低温陈化法制备SO42-/ZrO2-TiO2超强酸及其催化性能和稳定性研究

本文采用低温陈化法制备了SO₄^2-/ZrO₂-TiO₂固体超强酸,并将其用于催化乙酸正丁酯的酯化反应,采用TEM、IR和XRD等对样品进行了检测。结果表明,低温陈化的样品具有较强的酸性和催化活性,空气中放置30天后其酸性和催化活性变化不大。XRD谱图显示,低温陈化的样品经550℃焙烧后出现了较强的锐钛矿晶相衍射峰。     

双酸位SO42-/ZrO2-SiO2固载离子液体催化剂的构筑及性能

采用一步共缩合-水热法合成酸性载体SO₄^2-/ZrO₂-SiO₂,化学法接枝酸性离子液体磺酸功能化咪唑硫酸氢盐（[Ps-im]HSO₄）,构筑拥有Brönsted与Lewis双酸位的离子液体固载型催化剂SO₄^2-/ZrO₂-SiO₂-IL。采用X射线衍射、傅里叶红外、N₂吸附-脱附、X射线光电子能谱、热重以及透射电镜对催化剂的结构进行表征,结果表明：锆原子和酸性结构SO₄^2-被成功引入纯硅材料,所合成的载体具有一定酸性;离子液体成功固载于酸性介孔材料SO₄^2-/ZrO₂-SiO₂,且固载后的催化剂保持其介孔结构。以大豆油和甲醇的酯交换反应为探针,考察了SO₄^2-/ZrO₂-SiO₂-IL催化剂的催化性能。在反应温度为150℃、反应时间为4 h、催化剂量5%（w/w）、醇油物质的量之比为24：1的反应条件下,生物柴油的收率超过92%,且回收利用5次后,生物柴油的收率仍达86%。     

纳米SO42-/ZrO2的合成及其在酯交换反应中的催化性能

采用两步晶化-后浸渍法合成了纳米SO₄^2-/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SO₄^2-/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。     

Cu/SO42-/La2O3-ZrO2-Al2O3催化剂的制备及其对C3H6选择还原NO的催化性能

以Al₂O₃为基质，添加ZrO₂和La₂O₃，制成La₂O₃-ZrO₂-Al₂O₃复合载体，然后采用SO₄^2-进行改性，再负载上Cu²⁺，制备了铜基SO₄^2-改性的复合载体催化剂(Cu/SO₄^2-/La₂O₃-ZrO₂-Al₂O₃)。考察了它在富氧条件下对丙烯选择还原NO的催化性能，并借助XRD、SEM、TG、Py-IR、NH₃-TPD、FTIR和TPR等方法研究了Cu/SO₄^2-/La₂O₃-ZrO₂-Al₂O₃的结构和性能的关系。结果表明，ZrO₂的加入主要有利于提高催化剂的低温活性；La₂O₃的加入则主要有利于提高催化剂的热稳定性和还原性能；SO₄^2-能够与Zr形成螯合双配位结构，大幅度促使催化剂表面酸量增加并且酸性增强；因此，有效地提高了Cu/SO₄^2-/La₂O₃-ZrO₂-Al₂O₃在富氧条件下对丙烯选择还原NO的催化活性和水热稳定性。在无水条件下，Cu/SO₄^2-/La₂O₃-ZrO₂-Al₂O₃能使NO的最大转化率高达84.3%，即使在275 ℃ 10%水蒸气存在的情况下，仍能使NO的转化率高达81.2%。     

磁性固体超强酸SO42-/ZrO2-Al2O3-Fe3O4的制备与性能研究

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H_o＜-13.8，酸强度大于浓硫酸(H_o=-11.93)。以柠檬酸三丁酯的合成作为磁性固体超强酸SO₄^2-/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。     

