Experimental study on agitated drying characteristics of sewage sludge under the effects of different additive age

Drying experiments of dewatered sewage sludge (DSS) were conducted on a agitated paddle dryer, and the effects of additive agents, i.e., CaO, pulverized coal (PC), heavy oil (HO), and dried sludge ("DS" through back mixing) on the agitated drying characteristics of DSS were investigated. The results indicated that CaO can significantly increase the drying rate of DSS. The drying rate at CaO/DSS (mass ratio) = 1/100 was 135% higher than that of CaO/DSS = 0. Pulverized coal has no obvious effect on drying rate, but the increase of PC/DSS can promote breaking up of sludge lump. Heavy oil was found to be slightly effective in improving the drying rate of DSS in the examined experimental range of HO/DSS = 0-1/20. It is also found thatHOcan reduce the torque of the dryer shaft, due to its lubrication effect. Back mixing of DS was found to be effective in alleviating the unfavorable effect of the lumpy phase by improving the mixing effect of the paddle dryer. There was a marked increase of drying rate with an increase of the DS/DSS in the experimental range of DS/DSS = 0-1/3.     

Aerobic granules cultivated and operated in continuous-flow bioreactor under particle-size selective pressure

A novel method based on the selective pressure of particle size （particle-size cultivation method, PSCM） was developed for the cultivation and operation of aerobic granular sludge in a continuous-flow reactor, and compared with the conventional method based on the selective pressure of settling velocity （settling-velocity cultivation method, SVCM）. Results indicated that aerobic granules could be cultivated in continuous operation mode by this developed method within 14 days. Although in the granulation process, under particle-size selective pressure, mixed liquor suspended solids （MLSS） in the reactor fluctuated greatly and filamentous bacteria dominated the sludge system during the initial operation days, no obvious difference in profile was found between the aerobic granules cultivated by PSCM and SVCM. Moreover, aerobic granules cultivated by PSCM presented larger diameter, lower water content and higher specific rates of nitrification, denitrifieation and phosphorus removal, but lower settling velocity. Under long term operation of more than 30 days, aerobic granules in the continuous-flow reactor could remain stable and obtain good chemical oxygen demand （COD）, NH4^＋-N, total nitrogen （TN） and total phosphorus （TP） removal. The results indicate that PSCM was dependent on the cultivation and maintenance of the stability of aerobic granules in continuous-flow bioreactors.     

硫酸铵和尿素对废物焚烧过程中多种途径生成氯苯类的抑制作用

氯苯类(CBz)是废弃物焚烧等过程中产生二英的前驱物,也被认为是实现二英在线检测的良好指示物,同时五氯苯(PeCBz)和六氯苯(HxCBz)也是持久性有机污染物(POPs).但氯苯在废物焚烧过程中的排放和控制尚没有受到足够重视,为此开展了模拟焚烧过程中硫酸铵和尿素对3种氯苯合成途径的抑制作用研究,包括飞灰合成,1,2-二氯代苯(1,2-DiCBz)转化高氯代苯等过程.结果表明,硫酸铵和尿素对氯苯的3种合成途径均有抑制作用,如1%尿素与废物混合焚烧对四氯苯、五氯苯和六氯苯的抑制效率分别达到了66.8%、57.4%和50.4%.比较硫酸铵和尿素对3种过程的抑制作用,认为尿素对氯苯具有更稳定的抑制能力.     

柱状污泥基活性炭制备方法及其除污染效能研究

以城市污水厂剩余污泥为原料,用氯化锌活化法研究一种柱状污泥基活性炭(CSAC)的制备方法及其工艺条件优化,并选择粉末污泥基活性炭(PSAC)和一种商品煤质碳(MAC)作为对照,考察了CSAC对重金属离子Cu(Ⅱ)和Pb(Ⅱ)及有机污染物硝基苯的吸附去除效能.结果表明,CSAC的比表面积及微孔容积分别是306.9 m2·g-1和0.109 cm3·g-1,仅为MAC的36.7%和23.6%,但其对Cu(Ⅱ)和Pb(Ⅱ)的平衡吸附量却远远高于MAC,说明CSAC表面存在的高含量酸性官能团在吸附去除重金属过程中起到了重要的作用.由于制备原料相同及制备工艺相似,CSAC与PSAC的理化性质基本相同,两种炭的表面酸性官能团含量较高,对Cu(Ⅱ)和Pb(Ⅱ)均具有较好的吸附去除效果,优于MAC,只是CSAC的比表面积和微孔容积略低于PSAC;在对硝基苯的吸附实验中,CSAC及PSAC的吸附效率均远远低于MAC,说明在对有机物硝基苯的吸附中,活性炭的比表面积等物理性质起到了较大的作用.同时,所制备的CSAC的稳定度大于95%,易于分离回收,不会造成二次污染,适合废水中重金属离子的吸附去除.     

基于代谢产物调控的活性污泥沉淀性能控制原理研究

通过对不同沉降性能活性污泥的胞外聚合物(EPS)进行荧光特性分析,探讨了荧光强度峰值、荧光区域积分等参数与污泥沉降性能的关系.研究表明,典型波长下荧光强度峰值与污泥沉降性能之间有很好关联性,据此,建立了微生物典型代谢产物与沉淀性能的调控曲线即活性污泥的安全操作线与微生物代谢状态曲线,确立了活性污泥沉淀性能调控区域即高代谢产物区可获得良好的固液分离效果.研究成果从微生物代谢的角度揭示了絮体结构的调控方法,具有重要的理论意义.     

