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1.
采用季铵盐阳离子(CTMA+)和有机螯合剂(Am)复合改性膨润土(IMB), 制得一系列螯合剂柱撑膨润土IMB-CTMA-Am. 利用X射线衍射(XRD)分析、差热-热重(TG-DTA)分析、比表面积测定(N2-BET)以及元素分析等手段对吸附剂样品进行了表征. 结果表明, CTMA+和Am已柱撑进入膨润土层间. 吸附实验结果表明, IMB-CTMA-Am能同时有效地去除有机污染物对硝基苯酚(PNP)和重金属铅(Pb2+), 其对水中对硝基苯酚的强吸附能力来源于分配作用的增加和层间距的增大, 而与比表面积无关. 傅里叶变换红外光谱(FTIR)显示, IMB-CTMA-Am吸附Pb2+后的N—H吸收峰向低频方向移动, 表明Pb2+和膨润土层间的Am形成了稳定的配合物. 有机螯合剂Am和Pb2+所形成配合物的稳定性越大, IMB-CTMA-Am对Pb2+离子的吸附能力也就越强.  相似文献   

2.
膨润土纳米复合材料的制备、表征及吸附性能研究   总被引:7,自引:0,他引:7  
用有机螯合剂(CA)和十六烷基三甲基溴化铵(HDTMAB)共同改性膨润土(IMB),制得一系列膨润土纳米复合材料IMB-HDTMA-CA。X射线衍射(XRD)、热分析(TG-DTA)、红外光谱(FTIR)以及N2-吸附脱附技术等研究发现,HDTMA+和CA已稳定柱撑在膨润土的片层结构中,其层间距增大、比表面积减小而疏水性增强。吸附实验表明,IMB-HDTMA-CA能协同吸附水中有机物对硝基苯酚(PNP)和重金属镉(Cd2+)。对水中对硝基苯酚的吸附源于PNP在膨润土层间有机相中分配作用的增加,其吸附容量和膨润土内有机碳含量和层间距大小一致,而与比表面积无关,依次为IMB-HDTMA-TEPA>IMB-HDTMA-TETA>IMB-HDTMA-En>IMB-HDTMA 》IMB;FTIR图谱显示,IMB-HDTMA-CA吸附Cd2+后的N-H吸收峰向低频方向移动,其吸附能力和所形成配合物的稳定性一致。  相似文献   

3.
膨润土对亚甲基蓝的吸附性能研究   总被引:13,自引:0,他引:13  
为将膨润土作为消化道粘膜保护剂提供依据,本文研究了钠质,钙质膨润土对亚甲基蓝的吸附性能。研究了在20℃下的吸附动力学,测试了肿附速率常数,绘制了20℃下各型膨润土的吸附等温线,并求得其饱和吸附量。结果表明,20℃时钠质膨润土的吸附速率要快于钙质膨润,各型膨润土的吸附行为符合Langmuir方程,钠质膨润土的饱和吸附量qm为86.51mg/g,与粘膜保护剂思密达比较接近,而钙质膨润土吸附能力相对较弱。  相似文献   

4.
有机膨润土改性高吸油树脂复合材料的合成及性质   总被引:1,自引:0,他引:1  
以十六烷基三甲基溴化铵为表面改性剂制备了有机膨润土,并制备了以甲基丙烯酸十六酯为单体的吸油树脂/有机膨润土复合材料.采用X射线衍射仪(XRD)、傅里叶变换红外光谱仪(FTIR)、扫描电子显微镜(SEM)对样品进行分析.结果表明,经十六烷基三甲基溴化铵改性的膨润土层间距由原来的1.12 nm增大到1.87 nm;所得有机膨润土/吸油树脂复合材料对四氯化碳的饱和吸油率为16.3 g/g.  相似文献   

