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。     

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.     

UBAF与纤维球过滤结合工艺应用于污水回用的试验研究

利用升流式曝气生物滤池 (UBAF)与纤维球过滤相结合的工艺对城市污水进行深度处理 ,使其达到回用的要求。结果表明 :对于经过二级处理后的可生物降解性较差的城市污水 ,应用UBAF和纤维球过滤相结合的处理工艺能够取得很好的效果 ,处理后的污水完全可以达到污水排放的一级标准和城市生活杂用水的标准     

造气含氰废水的生物治理

在塔式生物滤池生产性处理规模上考察了造气含氰废水在挂膜前后的处理效果。比较结果表明，未挂过氰化物的平均处理率仅为７９．２９％，挂膜后的处理率平均为９５．２６％，处理后的废水全部回用于生产，减少了氰化物的排放量，防止了造气废水对环境的污染。     

Effect of catalyzed diesel particulate filter and its catalyst loading on emission characteristics of a non-road diesel engine

In this study, the effects of a diesel oxidation catalyst (DOC) coupled with a catalyzed diesel particulate filter (CDPF) with different catalyst loadings on the power, fuel consumption, gaseous and particulate emissions from a non-road diesel engine were investigated. Results showed that the after-treatment had a negligible effect on the power and fuel consumption. The reduction effect of the DOC on the CO and hydrocarbon (HC) increased with the engine load. Further reductions occurred coupling with the CDPF. Increasing the catalyst loading resulted in a more significant reduction in the HC emissions than CO emissions. The DOC could increase the NO₂ proportion to 37.9%, and more NO₂ was produced when coupled with the CDPF below 250°C; above 250°C, more NO₂ was consumed. The after-treatment could reduce more than 99% of the particle number (PN) and 98% of the particle mass (PM). Further reductions in the PN and PM occurred with a higher CDPF catalyst loading. The DOC had a better reduction effect on the nucleation particles than the accumulation ones, but the trend reversed with the CDPF. The DOC shifted the particle size distribution (PSD) to larger particles with an accumulation particle proportion increasing from 13% to 20%, and the geometric mean diameter (GMD) increased from 18.2 to 26.0 nm. The trend reversed with the CDPF and the accumulation particle proportion declined to less than 10%. A lower catalyst loading on the CDPF led to a higher proportion of nucleation particles and a smaller GMD.     

唐钢一炼钢厂VD精炼炉直接冷却水系统设计

介绍了VD精炼炉直接冷却水处理常用的工艺流程及设计中应重点考虑的问题 ,如水处理单元的选择 ,供水泵与提升泵的匹配问题等     

污染源废气中氟的监测方法研究

本文叙述了有组织废气中氟化物的测定方法。该法用碱性滤膜捕集氟化物，使现场操作大为简化，并使精密度和准确度都比溶液吸收法有较大改善。本文给出了方法的研究结果，最后给出方法的操作程序     

基于TMS320F240 DSP的电网谐波抑制全数字化控制的研究

为治理电力系统谐波污染 ,提高电力系统运行的安全稳定性 ,笔者对混合式并联有源电力滤波系统的结构和工作原理进行了分析和研究。该系统由无源滤波器和小容量有源滤波器串联构成 ,与被补偿的谐波负载并联连接。基于TMS32 0F2 4 0DSP开发套件 ,设计数字控制器主程序和中断服务子程序。实验结果表明 ,采用TMS32 0F2 4 0DSP编程方便并直观 ,运算精度高 ,控制器参数调整方便 ,易于实现各种控制策略。研究成果对DSP在有源电力滤波系统中的应用有重要参考价值。     

滤膜法测定空气中氟化物的改进

测定环境空气中微量氟的方法一般采用滤膜法，但此法工作量大，针对这种情况，本文作两点改进：一是将采集的两张滤膜同时测定；二是将测定过程中的搅拌时间缩短，这样不影响测定结果的准确性，而且降低了工作量。     

过滤捕集法处理含DEP雾废气的研究

为了探讨玻璃纤维过滤器处理含DEP雾废气的效率问题,在实验室进行了DEP雾去除实验。考查了不同气体入口浓度、过滤流速下玻璃纤维过滤捕集装置对含DEP雾废气的净化能力,结果表明:利用玻璃纤维过滤器去除DEP雾,在DEP雾粒径主要分布为0.48～3.4μm之间,DEP雾浓度小于220 mg/m3,过滤流速小于10 cm/s情况下,玻璃纤维过滤器对DEP雾的去除率大于99%,最大气体流量下的压力降小于1610Pa;同时对含油(酸)雾废气除雾效果好,特别是对于粒径特别细微的油(酸)雾,捕集效率也很高,还可回收利用,不会产生二次污染。