阴-阳离子有机膨润土制备及其对铅离子的吸附

用十八烷基三甲基溴化铵（STAB）和十二烷基苯磺酸钠（SDBS）共同改性膨润土制备阴．阳离子有机膨润土，并用红外光谱分析法、热分析法和X粉晶衍射分析进行了表征；考察了阴-阳离子有机膨润土对铅离子的吸附性能。结果表明，用0．5CEC（cationexchangecapacity）十八烷基三甲基溴化铵和0．4CEC十二烷基苯磺酸钠改性的膨润土吸附铅的效果最佳；阴-阳离子有机膨润土吸附铅离子的能力比改性前明显增加，达到吸附平衡所需要的时间缩短；pH值强烈影响有机膨润土对铅离子吸附；有机膨润土对铅离子等温吸附过程符合Langmuir吸附模型；吸附热力学分析表明该吸附是一个放热过程，降低温度有利于铅离子的吸附。     

粉末状和颗粒状有机膨润土对克百威的吸附

用十六烷基三甲基溴化铵(CTMAB)和十二烷基苯磺酸钠(SDBS)制得粉末状CTMAB阳离子有机膨润土(简称CTMAB-膨润土)和CTMAB-SDBS阴阳离子有机膨润土(简称CTMAB-SDBS-膨润土),并利用聚乙烯醇(PVA)包埋固定化技术将2种粉末状有机膨润土制成颗粒状有机膨润土,研究了粉末状与颗粒状有机膨润土对水中克百威的吸附性能.结果表明:粉末状CTMAB-膨润土和CTMAB-SDBS-膨润土对克百威的吸附效果较好,最终去除率分别为90.9％和92.5％,颗粒状CTMAB-膨润土和CTMAB-SDBS-膨润土对克百威的最终去除率分别为55.5％和60.3％；有机膨润土对克百威的吸附等温线符合Freundlich方程；颗粒状有机膨润土吸附克百威最多可重复利用6次.     

阴/阳离子有机膨润土制备及其对苯酚吸附性能的实验研究

采用十六烷基三甲基溴化铵(CTMAB)和十二烷基硫酸钠(SDS)对辽宁黑山钙基膨润土进行不同工艺的阴/阳离子有机膨润土制备,并探讨其对被苯酚污染的地下水的吸附机理及其影响因素,为阴/阳离子有机膨润土在污染地下水修复新技术--渗透反应格栅(PRB)中应用的可行性提供必要的技术参数.研究结果表明,制备阴/阳离子有机膨润土的最佳工艺是加入3.0%(质量分数)的Na2CO3钠化,以120CTMAB/15SDS的投加量对其进行阴/阳离子有机改性;阴/阳离子有机膨润土对水中有机物具有协同去除效应;阴/阳离子有机膨润土Na-ACOMMT对苯酚吸附的最佳条件是投加60 g/L、80～100目的Na-ACOMMT,在温度20℃、pH为6～8、振荡转速200 r/min的条件下振荡30 min,此时苯酚的去除率高达78.74%,且吸附等温线符合Langmuir和Freundlich方程;Na-ACOMMT可通过多次吸附(累积吸附量为0.045 9 mg/g)达到降低成本的目的.但是Na-ACOMMT吸附被苯酚污染的地下水时,可能会有微量阴/阳离子表面活性剂的解吸.     

有机膨润土吸附苯胺的性能及工艺条件的优化

以钙基膨润土为原料，钠化后用溴化十六烷基三甲铵（CTMAB）进行有机改性，制得有机膨润土。在单因素吸附实验的基础上，采用L16（4^4）正交实验法对有机膨润土吸附水中苯胺的工艺条件进行了优化研究。结果表明，当矿物的粒径小于74／μm、振荡速度为150r／min、吸附液为25mL，并且以此三者为固定因素时，其优化工艺条件为有机膨润土投加量2．0g，温度40℃，pH7，吸附时间1．5h。     

改性膨润土对废水中六价铬的吸附过程研究

以广西宁明膨润土为原料,利用微波干法制备钠化膨润土和有机膨润土,并用制备的改性膨润土对含Cr（Ⅵ）模拟废水进行吸附实验。结果表明,在pH=5．6（为废水初始pH）,加土量为2g／L,吸附时间为30min的条件下,有机膨润土对含50mg／L的Cr（Ⅵ）废水的去除率达95％。有机膨润土吸附Cr（Ⅵ）的机理主要为离子交换吸附及络合物沉淀吸附,钠化膨润土对Cr（Ⅵ）主要为表面吸附。     

无机—有机柱撑膨润土的制备及其在水处理中的应用进展

无机－有机柱撑膨润土是一种新型的吸附剂,对水中污染物有很好的吸附去除能力。本文介绍了无机－有机柱撑膨润土的制备及其在水处理中的研究进展。综述了各种柱撑膨润土制备方法、对不同类型的水中污染物的吸附行为及机理。     

