污泥中重金属的稳定化研究进展与去除方法简述

通过"十一五"污水处理厂的建设,我国污泥产量也随之大幅增长,污泥的处理处置已经成为制约社会经济发展的重要问题。国际上的经验表明土地利用是污泥最终处置的主要发展方向,然而污泥中的重金属成为其土地利用的主要障碍。越来越多的研究者意识到,重金属的环境危害不仅仅取决于其总量,更取决于重金属存在形态。目前,Tessier分步提取法作为主流的污泥重金属划分方法,取得了广泛应用,该法将污泥中的重金属分成5种形态,分别为可交换态、碳酸盐结合态、铁锰氧化物结合态、有机结合态和残渣态。本文以此为基础综述了目前国内外主要的污泥重金属稳定和去除方法的原理及研究进展,比较了不同重金属稳定及去除方法的优点与不足,并提出了新的展望。     

3种载体固定化菌藻共生系统脱氮除磷效果的对比

采用3种不同载体（海藻酸钠、聚乙烯醇、复合载体）,分别将小球藻和栅藻与活性污泥固定成菌藻共生系统,制成菌藻凝胶小球,单独菌、单独藻的凝胶小球,用于处理人工污水。结果表明,（1）复合载体固定的菌藻共生系统氮磷去除效果最好,PVA载体的脱氮除磷效果次于复合载体优于海藻酸钠;（2）固定化菌藻共生系统的脱氮除磷效果明显优于单独固定菌和单独固定藻,固定菌的效果较差;（3）3种载体包埋下的固定化小球藻的脱氮除磷效果均较相同载体固定化的栅藻效果好。     

天然黄铁矿的除磷性能

除磷是控制水体富营养化的重要手段。为了考察黄铁矿的除磷特征,采用序批实验,分别研究了反应时间、初始磷浓度和干扰离子（NH4＋、NO3- 和SO24-）对黄铁矿除磷的影响。动力学表明,黄铁矿的除磷过程符合伪二级动力学模型。pH=6．5时,磷的平衡去除量为6．82mg／kg。Langmuir方程能较好描述黄铁矿除磷的吸附等温过程,其磷的饱和吸附量为11．01mg／kg。NH4＋、NO3-和SO24- 对黄铁矿除磷基本没有影响。磷的去除主要是通过铁磷沉淀和铁氧化物及氢氧化物的吸附,去除的磷主要以可被生物利用的Fe、Al-P形态存在。黄铁矿的这些除磷性能和机制对选取黄铁矿作为人工湿地填料实现同步脱氮除磷具有重要指导作用。     

曝气沉砂池除砂机理分析

针对曝气沉砂池小试装置模型,通过配砂实验对沉砂池除砂率进行统计分析,研究曝气强度与HRT对沉砂池除砂率的影响。实验结果表明,不同曝气强度下,随着HRT变化,除砂率逐渐上升,并最终趋于平衡状态;不同HRT下,曝气强度与除砂率近似呈现一定的线性关系,且随着曝气强度的增大,除砂率降低;在HRT小于1min时,砂粒的运行路径和沉降时间缩短,不利于砂粒的去除;在HRT大于1min时,其中1、3和4min,随着气水比的增加除砂率降低幅度相对较小,曝气所引起的横向环流在一定程度上有利于砂粒的沉降,而HRT为2min时,除砂率降幅却很大,这与砂粒在曝气沉砂池池体断面分布有关,即断面处旋转流速和水平流速的大小变化将影响砂粒的运动;相比曝气强度,HRT对除砂率的影响较大。     

2种新分离微藻的生长、氮磷去除和营养特性的比较研究

为了解2种新分离微藻的净化和资源化潜力,研究比较了其生长、氮磷去除和营养特性。结果表明,栅藻和月牙藻的最大生物量（干重）分别为0．78g／L和0．53g／L;最大生物量（干重）增长速率分别为0．05g／（L·d）和0．03g／（L·d）。培养至第23天,栅藻和月牙藻对TN的去除率分别为85．1％和72．5％;对TP的去除率为82．6％和79．7％,但栅藻较月牙藻更易释放较多的No2--N进入藻液。稳定期时,栅藻、月牙藻的粗蛋白质含量和粗蛋白产量（干重）分别为31．8％、19．2％和0．24g／L、0．09g／L;粗脂含量和粗脂产量（干重）分别为7．81％、9．26％和0．06g／L、0．05g／L。综上,与月牙藻相比,栅藻具有明显的生长、氮磷去除和营养优势,在进行水产养殖废水的净化和资源化利用上可作为优选藻种。     

