联合NaOH和Ca(OH)2强化剩余污泥厌氧发酵生产挥发性脂肪酸

以剩余污泥为研究对象,在序批式厌氧反应器中探究了NaOH和Ca（OH）2联合作用对污泥厌氧发酵产挥发性脂肪酸（VFA）的影响。结果表明,相较于NaOH单独发酵,NaOH和Ca（OH）2的联合作用能够进一步促进VFA的积累,且NaOH和Ca（OH）2的质量比例为50：50时,VFA的最大积累量为286 mg COD·g-1VSS。机理研究表明,NaOH和Ca（OH）2联合作用能够促进污泥溶解过程,并且溶解性COD（SCOD）的最大含量为3 650 mg·L-1,同时NaOH和Ca（OH）2联合作用能够促进胞外聚合物内部有机物向外部的转移。NaOH和Ca（OH）2联合作用能够进一步遏制产甲烷古菌的活性,甲烷的最大积累量为165 mL,远小于NaOH单独影响下甲烷的积累量。研究结果对指导污泥厌氧发酵回收能源物质具有一定的指导意义。     

脂肪酶对餐厨垃圾厌氧产气的影响

在序批式厌氧反应器中探究了脂肪酶对餐厨垃圾厌氧消化的影响,结果表明脂肪酶能强化甲烷的积累量,且最佳的脂肪酶投加量为0.4 g·L-1,相应的甲烷积累量为356 mL·g-1 VSS,该数值是空白对照组的1.3倍。进一步机理研究表明脂肪酶能够促进溶解性COD的释放,提高生物脱氢酶的活性而减少长链挥发性脂肪酸的积累,进而提高甲烷的积累量。     

On the hydro-dispersive equivalence between multi-layered mineral barriers

In the context of municipal solid waste and hazardous waste disposal, the notion of "equivalence" between different barrier designs appears in regulatory documents from several industrialized countries. While in the past, equivalence has been thought of mainly in terms of contaminant travel times, in recent years it has been defined more in terms of the magnitude of a disposal site's potential impact on groundwater resources. This paper presents some original analytical solutions to the problem of contaminant migration through a multi-layered mineral barrier. The solutions account for the two major mechanisms of subsurface contaminant migration, namely, advection and diffusion-dispersion. An example application using the proposed solutions and a numerical model illustrates how one multi-layered mineral barrier can be considered superior to another from a strictly hydro-dispersive viewpoint. The influence of partial saturation of the mineral barrier is investigated using a numerical solution to the Richards equation for unsaturated flow. It is emphasized that conclusions relative to the superiority of one multi-layered barrier, with respect to another, should not only consider hydro-dispersive aspects, but also other processes such as the mechanical and chemical evolutions of the different barrier components. Although such phenomena are poorly addressed by existing models, failure to take them into account, at least in a qualitative fashion, may lead to unconservative conclusions with respect to barrier equivalence.     

Baseline levels of PCDD/Fs in soil and herbage samples collected in the vicinity of a new hazardous waste incinerator in Catalonia,Spain

The construction in Constantí (Catalonia, Spain) of a new hazardous waste incinerator (HWI), which is the first one in Spain, finished in 1999. In order to determine the temporal variation (1996–1998) in the concentrations of polychlorinated dibenzo-p-dioxins (PCDDs) and dibenzofurans (PCDFs) in the vicinity of the new HWI, 40 soil and 40 herbage samples were collected (1998) at the same sampling points in which samples had been taken two years before (1996). Each sample was analyzed for PCDDs and PCDFs by high resolution gas chromatography/high resolution mass spectrometry. In the 1996 survey, PCDD/F concentrations in soils ranged from 0.13 to 24.20 ng I-TEQ/kg (d.m.), with median and mean values of 0.67 and 1.68 ng I-TEQ/kg (d.m.), respectively. In the present study, PCDD/F concentrations ranged from 0.12 to 17.20 ng I-TEQ/kg (d.m.), with a median value of 0.75 ng I-TEQ/kg (d.m.) and a mean value of 1.59 ng I-TEQ/kg (d.m.). In turn, in the present study PCDD/F concentrations in vegetation ranged from 0.14 to 2.01 ng I-TEQ/kg (d.m.) (median and mean values: 0.23 and 0.31 ng I-TEQ/kg, respectively), while in the 1996 survey PCDD/F concentrations ranged from 0.24 to 1.22 ng I-TEQ/kg (d.m.) (median and mean values: 0.53 and 0.61 ng I-TEQ/kg, respectively). According to the present (1998) and the previous (1996) levels of PCDD/Fs found in soils and vegetation, the area under potential influence of the new facility shows a rather low contamination by these compounds. The current results should be useful to establish the environmental impact of the HWI.     

