首页 | 本学科首页   官方微博 | 高级检索  
相似文献
 共查询到18条相似文献,搜索用时 62 毫秒
1.
通过批量实验探讨了给水厂废弃铁铝泥(Ferric and Alum Water Treatment Residuals,FARs)对Cd2+的吸附特征及影响因素.实验结果表明,在最初的6 h内,FARs对Cd2+的吸附量已经达到其平衡吸附量的90%,吸附较符合伪二级动力学模型(R2=0.99),并且Langmuir(R2=0.99)和Freundlich(R2=0.90)方程均能较好地描述FARs对Cd2+的等温吸附过程,其Cd2+的饱和吸附量达35.39 mg·g-1.初始溶液p H由3.0增加到8.0时,FARs对Cd2+的吸附量缓慢增加,当p H升为9.0时,其对Cd2+去除率可达97%.FARs对Cd2+的吸附量随溶液体系离子强度的增加而减小.随着柠檬酸浓度的升高,FARs对Cd2+的吸附量显著降低,而水杨酸和酒石酸则微弱促进了对Cd2+的吸附.解吸实验证明,在p H为3.0时Cd2+的解吸率最高,但仅为11%左右.分级提取结果进一步表明,被吸附的Cd2+主要以酸溶态和残渣态存在.综合实验结果表明,FARs可以作为一种高效的吸附剂用于水体除镉.  相似文献   

2.
给水厂废弃铁铝泥(Ferric and aluminum residuals,FARs)可用于控制湖泊沉积物磷释放.因此,在实际应用之前对FARs的风险进行评估非常重要.本研究通过室内富集实验,考察FARs对沉积物中氨氧化菌(ammonia-oxidizing bacteria,AOB)活性、丰度和多样性的影响.结果表明:投加FARs后,沉积物对氨氮的去除能力微弱提高.富集后沉积物中AOB丰度增加,投加FARs的沉积物中AOB丰度达到1.32×108copies·g-1,而未投加FARs的沉积物中AOB丰度为1.14×108copies·g-1.此外,amo A基因的系统发育分析表明富集前后沉积物中的AOB均附属于Nitrosospira和Nitrosomonas两个种属,并且投加FARs沉积物中AOB的多样性略高于未投加的.综上结果表明,FARs回用于湖泊富营养化控制的同时,将有益于沉积物中好氧氨氧化作用的进行.  相似文献   

3.
给水处理厂废弃铁铝泥对正磷酸盐的吸附特征   总被引:1,自引:4,他引:1  
王昌辉  裴元生 《环境科学》2011,32(8):2371-2377
以给水处理厂废弃铁铝泥(ferric-alum residuals,FARs)为载体,探究了FARs对正磷酸盐的吸附特征.ICP、SEM和XRD测试结果表明,FARs富含铁铝元素且为无定形结构.批量平衡实验法证实,FARs对正磷酸盐的吸附较符合伪二级动力学模型.在酸性环境条件下,磷的吸附效果最好,当pH值从4.6升至7...  相似文献   

4.
给水厂污泥改良生物滞留填料除磷效果的研究   总被引:3,自引:5,他引:3  
王建军  李田  张颖 《环境科学》2014,35(12):4642-4647
通过静态吸附实验研究了土壤、给水厂污泥对磷的吸附特性,采用生物滞留模拟柱,考察生物滞留技术对城市径流中磷的去除效果,评价以给水厂污泥改良填料的可行性.结果表明,给水厂污泥对磷的吸附能力远大于土壤.在进水磷浓度为1.0 mg·L-1条件下,传统填料模拟柱出水总磷随着进水量的增加浓度逐渐增大,而改良填料模拟柱表现出稳定的长期去除效果,经7个月的连续运行,改良填料模拟柱出水总磷的浓度仍小于0.050 mg·L-1,满足地表水Ⅲ类水质标准.根据静态吸附实验估算结果,相同的控制条件下,添加4%给水厂污泥的改良填料对磷的吸附能力约为传统填料的4倍.无定型铁铝的沉淀、吸附作用是改良填料截留进水中磷的主要机制,工程应用中可在填料中添加4%~5%比例的给水厂污泥以提高生物滞留设施控制受纳水体富营养化的效果.  相似文献   

