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1.
磁性固体超强酸SO42-/ZrO2-Al2O3-Fe3O4的制备与性能研究   总被引:3,自引:0,他引:3  
利用化学共沉淀法将磁性基质与固体酸组装制备磁性纳米固体超强酸催化剂,利用XRD、Raman、TG-DSC、M?ssbauer、TEM、HRTEM等手段对样品性质进行表征。结果表明:磁性基质的引入赋予固体超强酸以超顺磁性;Fe3O4、Al2O3粒子弥散在ZrO2基质中,烧结过程中阻碍了扩散传质的进行以及晶界移动,抑制了ZrO2晶体生长,稳定了四方晶相(T-ZrO2);样品粒径分布集中,平均约为32 nm;HRTEM显示T-ZrO2晶体生长取向于(101)方向,晶面间距d(101)=0.29 nm;Hammett指示剂法测得经600 ℃焙烧后产物的酸强度Ho<-13.8,酸强度大于浓硫酸(Ho=-11.93)。以柠檬酸三丁酯的合成作为磁性固体超强酸SO42-/ZrO2-Al2O3-Fe3O4催化剂的探针反应,结果表明外磁场的引入提高了柠檬酸的转化率。  相似文献   

2.
采用共沉淀的方法制备了不同Fe 掺杂量的SO42-/SnO2-Fe2O3固体超强酸催化剂. 利用傅里叶变换红外(FTIR)光谱, 粉末X射线衍射(XRD), N2吸附-脱附实验(BET), 热重(TG)分析和扫描电镜(SEM)等方法对样品进行了表征. 考察了所得催化剂对4-叔丁基环己酮与乙二醇缩合反应的催化性能. 实验结果表明, 与未经过掺杂改性的SO42-/SnO2固体酸催化剂相比, 改性后催化剂的催化性能得到了改善. 研究了以Fe/Sn 摩尔比为0.5的SO42-/SnO2-Fe2O3固体酸为催化剂, 部分醛酮类化合物与乙二醇及1,2-丙二醇的缩合反应. 考察了反应时间、催化剂用量等因素对反应的影响. 同时, 将所得催化剂应用于环酮Baeyer-Villiger 氧化反应中, 催化剂表现出良好的催化活性, 且催化剂具有一定的循环使用性.  相似文献   

3.
宋华  董鹏飞  张旭 《物理化学学报》2010,26(8):2229-2234
通过向SO2-4 /ZrO2催化剂中同时引入适量的Pt和Al2O3, 制备出了具有较高催化性能和稳定性的Pt-SO2-4 /ZrO2-Al2O3型固体超强酸催化剂. 以正戊烷异构化反应为探针, 考察了Al含量对催化剂性能的影响; 并采用X射线衍射(XRD)、比表面积测定(BET)、红外(IR)光谱、程序升温还原(TPR)、热重-差热分析(TG-DTA)和氨-程序升温脱附(NH3-TPD)手段对催化剂进行了表征. 结果表明, Al能够提高ZrO2的晶化温度, 抑制硫的分解, 增加催化剂的比表面积, 增强硫氧键的结合, 提高催化剂的还原性能, 增加催化剂的酸强度和酸总量. 当Al2O3含量(质量分数, w)为5.0%时, Pt-SO2-4 /ZrO2-Al2O3固体超强酸催化剂的催化活性最好, 在100 h内异戊烷收率可稳定在52.0%以上, 选择性在98.2%以上.  相似文献   