改性膨润土联合混凝剂处理微污染水中有机物

采用十二烷基多糖苷季铵盐作为改性剂制备改性膨润土,研究了改性膨润土联合混凝剂去除有机物的效果,考察了有机改性剂用量、微波辐射功率、辐射时间、膨润土投加量、pH值对有机物去除效果的影响,探讨了改性膨润土的改性和去除机理。结果表明,经微波改性后,实现了十二烷基多糖苷季铵盐阳离子对膨润土的插层,增大了层间距,提高了膨润土的吸附性能。联合混凝剂投加改性膨润土能够改善絮凝性能,显著提高有机物的去除效果。在最佳条件下,改性膨润土与PAC联合后的强化混凝,对初始浓度15.3 mg/L的微污染水中有机物的去除率达到95%以上,吸附符合Freundlich吸附等温方程。     

有机膨润土吸附苯胺的性能及其在水处理中的应用

分别用氯化十六烷基吡啶(CPC)和溴化十六烷基三甲铵(CTMAB)改性的有机膨润土吸附处理水中的苯胺,研究了两种有机膨润土吸附处理苯胺的性能及适宜条件.结果表明,有机膨润土对苯胺的去除率比原土增大了十几倍,CTMAB-膨润土、CPC-膨润土及原土的饱和吸附容量分别为130mg/g、87.5mg/g及37.5mg/g.     

有机膨润土在废水处理中的应用及其进展

本文简单介绍了膨润土的基本性质，膨润土及改性膨润土在废水处理中的应用；重点综述了有机膨润土的制备方法，吸附水中有机物的性能、机理、规律及影响因素，有机膨润土在废水处理中的应用及其进展。     

有机膨润土吸附苯胺的性能及工艺条件的优化

以钙基膨润土为原料,钠化后用溴化十六烷基三甲铵(CTMAB)进行有机改性,制得有机膨润土。在单因素吸附实验的基础上,采用L16(44)正交实验法对有机膨润土吸附水中苯胺的工艺条件进行了优化研究。结果表明,当矿物的粒径小于74μm、振荡速度为150 r/m in、吸附液为25 mL,并且以此三者为固定因素时,其优化工艺条件为有机膨润土投加量2.0 g,温度40℃,pH 7,吸附时间1.5 h。     

Preparations of organobentonite using nonionic surfactants

Due to hydrophilic environment at its surface, natural bentonite is an ineffective sorbent for nonpolar nonionic organic compounds in water even though it has high surface area. The surface properties of natural bentonite can be greatly modified by simple ion-exchange reactions with large organic cations (cationic surfactants) and this organobentonite is highly effective in removing nonionic organic compounds from water. Cationic surfactant derived organobentonites have been investigated extensively for a wide variety of environmental applications. In this study, the preparation of organobentonite using nonionic surfactants has been investigated for the first time. Results indicate that nonionic surfactants intercalates into the interlamellar space of bentonite and may demonstrate higher sorption capacity than cationic surfactant. It is possible to create large interlayer spacing and high organic carbon content organobentonite by use of nonionic surfactants with suitable balance between the hydrocarbon and ethylene oxide chain lengths. In addition, nonionic surfactant derived organobentonites are more chemically stable than cationic surfactant derived organobentonites.     

Efficient removal and mechanisms of water soluble aromatic contaminants by a reduced-charge bentonite modified with benzyltrimethylammonium cation

A novel strategy utilizing the phenyls interaction and the hydrophobic affinity of available siloxane surface in the interlayer of bentonite was proposed to improve the sorption capabilities of organobentonites for water soluble aromatic contaminants. A unique organobentonite (65BTMA) was synthesized by intercalating benzyltrimethylammonium cation (BTMA⁺) into the interlayer of a reduced-charge bentonite with cation exchange capacity (CEC) of 65 cmol kg⁻¹. Phenol, aniline and toluene were used as model compounds of water soluble aromatic contaminants. Their respective removal efficiencies by 65BTMA were achieved at 83.3%, 89.2% and 97.3% at the initial concentration of 20 mg l⁻¹. To reveal the sorption mechanism, sorption characteristics of aromatic contaminants to 65BTMA were compared with that of aliphatic contaminants in similar molecular size. And various organobentonites were prepared by combining TMA⁺ (tetramethylammonium), BTMA⁺, HTMA⁺ (heptyltrimethylammonium) and CTMA⁺ (cetyltrimethylammonium) with two bentonites (CEC = 108 and 65 cmol kg⁻¹). To 65BTMA, sorption magnitudes of aromatic contaminants were much greater than that of aliphatic compounds with similar size; and dramatically higher than those to other organobentonites at low pollutant concentrations. These observations revealed that the strong phenyls interactions contributed significantly to sorb the aqueous soluble aromatic contaminants to 65BTMA (>90%), and which favored to design uniquely powerful sorbents.     