5.
以有机插层剂双十八烷基二甲基氯化铵(DHAC),对新疆夏子街膨润土进行插层改性,制备DHAC改性膨润土。红外光谱(FTIR)分析表明,双烷基阳离子插层进入蒙脱石片层。X射线衍射(XRD)表明,DHAC改性膨润土片层间距为3.772 nm,为改性前的2.07倍,表明改性后蒙脱土片层间距增大。SEM分析观察, DHAC捕层改性后膨润土颗粒更加疏松,蒙脱石颗粒表面有明显的刻蚀痕迹。通过研究改性膨润土的吸附机理分析表明,DHAC改性膨润土在不同温度下的等温吸附模型符合Freundlich模型,且相关性较高。挥发酚在改性膨润土上的吸附焓值为-2.64 kJ/mol,属于物理吸附,且△Gθ<0,说明该吸附为自发的放热过程。室温下DHAC改性膨润土吸附挥发酚的动力学模型遵循Bingham和Langmuir速率方程。  相似文献   

6.
插层型NBR/膨润土混杂材料及其对PVC增韧作用的研究   总被引:2,自引:0,他引:2  
研究了胶乳插层法制备的丁腈橡胶 /有机改性膨润土 (NBR/OMB)混杂材料的力学性能和微观结构及其对聚氯乙烯 (PVC)的增韧作用。结果表明 :胶乳插层法制备的NBR/OMB混杂材料具有优异的力学性能 ;TEM和XRD结果表明 ,有部分NBR大分子嵌入到膨润土层间 ,形成较均匀、细致的分散。NBR/OMB混杂材料增韧PVC的效果明显优于NBR ,增韧后拉伸强度和弯曲强度的保持率明显提高  相似文献   

7.
螯合剂柱撑有机膨润土IMB-TMA-Am能有效吸附水中有机物对硝基苯酚(PNP)和重金属离子Cu2 ,其中IMB为内蒙膨润土;CTMA为溴化十六烷基三甲基季铵盐阳离子;Am分别为有机螯合剂乙二胺(En)、三乙烯四胺(TETA)和四乙烯五胺(TEPA)。实验结果表明:螯合剂柱撑有机膨润土对有机污染物的吸附主要表现为有机物在长碳链疏水介质中的分配,其吸附能力和膨润土内有机碳、氮含量一致;对水中重金属离子的吸附机理是Cu2 和进入膨润土层间的有机螫合剂Am形成了配合物,其吸附能力和所形成配合物的稳定性一致。  相似文献   

8.
阳离子膨润土对分散染料的吸附动力学研究   总被引:13,自引:1,他引:13  
研究了阳离子膨润土(EPI-DMA/Bt, PD/Bt, CTMAB/Bt)对分散染料(分散黄棕S-2RFL, 分散大红S-R, 分散蓝SBL, 分散黄SE-6GFL)的吸附动力学行为. 结果表明, 阳离子膨润土对分散染料的吸附过程符合二阶段吸附速率方程, 各阶段具有不同的吸附动力学常数(k1, k2)以及吸附活化能(Ea1, Ea2)、活化焓(ΔH*1, ΔH*2)和活化熵(ΔS*1, ΔS*2); 在阳离子膨润土对分散染料的吸附过程中, k1随着阳离子插层剂烷烃链的增加而增大, 表明较大的晶片层间距, 疏水的层间域和表面正电荷增加均有利于吸附速率增大; 对于两个吸附动力学阶段, ΔH★1<-TavΔS★1, △H★2<-TavΔS★2和ΔG★>0表明整个吸附过程活化熵的影响大于活化焓.  相似文献   

9.
本文主要以钠基膨润土为原料,用十六烷基二甲基苄基氯化铵和乙二胺四乙酸二钠盐对膨润土进行复合改性,制得改性膨润土,用XRD对其结构进行表征,研究了改性后的膨润土对2,4,6-三氯苯酚和Pb~(2+)的吸附行为,结果表明,改性后的膨润土对2,4,6-三氯苯酚和Pb~(2+)的吸附性能明显提高,吸附等温线较好地符合Langmuir模型,改性膨润土对2,4,6-三氯苯酚和Pb~(2+)的最大吸附量分别为238.1mg/g和191.20mg/g,吸附动力学符合准二级反应动力学方程,其二级反应速率常数为分别为8.34×10~(-5)g/mgámin和5.62×110~(-5)g/mgámin,改性膨润土对2,4,6-三氯苯酚的吸附为吸热反应,而对Pb~(2+)的吸附为放热反应。  相似文献   

