铜渣基磷酸铁化学键合材料固化重金属Pb

铜渣堆积会造成资源浪费和环境污染等问题,利用铜渣与磷酸盐反应制备铜渣基磷酸铁化学键合材料(CBIPCs),并用其固化重金属Pb。研究铜渣与磷酸二氢铵(m(CS)/m(P))配比、缓凝剂以及硝酸铅掺量对CBIPCs固化重金属Pb的影响。结果表明：随着硝酸铅掺量的增加,固化体抗压强度降低,Pb毒性浸出浓度略增大;在m(CS)/m(P)=3:1和硼砂掺量为2%的条件下,当硝酸铅掺量为12%,固化体自然养护28 d的抗压强度仍达到24.5 MPa,Pb毒性浸出浓度为0.086 mg·L-1,远低于《危险废物鉴别标准 浸出毒性鉴别》(GB 5085.3-2007) 要求的最高限值5.0 mg·L-1。XRD和SEM/EDS分析表明,固化体中生成了PbHPO4、Pb3(PO4)2、Pb5(PO4)OH等铅类磷酸盐产物,并被胶凝相物质紧密包裹。铜渣与磷酸盐反应制备的铜渣基磷酸铁化学键合材料(CBIPCs),可通过化学键合和物理固封双重作用实现对重金属Pb的稳定固化。     

机械力活化固硫灰固化处理生活垃圾焚烧飞灰

为实现城市生活垃圾焚烧飞灰的安全处理,通过机械力化学法活化循环流化床燃煤固硫灰,探讨了球磨样品制备固化体的参数。并采用X射线衍射仪（XRD）和傅里叶变换红外光谱仪（FTIR）手段对垃圾焚烧飞灰中重金属的固化机制进行了研究。结果表明,当垃圾焚烧飞灰掺加比为60%,球磨转速为600 r·min-1,球磨时间为5 h,养护温度60 ℃时的固化体28 d和56 d抗压强度分别达到15.6 MPa和17.9 MPa,采用原子吸收光谱仪（AAS）测得固化体中Zn、Pb、Cu、Cd和Cr重金属浸出量均低于GB 5085.3-2007规定限值。XRD和FTIR表征结果表明,在水化过程中,该混合体系生成了水化硅酸钙（C—S—H）、斜方钙沸石和钙矾石（AFt）等水化产物,并且C—S—H凝胶可通过物理包裹的形式固化垃圾焚烧飞灰中重金属;斜方钙沸石和钙矾石以化学吸附的方式使垃圾焚烧飞灰中的重金属离子达到固化/稳定化效果,实现了垃圾焚烧飞灰中重金属的安全处理。     

城市污水厂污泥内循环自热高温微好氧消化的处理

利用一种新型的内循环自热式污泥高温微好氧消化装置对城市污泥进行消化处理。通过在反应器中增加内筒的方法,使得内筒中污泥通过搅拌器的提升作用在内外筒之间循环以提高消化速率。结果表明,增加内筒之后,消化系统的污泥VS去除率在第16天达到了41.52%,而未添加内筒的反应器污泥到第20天时仍未到达稳定化水平。因此,加了内筒的单段式ATAD消化反应器与不加内筒的单段式ATAD消化反应器相比可以使得污泥更快地达到稳定状态。另外,与没有内筒相比,增加内筒后反应器顶部和底部的ORP和pH值均维持较高水平,消除了曝气死角。增加内筒后,顶部和底部污泥上清液中SCOD、VFA、TN、NH4+-N和TP浓度基本保持一致,而没有内筒则相差较大,表明增加内筒后,反应器内污泥混合更加均匀。     

红壤和磷灰石对沉积物重金属稳定化的影响

利用磷灰石、红壤及两者复配组合对污染沉积物中重金属进行稳定化处理,通过TCLP和改进的BCR连续提取法对稳定化效果进行分析和评价。结果表明,在稳定化试验中,对Cu、Cd和Zn的稳定效果由大到小为红壤+磷灰石、磷灰石、红壤;其中,红壤+磷灰石对Pb的稳定效果与磷灰石单独添加相近,显著大于红壤。5%磷灰石+5%红壤添加3个月后,Cu、Cd、Zn和Pb的稳定效率分别达到59.83%、29.43%、31.00%、96.06%。添加5%磷灰石时,Cu、Cd、Zn和Pb的稳定效率分别为52.46%、24.67%、25.23%、96.06%。红壤的添加不同程度地促进了磷灰石对Cu、Cd和Zn的稳定效率。连续提取试验结果表明.磷灰石单独和复配添加均使Cu、Zn和Pb的生物可利用态和潜在生物可利用态占比降低,生物不可利用态占比增大。5%磷灰石+5%红壤处理中,Cu、Cd、Zn和Ph的生物可利用态和潜在生物可利用态的比例总和分别降低了19.31%、5.11%、20.11%和68.97%。相比磷灰石单独处理,复配处理进一步促进了Cd和Zn的酸溶态向残渣态转化。磷灰石和红壤+磷灰石复配处理能有效降低沉积物中重金属的危害。     

含油污泥无害化处理及综合利用的途径

原油脱水以及油田和炼油厂的污水处理系统会排出大量的含油污泥,从环境保护角度出发,必须进行无害化处理或综合利用。处理含油污泥的方法很多,有固化处理法、土地耕作法、回收污油法、固液分离处理及综合利用等方法。较为详细地叙述了各种方法的原理、特点及适用情况等,这些方法各有利弊。今后还应进一步加强含油污泥性质与特征的基础性研究,积极寻求多种利用途径,彻底解决含油污泥污染问题     

