改性介孔微孔分子筛去除水中亚甲基蓝的研究

以壳聚糖包覆介孔-微孔复合分子筛(CS/MCM-41-A)为吸附剂去除水中的亚甲基蓝,研究了反应时间、溶液pH、溶液亚甲基蓝初始浓度、CS/MCM-41-A投加量、竞争离子对吸附的影响,分析了CS/MCM-41-A的吸附动力学和热力学特征。结果表明,25℃下,当CS/MCM-41-A投加量为0.3 g/L,溶液亚甲基蓝初始浓度100 mg/L,pH为6,吸附时间为40 min时,溶液中亚甲基蓝的去除率达到92.57%。CS/MCM-41-A吸附亚甲基蓝符合拟二级动力学方程,吸附等温线更好地符合Langmuir方程,CS/MCM-41-A对亚甲基蓝的有良好的吸附性能。     

MCM-41介孔分子筛吸附性能的热力学和动力学分析

实验以亚甲基蓝作为模型吸附质,探讨了MCM-41介孔分子筛对模型吸附质亚甲基蓝的吸附性能,并对其吸附过程进行了热力学和动力学分析。结果表明,MCM-41介孔分子筛的吸附率高达94%,对亚甲基兰的吸附符合二级吸附动力学,MCM-41对亚甲基兰的吸附行为属于Freundlich等温吸附,整个吸附过程属于放热反应。     

改性MCM-41分子筛的合成与亚甲基蓝吸附性能

选用TEOS（正硅酸乙酯）做为硅源,CTAB（十六烷基三甲基溴化铵）做为表面活性剂,在碱性条件下水热合成MCM-41。实验采用3-氨丙基三甲基硅烷对MCM-41进行改性,成功得到氨基改性介孔材料NH₂-MCM-41吸附剂,并使用X射线衍射（XRD）对其做了表征。考察了各种实验条件下,比如温度、吸附剂的量、pH、亚甲基蓝初始浓度等条件下MCM-41和NH₂-MCM-41对水溶液中亚甲基蓝（MB）的吸附能力。MCM-41和氨基改性介孔材料NH₂-MCM-41均为平面六方介孔结构。结果表明,温度和pH是影响MCM-41和NH₂-MCM-41对亚甲基蓝吸附的最主要的因素。随着温度的升高,材料吸附能力增强,而过高或者过低的pH都会降低MCM-41和NH₂-MCM-41对亚甲基蓝的吸附能力。     

银耳对水中亚甲基蓝的吸附动力学研究

以亚甲基蓝为例,用银耳粉末作为吸附剂,对有机染料废水进行吸附研究。考察pH值、吸附时间以及银耳投入量等因素对吸附的影响,并分析了其吸附动力学模型。结果表明,银耳吸附废水中亚甲基蓝过程符合假二阶动力学模型。在25℃、亚甲基蓝起始浓度0.1 mmol/L以及吸附剂浓度8 mg/mL的条件下,吸附1 h,吸附率为93.44%。     

银耳对水中亚甲基蓝的吸附动力学研究

以亚甲基蓝为例,用银耳粉末作为吸附剂,对有机染料废水进行吸附研究。考察pH值、吸附时间以及银耳投入量等因素对吸附的影响,并分析了其吸附动力学模型。结果表明,银耳吸附废水中亚甲基蓝过程符合假二阶动力学模型。在25℃、亚甲基蓝起始浓度0.1 mmol/L以及吸附剂浓度8 mg/mL的条件下,吸附1 h,吸附率为93.44%。     

活性炭对水中亚甲基蓝的吸附性能研究

以活性炭为吸附剂,亚甲基蓝(MB)为吸附质,考察了吸附剂用量、吸附时间、温度对活性炭去除亚甲基蓝的影响。分别采用伪一级、伪二级动力学模型和Langmuir,Freundlich吸附等温线模型对吸附动力学和等温线进行分析。实验表明,在活性炭用量为0.667 g/L,吸附时间为360 min,反应温度为298 K时,活性炭对亚甲基蓝的最大吸附量为249.081 mg/g。吸附反应在前30 min内速率很快,并约在360 min内达到吸附平衡,吸附动力学符合伪二级动力学模型。吸附反应为放热反应,等温吸附过程符合Langmuir和Freundlich吸附等温模型,相关系数高于0.99。活性炭对去除水中亚甲基蓝效果好,是一种优良的吸附剂。     

