电石渣－铁屑法去除硫酸废水中的氟和砷

对各种处理含氟、砷废水的方法进行了探讨，选择了以电石渣和废铁屑为药剂去除硫酸废水中氟和砷的方法，取得了较好的效果。该法以废治废、工艺简便、运行费用低，处理后的废水可达排放标准。     

混凝与Fenton联用处理垃圾渗滤液的效能及成本

为对混凝/Fenton工艺与Fenton/混凝工艺处理垃圾渗滤液的效果和成本进行比较,分别对年轻渗滤液和老龄渗滤液原液按照混凝/Fenton工艺与Fenton/混凝工艺2种技术路线进行处理。实验结果表明,Fenton试剂对年轻垃圾渗滤液和老龄垃圾渗滤液COD去除率最高的反应条件为pH=3.5、H2O2和Fe2+的摩尔比为6、H2O2和渗滤液原液的COD质量比为3、反应时间4 h;在PAC与渗滤液原液的COD质量比为0.6时,PAC混凝对渗滤液原液的COD去除率最高。在对渗滤液COD去除率最高的Fenton反应和PAC混凝反应条件下,混凝/Fenton工艺对年轻渗滤液和老龄渗滤液的COD去除率分别为90.56%和86.56%;Fenton/混凝工艺对年轻渗滤液和老龄渗滤液的COD去除率分别为89.99%和85.99%,2种技术路线对渗滤液COD的去除率相差不大,但先PAC混凝后Fenton氧化工艺比先Fenton后混凝工艺每t节省62.6元,是更优化的渗滤液处理工艺。     

纳米零价铁的制备及其去除水中对氯硝基苯的研究

通过FeSO4与KBH4反应,利用液相还原法制备纳米零价铁颗粒(NZVI),用XRD、SEM和BET对其性能进行表征。在常温常压下利用纳米铁还原废水中的对氯硝基苯(p-CNB),探讨了反应条件对还原率的影响。结果表明,制备过程中碱性物质(NaOH)的添加可以明显减小颗粒粒径,增大比表面积,提高纳米铁还原反应的效率。NZVI对于对氯硝基苯有很好的去除效果,NZVI用量、p-CNB初始浓度和pH值均对其去除效率产生影响。在纳米铁投加量为1 g/L,pH=2的条件下,添加NaOH的纳米铁能在120 min内将质量浓度为50 mg/L的对氯硝基苯基本完全降解,降解率为98.8%。此外,还对NZVI还原对氯硝基苯的机理进行了初步探讨。     

Emission of volatile organic sulfur compounds (VOSCs) during aerobic decomposition of food wastes

Food wastes collected from typical urban residential communities were investigated for the emission of volatile organic sulfur compounds (VOSCs) during laboratory-controlled aerobic decomposition in an incubator for a period of 41 days. Emission of VOSCs from the food wastes totaled 409.9 mg kg^?1 (dry weight), and dimethyl disulfide (DMDS), dimethyl sulfide (DMS), methyl 2-propenyl disulfide, carbonyl sulfide and methyl 1-propenyl sulfide were the five most abundant VOSCs, with shares of 75.5%, 13.5%, 4.8%, 2.2% and 1.3% in total 15 VOSCs released, respectively. The emission fluxes of major VOSCs were very low at the beginning (day 0). They peaked at days 2–4 and then decreased sharply until they leveled off after 10 days of incubation. For most VOSCs, over 95% of their emission occurred in the first 10 days. The time series of VOSC emission fluxes, as well as their significant correlation with internal food waste temperature (p < 0.05) during incubation, suggested that production of VOSC species was induced mainly by microbial activities during the aerobic decomposition instead of as inherited. Released VOSCs accounted for 5.3% of sulfur content in the food wastes, implying that during aerobic decomposition considerable portion of sulfur in food wastes would be released into the atmosphere as VOSCs, primarily as DMDS, which is very short-lived in the atmosphere and thus usually less considered in the sources and sinks of reduced sulfur gases.     