纳米固体超强酸SO42-/Fe2O3的制备及其催化合成乙酸乙酯

将Fe₂O₃纳米粉体经一定浓度的H₂SO₄浸泡活化后制成纳米固体超强酸SO₄^2-/Fe₂O₃,将其用于催化合成乙酸乙酯以考察其活性。利用均匀设计分析了超强酸制备过程及酯化反应过程中各因素的影响,研究结果表明较好的制备条件是:H₂SO₄浓度:2.5mol·L^-1;浸泡时间:1h;活化温度:167℃;活化时间:1h,此时获得的固体超强酸SO₄^2-/Fe₂O₃的粒径小于50nm。当催化剂用量为冰乙酸质量的5%,n(乙醇)∶n(冰乙酸)为3∶1,反应3.5h后乙酸的转化率高于80%。该催化剂经H₂SO₄溶液浸泡、活化再生后可重新使用,推断出其酸强度H₀<-14.5。     

Na+，K+//Br-，SO42--H2O四元体系323 K相平衡研究

采用等温溶解平衡法研究了四元体系Na⁺,K⁺//Br^-,SO₄^2--H₂O在323 K的相平衡关系,测定了该体系323 K的溶解度及平衡液相的密度,绘制了该体系的相图。研究发现：平衡体系存在复盐钾芒硝Na₂SO₄·3K₂SO₄的结晶区。其相图由3个共饱和点,7条单变量曲线和5个结晶区组成。相区分别对应NaBr·2H₂O、Na₂SO₄、K₂SO₄、KBr和Na₂SO₄·3K₂SO₄结晶区。其中复盐钾芒硝Na₂SO₄·3K₂SO₄,Na₂SO₄和K₂SO₄有较大结晶区,而NaBr·2H₂O和KBr有较小结晶区。对比了等温条件下四元体系Na⁺,K⁺//Cl^-,SO₄^2--H₂O相平衡结果。实验结果表明溴化物对硫酸盐有较强盐析作用。     

不同稀土改性SO42-/ZrO2催化剂的结构与性能表征

Solid superacid catalyst SO₄^2-/ZrO₂ was modified by different rare earth compounds and applied to the esterification of acetic acid and n-butanol. The effects of rare earth elements loading on the catalytic properties were studied and the correlation between the structure and properties was investigated by means of XRD, IR, UV, DTA and TG. The results show that the (NH₄)₂Ce(NO₃)₆ modification can enhance catalytic activity more and exhibit better stability than the other two compounds La(NO₃)₃ and Ce(NO₃)₃. Meanwhile,(NH₄)₂Ce(NO₃)₆ modification can restrain the loss of SO₄^2- efficiently. The optimum calcination temperature and molar ratio of Ce(NH)∶Zr for SO₄^2-/ZrO₂ catalyst modified by (NH₄)₂Ce(NO₃)₆ are 450 ℃ and 2, respectively.     

正庚烷在超稳Y沸石(USY)负载超强酸催化剂上加氢异构化

The Pt-bearing SO₄^2-/ZrO₂ superacid catalysts supported on ultra stable Y (USY) zeolite were prepared by impregnation and characterized by X-ray diffraction, nitrogen adsorption and Hammett indicators. Their catalytic activities were evaluated in the hydroisomerization of n-heptane with an atmospheric fixed-bed reactor. The catalysts possessed a high surface area, superacidity and well maintained pore structure of USY support. The supported catalysts with a suitable SO₄^2-/ZrO₂ loading exhibited a higher catalytic activity and selectivity than the unsupported SO₄^2-/ZrO₂ catalyst or the Pt supported on USY catalyst without superacid. At the reaction temperature of 220 ℃, over the catalyst with a Pt loading of 0.8wt% and ZrO₂ loading of 10wt%, the conversion of n-heptane could be as high as 35.2% with a selectivity of 87.9% for isomerization products.     