5.
铁盐改性废弃蛋壳对水中磷的吸附特征研究   总被引:2,自引:2,他引:2       下载免费PDF全文
采用铁盐对废弃蛋壳进行化学改性,并研究改性蛋壳对水中磷的吸附特征.结果表明,改性蛋壳明显提高磷的吸附能力,磷在改性蛋壳中的吸附是一吸热过程,其吸附等温线符合Freundlich方程,磷在改性蛋壳中的吸附历时曲线遵循准二级反应动力学模型.溶液pH值显著影响磷在改性蛋壳中的吸附效果,当pH3时,改性蛋壳对磷具有吸附最大值.  相似文献   

6.
给水厂污泥具有较强的吸附能力,可作为从水溶液中去除重金属的潜在吸附剂。通过试验分析了给水厂污泥(WTR)作为吸附剂去除溶液中Hg(Ⅱ)时,pH值、Hg(Ⅱ)初始浓度、污泥粒径以及温度对Hg(Ⅱ)吸附性能的影响,确定了吸附过程的动力学及吸附等温模型,并探究了其吸附机理。结果表明:溶液pH值对给水厂污泥吸附Hg(Ⅱ)具有较大影响,当pH=8.0时吸附效果最佳。采用粒径较小的污泥有利于对Hg(Ⅱ)的吸附,污泥对Hg(Ⅱ)的吸附量随着初始浓度的增加而增加。给水厂污泥对Hg(Ⅱ)的吸附符合准二级动力学模型,平衡等温线符合Langmuir吸附等温模型,25℃条件下pH为7.0时污泥的饱和吸附量达到69.13 mg/g。升温有利于给水厂污泥对Hg(Ⅱ)的吸附。通过分析吸附前后污泥比表面积和微孔体积的变化发现,颗粒内扩散是给水厂污泥吸附Hg(Ⅱ)的限速步骤。  相似文献   

7.
在大多数生态系统中,磷(P)元素是植物生长的限制性元素,也是造成水体富营养化的主要原因.而水体中P的去除方法中尤以吸附法的研究和应用最为广泛.本文以稻草秸秆为原料,Ca Cl2(质量分数10%)为活化剂制备活性生物质炭,作为控制农业面源污染的吸P材料.通过控制稻草秸秆炭制备的炭化温度、浸渍比等工艺条件及溶液初始P浓度、吸附时间、秸秆炭用量、干扰离子、pH等试验条件,研究改性稻草秸秆炭吸P性能及其吸附机理.试验结果表明:在考虑经济性的前提下,稻草秸秆炭吸P性能最优的制备工艺条件为:炭化温度为700℃,浸渍比(m稻草∶m氯化钙)为1∶0.5;改性稻草秸秆炭处理含10 mg·L-1PO3-4-P(以P计)水样,P去除率可达到97%,溶液pH从6.87升至9.52;对稻草秸秆炭对P的吸附情况采用Langmuir和Freundlich吸附模型进行拟合,R2可分别达到0.947和0.892,说明其主要为单分子层化学吸附;此外,根据溶液的pH和P浓度的变化情况,推测P的吸附主要由离子交换实现,即PO3-4-P(主要为H2PO-4)取代结合在Ca离子上的氢氧根而被吸附,秸秆炭上的氢氧根释放,水样pH值上升.  相似文献   

8.
针对高效低廉的吸附材料——WTR(water treatment residuals,给水厂残泥)因颗粒细小在水处理工艺中难以应用的问题,利用免烧法制备出WTR陶粒,研究其对Pb和Cd的吸附特征.批量吸附试验结果表明,准二级动力学模型和Langmuir等温吸附模型能较好地描述WTR免烧陶粒对Pb和Cd的吸附动力学(R2>0.995 8)与等温吸附过程(R2>0.994 8).在溶液pH为5、恒温25℃、振荡24 h下,Langmuir等温吸附模型计算得到的WTR免烧陶粒对Pb和Cd的最大吸附容量分别为13.97和18.60 mg/g.单因素条件试验结果表明,WTR免烧陶粒对Pb和Cd的吸附量均随溶液初始pH的升高而增加,当pH由3升至9时,WTR免烧陶粒对Pb和Cd的吸附量分别增加了1.44和0.95倍;离子强度的增加不利于WTR免烧陶粒对Pb和Cd的吸附.批量等温解吸试验结果表明,在pH为4~8的溶液中,Pb和Cd较难从WTR免烧陶粒中解吸出来,解吸率均在3.5%以内;当溶液pH为3时,Pb和Cd的解吸率分别高达65.88%和45.01%.BCR分级提取结果表明,Pb和Cd均主要以酸提取态形式(占比在68.18%以上)存在于WTR免烧陶粒中;同时,随着初始吸附量的增加,酸提取态比例显著减少,而还原态和残渣态比例显著增加.研究显示,WTR免烧陶粒对Pb和Cd具有较强的吸附能力,可作为一种高效的重金属吸附材料应用于水处理工艺中.   相似文献   

