内循环厌氧反应器快速启动研究

本研究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/m^3.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。     

内循环厌氧反应器快速启动研究

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.     

ASBR反应器启动的研究

对有效容积为100L的中试规模ASBR反应器的启动方法和启动过程中颗粒污泥性质进行了研究。结果表明，反应器经过100d的启动运行，洗出沉降性能差的颗粒污泥，保留了大量活性高、沉降性能好的颗粒污泥，启动结束时反应器的有机负荷达到10gCOD／（L·d），COD去除率达859／6以上。反应器启动结束后，颗粒污泥的性质发生了显著变化：颗粒污泥平均直径由0．78mm增加到1．18mm，颗粒污泥沉降速度最大达到70．2m／h，比产甲烷活性几乎是接种颗粒污泥的4倍。     

IC反应器快速启动的试验研究

采用麸皮纤维作载体来启动IC反应器可促进厌氧污泥的颗粒化进程,加快IC反应器的启动．试验研究表明,投加麸皮纤维的IC反应器所需启动时间仅为41d,比不投加麸皮纤维的IC反应器提前了20d;投加麸皮纤维的IC反应器最高处理容积负荷是不投加麸皮纤维的IC反应器的1．38倍．     

同步脱氮微氧颗粒污泥的快速培养及供氧条件的影响

为了快速培养出能同时去除生活污水中化学需氧量(COD)和氮的微氧颗粒污泥,采用膨胀颗粒污泥床(EGSB)反应器接种污水处理厂剩余污泥,研究了微氧颗粒污泥的培养过程以及稳定运行条件下供氧量对处理效果和污泥性能的影响。结果表明,水力停留时间(HRT)为6h,微氧颗粒污泥的成功培养仅需1个月;供氧速率在2.8³.2gO2/d,COD,NH3-N和总氮(TN)的去除率最高分别可达91%,85%和81%,脱氮速率达1.7gN/d,出水水质最佳;成熟的微氧颗粒污泥粒径集中在0.453.2gO2/d,COD,NH3-N和总氮(TN)的去除率最高分别可达91%,85%和81%,脱氮速率达1.7gN/d,出水水质最佳;成熟的微氧颗粒污泥粒径集中在0.45²mm,当供氧速率低于2.3gO2/d时,颗粒污泥结构致密,供氧速率在2.32mm,当供氧速率低于2.3gO2/d时,颗粒污泥结构致密,供氧速率在2.3³.2gO2/d时,污泥性能稳定,供氧速率增加到3.2gO2/d时,污泥沉降性能下降,并出现颗粒解体和丝状菌生长优势。     

UASB工艺处理木薯酒精废液生产运行发现

论述了总有效容积2000m3的新型UASB装置,在中温条件下处理高浓度木薯酒精废水的启动运行和污泥含量控制的过程．当反应器稳定运行时,容积负荷可达7kgCOD／（m3·d）,水力停留时间为2d,污泥保持量在30％-41;％,COD去除率达95％以上,出水COD小于500mg／L．     

微氧颗粒污泥+硅藻土去除氨氮的研究

向两级EGSB反应器中投加硅藻土,考察焦化废水中氨氮的去除效果及影响因素。结果表明,当硅藻土投加量为0.5 g/L或5 g/L,两级反应器进水量均为1 L/h,上升流速分别为3.2 m/h、2.9 m/h的条件时,水力停留时间为12 h,可使出水中氨氮浓度达到排放标准。     

油田污水处理厂含油污泥处理研究

对目标污泥进行试验分析,获得最佳工艺条件后将含油污泥在经搅拌后静置分离,原油回收,泥水经机械脱水过滤。过滤后油泥利用氧化钙将除油后污泥在干燥反应器内发生的热化学反应,将细胞水在反应器内大部分蒸发,达到脱水、杀菌等目的。利用微波加热器将部分低温蒸汽加热至250℃以供再次强化干燥。经试验测定,经增钙干化后处理污泥含水率控制在35%以内。     

一体式生物膜反应器生物强化反硝化研究

在反应器挂膜启动阶段和运行阶段投加好氧反硝化菌纯培养物,进行生物强化反硝化研究。结果表明,在反应器启动过程中投加好氧反硝化菌,可缩短系统的启动时间;在反应器运行过程中间歇投加好氧反硝化菌能提高系统对污染物的去除效果,同时可增强系统处理的稳定性。     

工程实践中提高UASB反应器处理效率的研究

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。     

Quick start-up of EGSB reactor treating fresh leachate of municipal solid waste

An expanded granular sludge bed (EGSB) reactor inoculated with anaerobic granular sludge was started up with its COD removal performance, self-balancing of pH, biogas production rate and characteristics of the granular sludge during the start-up period being investigated. The results indicated that the EGSB reactor can be started up successfully in 27 d by increasing the organic loading rate rapidly. The removal efficiency of COD was maintained above 93% with influent COD concentration of 25 000 mg/L and OL...     