改性介孔氧化硅对亚甲基蓝吸附性能的影响

通过水热合成方法制备介孔氧化硅(SiO_2),运用氧化石墨烯(GO)对其改性,将所制备的样品应用在亚甲基蓝(MB)的吸附上,考查了酸碱度、温度、溶液浓度及吸附时间、吸附剂用量等因素对吸附过程的影响。结果表明该复合材料显示了对亚甲基蓝良好的吸附性能,溶液pH值、吸附剂量和温度对吸附有一定影响;对亚甲基蓝的吸附是一个准二级动力学过程;其吸附等温线符合Langmuir模型。     

高岭土对亚甲基蓝的吸附性能和等温吸附模型研究

以高岭土为吸附剂,研究了其对亚甲基蓝模拟废水的吸附行为、等温吸附模型和吸附动力学。探讨了吸附时间、高岭土投加量、亚甲基蓝初始浓度、盐浓度、p H值等因素对亚甲基蓝吸附效果的影响。结果表明,吸附时间120 min,高岭土投加量10 g/L,低温、碱性条件下就能达到更好的亚甲基蓝吸附效果。高岭土对亚甲基蓝吸附符合Langmuir和Freundlich等温吸附模型,吸附动力学符合准二级动力学模型。     

高岭土对亚甲基蓝的吸附性能和等温吸附模型研究

以高岭土为吸附剂,研究了其对亚甲基蓝模拟废水的吸附行为、等温吸附模型和吸附动力学。探讨了吸附时间、高岭土投加量、亚甲基蓝初始浓度、盐浓度、p H值等因素对亚甲基蓝吸附效果的影响。结果表明,吸附时间120 min,高岭土投加量10 g/L,低温、碱性条件下就能达到更好的亚甲基蓝吸附效果。高岭土对亚甲基蓝吸附符合Langmuir和Freundlich等温吸附模型,吸附动力学符合准二级动力学模型。     

化学师范专业活性炭吸附亚甲基蓝综合实验

为提高化学(师范)专业学生的综合实验能力,设计了"活性炭吸附亚甲基蓝"物理化学综合实验.以活性炭为吸附剂,亚甲基蓝( MB) 为吸附质,考察了吸附剂用量、吸附时间、 温度对活性炭去除亚甲基蓝的影响.探讨了水溶液中活性炭固体颗粒吸附阳离子有机染料亚甲基蓝的吸附热力学(吸附等温线类型)、吸附动力学方程和盐酸脱附条件.结果表明,活性炭对亚甲基蓝染料的热力学吸附行为符合 Langmuir 等温吸附方程,其动力学吸附行为符合准一级动力学方程.选择1:1浓盐酸未能有效的将吸附的亚甲基蓝脱附.     

改性介孔分子筛对布洛芬的吸附与控制释放

采用合成后改性将氨基嫁接进介孔MCM41和SBA-15孔道内,对功能化的2种分子筛进行药物吸附与控制释放的研究。利用红外光谱仪(IR)、智能重量分析仪(IGA)等表征手段对吸附剂的物理结构和化学组成进行表征。对药物布洛芬(IBU)的吸附量进行比较,结果表明,氨基改性的MCM41(MCM41-NH2)对布洛芬的吸附性能大...     

Pd-MCM-41介孔材料的合成、表征及催化性能研究

用微波辐射法合成了介孔分子筛MCM-41,采用浸渍法获得不同钯含量的Pd-MCM-41催化剂,用XRD、低温N2吸附-脱附、IR对MCM-41及组装体进行了表征;研究了Pd负载量、反应时间、反应温度等条件对葡萄糖氧化反应的影响,结果表明Pd-MCM-41能有效催化葡萄糖氧化反应。     

