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聚丙烯酰胺膨润土复合物的制备及其性能研究 总被引:3,自引:0,他引:3
采用盐酸对膨润土(BNT)进行酸活化改性,改性BNT再与氯化乙醇胺(EACl)进行阳离子交换反应,引入功能基团,得到胺化产物(ABNT-EACl).利用ABNT-EACl作为还原剂与Ce4 组成氧化还原引发体系,引发了丙烯酰胺(AM)单体的插层聚合得到了改性膨润土/聚丙烯酰胺无机/有机杂化物(ABNT/PAM).采用1H-NMR和FTIR对杂化物进行了结构表征,结果表明,杂化物中存在离子键合作用.通过实验对比研究了不同条件下的杂化物ABNT/PAM与普通絮凝剂处理工业印染废水的脱色效果,发现ABNT/PAM杂化物的效果优于普通絮凝剂. 相似文献
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腐殖酸以及共存阳离子对膨润土吸附废水中铅离子的影响 总被引:3,自引:0,他引:3
研究了钠基膨润土的理化性质及其对水中铅离子的吸附作用,考查了pH值、共存阳离子浓度、腐殖酸浓度对铅离子吸附的影响,结果表明,钠基膨润土对水中铅离子有较好的吸附效果.铅离子在膨润土上的吸附量随pH值的升高而增加,随共存阳离子浓度的升高而减少,随腐殖酸浓度的升高而增加.从热力学角度探讨了吸附机理,发现钠基膨润土对铅离子的吸附量随温度升高而增大,并且吸附等温线符合Freundlich模型.计算了相关的吸附热力学函数:△H=0.9594kJ/mol, △S=16.611 3kJ/(mol·K). 相似文献
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膨润土对复合污染中表面活性剂的吸附及机理 总被引:7,自引:2,他引:7
选取阳离子表面活性剂氯化十六烷基吡啶(CPC)、阴离子表面活性剂十二烷基苯磺酸钠(SDBS)及非离子表面活性剂Triton X-100(TX-100)为代表,研究了其在膨润土上的吸附行为,探讨了膨润土阳离子交换容量(CEC)、温度、盐度对CPC吸附的影响.结果表明,Na基膨润土对CPC的吸附性能最好,对SDBS基本无吸附,对TX-100的吸附介于两者之间.Na基膨润土对CPC的吸附是阳离子交换和疏水键缔合共同作用的结果,对TX-100的吸附主要是通过其与膨润土硅氧表面间的氢键作用,同时通过疏水键作用形成吸附双分子层;SDBS在Ca基膨润土上的吸附损失量先增大后减小,在1.5倍临界胶束浓度 (CMC)时达到极大值,主要机理是SDBS与膨润土中的Ca2+产生沉淀作用,而胶束具有再溶解沉淀的作用.膨润土对CPC的吸附量随着温度升高而降低,随着CEC的增大而增大,一定浓度NaCl的加入有利于其在膨润土上的吸附. 相似文献
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以铝柱撑膨润土负载纳米Fe_3O_4制备出性能良好的复合型催化剂。结合X射线粉末衍射(XRD)、扫描电镜(SEM)和比表面孔隙分析(BET)对催化剂的晶相、比表面积和粒度进行表征。负载的纳米Fe_3O_4粒径约为20~30nm,均匀分散到膨润土表面,未发生明显的团聚。在紫外光作用下用该催化剂对焦化厂二沉池出水进行深度处理。结果表明,在催化剂投加量为0.7 g/L,pH为2.5,温度40℃,H_2O_2初始浓度为17.6mmol/L的反应条件下,二沉池出水(化学需氧量COD=140mg/L,色度=400度)经催化氧化降解后,COD和色度可分别降低到54.44 mg/L和10度,达到国家工业再生用水水质标准GB/T 19923-2005(COD≤60 mg/L,色度≤30度)。催化剂重复使用4次时,废水COD和色度去除率保持稳定。 相似文献
16.
铁铜内电解-膨润土组合工艺处理含铬废水 总被引:1,自引:0,他引:1
研究利用铁铜内电解工艺和膨润土吸附的联合作用,对含铬废水进行处理。含铬模拟废水首先经过铁铜内电解法装置,该出水再经膨润土吸附,以达到去除效果。并考察此组合工艺的各种影响因素。结果表明:(1)铁铜内电解预处理确定最佳反应参数为:铁铜用量之比为8:1,反应时间为100 min,pH值为3.0;(2)膨润土最佳吸附条件为:膨润土用量为2 g/l,反应时间为20 min;(3)在最佳反应条件下,对初始浓度分别为30 mg/l和60 mg/l的实际制革废水中的铬进行了处理,都取得较好的去除效果,其Cr(VI)去除率分别为99.54%和99.32%。 相似文献
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The optimal condition for a one-step process removing organic compounds from coking wastewater by simultaneously synthesized organobentonite as a pretreatment was investigated. Results showed that sorption of organic compounds by organobentonite was positively correlated to the cation surfactant exchange on the bentonite and the octanol-water partition coefficient (Kow) of the solutes. With 0.75 g/L bentonite and 180 mg/L (60% of bentonite cation exchange capacity) cetyltrimethylammonium bromide, the removal efficiencies of the 16 polycyclic aromatic hydrocarbon (PAHs) specified by the US Environmental Protection Agency in coking wastewater except naphthalene were more than 90%, and that of benzo(a)pyrene was 99.5%. At the same time, the removal efficiencies of CODCr, NH3-N, volatile phenols, colour and turbidity were 28.6%, 13.2%, 8.9%, 55% and 84.3%, respectively, and the ratio of BOD5/CODCr increased from 0.31 to 0.41. These results indicated that the one-step process had high removal efficiency for toxic and refractory hydrophobic organic compounds, and could improve the biodegradability of the coking wastewater. Therefore it could be a promising technology for the pretreatment of toxic and refractory organic wastewater. 相似文献
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Inverse modeling of multicomponent reactive transport through single and dual porosity media 总被引:3,自引:0,他引:3
Compacted bentonite is foreseen as buffer material for high-level radioactive waste in deep geological repositories because it provides hydraulic isolation, chemical stability, and radionuclide sorption. A wide range of laboratory tests were performed within the framework of FEBEX (Full-scale Engineered Barrier EXperiment) project to characterize buffer properties and develop numerical models for FEBEX bentonite. Here we present inverse single and dual-continuum multicomponent reactive transport models of a long-term permeation test performed on a 2.5 cm long sample of FEBEX bentonite. Initial saline bentonite porewater was flushed with 5.5 pore volumes of fresh granitic water. Water flux and chemical composition of effluent waters were monitored during almost 4 years. The model accounts for solute advection and diffusion and geochemical reactions such as aqueous complexation, acid-base, cation exchange, protonation/deprotonation by surface complexation and dissolution/precipitation of calcite, chalcedony and gypsum. All of these processes are assumed at local equilibrium. Similar to previous studies of bentonite porewater chemistry on batch systems which attest the relevance of protonation/deprotonation on buffering pH, our results confirm that protonation/deprotonation is a key process in maintaining a stable pH under dynamic transport conditions. Breakthrough curves of reactive species are more sensitive to initial porewater concentration than to effective diffusion coefficient. Optimum estimates of initial porewater chemistry of saturated compacted FEBEX bentonite are obtained by solving the inverse problem of multicomponent reactive transport. While the single-continuum model reproduces the trends of measured data for most chemical species, it fails to match properly the long tails of most breakthrough curves. Such limitation is overcome by resorting to a dual-continuum reactive transport model. 相似文献