共查询到20条相似文献,搜索用时 234 毫秒
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通过溶液聚合法来制取功能高分子材料,并研究了引发剂、交联剂、单体用量等对材料吸附性能的影响,研究结果表明:交联剂用量在0.3%时,材料的吸附水和铅离子或铜离子的性能相对较好,对溶液中铜离子的吸附率达到95.2%,吸附量为143 mg/g,对铅离子的吸附率达到84.8%,吸附量为85 mg/g;引发剂用量在0.5%时,材料的吸附水和铅离子或铜离子的性能相对较好,对溶液中铜离子的吸附率达到94.8%,吸附量为142 mg/g,对铅离子的吸附率达到87.9%,吸附量为88 mg/g;当SAS用量为20%时,材料的材料的吸附水和铅离子或铜离子的性能相对较好,对溶液中铜离子的吸附率达到94.7%,吸附量为142 mg/g,对铅离子的吸附率达到87.8%,吸附量为88 mg/g. 相似文献
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研究了活性炭分别对铅、镉、铜及锌离子的吸附作用,研究了pH值、温度及活性炭的投加量等因素对吸附效果的影响。结果表明,当pH〉5时对四种离子的去除率均达到98%以上,能达到很好的吸附。低温有利于吸附的进行。随着活性炭的增加.重金属离子的去除率增加.而且铜离子的活性炭最佳用量是0.3000g.铅、镉和锌的活性炭最佳用量均为1.000g。随着吸附时间的增加,去除率上升。铜、铅、镉和锌离子的吸附平衡时间分别为3.5h、1h、1.5h和1.5h。铜离子的吸附符合Langmuir等温模式,而锌、铅和镉离子的吸附符合Freundlich等温模式。 相似文献
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以西宁盆地坡缕石黏土为吸附剂,研究了其对铅离子吸附性能的影响。考察了黏土的改性方法、搅拌时间、黏土投加量、吸附温度、溶液初始铅离子质量浓度等因素对吸附效果的影响。结果表明:西宁盆地坡缕石黏土对铅离子具有良好的吸附性能。适宜的吸附条件:采用硫酸为改性剂,硫酸用量为10 g黏土加入0.049 g硫酸;搅拌时间为50 min,黏土投加量为100 mL铅液加入0.10~0.15 g黏土,吸附温度为室温。在此条件下,当溶液中铅离子初始质量浓度为107.65 mg/L时,黏土对铅离子的吸附容量达到107 mg/g以上,铅离子去除率接近100%。在实验质量浓度范围内,铅离子在黏土上的吸附符合Langmuir等温线。 相似文献
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活性炭/粉煤灰处理含铜废水的研究 总被引:1,自引:0,他引:1
《应用化工》2015,(6):995-999
采用活性炭/粉煤灰处理模拟含铜废水,考察pH、吸附时间、吸附温度、投加量、质量比、活性炭、粉煤灰粒径、铜离子浓度等对吸附效果的影响。结果表明,单纯粉煤灰的吸附效果较差,但100目的粉煤灰与100目的活性炭混合,其吸附效果接近于纯活性炭。活性炭/粉煤灰处理100 m L、30 mg/L模拟含铜废水的最佳吸附条件为:吸附时间3 h,pH 6,吸附温度45℃,活性炭/粉煤灰(质量比1∶1)投加量2.5 g,活性炭和粉煤灰粒径均为100目。在此条件下,铜离子去除率可达97.33%,处理后水中铜离子浓度(0.811 4 mg/L)低于国家二级排放标准(1.0 mg/L)。 相似文献
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《应用化工》2022,(6):995-999
采用活性炭/粉煤灰处理模拟含铜废水,考察pH、吸附时间、吸附温度、投加量、质量比、活性炭、粉煤灰粒径、铜离子浓度等对吸附效果的影响。结果表明,单纯粉煤灰的吸附效果较差,但100目的粉煤灰与100目的活性炭混合,其吸附效果接近于纯活性炭。活性炭/粉煤灰处理100 m L、30 mg/L模拟含铜废水的最佳吸附条件为:吸附时间3 h,pH 6,吸附温度45℃,活性炭/粉煤灰(质量比1∶1)投加量2.5 g,活性炭和粉煤灰粒径均为100目。在此条件下,铜离子去除率可达97.33%,处理后水中铜离子浓度(0.811 4 mg/L)低于国家二级排放标准(1.0 mg/L)。 相似文献
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油茶果壳活性炭对铜离子的吸附性能 总被引:1,自引:0,他引:1
利用油茶壳活性炭吸附铜离子,探讨了时间、pH值、Cu(Ⅱ)初始质量浓度等因素对油茶壳活性炭吸附性能的影响;并分析了其吸附等温曲线和动力学方程。结果表明,油茶壳活性炭对铜离子吸附量可达到63.6 mg/g。油茶壳活性炭对铜离子的去除率随吸附时间的增加而增大,5 h后达到平衡;随着pH值的升高,油茶壳活性炭吸附铜离子的吸附量不断下降。油茶壳活性炭对铜离子的吸附等温数据符合Langmuir方程,吸附动力学过程可用准二级动力学模型进行模拟,相关系数为0.997 5。 相似文献
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以硫酸为改性剂,对钙基膨润土进行活化改性,考察了改性剂用量、改性膨润土加入量、吸附时间以及pH值等因素对改性膨润土去除模拟水样中重金属离子Ph^2+的影响。结果表明,用体积浓度为20%的硫酸溶液改性后的膨润土的除铅效果最好,在常温下,当改性膨润土用量为15g/L,吸附时间为30min,pH值为6-9时废水中铅的去除率最大,超过99.5%,处理后铅的剩余浓度小于1mg/L,达到国家第一类污染物排放标准。 相似文献
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Maria Harja Gabriela Buema Daniel-Mircea Sutiman Corneliu Munteanu Daniel Bucur 《Korean Journal of Chemical Engineering》2012,29(12):1735-1744