10.
双阳离子复合改性膨润土的吸附性能与构效关系   总被引:4,自引:0,他引:4  
膨润土是一种以蒙脱石为主要成分的天然吸附材料. 本文用2-巯基乙胺盐酸盐(MEA)与十六烷基三甲基溴化铵(HDTMA)复合改性内蒙钙基膨润土(IMB), 制得具有特殊结构与性能的吸附材料MEA-HDTMA-IMB. X射线衍射(XRD)、红外光谱(FT-IR)、热分析(TG-DTA)及比表面积(N2-BET)等结构表征表明: 复合改性膨润土的比表面积和层间距显著增大. 吸附研究发现: MEA-HDTMA-IMB能同时有效吸附混合水溶液中的有机物对硝基苯酚和重金属铜. 复合改性膨润土对水中有机物的吸附机理以分配作用为主, 其吸附能力强于用季铵盐阳离子单一改性的有机膨润土HDTMA-IMB; 对水中重金属的吸附主要为络合反应, 其吸附性能与用巯基铵阳离子单一改性的膨润土MEA-IMB相当.  相似文献   

11.
Adsorption kinetics of surfactants on solid surfaces has been studied by using computer simulation. Both bulk surfactant concentration and diffusion region are explicitly integrated in our model. Depending on the head-surface interaction, our simulation results indicate that there exist two different kinetic modes in adsorption process of surfactants on solid surfaces. One is the four-regime mode and the other is step-wise mode. For the strongly attractive head-surface interaction, four distinct regimes of surfactant adsorption are found: a diffusion-controlled regime, a self-assembly controlled regime, an intermediate coverage regime and a saturated regime. In particular, the adsorption in second regime displays a power-law time dependence with an exponent unrelated to bulk concentrations and diffusion coefficients. While for the weaker adsorption surfaces, the step-wise mode is found. The mode includes a low-coverage nucleation regime and the saturated regime after a sudden aggregation of surfactants on the substrates which occurs stochastically. Besides the head-surface interaction, in this work, the effects of surfactant diffusivity, bulk concentration, the length of diffusion zone and surfactant architecture on the adsorption kinetics are also considered. The simulated adsorption kinetics is compared qualitatively with experimental results.  相似文献   

12.
The concentration decay curves for the adsorption of phenol on organobentonite were obtained in an agitated tank batch adsorber. The experimental adsorption rate data were interpreted with diffusional models as well as first-order, second-order and Langmuir kinetic models. The surface diffusion model adjusted the data quite well, revealing that the overall rate of adsorption was controlled by surface diffusion. Furthermore, the surface diffusion coefficient increased raising the mass of phenol adsorbed at equilibrium and was independent of the particle diameter in the range 0.042-0.0126 cm. It was demonstrated that the overall rate of adsorption was essentially not affected by the external mass transfer. The second-order and the Langmuir kinetic models fitted the experimental data quite well; however, the kinetic constants of both models varied without any physical meaning while increasing the particle size and the mass of phenol adsorbed at equilibrium.  相似文献   

13.
The adsorption of erbium (Er) ions on activated charcoal (AC) is investigated at temperatures 10–40 °C from aqueous solutions to understand the kinetics behavior. The intra-particle diffusion, the pseudo-first order kinetic and pseudo-second order kinetic models were used to describe the kinetic data. Results shows that the adsorption of Er ions on AC occurs in two stages and the surface adsorption and diffusion phenomena are operative in the adsorption process. The result also reveals that intra-particle diffusion is not only the main rate determining step through out the adsorption process, but the boundary layer diffusion also play significant role in rate determination. Values of the intra-particle diffusion rate constant and the extent of the boundary layer diffusion were calculated. A comparison of the kinetics models on the overall adsorption rate indicates that the Er/AC system is best described by the pseudo-second order kinetic model than the pseudo-first order model, and the overall rate of the Er ions adsorption on AC appears to be controlled by more than one step, i.e., external mass transfer and diffusion mechanism.  相似文献   