9.
铝污泥酸化提取液改性沸石的除磷特性及机制   总被引:1,自引:1,他引:1  
韩芸  胡玉洁  连洁  杨思哲  齐泽宁 《环境科学》2019,40(8):3660-3667
为了提高沸石的除磷能力并降低改性成本,以给水厂铝污泥为铝源,采用酸化提取液合成层状双氢氧化物(LDHs)覆膜于沸石表面制备改性沸石,分别测定原沸石、Al-Zn改性沸石及铝污泥改性沸石的表面特性和化学组分,分析等温吸附及吸附动力学特性,探讨铝污泥改性沸石的除磷性能及除磷机制.结果表明,最佳酸化提取条件为60 min、150 r·min~(-1)和p H1. 0,该条件下1 g铝污泥(干重)可提取77 mg的铝;改性沸石的饱和吸附容量和解吸性能较原沸石显著提高,尤其是铝污泥改性沸石,其理论最大吸附量从30. 24 mg·kg~(-1)提升至170. 40 mg·kg~(-1);改性使得沸石对磷酸盐的主要吸附类型由物理吸附向化学吸附转变.以铝污泥为铝源改性沸石能有效地提高其对磷酸盐的吸附能力及再生能力,在降低磷浓度过高引发的水体富营养化风险的同时,实现以废治废的目的.  相似文献   

10.
文章以P、Fe为处理对象,考察了活性炭、沸石、陶粒和石英砂4种材料的吸附特性。结果表明:当pH为7.0时,P的饱和吸附量依次为活性炭(0.14 mg/g)沸石(0.09 mg/g)陶粒(0.08 mg/g)石英砂(0.06 mg/g),Fe的饱和吸附量依次为活性炭(0.79 mg/g)陶粒(0.76 mg/g)沸石(0.51 mg/g)石英砂(0.26 mg/g);颗粒内扩散模型表明各材料对P、Fe的吸附分为表面扩散和内扩散2个阶段,且内扩散为速率控制步骤,吸附饱和时间为240 min;(3)P和Fe的有利吸附条件分别为酸性和碱性,结合实际水体的pH和实验结果,pH为7.0最为合适;随材料投加量增加,P和Fe的单位吸附量减少,但去除率增大;吸附材料的最佳投加量为100 g/L。  相似文献   

11.
As safe byproducts of drinking water treatment processes,ferric and alum water treatment residuals(FARs) have the potential to be new phosphate(P) immobilization materials.In this study,batch experiments were conducted to investigate and compare the adsorption characteristics of three P species by FARs.The results showed that the kinetic processes of different P species’ adsorption by FARs could be described by a pseudo second-order model.The ranking list of the initial adsorption rates with respect to different phosphates was pyrophosphate,phytate,orthophosphate,hexametaphosphate and glycerophosphate.Of the six models considered,the two-site Langmuir model most effectively described the adsorption characteristics of the various P species.Upon fitting the results,the maximum adsorption capacities were determined to be 40.24 mg/g for phytate,18.04 mg/g for pyrophosphate,17.14 mg/g for orthophosphate,15.86 mg/g for hexametaphosphate and 10.81 mg/g for glycerophosphate.In addition,the adsorption processes of the different P species were spontaneous endothermic processes and were favored at lower pH values.The pH dependency was found to be especially true for orthophosphate,where the adsorption capacity decreased by 1.22 mg/g with an increase in pH from 5 to 9.Fractionation of the adsorbed P species from the FARs demonstrated that Al-P and Fe-P were the dominating forms,constituting approximately 80%-90% of the total P fractions,which indicated that the adsorbed P species had a low leaching risk and could stably exist in the FARs.Therefore,the FARs could be effective in controlling pollution in water caused by different P species.  相似文献   