We investigated the utilization of ash and modified ash as a low-cost adsorbent to remove copper ions from aqueous solutions such as wastewater. Batch experiments were conducted to determine the factors affecting adsorption of copper. The influence of pH, adsorbent dose, initial Cu2+ concentration, type of adsorbent and contact time on the adsorption capacity of Cu2+ from aqueous solution by the batch adsorption technique using ash and modified ash as a low-cost adsorbent were investigated. The optimum pH required for maximum adsorption was found to be 5. The results from the sorption process showed that the maximum adsorption rate was obtained at 300 mg/L when a different dosage of fly ash was added into the solution, and it can be concluded that decreasing the initial concentration of copper ion is beneficial to the adsorption capacity of the adsorbent. With the increase of pH value, the removal rate increased. When the pH was 5, the removal rate reached the maximum of over 99%. When initial copper content was 300 mg/L and the pH value was 5, the adsorption capacity of the zeolite Z 4 sample reached 27.904 mg/g. The main removal mechanisms were assumed to be the adsorption at the surface of the fly ash together with the precipitation from the solution. The adsorption equilibrium was achieved at pH 5 between 1 and 4 hours in function of type of adsorbent. A dose of 1: 25 g/mL of adsorbent was sufficient for the optimum removal of copper ions. For all synthesized adsorbents the predominant mechanism can be described by pseudo-second order kinetics. 相似文献
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An aminated bagasse (AB) with high‐adsorption capacity for mercury ions was prepared by grafting copolymerization of acrylonitrile onto sugarcane bagasse, followed by aminating with chelating molecule diethylenetriamine. Effects of grafting conditions such as irradiation dosage, acrylonitrile concentration, and solvents on the grafting yield were investigated. The adsorption performance for mercury ions were evaluated by batch adsorption experiments and kinetic experiments. The results show that AB is effective for the removal of mercury over a wide range of pH > 5. Adsorption isotherms of mercury ions on the modified bagasse can be well described by Langmuir equation. The equilibrium adsorption amount could be as high as 917.4 mg/g, and the removal percent of mercury ions can achieve 99%. The kinetic adsorption results indicate that AB could remove 80% of mercury ions in 2 h and 24 more hours are needed to achieve adsorption equilibrium. Regeneration experiments show that the adsorption capacity of recycled AB still can reach the level of 96% after four cycles. © 2010 Wiley Periodicals, Inc. J Appl Polym Sci, 2010 相似文献
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《分离科学与技术》2012,47(2):330-339