14.
We examined the adsorption kinetics of alpha-chymotrypsin (pH 8.6, 10(-2) to 0.5 M Tris buffer) on muscovite mica in conditions of laminar flow through a slit. The range of buffer concentrations is between two limits: (i) no adsorption in 1 M Tris and (ii) no desorption in 10(-3) M Tris. Studying the dependence of adsorption kinetics on the wall shear rate leads to the determination of the interfacial adsorption kinetic constant ka and the diffusion coefficient. The obtained value for the diffusion coefficient is close to the one expected from the molecular size of alpha-chymotrypsin. The interfacial adsorption kinetic constant of alpha-chymotrypsin decreases when ionic strength increases, while the initial desorption constant (over a part of all the adsorbed population) shows the contrary. Although alpha-chymotrypsin is almost at its isoelectric point, the effect of ionic strength on the adsorption kinetics suggests the importance of electrostatic interactions between the protein and mica. We observed an increase in the adsorption rate, at a surface coverage near 0.14 microg cm(-2), for adsorption in 10(-2) M Tris and the low wall shear rates (<300 s(-1)). This change in the adsorption rate suggests a structural transition, that we assume again to be due to electrostatic interactions, but between proteins. The large dipole moment of the protein may induce this transition, illustrated here by the ferroelectric/antiferroelectric pattern. The variation of the zeta potential with interfacial concentration seems to be in agreement with such a model.  相似文献   

15.
In this study, the adsorption of an industrial dye Supranol Yellow 4GL onto Cetyltrimethylammonium-bentonite (CTAB-bentonite) is investigated. The organobentonite is synthesised by exchanging cetyltrimethylammonium cations (CTAB) with inorganic ions on the surface of bentonite. The adsorption of Supranol Yellow 4GL onto organobentonite is found to be maximum when the concentration of CTAB exchanged is 100% according to the cation exchange capacity of the clay (CEC). The modification of organobentonite is examined using XRD and FTIR techniques. The effect of the process parameters such as: contact time, adsorbate concentration, adsorbent dose, pH and temperature are reported. Nearly 1200 seconds of contact time are found to be sufficient for the adsorption to reach equilibrium. The pseudo second order model is used to describe the kinetic data, and the rate constant is therefore evaluated. The dye adsorption to organobentonite is characterized by monolayer isotherm and caused by adsorption with relatively strong uptake. The Langmuir and Freundlich models adsorption are applied to describe the isotherm equilibrium and to determine its constants. The Langmuir and Freundlich models agree well with the experimental data with a adsorption capacity of 0.5 g of dye per g of organobentonite. A better fixation was obtained at acidic pH. The effect of temperature on the adsorption of dye has been also studied and the thermodynamic parameters ΔH, ΔS, ΔG, were determined. Organobentonite is found to be effective for removing Supranol Yellow 4GL dye from wastewater.  相似文献   

16.
The effects of soluble surfactant on the dynamic rupture of thin liquid films are investigated. A nonlinear coupling evolution equation is used to simulate the motion of thin liquid films on free surfaces. A generalized Frumkin model is adopted to simulate the adsorption/desorption kinetics of the soluble surfactant between the surface and the bulk phases. Numerical simulation results show that the liquid film system with soluble surfactant is more unstable than that with insoluble surfactant. Moreover, a generalized Frumkin model is substituted for the Langmuir model to predict the instability of liquid film with soluble surfactant. A numerical calculation using the generalized Frumkin model shows that the surfactant solubility increases as the values of parameters of absorption/desorption rate constant (J), activation energy desorption (nu(d)), and bulk diffusion constant (D(1)) increase, which consequently causes the film system to become unstable. The surfactant solubility decreases as the rate of equilibrium (lambda) and interaction among molecules (K) are increased, which therefore stabilizes the film system. On the other hand, an increase of relative surface concentration (the index of a power law), beta(n), will initially result in a decrease of corresponding shear drag force as beta and n increase from 0 to 0.3 and 0.85, respectively. This will enhance the Marangoni effect. However, a further increase of beta and n to greater than 0.3 and 0.85, respectively, will conversely result in an increase of the corresponding shear drag force. This will weaken the Marangoni effect and thus result in a reduction of interfacial stability. Copyright 2000 Academic Press.  相似文献   