碳氮磷比失调对污水生物脱氮除磷的影响

我国南方城市污水普遍存在低碳相对高氮磷特征,本文介绍了同时生物脱氮除磷的机理、对碳源的需求与竞争,以及一些针对此类污水生物脱氮除磷的改进工艺及其在实际运用中的效果,并对此类污水的处理方向进行了展望。     

Dairy washwater treatment using a horizontal flow biofilm system

In Ireland, dairy farmyard washwater commonly comprises farmyard run-off and dairy parlour washings. Land-spreading is the most widely used method for treating this wastewater. However, this method can be labour intensive and can cause, in some cases, the degradation of surface and ground waters, mainly due to nitrogen contamination. In this study, a horizontal flow biofilm reactor (HFBR) with step-feed was constructed and tested in the laboratory, to remove organic carbon and nitrogen from a agricultural strength synthetic washwater (SWW). The HFBR had an average top plan surface area (TPSA) of 0.1002 m(2) and consisted of a stack of 45 polystyrene horizontal sheets--15 sheets embedded with 25 mm deep frustums above 30 sheets with 10 mm deep frustums. The frustums acted as miniature reservoirs. The sheets were alternately offset to allow the wastewater to flow horizontally along each sheet and vertically from sheet to sheet down through the reactor. Biofilms developed on the sheets and treated the wastewater. During the 212-d study, the total hydraulic loading rate based on the TPSA of the sheets was 35 l m(-2) d(-1). SWW was pumped for 10 min each hour, in a step feed arrangement at a rate of 23.33 l m(-2) d(-1) on to the top sheet during Phases 1 and 2, and 11.67 l m(-2) d(-1) onto Sheet 16 during Phase 1 (days 1-92) and onto Sheet 30 during Phase 2 (days 93-212). The substrate loading rate during Phases 1 and 2 was 94.8 g total chemical oxygen demand (COD) m(-2) d(-1) and 10.5 g total nitrogen (TN) m(-2) d(-1), based on the TPSA. At steady state in Phase 2, the unit achieved excellent carbon removal of 99.7% 5-day biochemical oxygen demand (BOD(5)) and 96.7% total COD, equivalent to TPSA removal rates of 67.5 g BOD(5)m(-2)d(-1) and 91.7 g COD m(-2) d(-1). The nitrogen removal percentages were 98.3% total ammonium-nitrogen (NH(4)-N(t)) and 72.8% TN, which equated to TPSA removal rates of 4.8 g NH(4)-N(t) m(-2) d(-1) and 7.6g TN m(-2) d(-1). No sloughing of solids or clogging of media occurred during the study. The unit was simple to construct and operate, with little maintenance.     

燃煤锅炉湿式脱硫除尘一体化设备的综合分析

本文对湿式脱硫除尘一体化设备的结构和性能进行了较为全面的分析,指出了该设备存在的诸多弊病,提出了解决方案--脱硫、除尘分体组合式的思路.     

Modification of ferrite–manganese oxide sorbent by doping with cerium oxide

Fe–Mn oxide and Ce-doped Fe–Mn oxide sorbents were studied on the structural and desulfurization behavior in COS removal from syngas. The effects of cerium oxide on the Fe–Mn oxides have been investigated by XRD, BET, TPR, XPS and TEM methods. Analysis data show that the Ce-doped sorbent has larger specific surface area and better particles’ dispersion compared with non-modified Fe–Mn sorbent. The addition of Ce improves the reduction performance of Fe–Mn species. The desulfurization experiments show that the desulfurization activity of sorbent can be increased because of the promotion of the structural and redox properties by ceria doped. The Ce-doped sorbent can reduce COS from 15,000 ppmv to less than 0.1 ppmv at 325 °C and a space velocity of 1000 h⁻¹.     

DDTC—TX—100胶束增溶直接光度法测定水中低含量铜

ＴｒｉｔｏｎＸ１００对ＤＤＴＣ（二乙基二硫代氨基甲酸钠）与铜反应生成的络合物Ｃｕ（ＤＤＴＣ）２有增溶增敏作用,建立了低含量铜直接光度测定法。操作简便快速,选择性、精密度和回收率均较好,相对标准偏差为０８％～４３％,回收率为９６％～１０６％,摩尔吸光系数ε＝６４×１０３Ｌ／（ｍｏｌ·ｃｍ