嗜高浓度甲醛废水的活性污泥净化性能研究

对培养嗜高浓度甲醛废水的活性污泥的净化性能进行了研究,研究中采用序批式活性污泥法（SBR）及脱氮除磷工艺（A2/O工艺）．考察了停留时间、溶解氧多少、进水的pH值和水温等对微生物净化高浓度甲醛废水的影响。实验结果表明,进水的pH值在7～9范围内,水温在10～30℃,停留时间控制在48小时,并根据进水浓度的变化选择合适的溶解氧,获得的活性污泥的净化性能最佳。     

IC多功能污水厌氧实验装置的研制

研制了一种用于生活污水或有机工业废水厌氧处理研究的多功能实验装置，该装置可作为IC反应器和UASB反应器分别用于研究在一定的处理效果下的工艺参数的确定、运行参数的确定、颗粒污泥特性研究、三相分离器性能研究、环形布水器性能研究、沼气产率分析等，为学生掌握厌氧污水处理技术提供了坚实的实验基础。     

Technological feasibility of biodiesel production from bioaugmented hydrolysate of waste sludge in a municipal wastewater treatment plant

The hydrolysate of waste sludge was used as the feedstock of biodiesel production, and its technological feasibility was investigated. Waste sludge, collected from No.3 Municipal Wastewater Treatment Plant of Xi＇an, was hydrolyzed in two parallel reactors firstly. Yeast was added into one reactor for bioaugmentation, and the other reactor without yeast was used as a control. Then an acid-catalyzed in situ esterification process was carried out to convert the hydrolysate to biodiesel. The results of hydrolysis showed that the reactor bioaugmented with yeast could promote hydrolysis compared with the control one because of an obvious variance in total suspended solid （TSS）, volatile suspended solid （VSS） and soluble chemical oxygen demand （SCOD）. Furthermore, gas chromatography （GC） analysis exhibited that the total volatile fatty acid （VFA） was low in the hydrolysate of bioaugmentation reactor; however, its yield of the fatty acid methyl esters （FAMEs） by in situ esterification was obviously higher when compared with the control one. Therefore, it may be inferred that the hydrolysate of bioaugmentation was mainly inclined to longer-chain fatty acid rather than to VFA. Anyway, an FAMEs yield of 9.24% （wt%） from dried sludge was attained after the 12-d bioaugmentation hydrolysis and succedent esterification. This value was not only higher than that of the control one but also higher than that reported in previous literature. The above results illuminated that it was feasible to produce biodiesel from the bioaugmented hydrolysate of waste sludge.     

Activating lignite and sludge by electro-hydraulic impulse

1. Introduction At present, it is necessary to use fertilizer to ensure the stable and high agricultural productivity. However, as we all know, the fertilizer not only decreases the self-fertility of soil, but also is accompanied with pesticide. Food poisoning caused by remnant pesticide in fruits and vegetables is often reported, and in such cases, chronic poisoning is the majority. The remnant pesticide accumulates in body gradually, and then induces kinds of disease. As reported, the Miyu…     

Characterization of the start-up period of single-step autotrophic nitrogen removal in a sequencing batch reactor

The characteristics of the start-up period of single-step autotrophic nitrogen removal process were investigated. The autotrophic nitrogen removal process used a sequencing batch reactor to treat wastewater of medium to low ammonia-nitrogen concentration, with dissolved oxygen （DO）, hydraulic retention time （HRT） and temperature controlled. The experimental conditions were temperature at （30±2） ℃, ammonia concentration of （60 to 120） mg/L, DO of （0.8 to 1.0） mg/L, pH from 7.8 to 8.5 and HRT of 24 h. The rates of nitrification and nitrogen removal turn out to be 77% and 40%, respectively, after a start up period going through three stages divided according to nitrite accumulation： sludge domestication, nitrifying bacteria selection and sludge adaptation, It is demonstrated that dissolved oxygen is critical to nitrite accumulation and elastic YJZH soft compound packing is superior to polyhedral hollow balls in helping the bacteria adhere to the membrane.     

厌氧折流板反应器的工艺特性及其应用

综合讨论了厌氧折流板反应器(ABR)工艺特征,阐述了国内外关于ABR启动及实际应用的研究现状。认为ABR具有耐冲击负荷、对有毒物质适应性强、固液分离效果好等显著特点。因此,ABR作为一种新型高效生物处理技术,在我国废水处理中,特别是对高浓度有毒工业废水处理具有良好的研究开发价值。