交联阳离子淀粉螯合剂对铬渣的处理研究

合成了作为重金属鳌合剂的交联阳离子淀粉，并将它用于铬渣的固化实验，对固化体的浸出毒性、表面浸出率、抗压强度等指标进行了测试。结果表明，添加高分子鳌合剂后的固化体的浸出毒性降低66．4％，远远小于国家标准的1．5mg／L；28d后的表面浸出率仅为10^-6数量级；抗压强度有所下降，但28d养护后的抗压强度大于30MPa，符合填埋或建筑综合利用的强度要求。     

铬渣水泥固化及固化体浸出毒性的研究

铬渣水泥固化时要加入硫酸亚铁和添加剂矿渣、粉煤灰 ,硫酸亚铁可以部分地把六价铬还原为三价铬 ,能把得到的固化体六价铬浸出毒性降到低于国家标准 ,抗压强度可达 30MPa以上 ,可综合利用。与此同时 ,本文考虑日晒、振荡时间和固化体粒度对浸出毒性的影响以及固化体表面浸出率、模拟酸雨淋溶对固化体性能的影响。     

水泥、粉煤灰及DTCR固化/稳定化重金属污染底泥

采用水泥、粉煤灰及有机硫稳定剂DTCR固化/稳定化处理重金属污染的底泥,考察固化体的抗压强度及重金属浸出毒性,确定了底泥固化/稳定化的最佳工艺条件。结果表明:仅用水泥固化/稳定化重金属污染底泥,固化体抗压强度随水泥用量的增加而上升,重金属浸出浓度则下降,当水泥∶干底泥质量比为0.6∶1.0时,固化体7 d抗压强度能达到0.99 MPa的标准值;进一步研究发现,水泥∶粉煤灰∶干底泥质量比为0.54∶0.06∶1.0时,重金属浸出浓度有所上升,但7 d及28 d抗压强度仍能分别达到1.2 MPa和2.8 MPa;加入DTCR后,当水泥∶粉煤灰∶DTCR∶干底泥质量比为0.54∶0.06∶0.012∶1.0时,固化体7 d及28 d抗压强度分别为1.1 MPa和2.1 MPa,醋酸缓冲溶液法浸出的Cd、Pb、Zn和Cu浓度分别为0.102、0.189、0.180和0.032 mg/L。     

垃圾焚烧飞灰中Cd、Pb、Zn的螯合稳定与水泥固化处理

采用有机硫稳定剂(DTCR)与水泥对城市垃圾焚烧飞灰进行稳定/固化处理,研究了飞灰中Cd、Pb、Zn的浸出毒性和固化体的抗压强度,比较了螯合稳定与水泥固化对Cd、Pb、Zn的处理效果、养护时间对固化体抗压强度的影响,并对飞灰的结构形貌进行了分析。结果表明,在稳定固化过程中飞灰中发生了复杂的螯合、水化反应,重金属形态由不稳定态向稳定态转变,螯合稳定对Cd的处理效果最好,水泥固化更适用于Pb、Zn。固化时间大于7 d后,飞灰中的重金属以及固化体的抗压强度已较为稳定。螯合稳定协同水泥固化的处理效果优于单一的稳定或固化方法,飞灰在固化7 d后可同时达到重金属浸出毒性和抗压强度标准,满足安全填埋要求。     

铬渣水泥固化及固化体浸出毒性的研究

铬渣水泥固化时要加入硫酸亚铁和添加剂矿渣、粉煤灰，硫酸亚铁可以部分地把六价铬还原为三价铬，能把得到的固化体六价铬浸出毒性降到低于国家标准，抗压强度可达30MPa以上，可综合利用。与此同时，本文考虑日晒、振荡时间和固化体粒度对浸出毒性的影响以及固化体表现浸出率、模拟酸雨淋溶对固化体性能的影响。     

城市河涌受污染底泥的固化/稳定化处理

为了给河涌疏浚底泥的资源化提供技术支持,以广州市车陂涌表层受污染底泥为研究对象,用水泥、石灰、粉煤灰、膨润土等材料对底泥进行固化/稳定化处理实验。通过无侧限抗压强度、污染物在模拟自然条件下(中性)的释放特征、毒性浸出实验(酸性条件)对固化/稳定化处理效果进行综合分析。结果表明:经合适的处理后,固化体抗压强度能高于300 kPa;固化体自然条件下重金属的释放量明显减少,固化/稳定化处理能够有效减缓和减少固化体的二次污染;毒性浸出实验结果表明,河涌底泥经固化/稳定化处理后其重金属浸出能力显著降低。     