NO2-对乳酸-丙酮-BrO3--Mn2+-H2SO4化学振荡反应的影响

研究NO₂^-对乳酸-丙酮-BrO₃^--Mn²⁺-H₂SO₄化学振荡反应的影响时发现,NO₂^-对振荡反应的诱导期t_in、周期t_p有显著的影响。NO₂^-的浓度C_NO2^-与诱导期倒数的对数ln(1/t_in)、NO₂^-浓度的对数lnC_NO2^-与周期的对数lnt_p均有良好的线性关系,线性范围为7.46×10^-5～2.99×10^-3mol·L^-1。在此浓度范围内,NO₃^-无影响,是一重现性好,灵敏度高,操作简单的NO₂^-动力学分析测试体系。获得诱导期、周期的表观活化参数E_in、E_p分别为56.82kJ·mol^-1、64.51kJ·mol^-1。结合被动采样法,测得室外大气中NO₂日平均浓度值为1.59×10^-9mol·L^-1,最后对NO₂^-共存时的振荡反应诱导期机理进行了初步探讨。     

陈化温度和Fe/Zr配比对SO42-/Fe2O3-ZrO2固体超强酸结构与性能的影响

用低温陈化法制备了SO42-/Fe2O3-ZrO2(简称SFZ)固体超强酸催化剂,用红外光谱(IR)和X光衍射(XRD)对其结构进行了表征,并考察了它对合成癸二酸二正丁酯的催化性能.IR谱显示,低温陈化的SFZ样品在1070 cm-1处吸收峰远强于常温陈化样品.XRD分析则显示,在焙烧温度为650℃、 Fe/Zr为2 ∶ 1时,低温陈化的样品出现了亚稳态的ZrO2四方晶相.该样品在催化酯化反应中使产率达90%以上,高于常温陈化样品的30%.研究结果表明: 在其他条件不变时,低温陈化所出现的亚稳态的ZrO2四方晶相是表面酸性和催化活性增加的微观原因.     

大孔SO42-/ZrO2-SiO2复合固体酸制备及催化性能

利用浸渍水解法在大孔SiO2载体上组装固体酸制备出大孔径SO42-/ZrO2-SiO2复合固体酸催化剂。用扫描电镜、红外光谱仪和粉末X射线衍射仪等对其进行表征,结果表明:大孔SiO2载体的毛细管效应促使ZrO2以纳米薄层方式均匀地沉积在SiO2薄层表面,并抑制了ZrO2晶体的生长和晶相的转变,载体的大孔全连通的结构赋予该复合材料高的通透性(孔径在1~2μm)、两面活性点和大的比表面积(约156 m2.g-1)。Hammett指示剂法测得经550℃焙烧后产物的酸强度H0值小于-13.75,属于固体超强酸。以乙酸正丁酯的合成为探针反应考察硫酸浸渍液浓度、焙烧温度等制备条件对其催化活性的影响,结果表明,该SO42-/ZrO2-SiO2固体酸具有较好的催化活性,当焙烧温度为550℃和硫酸浸渍液浓度为1.5 mol.L-1时,超强酸对酯化反应的催化酯化率达到97%。     

固体酸SO42-/ZrO2-CeO2催化小桐子油脂肪酸制备生物柴油的实验研究

用沉淀浸渍法制备了固体酸催化剂SO₄^2-/ZrO₂-CeO₂,用于催化小桐籽油脂肪酸与甲醇酯化制备生物柴油。考察了焙烧温度和CeO₂负载量对催化剂活性的影响,并进行了单因素实验和动力学研究。研究表明,SO₄^2-/ZrO₂-CeO₂有较高的催化活性,当甲醇与脂肪酸体积比 2∶1,反应温度150 ℃,催化剂用量为脂肪酸质量的8%,反应60 min时,脂肪酸转化率可达0.9403。动力学计算表明,该酯化反应的表观活化能为45.31 kJ/mol,动力学模型为-dc_A/dt=38371e^-45310/RTc_A^1.44。     

复合固体超强酸催化剂SO2-4-WO3-ZrO2的结构研究

Solid superacid catalyst SO4(2-)-WO3-ZrO2 was characterized by means of XRD,DTA-TG, and surface area measurement techniques. The dependence of the surface area, SO42- content of the catalyst on calcination temperature was measured. It was found that there is a synergy to a certain degree between SO42- and WO3 with respect to the delay of ZrO2 crystallization, the stabilization of the tetragonal ZrO2 and the enlargement of the surface area of the catalyst. The addition of WO3 is beneficial to the stabilization of SO42- and remarkably increases the stability of SO42- at high temperature.     

