The Variability of Estimates of Variance, and Its Effect on Power Analysis in Monitoring Design

Power analysis can be a valuable aid in the design of monitoringprograms. It requires an estimate of variance, which may come from a pilot study or an existing study in a similar habitat. For marine benthic infauna, natural variation in abundances canbe considerable, raising the question of reliability of varianceestimates. We used two existing monitoring programs to generatemultiple estimates of variance. These estimates were found to differ from nominated best estimates by 50% or more in 43% of cases, in turn leading to under or over-estimation of samplesize in the design of a notional monitoring program. The twostudies, from the same general area, using the same samplingmethods and spanning a similar time scale, gave estimatesvarying by more than an order of magnitude for 25% of taxa.We suggest that pilot studies for ecological monitoring programsof marine infauna should include at least two sampling times.     

UASB反应器常温下处理生活污水的中试研究

中试试验研究讨论了利用颗粒污泥接种的UASB反应器常温下处理生活污水的运行性能。在7～31℃温度范围内处理生活污水,考察了不同温度、不同负荷条件下反应器的处理效率,讨论了各参数对反应器运行的影响,为UASB反应器常温下处理生活污水提供理论和实践指导。     

Treatment of 2-phenylamino-3-methyl-6-di-n-butylaminofluoran production effluent by combination of biological treatments and Fenton＇s oxidation

High strength refractory organic stream is produced during the production of 2-phenylamino-3-methyl-6-di-n-butylaminofluoran （One Dye Black 2, abbr. ODB 2）, a novel heat-sensitive material with a promising market. In this study, a combination of acidificationprecipitation, primary biological treatment, Fenton＇s oxidation and another biological treatment was successfully used for the removal of COD from 18000-25000 mg/L to below 200 mg/L from the ODB 2 production wastewater in a pilot experiment. A COD removal of 70%-80% was achieved by acidification-precipitation under a pH of 2.5-3.0. The first step biodegradafion permitted an average COD removal of 70% under an hydraulic residence time （HRT） of 30 h. By batch tests, the optimum conditions of Fenton＇s oxidation were acquired as： Fe^2＋ dose 6.0 mmol/L; H2O2 dose 3000 mg/L; and reaction time 6 h. The second step biological treatment could ensure an effluent COD below 200 mg/L under an HRT of 10 h following the Fenton＇s treatment.     

焚烧飞灰熔融过程重金属迁移特性中试研究

通过中试试验研究垃圾焚烧飞灰熔融过程重金属Cd、Pb、Zn、Cu、Cr和Ni的迁移特性,着重研究重金属在熔渣中的固化效果,考察了温度（1 290℃、1 320℃、1 360 ℃）、助熔剂（10 %的玻璃粉）、冷却方式（水冷、空冷）对重金属固定率的影响.结果表明,温度的提高使Pb、Zn、Cu、Cr和Ni的固定率都有一定的提高;加入10%的玻璃粉使各种重金属的固定率都有显著提高,只有Zn例外;对Zn、Cu、Cr和Ni,空气冷却方式下的重金属固定率比水冷方式下的高.     

Reuse of wastewater for industrial needs: the Pontedera case

This paper presents result from an economic and technical point of view evaluation study, which has sought to establish the potential for replacing well-water that is currently used at the Piaggio industrial plant in Pontedera with recycled wastewater. The study is based upon a pilot wastewater treatment plant, which has been used to test wastewater treatment processes and to compare with achieved quality of recycled waters with that of water drawn on-site from physical/chemical pre-treatment and end with a reverse osmosis and air stripping stage. However, after the physical/chemical pre-treatment, the first option uses oxidation with ozone followed by activated carbon filtration, whereas the second method uses ultrafiltration. The first method is more effective at reducing chemical oxygen demand (COD) whereas the second method is more effective in removing bacteria. Nonetheless, both methods deliver water for re-use of a quality comparable with or better than that of well-water. In principle, the reverse osmosis permeate from either process could be re-used in all production phases at the industrial plant. However, the method base upon oxidation with ozone followed by activated carbon filtration is preferred, because, the process is simpler and continuous. The economic analysis of this process gives an estimated cost of Euro 0.55 per m³ for treated water. This compares favorably with other treatment processes and with the cost of other forms of water supply, which are projected to increase in any case.     