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PbHPO_4、Pb_3(PO_4)_2、Pb_5(PO_4)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。     

稳定剂协同水泥固化/稳定化重金属污染土壤的工程特性

采用稳定剂(SR)协同水泥(PC)固化/稳定化重金属污染土壤,以Pb、Zn浸出毒性和药剂吨处理成本为综合指标确定PC和SR的最优配比,并对固化土体进行无侧限抗压强度、不固结不排水三轴压缩实验和柔性壁渗透实验,探讨固化土体强度以及渗透特性。结果表明,最优配比为SR掺量2.5%,PC掺量8%;最优配比下固化土体中重金属铅锌的浸出浓度分别降低97.5%和74.5%,均低于固体危险废物浸出标准值。其养护28 d无侧限抗压强度达到1 080 kPa,比未固化土体对应值高9.6倍;随着PC掺量增加,固化体的有效黏聚力及有效内摩擦角均不断增大,其中最优配比固化土体有效黏聚力达到216.9 kPa,有效内摩擦角为34.8°。加入稳定剂SR使固化体渗透系数增大,但随着PC掺量增加,渗透系数急剧降低。其中最优配比固化土体渗透系数相对未固化复合污染土体降低一个数量级至10~(-6)cm·s~(-1),可有效增强土体的防渗阻隔能力,提高稳定化土壤的安全利用率。     

磷渣-粉煤灰基地聚物材料固化含砷废渣

为了处理有色金属冶炼厂产生的含砷废渣,利用磷渣-粉煤灰基地聚物材料对其进行固化处理。在磷渣∶粉煤灰=60∶40的基础上,通过单因素实验考察了石灰的掺量、化学激发剂水玻璃的模数及掺量、含砷废渣掺量等因素对砷固化体力学性能及砷毒性浸出特性的影响。结果表明:石灰外掺掺量为10%,水玻璃的模数为M=1.2,且其掺量为4%时,砷固化体的抗压强度和As毒性浸出浓度等指标综合效果达到最佳,地聚物材料对含砷废渣的最大固化容量为34%,其固化体抗压强度可达13.6 MPa,砷毒性浸出浓度为2.4 mg·L~(-1),满足危险废弃物堆存国家标准要求。通过XRD、SEM等手段分析可以得出,固化后砷通过化学键合的方式变成难溶盐的形式被地聚物材料牢牢地包裹,结构更加密实。     

城市生活垃圾焚烧飞灰水泥固化技术研究

用硫铝酸盐水泥对城市垃圾焚烧飞灰(简称飞灰)进行固化实验,研究了飞灰重金属浸出特性,分析了飞灰掺量、浸提剂p H值对重金属浸出特性以及飞灰掺量对不同龄期(3、7、28 d)飞灰固化体抗压强度的影响,并对飞灰及其固化体进行XRD分析。结果表明,在HJ/T 299-2007和HJ/T 300-2007两种不同浸出体系下,飞灰中Cu、Zn、Cd、Pb、Cr和Mn等重金属浸出浓度差别较大,建议应根据评价目标合理选择重金属浸出测量方法。其中,飞灰中Pb的浸出浓度超过《危险废物鉴别标准浸出毒性鉴别》(GB 5085.3-2007)限值的3.35倍,因此被列为危险废物,应妥善处理。除飞灰掺量小于40%时的固化体Cd符合标准,其余飞灰固化体Pb和Cd的浸出浓度仍超过《生活垃圾填埋场污染控制标准》(GB 16889-2008)限值,故达不到卫生填埋的要求。固化体抗压强度随飞灰掺量增大而降低,重金属浸出浓度与之相反。飞灰掺量为40%时,固化体中重金属浸出浓度随浸提剂p H值降低而增大,但p H值大于5时,未测出重金属浸出。XRD结果表明:飞灰中可溶性盐参与水泥水化反应,重金属Cr以CrO_2-4的形式固化于钙矾石中。     