4.
采用过量浸渍结合溶剂蒸发将磷钨杂多酸(TPA)分散于ZrO2气凝胶表面(TPA的质量分数为5%-45%), 再经750 °C空气气氛焙烧得到多钨酸盐修饰ZrO2固体酸催化剂. 借助N2吸附、X射线衍射(XRD)、傅里叶变换红外(FTIR)光谱、氨程序升温脱附(NH3-TPD)和吡啶吸附红外(Py-IR)光谱对催化剂的结构及酸性质进行表征, 针对四氢呋喃(THF)开环聚合反应考察其酸催化性能. 研究发现, TPA与ZrO2之间较强的相互作用抑制了ZrO2的晶化, 同时也在一定程度上稳定了TPA的Keggin(凯金)-阴离子结构. 高温焙烧的催化剂中, 活性组分以ZrO2锚定的表面相(包括含有畸变或缺陷型Keggin单元的杂多酸盐及以Zr为杂原子的类杂多酸物种等)和TPA完全分解形成的氧化物体相存在, 各物种的相对量取决于TPA的负载量. 催化剂表面同时具有中等强度的布朗斯特德(Brönsted)酸与路易斯(Lewis)酸中心, 且初始TPA负载量为20%的催化剂实现了活性组分在载体表面的单层覆盖, 因而显示最大的总酸量, 对THF聚合反应也表现出最高的催化活性. 在反应温度为40 °C、时间为20 h条件下, 聚合物收率达30.9%±2%, 数均相对分子质量为2698±100; 在催化剂重复使用6次过程中, 活性未见明显降低.  相似文献   

5.
用酸中和法制备了活性γ-Al2O3, 并在其表面负载SO3得到固体酸催化剂SO3/γ-Al2O3, 用XRD, TG-DTA, FT-IR,NMR, NH3-TPD等对其进行了结构和酸性研究. 结果表明: 在SO3/γ-Al2O3的制备过程中形成少量的Al2(SO4)3, 同时SO3与γ-Al2O3表面上的羟基反应, 形成强的Brönsted酸位, 根据1H/27Al 双共振(TRAPDOR)MAS NMR与FT-IR实验结果提出了Brönsted酸结构模型. SO3/γ-Al2O3表面存在两种不同强度的酸中心, 其酸强度大于分子筛HZSM-5, 但弱于传统的固体超强酸 /γ-Al2O3.  相似文献   

6.
采用两步晶化-后浸渍法合成了纳米SO42-/ZrO2固体酸催化剂,并考察了其在植物油与甲醇酯交换反应中的催化性能。XRD、N2吸附-脱附和TEM等结果表明,经过600℃焙烧,催化剂仍保持单一四方相,粒径大小为5~10 nm,比表面积为137 m2·g-1,孔径为3.6 nm。NH3-TPD结果表明,随着焙烧温度升高,催化剂表面的酸含量和酸强度逐渐增加,超强酸含量的增加,更有利于反应在温和条件下进行。在酯交换反应中,当醇油物质的量之比为20:1,反应温度为135℃,反应时间为6 h,600℃焙烧后催化剂用量为5%(w/w)时,植物油能够完全转化为脂肪酸甲酯。与传统的SO42-/ZrO2催化剂相比,该催化剂在低温反应条件下具有更高的催化性能和良好的重复使用性。  相似文献   

7.
分别以HY,Hβ,HMOR为母体,与拟薄水铝石、铝溶胶混合,采用机械挤出法制备催化剂,采用XRD、N2等温吸附-脱附(N2-sorption)、NH3-TPD、吡啶吸附红外光谱(Py-IR)等分析手段进行表征,探讨了其物化性能的差异,并采用固定床反应器考察了上述催化剂对苯胺缩合制二苯胺反应的催化性能.结果表明,分子筛中强酸对催化剂活性有决定性作用,酸类型对催化性能影响不大;分子筛孔径对二苯胺选择性有显著影响,较小的孔径不利于二苯胺的生成和扩散,降低了目标产物的选择性.因此,在设计和选择苯胺缩合制二苯胺催化剂时应考虑酸性质和孔道尺寸对苯胺转化率和二苯胺选择性的影响来优化催化剂.  相似文献   

8.
采用共沉淀法制备了Zr0.5Ti0.5O2载体材料,将其掺杂在CeO2-Al2O3 (CA)基催化剂中, 并对其催化活性进行了超临界裂解测试, 采用全自动吸附仪、X射线衍射(XRD)、透射电镜(TEM)、程序升温脱附(TPD)等方法对催化剂进行了表征. 实验结果表明, 催化剂能够明显降低裂解反应的温度, 600 ℃ CA基催化剂产气率是热裂解的2.8倍, 掺杂Zr0.5Ti0.5O2载体材料的CA基催化剂是热裂解的4.0倍, 650 ℃时, 掺杂Zr0.5Ti0.5O2载体材料的CA基催化剂热沉提高了0.55 MJ·kg-1. BET结果表明, 掺杂Zr0.5Ti0.5O2载体后催化剂出现双孔结构, 部分小孔的出现使得乙烯的选择性提高; NH3-TPD结果表明, 掺杂Zr0.5Ti0.5O2载体材料后, 催化剂强酸位的酸量增加了4.0倍,催化剂表现出更强的表面酸性和更集中的强酸酸中心密度, 有利于裂解多产烯烃.  相似文献   

