximately 80% due to the defluidization. Defluidization is mainly caused by the rapid sintering of the newly formed Fe NPs. The proposed two‐stage fluidization approach successfully resolves the defluidization problem through the self‐agglomeration of nanoparticles cultivated at low temperatures. These self‐agglomerated NPs showed an improved resistance to sintering at high temperatures. The high‐purity Fe NPs prepared by this approach exhibited excellent combustion activity, indicative of the potential as oxygen carriers in chemical looping combustion systems. © 2016 American Institute of Chemical Engineers AIChE J, 63: 459–468, 2017 相似文献
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磁稳流化床(MSFB)作为一种新型反应器,兼具固定床和流化床的众多优点,具有巨大的应用前景。本文综述了MSFB近年来在基础研究和应用上取得的进展。基础研究方面主要介绍了磁场强度和液相流速对床层结构的影响,以及床层空隙率、操作稳定性和传递特性等研究情况;应用方面介绍了MSFB在生物化工、能源和环境工程等领域的应用。最后分析了MSFB目前存在的不足,如对于一定的反应体系未找到相应合适的磁性催化剂、操作温度高于磁性载体的居里温度时,MSFB将无法操作、磁场发生装置释放出大量的热量对磁性载体和反应过程产生影响、难以确定稳定操作区域。并指出其今后的主要研究方向为磁性载体催化剂的研究与开发及对MSFB的稳定性判据、传热、传质、强化反应过程机理、反应器放大规律、工业化应用装置设计等方面的研究。 相似文献
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Plamen I. Grigorov Benjamin J. Glasser Fernando J. Muzzio 《American Institute of Chemical Engineers》2013,59(12):4538-4552
A manufacturing method is presented for solid dosage forms using fluidized‐bed impregnation, which could eliminate many of the challenges during solid dosage manufacturing. The main difference between impregnation and dry blending is the placement of the active pharmaceutical ingredient (API) inside a porous carrier. This makes the final material flow properties independent of the physical properties of the API. The method consists of spraying an API solution in appropriate solvent onto a carefully chosen porous excipient in a fluidized state. The solution penetrates the porous carrier due to capillary forces and the solvent is evaporated soon after that. Impregnation and drying occur simultaneously, which makes this impregnation method suitable for continuous implementation. Carefully choosing the operating conditions allows impregnation to occur without introducing spray drying or spray coating of the API. The method is shown to generate an impregnated excipient with very high degree of homogeneity independent of the API loading. It is also shown that mild milling further improves blend uniformity to RSD levels below 1%, which are challenging to achieve using conventional techniques. On impregnation, the final physical properties of the material are seen to be mainly unchanged from the initial excipient properties. A study of this one‐step manufacturing method is described, using acetaminophen as the model drug and anhydrous calcium phosphate dibasic as the porous excipient. The experimental work presented establishes a proof of concept and investigates in detail blend uniformity, physical state of impregnated API, final physical properties of impregnated material, compressibility during tableting, capsule filling, and release profile of the final capsule formulation. It also discusses potential ways for drug release control and improvements using impregnation. © 2013 American Institute of Chemical Engineers AIChE J, 59: 4538–4552, 2013 相似文献