17.
We present static adsorption studies of anionic surfactants on crushed Berea sandstone. The maximum adsorption density was 0.9604 mg/g. The kinetics of adsorption process was modeled using pseudo-first-order and pseudo-second-order rate equations at 25°C and 70°C. The equilibrium adsorption process was validated using Langmuir and Freundlich adsorption models. In addition, the effects of different parameters that govern the effectiveness of these surfactants such as pH and temperature were also investigated. The kinetic study results show that the surfactant adsorption is a time dependent process. The apparent rate constant of adsorption process determined by the first-order kinetic model at 25°C and 70°C were 0.11768 and ?0.04513, respectively. The rate constant for pseudo-second-order kinetic model was 0.0086 at 25°C and 0.0101 at 70°C. The adsorption of anionic surfactant followed pseudo-second-order kinetic model. The Freundlich and Langmuir model constant were 1.6509 × 10?4 and ?9.775 × 10?5, respectively. The equilibrium results showed that the adsorption of anionic surfactant onto Berea sandstone was well described by Langmuir adsorption model. It was concluded that anionic surfactants performed better at higher pH and temperature.   相似文献   

18.
19.
The adsorption of SPADNS (trisodium salt of 2-(p-sulfophenylazo)-1,8-dihydroxynaphthalene-3,6-disulfonic acid) onto resins XAD 2, XAD 7 and silica gel was studied in the presence and in the absence of the cationic surfactant CTAB (cetyl trimethylammonium bromide). At a ratio of 2.5 CTAB to 1 SPADNS, the surfactant caused a marked increase in SPADNS adsorption. The experimental results for adsorption versus time were applied on the basis of three kinetic models (pseudo-first-order Lagergren, pseudo-second-order, and intraparticle diffusion). The interaction between CTAB and SPADNS was investigated using spectrophotometric, conductometric, and computational techniques. Theoretical results point to the formation of an ion pair between CTAB and SPADNS that influences the solution spectra, in agreement with conductometric and spectrophotometric data.  相似文献   

20.
Kinetics of polymer surfactant interactions and the effect of surfactant binding on the conformational dynamics of the polymer were explored in this work using surface plasmon resonance spectroscopy. Polyacrylic acid was modified with thiol to varying degrees so as to force the polymer to form different loop sizes upon adsorption on the gold SPR sensor surface. Dodecyltrimethylammonium chloride in solution was flowed over the polymer-coated sensor surface and the binding was followed in real time. It was found that control of the loop size of the polymer on the solid surface enabled in turn the control of surfactant binding, with the largest loop allowing the maximum amount of surfactant to bind and vice versa. The kinetic plot of the binding showed three distinct segments. The first segment followed convective-diffusive kinetics. The second and third segments followed first-order kinetics with the second rate being significantly faster than the first one. Careful analysis of the second segment showed that it is possible to divide it into two different segments, each following a first-order kinetics, with the second rate being slightly slower than the first one suggesting a gradual slow down of the reaction due to convolution from the polymer conformational changes. Mechanistically, the sudden increase in the rate for the third segment of surfactant binding implies that the polymer matrix is opening up so as to incorporate more surfactant molecules. This was attributed to the formation of charged double surfactant species the repulsive interaction of which prevented the polymer network from imploding. Studies using unmodified polymers suggested the possibility of sudden conformational rearrangement in the polymer network, with progress in surfactant binding. Furthermore, the reflectance of the SPR spectrum was found to increase upon surfactant binding, implying that there is a decreased efficiency of coupling of the incident radiation into the surface plasmon mode of the metal, which suggests that the surfactant actually penetrated the polymer matrix.  相似文献   

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