9.
以硫酸盐为原料,添加NaOH和NaHCO3以制备出碱式碳酸盐前驱体,合成出新型的纳米固体超强酸催化剂SO42-/ZnFe2O4,经XRD、BET、IR等检测,粒径为35nm,比表面积很大(137m2-1),粒度均匀。首次以该固体酸为催化剂,癸二酸和无水乙醇为原料合成癸二酸二乙酯,考察了影响反应的因素。结果表明,醇酸摩尔比为4.0∶1,催化剂用量为1.0g(癸二酸0.1mol),带水剂苯15mL,反应时间2.5h是最佳反应条件,酯化率可达91%,并推断出该催化剂的酸强度-16.02< Ho< -14.52.  相似文献   

10.
木糖转化到糠醛一般包括两步: 首先在酶、碱或路易斯(L)酸的催化作用下异构化木糖到木酮糖, 接下来木酮糖在酸的作用下脱水得到糠醛. 针对木糖水相脱水一步制备糠醛, 利用十六烷基三甲基溴化铵(CTAB)为模板剂, 借助软模板合作策略制备了一种抗水的新型固体酸催化剂, 介孔磷酸铌, 并利用X射线衍射(XRD)、N2吸脱附、透射电镜(TEM)、氨气程序升温脱附(NH3-TPD)和吡啶吸附傅里叶变换红外(Py-FTIR)光谱对材料的结构和酸性质进行了表征. 研究发现介孔磷酸铌不仅具有很高的比表面积(>200 m2·g-1), 比较窄的孔径分布(3.5nm), 同时还具有很强的L酸性和布朗斯特(B)酸性. 通过L酸催化的木糖异构化为木酮糖/来苏糖和B酸催化的木酮糖/来苏糖进一步脱水得到糠醛, 实现了一步由木糖到糠醛的高效转化. 为了优化反应条件, 考察了水溶液中反应温度、投料质量比及反应时间对木糖转化率和糠醛收率的影响, 在最佳的反应条件下, 木糖的转化率为96.5%, 糠醛的收率达49.8%. 进一步地, 为了提高收率且易于分离, 利用4-甲基-2-戊酮(MIBK)/NaCl水溶液(体积比为7:3)作为反应混合溶剂, 使糠醛收率提高到68.4%.  相似文献   

11.
The hydration of dimethyl ether (DME) to methanol over various solid acids was studied. The acidity of the catalysts is determined by FTIR spectroscopy. The hydration is found to occur predominantly on the Br?nsted acid sites. Among the catalysts studied, WOx/ZrO2 and H-ZSM-5 appeared to be most active and selective.  相似文献   

12.
Replacing fossil fuels with biodiesel enables the emission of greenhouse gases to be decreased and reduces dependence on fossil fuels in countries with poor natural resources. Biodiesel can be produced by an esterification reaction between free fatty acids (FFAs) and methanol or by transesterification of triglycerides from oils. Both reactions require homogeneous or heterogeneous catalysis. Production of biodiesel catalyzed by heterogeneous catalysts seems to be the preferred route, enabling easy product separation. As we have previously shown, the Lewis acids AlCl3 and BF3 can serve as highly efficient catalysts under ultrasonic activation. The present study focused on the development of oleic acid (OA) esterification with methanol by the same catalysts immobilized in silica matrices using the sol–gel synthesis route. During the course of immobilization, AlCl3 converts to AlCl3 × 6H2O (aluminite) and BF3 is hydrolyzed with the production of B2O3. The immobilized catalysts can be reused or involved in a continuous process. The possibility of biodiesel production using immobilized catalysts under ultrasonic activation is shown for the conversion of FFAs into biodiesel in batch and continuous mode.  相似文献   