MCM-41介孔材料的合成条件和特性对吸附镉离子的影响

以气相氧化硅为硅源,十六烷基三甲基溴化铵(cetyl trimethyl ammonium bromide,CTAB)为模板剂,分别在碱性[氢氧化钠(NaOH),四乙基氢氧化铵,tetraethyl ammonium hydroxide,(C2Hs)4NOH(TEAOH)]和酸性介质条件[盐酸(HCl)]T水热合成了MCM-41有序介孔材料MCM-41-N,MCM-41-T和MCM-41-H.用X射线衍射、氮气吸附-脱附等手段对比分析了合成的3种MCM-41介孔材料的物相、比表面积、孔径、孔体积等,发现酸性介质中合成的介孔材料的孔径最大.在此基础上,利用MCM-41介孔材料对比研究了处理含镉离子(Cd2 )废水的效果和机理,确定了不同介孔材料用量、不同初始pH值条件下MCM-41介孔材料对水中Cd2 的吸附率和吸附量.结果表明:介孔材料用量相同时,溶液pH值的增大有利于提高3种MCM-41介孔材料对水中Cd2 的处理效果.在pH值从7.0到8.0的过程中,其吸附率有1个突变,MCM-41-T的Cd2 吸附率从35.65%提高到62.15%;MCM-41-N的从38.80%提高到69.40%;MCM-41-H的从50.22%提高到73.47%.孔径最大的MCM-41-H对Cd2 的吸附效果最佳,最大吸附率为89.56%,最大吸附容量为8.57 mg/g.吸附溶液pH值的大小和介孔材料的孔径尺寸是决定吸附量大小的关键因素,因此,重点应通过优化合成工艺提高介孔材料的孔径.     

Investigation of equilibrium and kinetic parameters of methylene blue adsorption onto MCM-41

Mesoporous MCM-41 was synthesized at room temperature using tetraethoxysilane (TEOS) with cetyltrimethylammonium bromide (CTAB) and employed as an effective adsorbent for the adsorption of methylene blue dye from aqueous solution. The as-synthesized MCM-41 was calcined at 250 and 550°C to study the relation between the surface area and pore volume with surfactant removal. The synthesized MCM-41 was characterized using thermo gravimetric analysis (TGA), X-ray diffraction (XRD) patterns, nitrogen adsorption/desorption isotherms and Fourier transform infrared (FT-IR) spectroscopy. The MCM-41 calcined at 550°C showed higher surface area (1,059 m² g^?1) with pore volume of 0.89 ml g^?1 and was used for the investigation of adsorption isotherms and kinetics. The experimental results indicated that the Freundlich and Redlich-Peterson models expressed the adsorption isotherm better than the Langmuir model. In addition, the influence of temperature and pH on adsorption was also investigated. The decrease in temperature or the increase in pH enhanced the adsorption of dye onto MCM-41. A maximum adsorption capacity of 1.5×10^?4 mol g^?1 was obtained at 30°C. The kinetic studies showed that the adsorption of dye on MCM-41 follows the pseudo-second-order kinetics.     

席夫碱锌改性介孔硅对毒死蜱的吸附与缓释

以3-氨丙基三乙氧基硅烷（APTES）、水杨醛和锌离子为改性剂,通过共缩聚法合成席夫碱锌配合物改性MCM-41（Zn-MCM-41）,并以毒死蜱为模型药物,制备了毒死蜱/席夫碱锌配合物改性MCM-41缓释体系。利用XRD、N₂吸附-脱附、FTIR、DSC和XPS对MCM-41、氨基改性MCM-41（NH₂-MCM-41）、水杨醛席夫碱改性MCM-41（SA-MCM-41）的结构、毒死蜱的分布形态和Zn-MCM-41的配位情况进行了表征,考察了MCM-41在改性前后对毒死蜱的吸附量,并着重探究了其对毒死蜱的吸附动力学、吸附热力学以及缓释性能。结果表明,APTES和水杨醛席夫碱改性后的MCM-41仍具有较为有序的介孔结构。MCM-41对毒死蜱的吸附量为54 mg·g^-1,Zn-MCM-41的吸附量为186 mg·g^-1,相对于MCM-41,其吸附量增加了244%。改性前后的MCM-41对毒死蜱的吸附动力学和吸附热力学分别符合准一级动力学模型和Freundlich模型。毒死蜱/席夫碱锌配合物改性MCM-41缓释体系的释药行为可用Riger-Peppas动力学模型来描述,其药物释放由Fick扩散控制。     