12.
林璐  胥嘉瑞  吴昊  王昌辉  裴元生 《环境科学》2013,34(7):2758-2765
以给水处理厂废弃铁铝泥(ferric and alum water treatment residuals,FARs)为载体,考察了不同粒径FARs对砷(Ⅲ)的吸附效果.不同粒径FARs的有效铁铝含量、比表面积和孔体积分别为523.72~1 861.72 mmol.kg-1、28.15~265.59 m2.g-1和0.03~0.09 cm3.g-1,总有机质、富里酸、胡敏酸和胡敏素分别为46.97~91.58、0.02~32.27、22.27~34.09和10.76~34.22 mg.kg-1.SEM和XRD检测表明,不同粒径FARs均以无定形结构存在.批量实验结果表明,准一级和准二级动力学方程均能较好地反映FARs吸附砷(Ⅲ)的动力学过程.不同粒径FARs对砷(Ⅲ)的吸附量随着浓度的增加而增高,用Langmuir等温线方程拟合获得理论饱和吸附量在6.72~21.79 mg.g-1之间.pH值对FARs吸附砷(Ⅲ)的作用影响不大.砷(Ⅲ)吸附量大小与不同粒径FARs的理化性质的变化趋势基本一致,由相关性分析可得,有效铁铝含量和孔体积大小是影响FARs对砷(Ⅲ)吸附的主要因素.  相似文献   

13.
给水厂浓缩污泥的稳态流变特征研究   总被引:2,自引:2,他引:2  
针对给水厂浓缩污泥,采用旋转流变仪研究了其稳态流变特性,分别探讨了污泥的典型流变图、污泥浓度和温度对浓缩污泥极限粘度的影响.结果表明,污泥具有触变及剪切变稀的性质,其极限粘度(η∞)与污泥浓度(TSS)的关系符合指数关系,可用方程η∞=24.43-494.62e-0.14TSS描述.极限粘度与温度的关系服从于阿伦尼乌斯公式,相应的反应活化能为14.91J·mol-1.此外,宾汉模型可以描述污泥的流变性质,屈服应力随污泥浓度的升高而增加.  相似文献   

14.
Drinking water treatment residuals(WTRs) have a potential to realize eutrophication control objectives by reducing the internal phosphorus(P) load of lake sediments. Information regarding the ecological risk of dewatered WTR reuse in aquatic environments is generally lacking, however. In this study, we analyzed the eco-toxicity of leachates from sediments with or without dewatered WTRs toward algae Chlorella vulgaris via algal growth inhibition testing with algal cell density, chlorophyll content, malondialdehyde content, antioxidant enzyme superoxide dismutase activity, and subcellular structure indices. The results suggested that leachates from sediments unanimously inhibited algal growth, with or without the addition of different WTR doses(10% or 50% of the sediment in dry weight) at different p H values(8–9), as well as from sediments treated for different durations(10 or 180 days). The inhibition was primarily the result of P deficiency in the leachates owing to WTR P adsorption, however, our results suggest that the dewatered WTRs were considered as a favorable potential material for internal P loading control in lake restoration projects, as it shows acceptably low risk toward aquatic plants.  相似文献   

15.
Phosphate is one of the most predominant pollutants in natural waters. Laboratory experiments were conducted to investigate the phosphate adsorption performance of a(NFS) made from drinking water treatment residuals. The adsorption of phosphate on the NFS fitted well with the Freundlich isotherm and pseudo second-order kinetic models. At p H 7.0, the maximum adsorption capacity of 1.03 mg/g was achieved at 15°C corresponding to the wastewater temperature in cold months, and increased notably to 1.31 mg/g at 35°C.Under both acidic conditions(part of the adsorption sites was consumed) and basic conditions(negative charges formed on the surface of NFS, which led to a static repulsion of PO43-and HPO42-), the adsorption of phosphate was slightly inhibited. Further study showed that part of the adsorption sites could be recovered by 0.25 mol/L Na OH. The activation energy was calculated to be above 8.0 k J/mol, indicating that the adsorption of phosphate on NFS was probably a chemical process. Considering the strong phosphate adsorption capacity and recoverability, NFS showed great promise on enhancing phosphate removal from the secondary treated wastewater in the filtration process.  相似文献   