水泥回转窑固化处理废弃重金属元素的实验研究

废弃的重金属化学试剂是一类危险的固体废物.通过在水泥回转窑中添加质量小于水泥质量的重金属化学试剂的实验研究表明(本实验添加质量约为水泥的0.1%):掺加化学试剂重金属元素后,各水泥熟料的XRD图谱相似,水泥熟料主要矿物相没有发生大的改变;重金属化学试剂的添加对水泥的7 d、28 d抗压强度的影响较小,符合国家标准;熟料试样在其水化28 d时各重金属的浸出量都很低,已低于工业固体废物浸出毒性鉴别标准规定的指标,由此表明利用水泥回转窑处理废弃化学试剂方法可行.     

高稳定性污泥蛋白发泡剂的发泡特性及应用研究

以污泥蛋白为实验材料，通过加入不同量的稳定剂GP-1，配制成高稳定性污泥蛋白发泡剂，并对高稳定性污泥蛋白发泡剂的发泡特性和影响因素进行研究。结果表明，以污泥蛋白10 mL、水90 mL、GP-1 0.4 g配方组合为研究对象，所制备的泡沫初始体积为770 mL，泡沫泌水时间大于15 h，泡沫半衰期大于64 h，泡沫综合发泡能力为2.2×10⁶ mL·min，泡沫的最佳搅拌时间为5 min，泡沫的泌水时间和泡沫的半衰期都是随着温度的上升而下降，在pH为3～13时泡沫稳定。经过对高稳定性污泥蛋白发泡剂发泡特性研究以及对水泥的胶凝时间、特性进行比较，研制出污泥蛋白泡沫混凝土发泡剂，并制备污泥蛋白泡沫混凝土块；结果表明，当污泥蛋白泡沫混凝土发泡剂的用量分别为0、6、6.8、7.6、8.4和9.2 mL，水泥为200 g时，制备泡沫混凝土块，其密度由2.07 g/cm³下降到0.34 g/cm³，体积由130 cm³ 上升到755 cm³；在泡沫混凝土块脱模后的第1 d、第7 d、第28 d分别称量他们的重量变化情况，结果表明，泡沫混凝土块第1 d和第7 d无重量变化，第28 d的重量明显减轻。该研究为污泥蛋白研制成为泡沫混凝土发泡剂，并应用于屋面隔热、保温建立前期基础。     

Electrokinetic remediation of concrete: effect of chelating agents

Contamination of concrete at various nuclear power plants and spent nuclear fuel reprocessing facilities by radionuclides represents a significant problem for the world's nuclear power industries and nuclear waste management. The present publication summarizes the most recently published data on Electrokinetic Remediation (EK) of various concrete installations and advantageous effects of the combination of EK with different chelating agents. The specific aspects of decontamination of concrete and mortar surfaces are analyzed, such as: (a) effect of chelating agents (EDTA, citric acid), (b) effect of the zeta-potential (zeta) of concrete surface, (c) effects of sorption and complex formation equilibrium, and (d) specific advantages and problems of the electrokinetic decontamination process. The results of laboratory and in situ tests of chelating agent assisted EK removal of radionuclides are reported. It is demonstrated that the correct combination of EK with specific chelating agents can be effectively employed for decontamination of concrete surfaces.     

Effects of injected activated carbon and solidification treatment on the leachability of polychlorinated dibenzo-p-dioxins and dibenzofurans from air pollution control residues of municipal waste incineration

To assess the effectiveness of the injected activated carbon, cement, and sulfur-containing chelating agent in controlling polychlorinated dibenzo-p-dioxins and dibenzofurans (PCDD/Fs) release from the surface of air pollution control (APC) residues, this study examined the leachability of PCDD/Fs from APC residues generated by municipal solid waste incinerators. Results showed that PCDD/Fs were stably retained in the APC residues when the samples were leached with acetic acid solution. Highly chlorinated PCDD/F homologues (i.e., hepta- and octa-CDDs and CDFs) were relatively easy to leach. The leaching percentages of PCDD/Fs from raw APC residue samples containing activated carbon were smaller than those from samples without activated carbon, especially when n-hexane was used as the leachant. These results indicate that the flue gas injected activated carbon not only controls PCDD/F emissions, but also suppresses the leachability of PCDD/Fs from the APC residues. Solidification/stabilization (S/S) processes with 30wt% cement and 5wt% sulfur-containing agent can additionally decrease the leachability of PCDD/Fs with humic acid. Using n-hexane as the leachant, S/S processes increased the leachability of PCDD/Fs. Various low chlorinated PCDD/F congeners were moreover leached out of the APC residue samples, markedly increasing the leachate toxicity. The enhancement of leachability and toxicity owing to S/S processes may negatively impact the environment when APC residues are exposed to nonpolar organic solvents.     