表面活性剂改性4A分子筛对Cr(VI)的吸附行为

采用浸渍法对4A分子筛进行表面改性,通过引入阳离子表面活性剂,使4A分子筛表面附着季铵型阳离子,并与反离子Br-形成"阴离子交换膜",从而促使更多的Cr(VI)阴离子通过离子交换吸附到改性4A分子筛上,通过X-射线衍射(XRD)和傅里叶变换红外光谱(FTIR)对样品的物相结构和组成进行表征分析。研究表明,表面活性剂的类型和疏水碳氢链结构会影响4A分子筛的吸附能力,十八烷基三甲基溴化铵(OTAB)碳氢链长,在分子筛表面形成的双分子层密,对Cr(VI)的吸附量最大。采用准一级、准二级、Elovich和Bangham动力学模型对六价铬的吸附数据进行拟合,其中准一级动力学方程最符合十八烷基三甲基溴化铵改性分子筛的吸附行为。同时,分别从Langmuir和Redlich-Peterson等温吸附模型获得六价铬的最大吸附量为13.98 mg/g,且改性分子筛以均一表面吸附为主。     

Influence of synthetic surfactants on the uptake of Pd, Cd and Pb by the marine macroalga, Ulva lactuca

Uptake of Pd, Cd and Pb by the marine macroalga, Ulva lactuca, has been studied in the presence of an anionic (sodium dodecyl sulphate, SDS), cationic (hexadecyltrimethylammonium bromide; HDTMA) and non-ionic (Triton X-100; TX) surfactant. Compared with the surfactant-free system, metal sorption was reduced in the presence of SDS or TX. Neither surfactant, however, had any measurable impact on cell membrane permeability, determined by leakage of dissolved free amino acids (DFAA), or on metal internalisation. We attribute these observations to the stabilisation of aqueous Cd and Pb by SDS and the shielding of otherwise amenable sorption sites by TX. Presence of HDTMA resulted in a reduction in the extent of both sorption and internalisation of all metals and a significant increase in the leakage of DFAA. Thus, by enhancing membrane permeability, HDTMA exerts the greatest influence on metal behaviour in the presence of U. lactuca.     

Binding of dialkylated disulfonated diphenyl oxide surfactant onto alumina in the aqueous phase

Adsorption of a gemini surfactant that has two monomers and a spacer in a molecule (dialkylated disulfonated diphenyl oxide with alkyl chain lengths of twelve, DADS-C12) onto positively-charged aluminum oxide in water was studied and compared with a single-monomer anionic surfactant (sodium dodecylbenzene sulfonate, SDDBS). More mass of the gemini surfactant was adsorbed than the conventional single-monomer SDDBS. Fewer moles of the first were bound to the substrate than the second indicating that larger molecular structure of the gemini surfactant does not hinder the sorption. Both surfactants followed similar sorption mechanisms, however, stronger hydrophobic interactions were shown in the bilayer formation of the adsorbed gemini surfactant.     

Enhanced desorption of phenanthrene from contaminated soil using anionic/nonionic mixed surfactant

A new approach using an anionic/nonionic mixed surfactant, sodium dodecyl sulphate (SDS) with Triton X-100 (TX100), was utilized for the desorption of phenanthrene from an artificial contaminated natural soil in an aim to improve the efficiency of surfactant remediation technology. The experimental results showed that the presence of SDS not only reduced the sorption of TX100 onto the natural soil, but also enhanced the solubilization of TX100 for phenanthrene, both of which resulted in the distribution of phenanthrene in soil-water systems decreasing with increasing mole fraction of SDS in surfactant solutions. These results can be attributed to the formation of mixed micelles in surfactant solution and the corresponding decrease in the critical micelle concentration of TX100 in mixed solution. The batch desorption experiments showed that the desorption percentage of phenanthrene from the contaminated soil with mixed solution was greater than that with single TX100 solution and appeared to be positively related to the mole fraction of SDS in surfactant solution. Thus, the anionic/nonionic mixed surfactants are more effective for the desorption of phenanthrene from the contaminated soil than a single nonionic surfactant.     

