表面过滤技术及其在袋式除尘器上的应用

本文介绍了一种新型的过滤技术(表面过滤技术)在袋式除尘器中的应用及其特点,该技术的采用可减少除尘器的压力损失,提高滤袋的使用寿命和除尘效率.     

染化废水厌氧生物处理技术的研究

鉴于厌氧微生物对偶氮染料的还原裂解作用，开发了以易降解工业有机废水作为外加碳源的染化废水厌氧生物处理的新技术．试验结果表明：在进水ＣＯＤ３１００—３５００ｍｇ／Ｌ，ＣＯＤ总／ＣＯＤ染化比值４０，ＨＲＴ３．０ｄ下，ＣＯＤ去除率＞８０％，最低染化ＣＯＤ去除率＞４５％，色度去除率＞８５％；实验证实，在厌氧处理过程中，染料组分的结构已发生了明显的变化；反应器内的污泥大多呈颗粒状；污泥活性和工艺性能可控制工艺运行参数得以维持．     

Acid resistance of methanogenic bacteria in a two-stage anaerobic process treating high concentration methanol Wastewater

In this study, the two-stage upflow anaerobic sludge blanket (UASB) system and batch experiments were employed to evaluate the performance of anaerobic digestion for the treatment of high concentration methanol wastewater. The acid resistance of granular sludge and methanogenic bacteria and their metabolizing activity were investigated. The results show that the pH of the first UASB changed from 4.9 to 5.8 and 5.5 to 6.2 for the second reactor. Apparently, these were not the advisable pH levels that common methanogenic bacteria could accept. The methanogenic bacteria of the system, viz. Methanosarcina barkeri, had some acid resistance and could still degrade methanol at pH 5.0. If the methanogenic bacteria were trained further, their acid resistance would be improved somewhat. Granular sludge of the system could protect the methanogenic bacteria within its body against the impact of the acidic environment and make them degrade methanol at pH 4.5. The performance of granular sludge was attributed to its structure, bacteria species, and the distribution of bacterium inside the granule. Translated from Acta Scientiae Circumstantiae, 2004, 24(4): 633–636 [译自: 环境科学学报]     

人工生物浮岛载体的研究进展

为改善浮岛性能,减少有机高分子材料所造成的"白色污染",有必要研制开发新型浮岛载体-轻质高效微生物载体.从国内外浮岛的研究现状看,目前在工程实例中广泛采用的是有机高分子材料载体,无机材料的浮岛尚处于实验研究阶段.在对几种典型无机材料-轻质滤料的物理特性、成分、化学稳定性、价格、来源等方面进行综合分析后可知,用无机材料制作有机浮岛载体的替代品是可行的,具有广阔的发展前景,但还需进一步的研究和探索.     

升流式厌氧污泥床筛分强度数学模型研究

通过对升流式厌氧污泥床的流动分析，提出了用离散数Ｄ定量地表示筛分强度。通过实验和回归分析，建立了Ｄ与水力负荷（Ｌ）和沼气沼气容积产量（Ｇ）的数学关系：Ｄ＝０．００３３Ｌ＋０．０４５Ｇ＋０．０７３。当Ｄ在０．０８８－０．０９５之间，用生活污水作基质，成功地培养出了颗粒污泥。     

污泥流化床焚烧产物的重金属排放特性研究

采用小型流化床装置对西湖底泥和四堡污泥进行燃烧实验。用原子吸收法测量污泥及不同温度燃烧产物中Cu、Cr、Cd、Hg等重金属元素,分析金属元素在燃烧过程中的排放特性。     

生物滤池挂膜的生产实践

通过能生物滤池挂膜的工程实践的论述，阐述了生物膜法处理工艺挂膜的机理，并深入分析了在挂膜过程中的一些影响因素，取得了一些相关的运行数据，很好的指导了生产。     

流化床电偶反应器

探讨了流化床电偶反应器的工作原理 ,阐述了流化床电偶反应器的结构特点及工艺性能 ,重点介绍了该反应器对多种有机废水和重金属离子废水净化的作用。     

厌氧酸化-二级PSB流化床工艺处理高浓度有机废水

采用厌氧酸化+二级光合细菌(PSB)流化床的组合工艺对植物压榨发酵废水进行降解实验,一级流化床(PSB1)中填料为轻质多孔炭渣,二级流化床(PSB2)为活性炭,扰动方式分别采用机械流化和机械气动组合流化,稳定运行40d。结果表明,进水酸化12h后CODCr由80000~120000mg/L降至63000~95000mg/L,进而由系统出水回流稀释至8000~12000mg/L,进入二级流化床反应器,PSB1白天厌氧光照、夜间微好氧,PSB2白天微好氧、夜间好氧,停留48h,CODCr降至295.8~384mg/L,稳定实现96.2%以上的CODCr去除率,TN去除率为71.3%。     

Biological pretreatment of Yellow River water

Bio-ceramic filter(BF) and moving-bed biofilm reactor(MBBR) were used for biological pretreatment of Yellow River water in this study. The BF only had slight advantage over MBBR for TOC and ammonia removal. However, like UV254, the average removal rate of THMFP in the BF was much higher than that in the MBBR. UV254 removal did not show obvious correlation with trihalomethane formation potential(THMFP) removal. Hexachlorocyclohexane could be effectively removed in both BF and MBBR. As for diatom and cyanobateria removal the MBBR had better performance than the BF, which was contrary to the average chlorophyll-a(Chl-a) removal rate. The proposal was made in this study that biological flocculation and sedimentation of sloughed biofilm should play a more important role on algae removal in the MBBR than in the BF. The BF and MBBR could effectively remove microcystins. Moreover, MBBR could be a promising technology for biological pretreatment.