16.
A study on the removal of Co(Ⅱ) from aqueous solutions by water treatment residuals(WTR)was conducted in batch conditions. The sorption process of Co(Ⅱ) followed pseudosecondorder kinetics, with 30 hr required to reach equilibrium. Using the Langmuir adsorption isotherm model, a relatively high maximum sorption capacity of 17.31 mg/g Co(Ⅱ) was determined. The adsorption of Co(Ⅱ) was dependent on pH values and was affected by the ionic strength. Results show that Co(Ⅱ) adsorption was a spontaneous endothermic process and was favorable at high temperature. Most of the adsorbed Co(Ⅱ) stayed on the WTR permanently, whereas only small amounts of adsorbed Co(Ⅱ) were desorbed. The shifting of peaks in FT-IR spectra indicated that Co(Ⅱ) interacted with the WTR surface through strong covalent bond formation with Fe(Al)–O functional groups. It was concluded that WTR can be a suitable material from which to develop an efficient adsorbent for the removal of Co(Ⅱ) from wastewater.  相似文献   

17.
Batch experiments were conducted to investigate the phosphorus(P) adsorption and desorption on five drinking water treatment residuals(WTRs) collected from different regions in China. The physical and chemical characteristics of the five WTRs were determined. Combined with rotated principal component analysis, multiple regression analysis was used to analyze the relationship between the inherent properties of the WTRs and their P adsorption capacities. The results showed that the maximum P adsorption capacities of the five WTRs calculated using the Langmuir isotherm ranged from 4.17 to8.20 mg/g at a p H of 7 and further increased with a decrease in p H. The statistical analysis revealed that a factor related to Al and 200 mmol/L oxalate-extractable Al(Alox) accounted for 36.5% of the variations in the P adsorption. A similar portion(28.5%) was attributed to an integrated factor related to the p H, Fe, 200 mmol/L oxalate-extractable Fe(Feox), surface area and organic matter(OM) of the WTRs. However, factors related to other properties(Ca,P and 5 mmol/L oxalate-extractable Fe and Al) were rejected. In addition, the quantity of P desorption was limited and had a significant negative correlation with the(Feox+ Alox) of the WTRs(p 〈 0.05). Overall, WTRs with high contents of Alox, Feoxand OM as well as large surface areas were proposed to be the best choice for P adsorption in practical applications.  相似文献   

18.
氢氧化铁对砷的吸附与沉淀机理   总被引:14,自引:1,他引:13  
研究了吸附反应时间为50d和1120d时,As(V)初始浓度和pH值对氢氧化铁吸附砷的影响,并利用傅利叶红外光谱(FTIR)和粉末X射线衍射技术对吸附砷后的氢氧化铁固体进行了表征.结果表明,氢氧化铁对砷的吸附能力与pH有关,在弱酸性到弱碱性条件下,吸附砷的能力最强;在低初始砷浓度(0.01~1 mmol·L-1)和相同pH条件下,吸附率随砷浓度增高而增大.当pH=3、7和12时,吸附等温线都可用Freundlich公式来进行拟合,低初始砷浓度下(0.001~1 mmol·L-1),R2>0.99,高初始砷浓度下(5~1000 mmol·L-1),R2>0.93,吸附反应时间对吸附能力影响不大.红外光谱分析表明,在pH=3条件下,初始砷浓度为50mmol·L-1和500mmol·L-1时,吸附后氢氧化铁固体的红外光谱图上As-O键的伸缩振动谱带分别位于806.11cm-1和821.54cm-1;表明吸附后的氢氧化铁表面有少量的砷酸铁晶体沉淀存在,砷在氢氧化铁表面的平均密度对砷在氢氧化铁表面存在形态有影响.X射线衍射分析表明.在中性和酸性条件下,砷可能是以双配位表面络合的质子化的=FeO2As(O)(OH)-和非质子化的=FeO2As(O)2-形态存在于氢氧化铁表面.  相似文献   

设为首页 | 免责声明 | 关于勤云 | 加入收藏

Copyright©北京勤云科技发展有限公司  京ICP备09084417号