制备条件及添加稀土对SO42- /ZrO2 -Al2O3固体超强酸酸性影响的研究

用共沉淀法制备了SO42-/ZrO2-Al2O3固体超强酸,并采用低温陈化和添加稀土La对其制备方法进行改进.通过样品催化正丁烷异构化反应考察了该固体超强酸中nZr和nAl的最佳配比为1∶ 2.该法制备的样品的IR显示,在1393 cm-1处的吸收峰强度较常温陈化样品大大增加.XRD分析表明,低温陈化和加入稀土添加剂的样品在650℃焙烧温度下,出现了亚稳态的ZrO2 四方晶相的晶体是表面酸性和催化活性增加的微观原因.样品催化合成八乙酸蔗糖酯反应结果同样证明,在相同的时间内,低温陈化和添加稀土添加剂的样品具有较好的催化活性.     

Effects of Zr/Ti molar ratio in SO42-/ZrO2-TiO2 calcined at different temperatures on its surface properties and glucose reactivity in near-critical methanol

Effects of Zr/Ti molar ratio in SO42-/ZrO2-TiO2 solid acid catalyst calcined at different temperatures on its surface properties and catalytic activity were thoroughly investigated in this paper. The physicochemical characteristics of prepared samples were determined by N2 adsorptiondesorption, XRD, NH3-TPD and XPS techniques, respectively. It was found that the crystallization temperature of the samples increased after the combination of ZrO2 and TiO2; and phase transformations from the anatase to the rutile of TiO2 species and the tetragonal to the monoclinic of ZrO2 species were effectively suppressed at higher temperature. The sample with a Zr/Ti molar ratio of 3/1 calcined at 450℃ showed the highest surface area and the most acid sites among all the tested samples. The acid site densities of samples were relatively closed to each other if they were calcined at the same temperature, however, decreased with the calcination temperature. The result indicates that the sulfur content in samples is a crucial factor to control the acid site density. Calcining the sample at 650℃ and higher temperatures resulted in a significant desorption of sulfate ion on the samples. The synthesized samples were evaluated as a potential catalyst for glucose conversion under the near-critical methanol conditions (200℃/4 MPa). The results suggested that the relatively weaker acid sites of the catalyst were more favorable for the accumulation of methyl glucosides, while the moderate acid sites were responsible for the formation of methyl levulinate. The catalytic activity for methyl levulinate production almost increases linearly with the catalyst acid site density. The catalyst deactivation is due to the loss of sulfate ion and the two catalysts with Zr/Ti molar ratios of 3/1 and 1/3 could effectively alleviate the deactivation caused by sulfate solution in the reaction medium and can be reused after calcination with the reuse rate of over 90% in terms of the methyl levulinate selectivity.     