Introduction of xanthate group onto sugarcane (Saccharum officinarum) bagasse has been investigated for the removal of cadmium, lead, nickel, zinc, and copper from their aqueous media. The charred xanthated sugarcane bagasse (CXSB) was found to have significant adsorption capacity which is more than that of various bio-sorbents mentioned in the available literatures. The newly developed bio-sorbent was characterized by SEM, FTIR, TGA/DTA, and elemental analysis. The velocity of sorption of the tested metals was fast, reaching equilibrium within 40 min. The maximum loading capacities was found to be 225 for Cd(II), 318 for Pb(II), 144 for Ni(II), 164 for Zn(II), and 178 for Cu(II) mg g?1, respectively. The fast kinetics results and high adsorption capacity indicated that CXSB can be applied as the selective adsorbent for the treatment of heavy metal ions from aqueous solutions. 相似文献
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将颗粒状活性炭作为三维电极的粒子,采用三维电极法去除配位电镀废水中的镍离子和铜离子。考察了pH值、电流、极板间距、炭水比(粒子电极活性炭与处理水量的体积比)对镍离子和铜离子去除率的影响。在设定的范围内,镍离子和铜离子的去除率随pH值的升高呈现先升后降的变化趋势,随电流和炭水比的增大而升高,随极板间距的增大而降低。当废水中镍离子和铜离子的初始质量浓度分别为82.309 3mg/L和52.761 5mg/L、活性炭的体积为1 000mL、处理时间为2.0h时,最佳的处理工艺条件为:pH值4、电流0.6A,极板间距20cm,炭水比10∶9。此时,镍离子和铜离子的去除率分别为83.40%和86.20%。出水经过混凝沉淀后,镍离子和铜离子的去除率分别达到99.87%和99.68%,在出水中的质量浓度分别为0.107 2mg/L和0.169 3mg/L,出水水质达到《电镀污染物排放标准》(GB 21900—2008)中表2的排放限值。 相似文献
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采用共沉淀法制备了硝酸根型层状复合金属氢氧化物NiCoFe-LDHs,研究其对水中的三价砷的吸附性能,系统研究溶液初始浓度、吸附时间以及溶液pH值等因素对吸附性能的影响。结果表明,当As(Ⅲ)溶液浓度为2 mg/L时,吸附率达到了81.1%,吸附量在As(Ⅲ)溶液浓度为4 mg/L时,达到了15.72 mg/g,而溶液pH值为8时,吸附性能最好,且吸附过程在30 min内可以达到平衡。热力学和等温吸附式的研究表明NiCoFe-LDHs对As(Ⅲ)的吸附过程,符合Langmuir模型和伪二级动力学模型,因此吸附过程发生在吸附剂表面,且吸附过程为化学吸附。 相似文献
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以异丙醇钛为前体,十二烷胺为模板剂,采用配体辅助模板法合成高比表面积多孔二氧化钛材料,利用氮气吸附对其孔径性质进行分析。通过静态吸附实验研究了多孔二氧化钛对刚果红的吸附行为,考察了吸附时间、温度、搅拌速度、吸附剂用量和初始浓度对刚果红吸附效果的影响。分别在相关条件下,结果表明:当吸附时间为30min时,脱除率达98%以上;吸附温度为45℃时,脱除率可达98%;摇床转速为160r/min时,脱除率达到最大;当吸附剂使用量为0.10g时,脱除率能够达到98%左右,已能够满足应用要求;多孔二氧化钛吸附刚果红的吸附量与刚果红初始浓度成正比。 相似文献
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以钠基蒙脱石(Na-MMT)、钛酸四丁酯作基质材料,通过溶胶-凝胶法制备了钛柱撑蒙脱石(Ti-MMT)。利用XRD、FTIR及SEM对Ti-MMT进行了结构表征,考察了不同吸附条件对Ti-MMT吸附Ni~(2+)和Mn~(2+)的影响,并重点分析水溶液pH对Ti-MMT Zeta电位及吸附的影响,探究了Ti-MMT吸附Ni~(2+)和Mn~(2+)的机理。结果表明:Ti-MMT具有较大的晶面间距(d001=2.94 nm);pH对吸附Ni~(2+)与Mn~(2+)有较大影响,去除率随初始水溶液pH增加而提高。在pH=7,Ni~(2+)和Mn~(2+)初始质量浓度为50 mg/L,Ti-MMT投加量分别为5和9 g/L时,Ni~(2+)在318 K下吸附120 min,吸附量可达9.46 mg/g,去除率可达94.59%,Mn~(2+)在328 K下吸附180 min,吸附量可达4.82mg/g,去除率可达86.73%。此外,Ti-MMT对两种离子的吸附都更符合Temkin等温吸附模型及拟二级动力学模型,吸附过程受液膜扩散、颗粒内扩散等环节控制,且以离子交换的化学吸附为主。热力学分析表明,Ti-MMT对Ni~(2+)的吸附属于自发吸热熵增过程,而Mn~(2+)属于吸热熵增的非自发过程。 相似文献
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