共查询到19条相似文献,搜索用时 62 毫秒
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厌氧生物膜法处理聚酯高浓度废水 总被引:3,自引:0,他引:3
采用上流式厌氧生物膜工艺处理PET聚酯生产高浓度废水实际运行情况,表明厌氧生物膜法抗冲击负荷能力较强,温度低于30℃仍有较高的去除率,微碱性有利于甲烷菌的生长。 相似文献
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厌氧流化床处理硫酸盐草浆废水的研究 总被引:7,自引:0,他引:7
本文研究了AFB反应器在中温(30±2)℃条件下处理硫酸盐草浆废水的性能,其达到的指标为:当进水COD浓度2000~5000mg/L,水力停留时间3~9h,COD去除率为50.1%~70.2%,容积产气率1.46~2.0m3/m3·d,有机容积负荷达43.2kgCOD/m3·d;并初步研究了废水中SO2-4、S2-等物质对厌氧生物的抑制作用,提出了消除其影响的方法。 相似文献
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综述了厌氧流化床(AFB)在国内外的研究现状,AFB作为现代微生物固定化技术与传质流化技术的产物,讨论了其相关的理论及实际操作问题,分析了反应存在的问题和今后的发展方向。 相似文献
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M. Fuentes N. J. Scenna P. A. Aguirre M. C. Mussati 《Chemical Engineering Communications》2008,195(6):600-621
This work deals with an experimental and theoretical investigation of anaerobic biofilm reactors for treating wastewaters. Bioreactors are modeled as dynamic (gas-solid-liquid) three-phase systems. The anaerobic digestion model proposed by Angelidaki et al. (1999) was selected to describe the substrate degradation scheme and was applied to a biofilm system. The experimental setup consists of two mesophilic (36°±1°C) lab-scale anaerobic fluidized bed reactors (AFBRs) with sand as inert support for biofilm development. The experimental protocol is based on step-type disturbances applied on the inlet substrate concentration (glucose and acetate-based feeding) and on the feed flow rate considering the criterion of maximum efficiency. The predicted and measured responses of biological and hydrodynamic variables are investigated. Experimental data were used to estimate empirical values of biofilm detachment coefficients. Under the evaluated operating conditions, the proposed model for biofilm detachment rate, assumed as a first-order function of the energy dissipation parameter, is appropriate to represent the interaction between biofilm systems and fluidization characteristics in non-highly disturbed flow conditions. Model validation was carried out using the experimental data reported by Mussati et al. (2006). The results do not differ from those above. This seems to indicate that the proposed AFBR model is able to reproduce the main biological and hydrodynamic successes in the bioreactor. 相似文献
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This work deals with an experimental and theoretical investigation of anaerobic biofilm reactors for treating wastewaters. Bioreactors are modeled as dynamic (gas-solid–liquid) three-phase systems. The anaerobic digestion model proposed by Angelidaki et al. (1999) was selected to describe the substrate degradation scheme and was applied to a biofilm system. The experimental setup consists of two mesophilic (36°±1°C) lab-scale anaerobic fluidized bed reactors (AFBRs) with sand as inert support for biofilm development. The experimental protocol is based on step-type disturbances applied on the inlet substrate concentration (glucose and acetate-based feeding) and on the feed flow rate considering the criterion of maximum efficiency. The predicted and measured responses of biological and hydrodynamic variables are investigated. Experimental data were used to estimate empirical values of biofilm detachment coefficients. Under the evaluated operating conditions, the proposed model for biofilm detachment rate, assumed as a first-order function of the energy dissipation parameter, is appropriate to represent the interaction between biofilm systems and fluidization characteristics in non-highly disturbed flow conditions. Model validation was carried out using the experimental data reported by Mussati et al. (2006). The results do not differ from those above. This seems to indicate that the proposed AFBR model is able to reproduce the main biological and hydrodynamic successes in the bioreactor. 相似文献
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The effects of a magnetic field on wastewater treatment with a fluidized bed biofilm reactor was investigated. With glucose being the sole carbon source, the activated sludge obtained from a real wastewater treatment plant was used as a seed. Magnetically loaded polystyrene beads at the size of 500-595 μm were used as support materials for biofilm formation in a fluidized bed biofilm reactor. Magnetic field application allowed the operation of the column at high liquid flow rates, thus external diffusion limitations on the biofilm surface were lowered and the efficiency of biodegradation was increased. Denser, thinner, and more active biofilm was obtained with magnetic field application, especially in pulsed form. As expected, the system performance changed with operational parameters, and the increase in substrate removal reached up to 26% with pulsed application of a 17.8 mT DC-magnetic field under optimum conditions. 相似文献
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流化式反应器生物膜特性的研究 总被引:6,自引:0,他引:6
本文在采用流化式生物膜反应器进行连续流废水处理试验的同时,研究了探讨了生物膜特性,进一步为流化式生物膜废水处理法的应用与开发提供实验依据。 相似文献
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论述了快速床区流体动力学的结构,研究了快速床区纵向和横向悬浮密度分布的规律及相应的计算公式。对影响快速床区动力学结构的主要因素,如固体颗粒的循环率、气体速度等进行了试验研究,对循环流化床锅炉的设计和运行有一定的指导意义。 相似文献