壳聚糖活性污泥复合吸附剂的制备研究

为了提高污泥细胞吸附重金属离子的应用能力,采用壳聚糖包埋固定活性污泥,制备了粒径2~3 mm的壳聚糖活性污泥复合吸附剂SCTS.以吸附溶液中CrO2-4的吸附率为指标,通过单因素实验对制备过程中采用的2种固化液及5种发泡剂进行比选,考察了固化液浓度、发泡剂量、交联剂量、活性污泥与壳聚糖用量比值及发泡温度对SCTS吸附能力的影响,由正交实验确定影响因素主次顺序及最优水平组合.结果发现,固化液浓度、发泡剂量、污泥与壳聚糖用量比值及发泡温度对SCTS吸附能力影响较强,影响次序为固化液浓度发泡剂量活性污泥与壳聚糖用量比值发泡温度.最优水平组合为4 g·L-1三聚磷酸钠(STPP)固化液、剂量为吸附剂质量10%的NH4HCO3发泡剂、活性污泥与壳聚糖用量比值0.5、发泡温度100℃,此时CrO2-4吸附率最高可达97.3%.该吸附剂的制备研究为污泥的资源化利用探索了新的途径.     

不同添加剂对铅冶炼污染石灰性土壤的修复及土壤性质的影响研究

探讨了污水处理厂脱水污泥、枯草和磷矿粉对受铅冶炼污染的石灰性土壤(全Pb、Cd、Zn含量分别为2337、21.4、486 mg·kg-1,DTPA提取态Pb、Cd、Zn含量分别为1035、14.5、68.7 mg·kg-1)中重金属的稳定效果及对土壤性质的影响.其中,污泥和枯草均按200 g·kg-1(干重)的用量施用,磷矿粉按n(P)∶n(Pb)=2∶1比例施用,培养80 d.研究结果表明,单独施用污泥可使土壤DTPA-Pb含量降低18.0%(p0.05),并可显著降低土壤pH,增加土壤氮、磷有效性和电导率、DTPA-Cd、DTPA-Zn含量,其中,DTPA-Cd、DTPA-Zn含量增加比例均达到10%以上.单独施用枯草可使土壤DTPA-Pb含量降低10.7%(p0.05),土壤有机质含量增加26.4%(p0.05),对土壤其它性状影响较小.磷矿粉单独施用时对土壤性质影响较小.与污泥单独施用相比,磷矿粉与污泥配合施用时,可使土壤DTPA-Cd含量降低11.9%.     

碱改性净水污泥对水中氨氮的吸附效能研究

采用氢氧化钠浸渍法改性净水污泥,研究了碱改性净水污泥对水中NH+4的去除性能.同时,考察了模拟废水pH、吸附剂投加量、NH+4初始浓度、吸附温度及吸附时间对吸附性能的影响.结果表明,当pH为弱酸性或中性,投加碱改性净水污泥20 g·L-1时,在室温下对初始浓度为50 mg·L-1的NH+4模拟废水振荡吸附120 min,可达到氨氮排放二级标准.将实验数据分别用吸附等温模型和动力学模型进行拟合,发现净水污泥对NH+4的吸附符合Langmuir模型和二级动力学模型,且净水污泥对氨氮的吸附包括静电吸引和离子交换两种作用机理.     

中国危险废物和医疗废物焚烧处置行业二（口恶）排放水平研究

通过调研全国危险废物和医疗废物焚烧处置设施,对包含二噁英排放水平的设施按处置对象、炉型和处理量分类,并作系统分析和研究.结果表明现有危险废物焚烧设施烟气中二噁英的浓度比医疗废物低,达标率为74.19%;危险废物选用回转窑处置效果较好,达标率为66.67%;而医疗废物选用回转窑或热解炉,要综合考虑处置规模、生产成本和二英排放总量等因素;危险废物介于10~30 t·d-1和医疗废物介于10~20 t·d-1的处置设施要尤其注意二噁英的排放问题;医疗废物焚烧飞灰中二噁英的均值浓度为危险废物6倍以上,仅有16.67%满足填埋要求.二者烟气中二英的浓度分布以1,2,3,4,6,7,8-HpCDF、2,3,7,8-TCDF和OCDD为主.     

广州城市污泥中重金属形态特征及其生态风险评价

分析了广州市4个不同来源的城市污水处理污泥中重金属含量,考察了污泥样品中重金属形态分布和生物可利用性,并分别利用风险评价指数(RAC)和固废重金属毒性浸出方法评价了污泥中重金属生态危害风险和浸出毒性风险.结果表明,污泥样品中Cu、Cr、Pb和Zn含量较高,不同来源污水处理污泥中重金属含量差别较大.污泥样品中重金属绝大部分以非稳定态存在,酸性污泥中可迁移的酸溶态重金属比例较高.由单一萃取结果,1 mol·L-1NaOAc溶液(pH 5.0)和0.02 mol·L-1EDTA+0.5 mol·L-1NH4OAc溶液(pH 4.6)分别对酸性和碱性污泥中生物可利用态重金属具有较好的萃取能力.污泥酸性越强,其中生物可利用态重金属比例越大.污泥中重金属的迁移能力使其处于高生态危害风险程度;重金属的生物可利用性使酸性污泥大多处于极高危害风险程度,而使碱性污泥大多处于中等危害风险水平.除城市污水处理污泥外,污泥样品中重金属具有高的浸出毒性风险,萃取重金属生物可利用态后,污泥仍具有高浸出毒性风险,但由于浸出毒性风险降低使部分污泥可进行填埋处置.