异丙醇钛控制水解的小角X射线散射研究

由金属醇盐水解制备溶胶的方法已广泛应用于溶胶-凝胶法制备纳米孔无机膜,但对金属醇盐水解机理的认识十分有限。通过控制异丙醇钛[Ti（i-OC₃H₇）₄]在异丙醇（i-C₃H₇OH）中水解制备TiO₂溶胶,利用小角X射线散射（SAXS）方法研究了由不同H₂O/Ti（i-OC₃H₇）₄的反应混合物[Ti（i-OC₃H₇）₄：H₂O：i-C₃H₇OH=1：m：30（摩尔比）]形成TiO₂溶胶的过程,探讨了控制Ti（i-OC₃H₇）₄水解的过程中胶粒形成与长大的规律。研究结果表明,所合成的TiO₂溶胶的胶粒粒径小于10 nm,胶粒的形成和长大与H₂O/Ti（i-OC₃H₇）₄摩尔比密切相关。H₂O/Ti（i-OC₃H₇）₄（摩尔比） ≥ 2.0时,随着H₂O/Ti（i-OC₃H₇）₄增加,溶胶的稳定性下降。     

TiO_2-ZrO_2聚合溶胶形成过程的小角X射线散射研究

由金属醇盐(M(OR)_4)水解制备溶胶的方法已广泛应用于溶胶-凝胶法制备纳米孔无机膜。通过控制异丙醇钛[Ti(i-OC_3H_7)_4]和正丙醇锆[Zr(n-OC_3H_7)_4]的混合物在异丙醇(i-C3H7OH)中水解制备聚合型TiO_2-ZrO_2溶胶,利用小角X射线散射方法(SAXS)研究了初始反应混合物Ti(i-OC_3H_7)_4:Zr(n-OC_3H_7)_4:H2O:i-C_3H_7OH=0.9:0.1:m:30(摩尔比,m=1.8,2.0,2.2)形成TiO_2-ZrO_2溶胶的过程,探讨了水与醇盐摩尔比H_2O/M(OR)_4(M=Ti+Zr)、反应温度和正丙醇锆对TiO_2-ZrO_2溶胶形成的影响。研究结果表明,H_2O/M(OR)_4=1.8时,只有少量胶粒形成;H_2O/M(OR)_4=2.0~2.2时,TiO_2-ZrO_2溶胶中胶粒具有质量分形结构,分形维数1.2≤Dm1.4;随着H_2O/M(OR)_4增加,胶粒的形成时间缩短,胶粒大小和分形维数均增大,溶胶的稳定性显著下降。升高反应温度有利于胶粒形成。[Ti(i-OC_3H_7)_4+Zr(n-OC_3H_7)_4]混合物比Ti(i-OC_3H_7)_4水解快,H_2O/M(OR)_4相同时,TiO_2-ZrO_2溶胶比TiO_2溶胶稳定性差。     

TiO2-Al2O3复合粉体的制备及光催化性能

Al₂O₃陶瓷膜在过滤染料废水过程中容易被染料大分子堵塞,导致Al₂O₃陶瓷膜水通量下降。以钛酸丁酯、异丙醇铝为前驱体,采用溶胶-凝胶法制备Ti(OH)₄-AlOOH复合溶胶,经450 ℃烧成获得TiO₂-Al₂O₃复合粉体。以SEM、纳米粒度/电位仪作为主要表征手段,研究了不同Ti(OH)₄和AlOOH摩尔比对复合溶胶粒径分布的影响,进而探究TiO₂-Al₂O₃复合粉体的光催化性能。结果表明,Ti(OH)₄和AlOOH摩尔比为0~0.4时,随着Ti(OH)₄和AlOOH摩尔比的增大,胶粒的平均粒径从67.5 nm减小到34.0 nm,Ti(OH)₄-AlOOH复合溶胶的电位从43 mV升高至53 mV。当Ti(OH)₄和AlOOH摩尔比为0.4时,复合粉体对结晶紫的去除率高达79.3%,反应速率常数增大到了0.018 min^-1。TiO₂-Al₂O₃复合粉体制备的陶瓷膜能有效降解表面沉积的大分子,解决了陶瓷膜堵塞的问题。     