五乙烯六胺改性制备CO2吸附剂及其对模拟烟气中CO2捕集性能的研究（英文）

A novel solid support adsorbent for CO2 capture was developed by loading pentaethylenehexamine (PEHA) on commercial y available mesoporous molecular sieve MCM-41 using wet impregnation method. MCM-41 sam-ples before and after PEHA loading were characterized by X-ray powder diffraction, N2 adsorption/desorption, thermal gravimetric analysis and scanning electron microscope to investigate the textural and thermo-physical properties. CO2 adsorption performance was evaluated in a fixed bed adsorption system. Results indicated that the structure of MCM-41 was preserved after loading PEHA. Surface area and total pore volume of PEHA loaded MCM-41 decreased with the increase of loading. The working adsorption capacity of CO2 could be significantly improved at 60%of PEHA loading and 75 °C. The effect of the height of adsorbent bed was investigated and the best working adsorption capacity for MCM-41-PEHA-60 reached 165 mg·(g adsorbent)?1 at 75 °C. Adsorption/desorption circle showed that the CO2 working adsorption capacity of MCM-41-PEHA kept stable. ? 2014 The Chemical Industry and Engineering Society of China, and Chemical Industry Press. Al rights reserved.     

疏水性MCM-41分子模板剂对水中U(VI)的吸附性能试验研究

采用水热合成法制备了疏水性介孔二氧化硅材料(MCM-41-dry)并经煅烧制得亲水性介孔二氧化硅材料(MCM-41-cal).试验探讨了pH值、吸附时间、投加量以及U(VI)初始浓度等因素对MCM-41材料煅烧前后吸附U(VI)效果的影响,利用SEM、EDS、BET和FTIR分析其吸附机理.试验结果表明, MCM-41-dry材料因具有有机模板剂,其吸附效果远高于MCM-41-cal的吸附效果;当pH值为5,吸附时间为180 min,温度为30 ℃,MCM-41-dry投加量为0.2 g/L,U(VI)初始浓度为10 mg/L时,其对U(VI)的吸附率可达99.2%;Langmuir吸附等温模型和准二级动力学方程能较好的拟合其吸附过程,当T=303 K时,理论饱和吸附量为241.935 mg/g,吸附为单分子层吸附,以化学吸附为主.通过BET、FTIR表征则说明MCM-41-dry具有六方形介孔结构能吸附U(VI),官能团羟基和氨基发挥了很大的作用.     

Changes in the oxidation state of transition metal containing MCM-41 during deNOx reactions

The oxidation state of Co, Pt and Rh containing MCM-41 after co-adsorption of NO, CH₄, and O₂ in the presence of water vapor was studied by in situ XANES experiments. All catalysts were oxidized after the adsorption of NO and reduced after the co-adsorption of NO and CH₄. The presence of water vapor did not influence the oxidation/reduction of Rh/MCM-41 and Pt/MCM-41, while Co/MCM-41 was oxidized by the presence of H₂O at reaction temperature. This revised version was published online in July 2006 with corrections to the Cover Date.     

Separation and Recovery of Tetramethyl Ammonium Hydroxide with Mesoporous Silica Having a Hexagonal Structure (MCM-41)

Separation and recovery of tetramethyl ammonium hydroxide (TMAH) was investigated using several types of MCM-41 (mesoporous silica having hexagonal structure) adsorbents. The MCM-41s were prepared by hydrothermal synthesis with structure-directing agents with different alkyl chains. The prepared MCM-41s were characterized with X-ray diffraction, transmission electron microscope, nitrogen gas adsorption, and zeta potential, and then used for adsorption of TMAH. The adsorption of TMAH with MCM-41s increased with pH up to pH ≈ 10 and then decreased as the MCM-41 dissolved. The adsorption of TMAH progressed via the Langmuir mechanism. The maximum adsorption corresponded to the pore diameter and the pore volume of the MCM-41s. MCM-41 also possesses selectivity for TMAH against phenol. The chromatographic operation was conducted using granulated MCM-41 to avoid excessive pressure-drop through the packed column and quantitative adsorption-elution processing of TMAH could be achieved.