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在内径 1 86mm、高 9m的提升管中 ,通过改变操作气速获得湍动流化床、快速流化床和稀相输送典型的操作状态 ,使用光纤密度探头在轴向不同截面的不同径向位置处测得密度脉动时间序列 ,以反映不同流型下 ,不同浓、稀相区的瞬态动力学行为 .利用确定性混沌理论分析了局部密度脉动信息 ,以Kolmogorov熵定量地表征系统的动力学特征 .实验结果表明 ,Kolmogorov熵随流型的变化能正确地反映相应流型的特点 ,可用来描述不同流型下的流动结构 .在忽略壁面附近行为的条件下 ,对 3种流型、不同的浓稀相区 ,局部熵值随局部固含率变化可分为两个区 :当局部固含率高于 0 0 5时 ,熵几乎不随局部固含率的变化而变化 ;当局部固含率低于 0 0 5时 ,熵随局部固含率的减小而急剧增大 .这说明系统的混沌特征与局部固含率关系密切 ,局部固含率对系统局部动态行为起控制作用 . 相似文献
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In this study, a pure culture of Zoogloea ramigera was grown as a film on active carbon particles in a differential fluidized bed biofilm reactor (DFBBR) as a novel experimental system for the application of diffusion-reaction models. The effective diffusion coefficients of the essential substrates; glucose, ammonium ion and oxygen in the active biofilm were simultaneously calculated. The values of effective diffusion coefficients in the active biofilm to those in water varied between 13–34, 48–96 and 28–48% for glucose, ammonium ion and oxygen, respectively, at different biofilm densities, which is in fair agreement with the literature. 相似文献
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阐述了大颗粒尿素的特点及当今世界上生产大颗粒尿素的主要造粒工艺,对海德鲁、东洋工程公司造粒工艺与双转鼓流化工艺大颗粒尿素技术进行了比较,对大颗粒尿素的前景进行了展望。 相似文献
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以Fe(NO3)3·9H2O、Fe2O3和Fe3O4为前驱体,凹凸棒(ATP)为惰性载体制备了系列Fe2O3/ATP载氧体。在流化床反应器内,以水蒸气作为气化-流化介质,900℃为还原温度,研究了载氧体与神木煤的反应活性及循环反应性能,同时考察了载氧体的抗磨损性能。实验结果表明:以Fe(NO3)3·9H2O为前驱体制备的Fe4ATP6(N)载氧体具有很高的反应活性和抗磨损能力。对其进行的10次还原/氧化循环实验表明:尾气中CO2平均含量先下降后升高,但都保持在95%以上,停留时间t95从14.8 min增加到16.1 min。SEM分析表明随着循环反应的进行载氧体表面小颗粒变成大颗粒,发生轻微烧结。 相似文献
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昭通褐煤气化扩大试验研究 总被引:1,自引:2,他引:1
针对昭通褐煤的特点 ,在气化煤量为 0 .3t/h的焦载热流化床气化扩大试验装置上进行了试验研究 .研究结果表明 ,煤气中焦油量很小 ,有利于煤气生产的后期处理 ;与移动床气化和普通流化床气化相比 ,煤气热值和气化产率都有较大增加 ,煤气热值已接近城市煤气的要求 ;加大气化煤量可增加提升段燃烧的易燃成分 ,从而提高了燃烧温度和气化温度 ;气化煤量的变化对褐煤气化产率和产量的影响较大 .对于开发昭通褐煤资源来说 ,采用本工艺技术生产城市煤气是一个较佳的方案 . 相似文献
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《分离科学与技术》2012,47(15):3307-3320
Abstract Dissolved organic matters and ammonia nitrogen are serious contaminants of surface water in Taiwan. These contaminants can interfere with the water treatment process and cause biological instability in the finished water. One solution is to employ a biological treatment stage prior to the conventional water treatment process. A continuous flow biological filter packed with reticulated PU foam was used to remove ammonia nitrogen and organic materials before the conventional water treatment practice. The effect of its operation mode, namely, empty bed contact time (EBCT) and backwash, on the removal efficiencies of ammonia and organic matter was examined. The results suggested that ammonia nitrogen and organic nitrogen can be effectively removed by controlling the operation mode of the biological fixed bed. Efficient ammonia nitrogen removal was achieved upon the combination of the backwash mode with short EBCT or extended EBCT without the backwash. Efficient organic nitrogen and DOC removals were observed at short EBCT without the backwash. This study provides insights into the function of biofiltration, which benefits the design of a fixed‐bed bioreactor for the treatment of polluted surface water. 相似文献
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利用微型流化床反应装置,结合快速过程质谱仪,在850~940℃操作温度下,研究了三种不同粒度分布烟煤和无烟煤在热解、气化和燃烧反应条件下四种主要气态氮产物HCN、NH3、NO和NO2的释放规律。结果表明,微型流化床可以实时检测挥发分氮和焦炭氮的动态释放序和类型,热解、气化和燃烧反应气氛的改变主要影响HCN和NH3的释放量。热解产物的气态氮主要是来自于挥发分,燃烧反应的HCN和NH3的释放量与温度有明显关系,而气化反应的各类气态氮释放量随温度变化波动不大。煤颗粒尺寸和温度变化对烟煤和无烟煤中各类气态氮释放量产生影响比较复杂,其中NH3的释放特性是区分挥发分N释放和半焦N释放的重要特征。 相似文献