13.
The energetically viable fabrication of stable and highly efficient solid acid catalysts is one of the key steps in large-scale transformation processes of biomass resources. Herein, the covalent modification of the classical Dawson polyoxometalate (POMs) with sulfonic acids (-SO3H) is reported by grafting sulfonic acid groups on the POM's surface followed by oxidation of (3-mercaptopropyl)trimethoxysilane. The acidity of TBA6-P2W17-SO3H (TBA=tetrabutyl ammonium) has been demonstrated by using 31P NMR spectroscopy, clearly indicating the presence of strong Brønsted acid sites. The presence of TBA counterions renders the solid acid catalyst as a promising candidate for phase transfer catalytic processes. The TBA6-P2W17-SO3H shows remarkable activity and selectivity, excellent stability, and great substrate compatibility for the esterification of free fatty acids (FFA) with methanol and conversion into biodiesel at 70 °C with >98 % conversion of oleic acid in 20 min. The excellent catalytic performance can be attributed to the formation of a catalytically active emulsion, which results in a uniform catalytic behavior during the reaction, leading to efficient interaction between the substrate and the active sites of the catalyst. Most importantly, the catalyst can be easily recovered and reused without any loss of its catalytic activity owing to its excellent phase transfer properties. This work offers an efficient and cost-effective strategy for large-scale biomass conversion applications.  相似文献   

14.
The Koch-type carbonylation of tert-butyl alcohol was studied over H-type zeolites. It was found that the catalytic carbonylation of a large amount of tert-butyl alcohol relative to the acidic sites of the H-zeolites in organic solvents requires an elevated temperature and CO pressure, although previous solid state NMR studies have revealed that the transformation of tert-butyl alcohol of an amount comparable to the acidic sites into 2,2-dimethylpropanoic acid proceeds just upon the CO co-adsorption in the H-zeolites at room temperature and atmospheric pressure. The catalytic performance of different H-zeolites and the influence of CO pressure, H2O addition and solvent effects on the carbonylation of tert-butyl alcohol have been investigated. H-ZSM-5 gives the highest selectivity for 2,2-dimethylpropanoic acid due to its adequate pore dimensions. The present work indicates the possible industrial application of solid acids as carbonylation catalysts instead of liquid acids for the Koch reaction to produce tert-carboxylic acids.  相似文献   

15.
Lignosulfonate (LS) is an organic waste generated as a byproduct of the cooking process in sulfite pulping in the manufacture of paper. In this paper, LS was used as an anionic supporting material for immobilizing cationic species, which can then be used as heterogeneous catalysts in some organic transformations. With this strategy, three lignin‐supported catalysts were prepared including 1) lignin‐SO3Sc(OTf)2, 2) lignin‐SO3Cu(OTf), and 3) lignin‐IL@NH2 (IL=ionic liquid). These solid materials were then examined in many organic transformations. It was finally found that, compared with its homogeneous counterpart as well as some other solid catalysts that are prepared by using different supports with the same metal or catalytically active species, the lignin‐supported catalysts showed better performance in these reactions not only in terms of activity but also with regard to recyclability.  相似文献   

16.

Water, as a byproduct in esterification, tends to adsorb on solid acid catalysts, causing loss of active components or decomposition of framework and thereby decreasing their reactivity and durability, while the development of water-tolerant solid acids is expected to solve these problems. In this review, the recent developments of major kinds of water-tolerant solid acids including zeolite, mesoporous silica, metal organic framework-based catalyst, magnetic nanoparticles, and polymeric catalyst are discussed in detail. Special attention has been paid to understand the role of hydrophobicity, acid strength, and structure of water-tolerant solid acids in catalytic performance and their stability. From the literature survey, it is found that despite the modified zeolites have a water contact angle as large as 160°, but their acid strength need to be improved and their small micropore sizes restrict their use in catalyzing the esterification of bulky molecules. In contrast, solid acids with abundant acid sites, suitable hydrophobicity, and abundant mesopores or macropores usually exhibit high activity and reusability. Among all the known solid acids, polystyrene-supported acidic ionic liquid catalysts (PS-CH2-[SO3H-pIM] [HSO4]) show a high yield of n-butyl acetate with 99.1% and high reusability of 13 times, which is a breakthrough over the traditional. This review aims to offer a comprehensive understanding for the water-tolerant solid acid catalysts in esterification.