Catalysis of SO42--ZrO2/TiO2 nanometer solid superacid

Superacid catalyst SO42--ZrO2/TiO2 was applied in esterification of Acetic Acid and Butanol. The particle size of ZrO2 in the catalyst was about 12.5 nm. In catalyst preparation conditions, the effect factor order on catalytic activity is H2SO4 concentration ＞ calcination temperature ＞ ZrO2 supported content. The optimum preparation condition is as follows: ZrO2 content 3.5g/g; calcination temperature 600℃, and H2SO4 concentration 0.5mol/L. The catalytic activity is 96.5 vol%.SO42-/MxOy solid superacid is a kind of green catalyst, whose application perspective is bright. In this paper, SO42--ZrO2/TiO2 solid superacid was prepared with nanometer compound carrying method. The acidic strength of catalysts was measured with the following Hammett indicators, 2,4-dinitrofluorobenzene (H0=-14.52) and p-nitrochlorobenzene (H0=-12.70). Catalytic activity was evaluated with esterification reaction of Acetic Acid and Butanol. Reaction temperature was at 105℃, and reaction time was only 1h. The conversion rate of Acetic Acid was analyzed by a gas chromatograph (GC-14C SHIMADZU in Japan)The experimental results showed that H2SO4 concentration had more influences on catalytic activity than other two factors, calcination temperature and ZrO2 supported content. Since sulfur absorbed on the surface of metal oxides is necessary to the acidity of SO42-/MxOy solid superacid,H2SO4 concentration in impregnation solution is needed enough high. But, it can't be too much high,otherwise, Zirconium sulfate formed on the catalyst surface will be harmful influences on catalytic activity. In researched cover, 0.5mol/L H2SO4 concentration is the most suitable, and the catalyst prepared with this concentration has very strong acidity.The optimum preparation condition is as follows: ZrO2 content 3.5g/g; calcination temperature 600℃, and H2SO4 concentration 0.5mol/L. In the catalyst prepared with above conditions, the acidic strength (H0) of the catalyst is smaller than ＜-14.52, and catalytic activity is 96.5 vol%. When it was re-used in esterification reaction, catalytic activity decreased gradually with re-used times increasing(seen in Table 1). But after catalyst is used repeatedly up to five times, catalytic activity (84.3 vol %)is still higher than that of H2SO4 catalyst.The X-ray diffraction patterns showed that ZrO2 supported in TiO2 belonged tetragonal zirconia phases. Through the calculation of Scherrer formula, the particle size of ZrO2 in the catalyst is about 12.5 nm. After SO42- promoted nanometer ZrO2/TiO2 compound carrier, the diffraction peaks of tetragonal zircoma become broader and the strength weaker. It shows that adding SO4 ions restrains the crystallization of ZrO2, diminishes the size of particles. This might be why SO42--ZrO2/TiO2 has high catalytic activity and stability in acidic catalysis reaction.     

低温陈化超声波共沉淀制备SO4^2-/ZrO2-La2O3催化剂

低温陈化超声波共沉淀法制得SO4^2-/ZrO2-La2O3前驱体,经H2SO4处理,在不同温度下焙烧得到纳米晶催化剂SO4^2-/ZrO2-La2O3;用Hammett指示剂法测定其酸性．用XRD、BET、TEM、IR和XPS对样品进行表征,其催化活性用醋酸和甘油的酯化反应进行了评价．结果表明经超声波搅拌和低温（-15℃）陈化,650℃焙烧4h得到的固体超强酸表现出较高催化活性．     

催化精馏专用填料型固体酸SO42-/ZrO2-Al2O3-Al的研究

为了研制催化精馏专用催化剂,采用铝阳极氧化法制备了Al2O3-Al一体型载体,并将活性固体超强酸SO42-/ZrO2引入到Al2O3-Al上,得到一种新型催化精馏专用填料式固体酸SO42-/ZrO2-Al2O3-Al催化剂.利用XRD、 SEM、 BET、 XPS、 NH3-TPD等手段对其进行了表征.结果表明,所制得的阳极氧化铝膜厚为56 μm, SO42-/ZrO2-Al2O3-Al固体酸具有比表面积大、酸强度适中的特点.XRD结果表明, ZrO2在Al2O3-Al上处于高度分散状态.将该固体酸用于乙酸/乙醇酯化反应中,显示出较高的催化活性,且稳定性较好.     

在SO42-/ZrO2 上苯与丙烯的烷基化反应

Super acidic catalyst SO42-/ZrO2 was prepared and characterized by XRD,IR,and Py-IR. Selectively catalytic gas phase flow reactions of benzene and propene over the catalyst were carried out in a made-to-measure high pressure flow reactor with a thermometer and a condenser. The benzene and propene were kept in pressure tanks at 8 : 1 ratio with N2 gas at 4. 0 MPa. The reactants were pumped into the quantifier where the pressure was maintained by N2 gas at 8. 0 MPa. They were then pumped into the reaction reactor using catalytic synthesis of isopropyl benzene. The collected liquid phase products were analyzed using GC-MS. Product analyses were carried out on SE-54. The effect of the preparative condition on the catalytic synthesis of isopropyl benzene over the catalysts has been tested. The result shows that the SO42-/ZrO2 can be used as a catalyst for the title reaction,and shows higher conversion（99.2%）for the propene and higher selectivity（93.3%）for the isopropyl benzene when the catalyst is preparated in some condition.