共查询到16条相似文献,搜索用时 125 毫秒
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啤酒厂厌氧池(UASB)的调节与恢复 总被引:1,自引:0,他引:1
针对某啤酒厂污水处理过程中使用的升流式厌氧池(UASB)进行了调节与恢复,通过监测厌氧池的pH与COD等数据找出UASB反应器处理效果差的原因,然后对三相分离器、布水管等进行调整,并二次启动厌氧池,恢复了UASB反应器的处理功能. 相似文献
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高浓度厌氧反应器流场的数值模拟 总被引:2,自引:1,他引:1
本文对高浓度搅拌桨厌氧反应器流场进行了数值模拟,计算采用多重参考系法和标准k-ε湍流方程。模拟结果表明,与牛顿流体形成的单循环流动相比,在反应器内的非牛顿流体形成了两个循环流动,这不利于厌氧反应器内的混合。在整个反应器内的湍流特性分布不均匀,局部湍动比较剧烈。在设计高浓度厌氧反应器时应考虑非牛顿流体特性的影响。 相似文献
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本文对侧伸式高浓度厌氧反应器流场进行了数值模拟,计算采用多重参考系法和标准k-ε湍流方程。模拟结果表明,由于高浓度流体具有牛顿流动特性,流体只在反应器底部形成了循环流动,在整个反应器内的湍流特性分布不均匀。在相同条件下,牛顿流体能够形成整体循环,湍流特性比较均匀。 相似文献
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近年来,有机污水处理技术的应用越来越广泛,尤其是高、中浓度有机污水处理领域。UASB(upflow anaerobic sludge blanket technique)污水处理技术,即上流式厌氧污泥床污水处理技术,主要用于处理高浓度有机废水。该技术是荷兰学者Lettinga等人在1980年提出的,它具有结构简单、负荷率高、水力停留时间短、能耗低和无需污泥回流装置等特点。目前,国外投入运行的生产性试验都取得了较好效果,投入运行的生产性装置已达数百座。国内在应用UASB反应器处理有机工业废水方面也做了大量的试验研究工作,总的来看,工业性生产装置建造的数量有限,尤其在工程实践中如何提高UASB反应器的处理效果、使设备稳定运行等方面的经验不多。 相似文献
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采用小型动态厌氧反应器(UASB)法和直接混凝两种方法对生物制药产生的废水进行预处理试验研究。结果表明:针对COD cr浓度为18000mg/L的废水,经USBA系统20小时处理,排放水质能达到COD cr≤5000mg/L以下。 相似文献
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本文研究IC反应器快速进行二次启动的方法及启动前后反应器内颗粒污泥性质的变化.研究结果表明,由于反应器内成功滞留了大量活性高、沉降性能好的颗粒污泥,二次启动可在15天内完成,反应器负荷可达12-15kg/m3·d,COD去除率可达80%以上,启动后反应器内颗粒污泥的最大比产甲烷活性几乎为初期4倍. 相似文献
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INTRODUCTION limiting conditions, obligatory aerobic and an- aerobic bacteria will survive in a mixed culture Sequential anaerobic/aerobic wastewater treat- (Gerritse et al., 1992). Little is know about thement has received increasing attention for effective change in the activity of anaerobic bacteria whennutrient removal, enhanced de… 相似文献
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陈红 《浙江大学学报(A卷英文版)》2004,5(6):727-732
Specific ATP content of volatile solids was measured to characterize the sludge activity in a sequential anaerobic/aerobic wastewater treatment system, with an upflow anaerobic sludge blanket (UASB) reactor and a three-phase aerobic fluidized bed (AFB) reactor. The wastewater COD level was 2000(3000 mg/L in simulation of real textile wastewater. The ATP content and the specific ATP contents of volatile solids at different heights of the UASB reactor and those of the suspended and immobilized biomass in the AFB reactor were measured. In the UASB reactor, the maximum value of specific ATP (0.85 mg ATP/g VS) was obtained at a hydraulic retention time (HRT) 7.14 h in the blanket solution. In the AFB reactor, the specific ATP content of suspended biomass was higher than that of immobilized biomass and increased with hydraulic retention time reaching a maximum value of 1.6 mg ATP/g VS at hydraulic retention time 4.35 h. The ATP content of anaerobes in the UASB effluent declined rapidly under aerobic conditions following a 2nd-order kinetic model. 相似文献
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Different two-equation k-ε models were used to simulate the gas flow field generated by a new type of circulating fluidized bed reactor with venturi gas distributor. The numerical results were compared with the experimental data. It has been shown that the simulation results from the standard k-ε model have the best match with the experimental data. Based on this model, the gas flow field in the venturi diffuser and riser was analyzed by the concept of velocity nonuniformity and dead zone percentage. Both the nonuniformity of gas velocity and the dead zone percentage reach the maximum at the venturi outlet due to the effect of the vortex. At the same time, it provides a good platform for the further optimization of the inlet configuration of circulating fluidized bed reactor. 相似文献
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气固并流顺重力场与逆重力场流动形成了迥然不同的流态化机制.与提升管相比,下行床具有气固速度及颗粒浓度径向分布较均匀、气固停留时间短而一致等特点,其流型更接近平推流. 相似文献