Graphic Abstract
  相似文献   

17.
Silica sol-gel entrapped acids, bases and organometallic catalysts are used successfully in one-pot reactions without interfering with each other. Both physically and covalently entrapped acids and bases were employed in these processes, including polystyrene sulfonic acid, 1-propane sulfonic acid, molybdosilicic acid (SiO2-MoO3), poly[(vinylbenzyltrimethyl)ammonium] hydroxide and 1,5,7-triazabicyclo[4.4.0]decene. The entrapped metal-based catalysts are Rh2Co2(CO)12 and RuCl2(PPh3)3. The one-pot reactions carried out with these heterogenized reagents and catalysts include formation of alkenes under acidic and basic conditions, C—C bond formation by condensation reactions with an -carbon to a carbonyl, hydroformylation and hydrogenation.  相似文献   

18.
Acylation of anisole and 3-methylanisole was performed with several acylating reagents (acetylation by AcCl and Ac2O and bromoacetylation by BrAcCl and (BrAc)2O) over different solid acid catalysts. The reaction conditions were optimized with respect to the acylation reagent, overall yield, solid acid catalyst, and the products selectivities. While acylation of anisole with acetyl chloride or acetic anhydride resulted in its full conversion to para-substituted acetophenone, the use of bromoacetyl bromide or bromoacetic anhydride yielded also the ortho-substituted product. Acylation of 3-methylanisole also yielded both para- and ortho-substitutions, and the products distribution was affected by the reaction conditions and catalyst type. It was found that while more acidic catalysts (caesium salt of heteropolyacid and zeolites) were the most active towards anisole acylation, the most active catalysts for the acylation of 3-methylanisole were ion-exchange catalysts. Employing HY-740 zeolite resulted in the highest ortho-selectivity in the acylation of anisole with bromoacetyl bromide and bromoacetic anhydride and in the acylation of 3-methylanisole with acetic anhydride.  相似文献   

19.
A green and effective approach for comprehensive hydrolyzation of cellulose has been described. Several carbon-based solid acids were successfully prepared using various biomass (glucose, microcrystalline cellulose, bamboo, and rice husk) and used to catalyze cellulose hydrolysis. The acid groups (–SO3H and –COOH) were successfully introduced onto the surface of the carbon-based solid acid catalysts as evidenced by Fourier transform infrared spectroscopy and X-ray photoelectron spectroscopy. The structure of the prepared catalysts was characterized by scanning electron microscope and X-ray diffraction. The catalysts showed excellent catalytic performance for hydrolysis of cellulose. To improve the reaction efficiency, ball-milling and solubilization in ionic liquids of cellulose were adopted. A maximum total reducing sugar yield of 81.8 % was obtained in ionic liquid 1-butyl-3-methyl imidazolium chloride at 125 °C for 90 min when the water addition was 10 % of ionic liquid. This study provided a promising strategy to synthesize solid acids from lignocelluloses, which were further used to convert biomass into biofuels and platform chemicals.  相似文献   

20.
Porous inorganic-organic hybrids have been prepared by the reaction of 4,4′-biphenylbis(phosphonic acid) with Zr(IV) in organic solvents. The resultant products consist of α-zirconium phosphate-type layers crosslinked by biphenyl pillars. By using an excess of Zr in the synthesis, surface areas of ∼400 m2/g have been obtained and the pores can be controlled to be the micro-type with diameters of 10-20 Å and a relatively narrow pore size distribution. The aromatic rings are readily sulfonated by SO3 under pressure to produce very strong Bronsted acid catalysts. An NMR procedure, utilizing the shift of the carbonyl carbon of acetone-2-13C sorbed onto the sulfonated products, indicated an acid strength for the Bronsted acid sites equal to that of 100% sulfuric acid. Unpillared Zr(O3PC6H4SO3H)2 has a somewhat lower acid strength, but still has a higher acid strength than zeolites HX and HY. The particles of this layered acid exfoliate in water and light-scattering data show that they are in 5 nm size range. They also exhibit high proton conductivity as solid membranes. These sulfonated materials have a potential as strong acid catalysts for a variety of reactions at a low temperature.  相似文献   

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