混凝-A3-MBR处理餐厨垃圾发酵废液运行条件优化与特性

采用混凝-两级厌氧/缺氧/好氧-膜生物反应器（A3-MBR）处理实际餐厨垃圾发酵废液,通过对运行参数进行优化确定最优工况,并考察其在该条件下长期运行的处理效果。结果表明,混凝预处理的最适pH为8,最佳混凝剂投加量为1 000 mg·L-1。A3-MBR系统在最优运行条件：总HRT为110 h,回流比为200%,进水COD负荷控制在2.3~3.6 g·（L·d）-1下可稳定运行。当系统进水COD、TN、NH3-N和TP浓度分别为（10 984±383）、（335.9±16.2）、（209.1±6.7）和（37.2±2.3）mg·L-1时,系统进水有机负荷为2.3~3.5 g·（L·d）-1,在最优条件下处理系统出水的COD、TN、NH3-N和TP分别为（202±23）、（62.1±7.1）、（0.33±0.13）和（8.3±0.9）mg·L-1,其去除率分别为98.2%、81.5%、99.8%和77.8%。A3-MBR系统对有机物具有良好的去除效果,厌氧段未积累挥发性脂肪酸。最终出水中溶解性有机物主要为II区芳香族蛋白质类似物,残留的挥发性有机物以酯类物质为主。     

白腐菌应用于堆肥处理含木质素废物的研究

白腐菌对木质素具有较强的降解能力。通过在含大量木质素的模拟垃圾堆肥中采取添加白腐菌菌剂与不添加该菌剂2组实验对比,在相同堆肥处理条件下,接种菌剂的堆肥中木质素总量由274988mg降至15438mg,降解率达4386%,远高于未接种菌剂的堆肥中木质素的降解率,表明白腐菌可有效用于含木质素废弃物的堆肥处理,并有望于加速堆肥腐熟,提高堆肥效率。     

铁黄生产中废水处理与废渣的回收利用

介绍了氧化铁黄生产中的废水治理情况，同时其产生的废渣可回收利用。经过治理产生的环境、经济和社会效益显著。     

玻纤布上胶车间有机溶剂废气净化处理

介绍了工厂有机溶剂废气处理方案和设计及实际运行效果,具有简单经济、净化彻底的特点.     

城市固体废物好氧生物反应器填埋方式的实验研究

MSW（城市固体废物）生物反应器型填埋是一种较新颖的方法.在系统分析现有填埋方法优缺点的基础上,对其加以改进,将强制通风好氧和渗滤液循环2种方式有机地结合在一起,构建了MSW好氧生物反应器.考察了NH3、CH4、CO2、pH和温度等因素,并监测分析了渗滤液中的COD、BOD5、Zn^2＋、NH4^＋和NO3^-等指标,旨在研究其中垃圾的降解及渗滤液中COD、BOD5、Zn^2＋、NH4^＋和NO3^-的去除情况,探讨该生物反应器对垃圾和渗滤液相关参数的作用机理.结果表明,该反应器对渗滤液中COD、BOD5、NO3^-的去除率分别达到96.34%、94.58%和99.9%,对其中的Zn^2＋也有较好的脱除效果.     

宁波市城市污水处理厂污泥处置方案探讨

随着城市污水处理率提高导致的污水污泥产量的增长趋势也使得污水污泥的处理问题更为突出。在总结国内外城市污泥处置技术发展趋势的基础上,结合宁波市的实际情况,根据无害化、减量化和资源化的原则,提出城市污泥近远期处置方案,并对处置方案作出可行性分析。