太阳光/TiO2-γ-Al2O3光催化处理垃圾渗滤液的研究

采用液相共沉淀法制备了TiO₂-γ-Al₂O₃复合催化剂,在其最佳合成条件下,比较了太阳光/TiO₂-γ-Al₂O₃与UV/TiO₂处理垃圾渗滤液的性能。结果表明,当Ti（SO₄）₂与Al₂（SO₄）₃·18H₂O摩尔配比为1:2、聚乙二醇2000投加质量分数为1.25%、焙烧温度为650℃时,TiO₂-γ-Al₂O₃的催化活性最强。当催化剂投加量与垃圾渗滤液COD质量比为1.75、反应时间为90 min、渗滤液pH为3时,太阳光/TiO₂-γ-Al₂O₃对COD、NH₄⁺-N的去除率几乎达到最高,分别为81.97%和54.95%,...     

Ti/nanoTiO2-ZrO2修饰电极电催化氧化葡萄糖

在无水乙醇和乙酰丙酮混合溶液中,电解Ti金属制得前驱体Ti（OCH₂CH₃）_（4-y）（acac）_y,再加入ZrCl₄,将上述溶液直接水解、干燥后在450℃煅烧2 h,粉体通过X射线衍射（XRD）分析表明：纳米TiO₂-ZrO₂粉体呈单分散结构。通过凝胶涂抹、煅烧得到高活性的     

稳定高效Ru/TiO2-ZrO2催化剂处理苯酚磺酸废水

催化湿式氧化（CWAO）技术可高效处理有机废水,但现有催化剂的性能,尤其是其稳定性距工业应用还有很大差距。利用ZrO₂对TiO₂载体进行掺杂调变,研制出了具有良好稳定性的Ru/TiO₂-ZrO₂催化湿式氧化催化剂。结果表明, Ru/TiO₂催化剂在进行连续5次催化湿式氧化降解苯酚磺酸（phenolsulfonic acid,PSA）废水的反应后,总有机碳（total organic carbon,TOC）转化率由99.1%降低至65.3%;而Ru/TiO₂-ZrO₂催化剂在Ti/Zr质量比为9∶1~7∶3范围内,能表现出优良的反应性能,在连续5次反应后, TOC转化率稳定保持在90%以上。X射线仪衍射（XRD）、N₂吸脱附（BET）、X射线扫描微探针电子能谱仪（XPS）、氢气程序升温还原（H₂-TPR）和电感耦合等离子体发射光谱（ICP-OES）表征结果表明：ZrO₂能够进入TiO₂的晶格,TiO₂-ZrO₂固溶体的生成阻止了TiO₂由锐钛矿相向金红石相的转变。另外,ZrO₂的调变加强了Ru与载体的相互作用,有效抑制了活性金属Ru的流失。稳定的载体结构和良好的抗流失性能是Ru/TiO₂-ZrO₂催化剂具有优良反应性能的主要原因。     

MgCO3·3H2O晶须的制备及其生长机制的研究

以MgCl₂·6H₂O和NH₄HCO₃为原料,CH₃COONa·3H₂O为形貌控制剂,采用沉淀结晶法制备MgCO₃·3H₂O晶须,考察了不同添加量的CH₃COONa·3H₂O对晶须结晶过程和形貌的影响,并研究了晶须在该体系中的生长机制。结果表明：当体系中加入质量分数为0.23%的CH₃COONa·3H₂O时可以成功制备长径比约为30的棒状MgCO₃·3H₂O晶须,CH₃COONa·3H₂O的存在促进了MgCO₃·3H₂O晶须的形成。该体系中晶须的生长过程：首先形成无定形的4MgCO₃·Mg（OH）₂·4H₂O,之后无定形4MgCO₃·Mg（OH）₂·4H₂O逐渐转变为MgCO₃·3H₂O并生长成较大长径比的棒状MgCO₃·3H₂O晶须。这是因为CH₃COONa·3H₂O电离产生的Na ⁺选择性吸附在MgCO₃·3H₂O晶体轴向的（101）晶面,抑制了该晶面生长,而径向晶面生长速率未受到影响,从而促使无定形MgCO₃·3H₂O生长成棒状晶须。     