An integrated method for the rapid dewatering and solidification/stabilization of dredged contaminated sediment with a high water content

• An integrated method, called PHDVPSS, was proposed for treating DCS. • The PHDVPSS method showed superior performance compared to conventional method. • Using the method, water content (%) of DCS decreased from 300 to<150 in 3 days. • The 56-day UCS from this method is 12‒17 times higher than conventional method. • Relative to PC, GGBS-MgO binder yielded greater reduction in the leachability. To more efficiently treat the dredged contaminated sediment (DCS) with a high water content, this study proposes an integrated method (called PHDVPSS) that uses the solidifying/stabilizing (S/S) agents and prefabricated horizontal drain (PHD) assisted by vacuum pressure (VP). Using this method, dewatering and solidification/stabilization can be carried out simultaneously such that the treatment time can be significantly shortened and the treatment efficacy can be significantly improved. A series of model tests was conducted to investigate the effectiveness of the proposed method. Experimental results indicated that the proposed PHDVPSS method showed superior performance compared to the conventional S/S method that uses Portland cement (PC) directly without prior dewatering. The 56-day unconfined compressive strength of DCS treated by the proposed method with GGBS-MgO as the binder is 12‒17 times higher than that by the conventional S/S method. DCS treated by the PHDVPSS method exhibited continuous decrease in leaching concentration of Zn with increasing curing age. The reduction of Zn leachability is more obvious when using GGBS-MgO as the binder than when using PC, because GGBS-MgO increased the residual fraction and decreased the acid soluble fraction of Zn. The microstructure analysis reveals the formation of hydrotalcite in GGBS-MgO binder, which resulted in higher mechanical strength and higher Zn stabilization efficiency.     

垃圾填埋场稳定化及其研究现状

文章对直埋场稳定化过程进行了初步描述,并从填埋气、渗滤液、垃圾组成和沉降等４个方面总结了填埋场稳定化的研究现状。     

有机负荷条件对间歇式气提内循环反应器中好氧颗粒污泥形成的影响

在R1、R2和R3共3组气提式内循环序批式反应器中启动好氧颗粒污泥工艺,探讨在无选择压作用下有机负荷对好氧颗粒污泥的形成及稳定性的影响.其中,R1、R2分别以7 kg.(m3.d)-1和3 kg.(m3.d)-1的目标COD负荷直接启动,R3以1.5kg.(m3.d)-1逐步增加至3 kg.(m3.d)-1的递增COD负荷方式启动.结果表明,3组反应器在启动期中均能快速形成好氧颗粒污泥,但以目标负荷启动方式易使好氧颗粒污泥反应器产生丝状菌污泥膨胀.通过对颗粒形成过程、粒径、性质以及胞外多聚物等指标分析,认为递增负荷的启动方式可有效抑制启动初期丝状菌污泥膨胀,且形成的颗粒更为稳定,生物降解效率更高.     

Effects of sepiolite on stabilization remediation of heavy metal-contaminated soil and its ecological evaluation

Stabilization in the remediation of heavy metal contaminated soils has been gaining prominence because of its cost-effectiveness and rapid implementation. In this study, microbial properties such as microbial community and enzyme activities, chemical properties such as soil pH and metal fraction, and heavy metal accumulation in spinach (Spinacia oleracea) were considered in assessing stabilization remediation effectiveness using sepiolite. Results showed that soil pH values increased with rising sepiolite concentration. Sequential extraction results indicated that the addition of sepiolite converted significant amounts of exchangeable fraction of Cd and Pb into residual form. Treatments of sepiolite were observed to reduce Cd and Pb translocation from the soil to the roots and shoots of spinach. Concentrations of Cd and Pb exhibited 12.6%–51.0% and 11.5%–46.0% reduction for the roots, respectively, and 0.9%–46.2% and 43.0%–65.8% reduction for the shoots, respectively, compared with the control group. Increase in fungi and actinomycete counts, as well as in catalase activities, indicated that soil metabolic recovery occurred after sepiolite treatments.     

某电镀厂六价铬污染土壤还原稳定化试剂筛选与过程监测

针对目前国内进行六价铬污染土壤修复过程关键性控制参数相对缺乏,且中长期稳定性效果相对较差等问题.选取北方某电镀厂六价铬污染严重的表层土壤,使用5组还原试剂进行还原稳定化试验,同时通过在线ORP(氧化还原电位)测试仪在线监测和定期取样测试,探索不同还原剂的反应效率和最终效果.其中试剂4对六价铬的还原稳定化率最高,基本上均在99.5%以上,六价铬浓度最低可达到2.4 mg·kg~(-1);从反应速率来看试剂1和4反应速率最快.反应过程的ORP、pH值监测数据也出现较大的区别,其中第1组土壤样品整个过程中ORP始终处于-400 m V左右;第4组反应在30 h以后,由-200m V逐步升高并稳定在100 m V左右.从反应体系中的pH值变化情况来看,唯一使土壤pH保持在7左右的是试剂4.综合判断试剂4(多硫化钙和亚铁盐复配试剂)的综合还原效果最佳.以试剂4为基础进行单独放大试验,通过ORP和电导率两个关键参数的变化情况发现还原反应过程大概需要160 h,从而为后期实际土壤修复过程中控制还原土壤的养护条件和过程监控提供理论支撑.