Leaching characteristics of stabilized/solidified fly ash generated from ash-melting plant

This study was designed to elucidate the leaching characteristics of stabilized/solidified (S/S) fly ash generated by ash-melting. For this study, pH-dependent leaching tests, sequential extraction procedures, and column leaching tests were carried out. The pH-dependent leaching test results for Pb, Cu, and Zn showed that the heavy metal concentrations in the high-pH range were lower than the predicted values for hydroxide and carbonate. During sequential extraction, Cu and Pb were principally distributed in the S/S ashes' organic matter fraction in the chelating agent, suggesting that metals bind to the chelating agent. The percentage of the water-soluble fraction for Pb and Cu was low (<0.2 %). The fly ashes treated with a chelating agent and cement had low leachability potential for metals in the high-pH range. Column tests for S/S fly ashes showed that two leaching stages were distinguishable: one for short time, corresponding to faster metal leaching, and another for the leaching rate. Kinetic speciation was then applied to data obtained from column leaching tests. The first-order reaction/diffusion model showed a better fit for Ca, Pb, and Cu, suggesting that the initial dissolution of soluble compounds, such as metal chloride, was controlled by the first-order reaction (surface wash off). Subsequently, insoluble compounds such as hydroxide or carbonate might penetrate into the porous matrix by diffusion.     

Formation, release and control of dioxins in cement kilns

Co-processing of hazardous wastes in cement kilns have for decades been thought to cause increased emissions of PCDD/PCDFs--a perception that has been evaluated in this study. Hundreds of PCDD/PCDF measurements conducted by the cement industry and others in the last few years, on emissions and solid materials, as well as recent test burns with hazardous wastes in developing countries do not support this perception. Newer data has been compared with older literature data and shows in particular that many emission factors have to be reconsidered. Early emission factors for cement kilns co-processing hazardous waste, which are still used in inventories, are shown to be too high compared with actual measurements. Less than 10 years ago it was believed that the cement industry was the main contributor of PCDD/PCDFs to air; data collected in this study indicates however that the industry contributes with less than 1% of total emissions to air. The Stockholm Convention on POPs presently ratified by 144 parties, classifies cement kilns co-processing hazardous waste as a source category having the potential for comparatively high formation and release of PCDD/PCDFs. This classification is based on early investigations from the 1980s and 1990s where kilns co-processing hazardous waste had higher emissions compared to those that did not burn hazardous waste. However, the testing of these kilns was often done under worst case scenario conditions known to favour PCDD/PCDF formation. More than 2000 PCDD/PCDF cement kiln measurements have been evaluated in this study, representing most production technologies and waste feeding scenarios. They generally indicate that most modern cement kilns co-processing waste today can meet an emission level of 0.1ngI-TEQ/m(3), when well managed and operated. In these cases, proper and responsible use of waste including organic hazardous waste to replace parts of the fossil fuel does not seem to increase formation of PCDD/PCDFs. Modern preheater/precalciner kilns generally seems to have lower emissions than older wet-process cement kilns. It seems that the main factors stimulating formation of PCDD/PCDFs is the availability of organics in the raw material and the temperature of the air pollution control device. Feeding of materials containing elevated concentrations of organics as part of raw-material-mix should therefore be avoided and the exhaust gases should be cooled down quickly in long wet and long dry cement kilns without preheating. PCDD/PCDFs could be detected in all types of solid samples analysed: raw meal, pellets and slurry; alternative raw materials as sand, chalk and different ashes; cement kiln dust, clinker and cement. The concentrations are however generally low, similar to soil and sediment.     