sol-gel法制备CeO2-TiO2/凹凸棒石复合材料的催化性能

以凹凸棒石(ATP)为载体,Ce(NO₃)₃·6H₂O和Ti(OBu)₄为原料,冰醋酸为抑制剂,采用溶胶-凝胶法制备CeO₂-TiO₂/ATP纳米复合材料。利用TG-DSC、TEM、XRD和N₂吸附/脱附仪对复合材料进行表征,考察铈钛摩尔比对所制备样品催化降解罗丹明B溶液性能的影响。结果表明,当Ce/Ti≥5/5时,具有立方萤石结构的氧化物颗粒以固溶体形式均匀分布在ATP表面,颗粒尺寸约5~10 nm;随Ti⁴⁺的进一步增加,样品中的CeO₂结晶不完全;当Ce/Ti<3/7时,样品中出现锐钛矿型TiO₂的分离相。适量的Ti⁴⁺掺杂能促进CeO₂产生较多的结构缺陷,有利于增加晶格氧空位的浓度,提高样品的催化活性。对罗丹明B的催化降解实验表明,当Ce/Ti=5/5时,样品的催化性能较好,对罗丹明B溶液的化学需氧量(COD)去除率可达96%以上。     

Cu2O/TiO2催化甲醛乙炔化反应的载体效应

以不同温度焙烧的TiO₂为载体,CuCl₂·2H₂O为铜源,NaOH为沉淀剂,L-抗坏血酸钠为还原剂,采用液相还原-沉积沉淀法制备了Cu₂O/TiO₂,借助X射线粉末衍射（XRD）、H₂程序升温还原（H₂-TPR）、N₂-物理吸附、透射电镜（TEM）、X射线光电子能谱（XPS）等手段,研究了TiO₂载体焙烧温度对Cu₂O/TiO₂甲醛乙炔化反应性能的影响。结果表明,低温焙烧得到的TiO₂载体以锐钛矿相存在,与Cu₂O物种间具有弱的相互作用,使得Cu₂O被过度还原为金属Cu,催化活性较低。随着载体焙烧温度的升高,TiO₂中出现金红石相,Cu₂O与载体间相互作用增强,Cu₂O高效转变为乙炔亚铜活性物种,使催化剂表现出最佳的催化性能。     

铋及钴掺杂TiO2陶瓷负载膜的制备及光催化性能

以钛酸四丁酯为钛源,Bi(NO₃)₃·5H₂O为铋源,Co(NO₃)₂·6H₂O为钴源,采用溶胶-凝胶法在陶瓷基片上分别制备了应用于固定式光催化反应器的Bi-TiO₂复合膜及Co-TiO₂复合膜。研究了涂膜方式及煅烧升温速率对膜表面形态的影响,并以甲基橙溶液为目标降解物,对比了旋涂法及浸渍提拉法制备的薄膜在不同升温速率下的光催化活性。通过热分析仪(TG-DSC)、X射线衍射仪(XRD)和扫描电镜(SEM)等测试手段分析了掺杂薄膜的结构。结果表明,采用旋涂法制备的薄膜与陶瓷基体结合较为紧密,而浸渍提拉法制备的薄膜催化活性较高。当煅烧温度为500 ℃,升温速率为10 ℃/min时,其对甲基橙的降解率较高。当摩尔比为0.010时Bi-TiO₂复合膜的催化活性较佳,100 min光降解甲基橙比率达到8.10%。钴或铋掺杂TiO₂均可提高TiO₂催化剂的光催化活性,Bi-TiO₂膜的催化活性优于Co-TiO₂膜。     

Pt/TiO_2催化二甲醚部分氧化重整制氢

二甲醚是一种理想的氢载体,可用于解决氢的储存和运输。以Pt/TiO_2为部分氧化催化剂,结合Ni/Al_2O_3重整催化剂,考察钛前驱体和焙烧温度对二甲醚部分氧化重整制氢反应的影响。结果表明,以Ti(C4H9O)4为原料制备的TiO_2为金红石相,Ti(SO4)2或Ti O(OH)2为原料制备的TiO_2为锐钛矿相;以Ti(C4H9O)4为原料制备的Pt/TiO_2-E催化剂催化性能略好,转化率接近100%,H2收率约90%,表明金红石相TiO_2负载的Pt催化剂略佳;以Ti(SO4)2为原料制备的Pt/TiO_2-S催化剂500℃焙烧可获得金红石相TiO_2。与Pt/Al_2O_3催化剂相比,Pt/TiO_2催化剂具有更好的催化性能,H2收率超过90%,而Pt/Al_2O_3催化剂H2收率约80%。     