规模化农田土壤重金属污染修复的中试试验研究——以某镇土壤污染治理为例

农用地重金属污染长期以来一直是生态环境的热点和难点问题。2017年,对某镇农田土壤重金属污染开展详查,单项污染指数评价结果表明,镉超标率为67.60%(Pi>1),基于内梅罗污染指数法的评价结果显示,57.30%的点位受到不同程度的污染(PN≥1.0);2018年,分别选取钝化修复和植物修复进行中试试验,经钝化修复后土壤有效镉和总镉含量分别平均降低32.73%和5.64%。经超富集植物籽粒笕种植一季修复后,土壤总镉含量降低15%以上。本次中试试验修复效果良好,能为下一阶段的土壤镉污染修复方案的制定和优化提供科学的依据,为全国农用地重金属污染修复提供了有价值的借鉴意义。     

长江原水臭氧-生物活性炭挂膜中试研究

为了探究面向长江水源的臭氧-生物活性炭深度处理工艺的挂膜技术,进行了长江原水常州段的臭氧-生物活性炭挂膜中试研究.结果表明,在挂膜前期,由于炭柱的物理吸附作用逐渐饱和,炭柱对DOC(溶解性有机碳)、UV_(254)和COD_(Mn)(高锰酸盐指数)的去除率逐渐降低,对氨氮几乎没有去除,在挂膜中后期,由于活性炭上生物膜逐渐成熟,生物降解起主导作用,有机物和氨氮去除率升高并趋于稳定.90 d后,炭柱对DOC、UV_(254)和COD_(Mn)这3个有机物指标的去除率分别稳定在30.64%、57.50%和30.00%以上,氨氮去除率稳定在88.93%左右,认为挂膜成功.扫描电镜图显示活性炭表面出现丰富的菌胶团,同时高通量测序也验证了活性炭中丰富多样的微生物群落结构.     

基于MBBR的CANON工艺处理消化液中试启动

基于移动床生物膜反应器（MBBR）成功启动了自养脱氮工艺（CANON）处理污泥消化上清液.采用8.55m³中试系统,反应器内部填充SPR-Ⅲ填料,填充率44%,通过动态流接CANON污泥（接种比例<1%）,经过70d成功启动CANON工艺.运行至200d,TN去除负荷稳定在0.9kgN/（m³·d）,出水氨氮浓度均值63.9mg/L,氨氮和总氮去除率均值分别为91%和85%.进水中存在的少量有机物使系统同时存在反硝化和厌氧氨氧化两种脱氮途径,促进了总氮的去除,对总氮去除的贡献分别占5%~7%和93%~95%.通过对pH值和曝气强度的控制,防止了悬浮载体结垢,平衡了DO、曝气强度以及生物膜厚度三者之间的关系,使生物膜始终处于适宜的厚度,稳定了系统的处理效果.高通量测序表明悬浮载体上的优势菌种为氨氧化菌（AOB）和厌氧氨氧化菌（AnAOB）,其丰度整体呈增长趋势,至稳定运行期可达到17%和14%.系统无NOB存在,短程硝化效果良好,反硝化菌群丰度在2%~3%并相对稳定,进水中存在的少量有机物不会影响厌氧氨氧化菌的增殖.     

飞行员人因可靠性定量预测

为有效预测飞行员的人因可靠性,以保障飞行安全,基于认知可靠性与失误分析法(CREAM)的扩展法,建立飞行员人因可靠性定量预测模型。依据飞行员的任务特点,调整认知行为及认知功能。通过优化共同绩效条件(CPC)因子水平等级,并增加新的因子,改进CPC因子依赖规则,用于修正因子的初始评估结果,解决扩展法未考虑因子间关系的问题,从而完成模型的建立。利用回看分析法验证模型的有效性,采用所建立的模型和扩展法分别对已发生的飞行案例进行预测,并与实际发生结果对比分析。结果表明,与扩展法相比,采用飞行员定量预测模型得到的预测结果与案例发生结果所反映的控制模式更为匹配。     

磷石膏制硫酸钾中试研究

以湿法磷酸副产的磷石膏和工业品氯化钾为原料 ,采用两步法 ,常温常压下 ,在 5 0 0 0t a工业化装置中 ,生产符合国标ZBG2 10 0 6 89农用一级品硫酸钾。整个过程流程较简单 ,能耗低 ,投资省 ,基本无“三废”排放。钾的收率达70 %。工艺条件稳定 ,产品质量稳定。中试结果与小试有较好的重复性 ,放大效果好。