温拌沥青混合料摊铺节能减排效果的定量化研究

通过对温拌沥青混合料(WMA)和热拌沥青混合料(HMA)生产能耗值的测量和计算,对利用WMA替代HMA作为路面材料的节能效果进行了定量核算;并结合沥青路面摊铺的实际工程设计检测方案,通过实地检测,对WMA替代HWA进行路面摊铺这一重要环节的减排效果进行了定量化。测试和分析结果显示,采用适当的温拌技术,生产能耗可降低22.4%,但是提高生产环节的能源利用效率才是降耗的重要途径。对摊铺施工的实地测量表明,WMA替代HWA摊铺可使沥青烟排放降幅53.1%,一氧化碳排放降低35.4%,二氧化氮排放降低53%,二氧化硫排放降低63.1%,综合挥发性有机物化合物VOC排放降幅达56.2%。利用WMA代替HWA作为路面材料节能减排效果十分明显。     

组合工艺处理填埋场渗滤液中溶解性有机污染物的去除特性

以采用"SBR+混凝+Fenton氧化+BAF"组合工艺处理的晚期垃圾渗滤液各级出水为研究对象,考察了HA、FA和HyI等溶解性有机物(DOM s)在各个工艺处理过程中的变化。结果表明,组合工艺COD和NH3-N去除率分别达到98.4%和99.3%;对DOM s的去除率为98.3%,其中胡敏酸(HA)、富里酸(FA)和亲水性有机物(HyI)的去除率分别为98.3%、99.5%和95.7%。各处理工艺中SBR和混凝工艺对HA和HyI的去除贡献较大,Fenton氧化工艺对FA去除率较高。Fenton氧化和BAF联用,可以有效去除难降解的溶解性有机污染物,使出水达到《生活垃圾填埋污染控制标准》(GB16889-2008)排放标准。     

废纸苯酚液化物合成热固型酚醛树脂

为了提高废纸的附加值,利用废纸苯酚液化物与甲醛在碱性环境中反应,进行热固型酚醛树脂合成实验。通过正交实验确定最优化的树脂化合成工艺为:n(甲醛)∶n(废纸液化物)=2.1,n(氢氧化钠)∶n(废纸液化物)=0.5,合成温度74℃,合成时间3.0h。在此工艺条件下制备的酚醛树脂压制的胶合板达到GB/T9846—2004《人造板及饰面人造板理化性能试验方法》中Ⅰ类胶合板的强度要求。     

磁絮凝处理废水工艺条件的响应曲面法优化研究

以聚硅硫酸铁(PFSS)为絮凝剂、磁流体为磁种,采用磁絮凝法处理模拟废水。在正交实验基础上,利用Matlab软件进行响应曲面分析,研究磁絮凝法处理模拟废水的各因素间具有的交互作用关系。回归拟合结果表明最佳工艺条件为:PFSS加入量36.8g/L,模拟废水pH7.4,磁种加入量14.7mg/L,搅拌转速266r/min。在最佳工艺条件下进行实验,TP去除率为97.70%。     

秦皇岛市天然矿泉水水质特征及开发利用前景研究

秦皇岛市天然矿泉水主要赋存在早太古代的花岗岩和变质岩的构造裂隙与风化裂隙之中,有锶、偏硅酸、锶及偏硅酸、锶溴及偏硅酸等4种类型。矿泉水水源地数量较多,水质优良,但开采程度较低,开发利用前景广阔。     

Negotiation System of Ecological Compensation of Water Source Areas

In view of no generally accepted ecological compensation standards and methods at present,this paper discusses the introduction of the negotiation system to the process of ecological compensation for water source areas.That is,the government in water source areas and the downstream regions of river basins should confirm their respective rights and obligations and then establish their compensation standards through negotiations according to the different purposes of water use.The amount of compensation should be determined in the comprehensive consideration of the quality,quantity and compensation price of water.Through open and fair negotiations,an institutional arrangement will be set up,which can make the water source areas and the downstream regions of river basins fully express their true preferences and their independent choices on the ecological environment.