Stable and efficient Ru/TiO2-ZrO2 catalysts for catalytic wet air oxidation of phenolsulfonic acid wastewater treatment

Catalytic wet air oxidation (CWAO) technology can efficiently treat organic wastewater, but the performance of existing catalysts, especially its stability, is far from industrial applications. In this study, ZrO₂ was used to modify TiO₂ support to form the stable Ru/TiO₂-ZrO₂ catalysts. It was found that the Ru/TiO₂-ZrO₂ catalysts showed excellent performance for catalytic wet air oxidation of phenolsulfonic acid wastewater. They gave high total organic carbon (TOC) conversions (>90%) and remained stable in 5 consecutive running in the Ti/Zr ratio range from 9∶1 to 7∶3. On the other hand, TOC conversion decreased from 99.1% to 65.3% in 5 consecutive cycles for the conventional Ru/TiO₂ catalyst. The characterization results of XRD, BET, XPS, H₂-TPR and ICP-OES indicated that ZrO₂ can enter the lattice of TiO₂ to form TiO₂-ZrO₂ solid solution, which prevented the transformation of TiO₂ from anatase to rutile. In addition, the modification of ZrO₂ strengthened the interaction between Ru and the support, which effectively inhibited the leaching of Ru metal. The stable support structure and good anti-loss performance are the main reasons for the excellent reaction performance of Ru/TiO₂-ZrO₂ catalyst.     

Preparation of catalyst precursors for selective oxidation of n-butane by exfoliation–reduction of VOPO4·2H2O in primary alcohol

A new method through intercalation and exfoliation of VOPO₄·2H₂O crystallites in primary alcohol (1-propanol or 1-butanol), followed by reduction with the alcohol, have been investigated for the preparation of catalyst precursor. Lamellar compounds, consisting of V⁴⁺, P⁵⁺ and alkyl group with thin film-like morphology, were formed and was characterized by means of XRD, IR, TG/DTA, and elemental analysis. The chemical formula of the precursor obtained by exfoliation–reduction in 1-butanol was shown to be VO{(n-C₄H₉)_0.16H_0.84}PO₄·0.8H₂O. On the other hand, a direct reduction of VOPO₄·2H₂O in the alcohol gave a mixed phase shown by (VOHPO₄·0.5H₂O)_0.3(VO{(n-C₄H₉)_0.3H_0.7}PO₄·3H₂O)_0.7 comprising plate-like microcrystallites. These precursors transformed to (VO)₂P₂O₇ phase during an activation process at 703 K in the presence of a mixture of n-butane 1.5% and O₂ 17% in He balance. The obtained (VO)₂P₂O₇ through the exfoliation–reduction was well crystallized and consisted of thin flaky crystallites. It was found that (VO)₂P₂O₇ thus prepared through the exfoliation–reduction was highly active and selective for oxidation of n-butane.     

Sn掺杂TiO2/ACF复合材料的制备、表征及光催化性能

以Ti(OC₄H₉)₄为前体,SnCl₄为Sn源,采用胶溶-回流法制备了Sn掺杂的TiO₂,利用浸渍提拉法将其负载到活性炭纤维(ACF)表面,并运用SEM、XRD、XPS、DRS等手段对TiO₂/ACF复合材料进行表征,考察了复合材料光催化降解气相甲醛的性能。研究结果表明,Sn元素掺入TiO₂晶格中,有利于抑制TiO₂晶粒的生长,促进TiO₂由锐钛矿型向金红石型的转化,光吸收范围发生一定程度红移;HNO₃的用量为0.015mol、掺锡量为6%、负载两层的TiO₂/ACF-50复合材料在紫外光照射下对甲醛的去除率复合材料可达85.2%,而在可见光下仅为65.3%。     

A study on the characteristics of the SO2 reduction using coal gas over SnO2-ZrO2 catalysts

