两阶段ASBR处理厨房垃圾的实验研究

应用两阶段ASBR技术对厨房垃圾进行实验室规模的处理研究。结果表明:总COD的去除率为77 6%,而总TS的去除率为72 21%,系统的产CH4率以TS和容积负荷计分别为212mL g和0 67L (L·d)。同时,研究发现适宜的pH值水解相为4～5,甲烷相为7～8;适宜的HRT水解相为5d,甲烷相为13 3d;适宜的固体浓度水解相TS为8%,甲烷相TS为7%;适宜的负荷(以TS计)水解相为16g (L·d),甲烷相为5 23g (L·d)。      

干式消解-原子吸收光谱法测定土壤中部分重金属的探讨

火焰原子吸收法测定土壤中的铜、锌、铅、镉、镍等重金属时,采用干式消解法对土壤样品进行处理,即在5 0 0℃加热灰化,然后用酸浸提。其测定结果与国家标准分析方法测定结果无显著性差异,对标准样品测定结果准确。测量过程方便快速。     

微波焙烧法与马弗炉焙烧法处理废脱硝催化剂的效果比较

用Na_2CO_3作为助溶剂、Na_2O_2作为消解剂,采用微波焙烧法和马弗炉焙烧法消解处理废钒钨钛脱硝催化剂。通过XRF、BET、XRD和NH_3-TPD技术对两种消解方法制得的钛钨粉样品进行了表征。表征结果显示,与马弗炉焙烧法相比,微波焙烧法得到的钛钨粉纯度更高,TiO_2与WO_3含量之和大于96.7%(w),且该钛钨粉还具有更高的比表面积和酸性,可以作为钒钨钛脱硝催化剂的生产原料再利用。     

Overcoming the toxicity effects of municipal wastewater sludge and biosolid extracts in the Yeast Estrogen Screen (YES) assay

For nearly two decades, the Yeast Estrogen Screen (YES) has been used as a valuable tool for determining the total estrogenic potency of various environmental samples, including influent and effluent streams at municipal wastewater plants. However, applying the YES assay to wastewater sludges and stabilized biosolids has been problematic. This is due to co-extracted compounds from the solids either proving toxic to the yeast or masking the presence of estrogenic substances. The present research describes the development and validation of sample preparation steps that mitigate the toxicity effects of municipal wastewater sludge and biosolid samples in the YES assay, while allowing for reliable dose-dependent expression of estrogenic activity. A copper work-up for sulfur removal and chromatographic cleanup with silica and alumina were required in addition to solid-phase extraction to adequately remove interfering compounds. Sample stabilization methods such as autoclaving, lyophilization and formaldehyde treatment were found to be detrimental to the assay. Hence, heat-drying is recommended to prevent cytotoxicity and the degradation of estrogenic substances.     

微波消解-原子荧光光谱法同时测定土壤中痕量砷和汞

建立了微波消解—原子荧光光谱法同时测定土壤中痕量砷和汞的方法。通过对消解体系以及灯电流、载气流量、屏蔽气流量等仪器参数进行优化,确定了最佳实验条件。在优化的实验条件下,采用原子荧光光谱法同时测定砷和汞的检出限分别为0.02μg/L和0.01μg/L,线性范围分别为0～40μg/L和0～4μg/L,两元素的加标回收率在92%～102%之间,相对标准偏差砷为0.9%～3.1%,汞为1.5%～3.4%,完全适用于土壤环境样品的检测。     

紫外分光光度测定总氮的影响因素探讨

本文介绍了测定总氮过程中,不同消解方法、碱性过硫酸钾的稳定时间、悬浮物粒径对总氮测定的影响。实验表明:碱性过硫酸钾避光在冰箱中至少可保存一个月,悬浮物粒径对总氮的测定无影响,消解总氮时,可在压力锅加热到120℃开始计时,恒温消解30分钟,自然冷却。     