Rapid screening of different chelating agents in the lead extraction from cathode ray tube (CRT) funnel glass

The cathode ray tube (CRT) glass is one of the most important problem that afflicts the electronic waste disposal whose solution lies in the identification of efficient and ecofriendly processes to detoxify and reutilize lead-contained funnel glass. This study is focused on a rapid screening of different chemical and mechanochemical processes to reduce lead content in waste CRT glass downgrading the risk correlated to it. In particular, as a possibility to clean waste CRT glass, treatments of lead-containing glass with different chelating agents (EDTA, NTA, ATMP, EDTMP and HEDP) were performed to evaluate their extractive capabilities. Furthermore, the influence of the grinding, the chelating agent functional groups (polyamino-carboxylic acid, carboxylic acid, and polyamino phosphonic acid), and the time and the temperature on lead content reduction were analyzed. ESEM and EDS analysis were performed on all the samples to evaluate the lead amount before and after the treatments.     

Arsenic leachability and speciation in cement immobilized water treatment sludge

Arsenic leachability and speciation in cement immobilized water treatment sludge were investigated with leaching tests and X-ray absorption near edge structure (XANES) spectroscopy. The As leachability in the sludge determined with the toxicity characteristic leaching procedure (TCLP) and the waste extraction test (WET) was 283 and 7490 microgl(-1), respectively. Extractions with a lower liquid to solid ratio, under anaerobic conditions, and using citric acid buffer solution dramatically increased the leachate As concentration. XANES results showed that the As(III) composition was reduced from 51.1% of the total As content in the sludge to 16.3% in the cement treated sample with 28 days of cure. When the cement treated sample was cured for two years, the As(III) composition was decreased to 7.4%. The cement treatment reduced the As leachability. The leachate As(III) and total As concentrations were of the same order of magnitude in the samples cured for 28 days as for 2yr. However, consistently lower concentrations were detected in samples with longer cure time. The results of this study improve our understanding of arsenic speciation and leachability in the cement matrix after long cure times.     

垃圾焚烧飞灰浸出特性及固化试验的研究

垃圾焚烧飞灰残留有重金属元素和二恶英等物质而被认为是危险废物,必须对之进行稳定化处理.通过试验研究分析了国内首家自主开发成功的广东省东莞市某回转窑垃圾焚烧发电厂垃圾焚烧飞灰的化学成分及矿物组成,研究了飞灰的浸出毒性,考察了水泥固化焚烧飞灰的效果,并与熔融/玻璃固化进行了比较.研究表明,该焚烧飞灰中重金属Cd的浸出毒性严重超标,并且随pH值的减小而增大,水泥固化效果随龄期的增大而更加显著.熔融/玻璃固化的效果优于水泥固化,但其经济性有待提高.     

Arsenic contaminated site at an abandoned copper smelter plant: waste characterization and solidification/stabilization treatment

A preliminary survey of an arsenic contaminated site from an abandoned copper smelting facility and feasibility study of using solidification/stabilization (S/S) process to treat the contaminant waste were undertaken. It was found that the waste, located in the three-flue gas discharge tunnels, contained 2-40% arsenic. The pH of the contaminated waste is extremely low (ranging from 1.8 to 3.6). The X-ray diffraction evidence indicates that the arsenic particles present in the flue gas mainly exist as As(III), or As(2)O(3). The total amount of arsenic contaminated waste is estimated to be 700 ton in the studied area. About 50% of the particle sizes are less than 2 mm. Arsenic is easily extracted from wastes with a variety of leaching solutions. In order to meet the arsenic leaching standard of the toxicity characteristic leaching procedure (TCLP), an extremely high cement dosage is required in the S/S process (cement/waste weight ratio>6). The waste with lower particle size having higher specific surface area exhibits somewhat positive effect on the S/S performance. The use of fly ash from municipal waste incinerators, in conjunction with the reduced amount of cement, is able to meet the TCLP arsenic and lead standards. The use of lime alone could meet the TCLP arsenic standard, but lead leaching concentrations exceeded leaching Pb standard. The results of semi-dynamic leaching tests of some solidified samples indicate higher accumulated arsenic leaching concentrations after only a few leachant renewals.