SO₂, which is an air pollutant causing acid rain and smog, can be converted into elemental sulfur in direct sulfur recovery process (DSRP). SO₂ reduction was performed over catalyst in DSRP. In this study, SnO₂-ZrO₂ catalysts were prepared by a co-precipitation method, and CO and coal gas, which contains H₂, CO, CO₂ and H₂O, were used as reductants. The reactivity profile of the SO₂ reduction over the catalysts was investigated at the various reaction conditions as follows: reaction temperature of 300–550 °C, space velocity of 5000–30,000 cm³/g_-cat. h, [reductant]/[SO₂] molar ratio of 1.0–4.0 and Sn/Zr molar ratio of SnO₂-ZrO₂ catalysts 0/1, 2/8, 3/5, 5/5, 2/1, 3/1, 4/1 and 1/0. SnO₂-ZrO₂ (Sn/Zr = 2/1) catalyst showed the best performance for the SO₂ reduction in DSRP on the basis of our experimental results. The optimized reaction temperature and space velocity were 325 °C and 10,000 cm³/g_-cat. h, respectively. The optimal molar ratio of [reductant]/[SO₂] varied with the reductants, that is, 2.0 for CO and 2.5 for coal gas. SO₂ conversion of 98% and sulfur yield of 78% were achieved with the coal gas.     

The effect of oxygen concentration on the reduction of NO with propylene over CuO/γ-Al2O3

The effect of oxygen concentration on the pulse and steady-state selective catalytic reduction (SCR) of NO with C₃H₆ over CuO/γ-Al₂O₃ has been studied by infrared spectroscopy (IR) coupled with mass spectroscopy studies. IR studies revealed that the pulse SCR occurred via (i) the oxidation of Cu⁰/Cu⁺ to Cu²⁺ by NO and O₂, (ii) the co-adsorption of NO/NO₂/O₂ to produce Cu²⁺(NO₃⁻)₂, and (iii) the reaction of Cu²⁺(NO₃⁻)₂ with C₃H₆ to produce N₂, CO₂, and H₂O. Increasing the O₂/NO ratio from 25.0 to 83.4 promotes the formation of NO₂ from gas phase oxidation of NO, resulting in a reactant mixture of NO/NO₂/O₂. This reactant mixture allows the formation of Cu²⁺(NO₃⁻)₂ and its reaction with the C₃H₆ to occur at a higher rate with a higher selectivity toward N₂ than the low O₂/NO flow. Both the high and low O₂/NO steady-state SCR reactions follow the same pathway, proceeding via adsorbed C₃H₇---NO₂, C₃H₇---ONO, CH₃COO⁻, Cu⁰---CN, and Cu⁺---NCO intermediates toward N₂, CO₂, and H₂O products. High O₂ concentration in the high O₂/NO SCR accelerates both the formation and destruction of adsorbates, resulting in their intensities similar to the low O₂/NO SCR at 523–698 K. High O₂ concentration in the reactant mixture resulted in a higher rate of destruction of the intermediates than low O₂ concentration at temperatures above 723 K.     

Hydrothermal synthesis of Ba(Ti, Sn)O3 fine powders and dielectric properties of the corresponding ceramics

Fine powders of submicron-sized crystallites of BaTiO₃ were prepared at 85–130°C by the hydrothermal method, starting from TiO₂.ξH₂O gel and Ba(OH)₂ solution. The products obtained below 110°C incorporated considerable amounts of H₂O and OH⁻ in the lattice. As-prepared BaTiO₃ is cubic and converts to the tetragonal phase after heat treatment at 1200°C, accompanied by the loss of residual OH⁻ ions. Hydrothermal reaction of SnO₂.ξH₂O gel with Ba(OH)₂ at 150–260°C gives rise to the hydrated phase, BaSn(OH)₆.3H₂O, due to the amphoteric nature of SnO₂.ξH₂O which stabilises Sn(OH)₆²⁻ anions in basic media. On heating in air or releasing the pressure in situ at 260°C, BaSn(OH)₆.3H₂O converts to BaSnO₃ through an intermediate, BaSnO(OH)₄. Solid solutions of Ba(Ti,Sn)O₃ are directly formed from (TiO₂ + SnO₂)..ξH₂O gel up to 35 mol% SnO₂. At higher Sn contents, the hydrothermal products are mixtures of BaSn(OH)₆.3H₂O and BaTiO₃, which on annealing at 1000°C result in monophasic Ba(Ti,Sn)O₃. The sintering characteristics and the dielectric properties of the ceramics prepared out of these fine powders are presented. The dielectric properties of fine-grained Ba(Ti,Sn)O₃ ceramics are explained on the basis of the prevailing diffuse phase transition behaviour.