Sorption kinetics and isotherm modelling of imidacloprid on bentonite and organobentonites

Bentonite was modified by quaternary ammonium cations viz. cetytrimethylammonium (CTA), cetylpyridinium (CP), rioctylmethylammonium (TOM) and pcholine (PTC) at 100% cation exchange capacity of bentonite and was characterized by X-ray diffraction, CHNS elemental analyser and Fourier transform infrared spectroscopy. The sorption of imidacloprid on organobentonites/bentonite was studied by batch method. Normal bentonite could adsorb imidacloprid only upto 19.31–22.18% while all organobentonites except PTC bentonite (PTCB), enhanced its adsorption by three to four times. Highest adsorption was observed in case of TOM bentonite (TOMB) (76.94–83.16%). Adsorption kinetic data were fitted to pseudo-first-order, pseudo-second-order and intraparticle diffusion models. For normal bentonite data were best fitted to pseudo-first-order kinetic, while for organobentonites fitted to pseudo-second-order kinetics. Sorption data were analysed using Freundlich, Langmuir, Temkin and Dubinin–Radushkevich isotherm models. Data were well fitted to Freundlich adsorption isotherm. Product of Freundlich adsorption constant and heterogeneity parameter (K_f.1/n) was in following order: TOMB (301.87) > CTA bentonite (CTAB) (152.12) > CP bentonite (CPB) (92.58) > bentonite (27.25). Desorption study confirmed hysteresis and concentration dependence. The present study showed that the organobentonite could be a good sorbent for removal of imidacloprid from natural water sample also. Percentage adsorption and Distribution coefficient (mL g^?1) value of different adsorbent was in following order: TOMB (74.85% and 297.54) > CTAB (55.78% and 126.15) > CPB (45.81% and 84.55) > bentonite (10.65% and 11.92).     

Distribution of polycyclic aromatic hydrocarbons in soil-water system containing a nonionic surfactant

The effect of a nonionic surfactant, Triton X-100 (TX100), on the distribution of four representative polycyclic aromatic hydrocarbons (PAHs), phenanthrene, fluorene, acenaphthene and naphthalene, in soil-water system was studied on a natural soil. The apparent soil-water distribution coefficient with surfactant (Kd*) for these compounds increased when TX100 equilibrium concentration from zero to around the critical micelle concentration (CMC), followed by a decrease in Kd* at TX100 equilibrium concentration greater than CMC. This is a direct result of surfactant sorption onto soil followed by PAHs partitioning to the sorbed surfactant. The values of carbon-normalized solute distribution coefficient (Kss) with the sorbed TX100 are greater than the corresponding partition coefficients with soil organic matter (Koc), which indicates the soil-sorbed nonionic surfactant is more effective per unit mass as a partitioning medium than the native soil organic matter for PAHs. When Kd* = Kd the corresponding initial concentration of surfactant was defined as critical washing concentration (CWC). Depending on the surfactant initial concentration below or above the CWC, the addition of nonionic surfactant can enhance the retardation of soil for PAHs or promote the removal of PAHs from soil, respectively. The values of Kd* and CWC can be predicted by a model, which correlates them with the compounds' octanol-water partition coefficients (Kow), soil property and the amount of soil-sorbed surfactant.     

Sorption of sodium dodecylbenzene sulfonate by montmorillonite

Sorption of linear alkylbenzene sulfonates by soils and sediments is an important process that may affect their fate, transport, toxicity and their application in remediation of contaminated soil and groundwater. In this study, batch experiments were conducted to elucidate the sorption of a widely used anionic surfactant, sodium dodecylbenzene sulfonate (SDBS), by montmorillonite. It was observed that: (i) SDBS was sorbed significantly by montmorillonite saturated with Ca(2+), but little by Na-saturated montmorillonite; (ii) the amount of SDBS sorbed by Ca(2+)-montmorillonite was enhanced by NaCl; and (iii) no significant intercalation of SDBS into Ca(2+)-montmorillonite was observed by X-ray diffraction (XRD) analysis. These results indicate that the removal of SDBS by Ca(2+)-montmorillonite was primarily attributed to the precipitation between DBS(-) and Ca(2+) in solution which was released from montmorillonite via cation exchange. These results will help us to understand the sorption behavior and environmental effects of anionic surfactants.     

Effect of cationic and anionic surfactants on the sorption and desorption of perfluorooctane sulfonate (PFOS) on natural sediments

Sorption and desorption of PFOS at water-sediment interfaces were investigated in the presence of a cationic surfactant, cetyltrimethylammonium bromide (CTAB), and an anionic surfactant, sodium dodecylbenzene sulfonate (SDBS). CTAB remarkably enhanced the sorption of PFOS on the sediment. In contrast, the influence of SDBS to the sorption of PFOS was concentration dependent. Two contrasting factors were responsible for the phenomenon. One was the sorption of the surfactant itself to the sediment, which enhanced the sorption of PFOS. The other was the increase in solubility of PFOS caused by the adding of surfactants, which decreased the sorption of PFOS. SDBS had a much lower sorption capacity, but rather strong ability to increase the solubility of PFOS. High levels of SDBS remarkably reduced the sorption of PFOS on the sediment. These results imply that cationic and anionic surfactants may have contrast impacts on the distribution and transport of PFOS in the environment.