两相厌氧反应器相分离实验研究

在两相上流式厌氧生物反应器(UASB)动力学启动成功的条件下,选用钼酸盐作为产甲烷菌抑制剂,进行进一步的分相实验。实验前3 d在产酸相反应器进水中投加2.0 mmol/L的钼酸钠溶液,出水不进入产甲烷反应器。然后停止投加钼酸钠溶液,再运行3 d,出水依然不进入产甲烷反应器。6 d后,产酸反应器出水开始进入产甲烷反应器。结果表明:在停止投加钼酸盐后产酸菌便迅速恢复,而钼酸盐对产甲烷菌的作用是杀灭性的;产酸相出水去除效果降低,但是其酸化率由50%左右上升并最终稳定在60%左右,同时两相厌氧反应器整体去除效率提高。     

蠕虫L.variegatus在污泥减量中的作用与应用前景分析

剩余污泥已成为污水处理厂亟待解决的棘手问题。虽然现有污泥减量技术众多,但或多或少都存在着技术或经济上的不足。蠕虫——L.variegatus应用于污泥减量具有较好的实际效果以及潜在的商业利用价值,因此,近年来受到人们关注。首先,介绍L.variegatus一般习性、对污泥减量的试验效果。然后,对L.variegatus应用于大规模连续系统的要点进行了技术分析。最后,对L.variegatus应用于实际污水处理厂污泥减量的技术与经济的合理性进行分析和估算。     

法国某生活污水厂污泥好氧消化工艺运行研究

为了提高出水质量,法国小镇Cagnes—sur—Mer的生活污水处理厂从2008年初开始实施高有机负荷的运行,但同时这也提高了出泥产量。由于污泥的处理费用及搬运污泥的交通费用很高,水厂对污泥进行了污泥好氧稳定工艺,工艺使用纯氧机（VSA装置）就地利用空气制氧。工艺投入运行后,每日对好氧消化池的入泥和出泥进行采样和检测（MLSS、MLVSS、pH、COD、DRYNESS etc）以建立完整的运行数据。污泥经好氧消化作用后其有机物含量减少60％以上,每月减少40吨的出泥。同时,消化池的使用还使水厂周日也能对曝气池中的污泥进行抽取,缓解了以往由于周日停止排泥而导致周一曝气池中污泥浓度过大的问题。从而达到优化出水水质的目的。消化池中的温度维持在40℃左右,因为反应为放热反应,所以无需加热设备。此项目所收集到的数据将为这种工艺的发展提供帮助。同时也可以为那些想要减少出泥量的水厂提供一种新的方法。因为它投资小,见效快,操作简单。     

Mass balance of anionic surfactants through up-flow anaerobic sludge blanket based sewage treatment plants

The outcome of a 21-month monitoring study on anionic surfactants (AS) at five (27–70 ML/d) up-flow anaerobic sludge blanket (UASB) based sewage treatment plants (STPs) is described. The average removals of AS were around 8–30%. Appreciable concentrations of AS were being discharged to the watercourse (average 4.30 mg/L; range 3.60–4.91 mg/L). On an average dried sludge contained 1452 mg AS/kg dry weight. Mass balance at three STPs indicated that, AS load of the order of 5–17% and ≈12% is removed by adsorption in UASB reactors and polishing ponds (PP) respectively. Biodegradation of AS under anaerobic conditions in UASB reactors and PP does not seem to take place. In the sludge stream, appreciable biodegradation (≈46%) of adsorbed AS under aerobic conditions on the sludge drying beds takes place. If influent AS mass flux is normalized to 100 units, than average of ≈74 and ≈7 units are discharged with treated effluent and dried sludge respectively, while 12 and 6 units are adsorbed/settled in PP and aerobically biodegrade on sludge drying beds respectively. At two STPs (34 and 56 ML/d), the filterable fluxes in UASBR increased so that the mass balance could not be computed.