分子筛硅铝比及晶粒粒径对 Cu-ZnO-Al2O3/HZSM-5催化剂直接合成二甲醚反应性能的影响

采用水热晶化法合成了硅铝比(SiO₂/Al₂O₃)为60、120、200和晶粒粒径分别为1.00和0.25 μm的HZSM-5分子筛,并以其为甲醇脱水活性组分与铜基甲醇合成活性组分(Cu-ZnO-Al₂O₃)组成双功能催化剂(Cu-ZnO-Al₂O₃/HZSM-5),在连续流动加压固定床反应器上考察了Cu-ZnO-Al₂O₃/HZSM-5对合成气直接制二甲醚反应的催化性能。结果表明,随着分子筛硅铝比的提高,二氧化碳副产物的生成量逐渐减少,从而使目的产物二甲醚的选择性逐渐增大。与常规分子筛相比,小晶粒分子筛的反应活性接近,但二氧化碳和烃类副产物的选择性较低。     

Co3O4/Ti电催化膜电极制备及其苯甲醇催化氧化性能

本文采用浸渍涂覆法成功制备出多孔Ti负载纳米Co₃O₄电催化膜电极（Co₃O₄/Ti）,以该膜电极为阳极,辅助电极为阴极,构建电催化膜反应器（electrocatalytic membrane reactor,ECMR）用于可控催化氧化苯甲醇制备苯甲醛和苯甲酸,并考察了 Co₃O₄/Ti 膜电极结构、电化学性能以及ECMR不同操作参数对苯甲醇转化率、苯甲醛和苯甲酸选择性的影响. 结果表明,负载Co₃O₄纳米颗粒可以显著提高Ti膜电极的电化学性能和催化活性. 在常温常压下,当反应物苯甲醇浓度为10 mmol·L^-1,pH为7.0,停留时间为5.0 min,电流密度为2.5 mA·cm^-2,苯甲醇的转化率达到49.8%,苯甲醛选择性为51.5%,苯甲酸选择性为23.6%.     

不同碱处理制备多级孔HZSM-5催化剂及噻吩烷基化性能研究

用Na₂CO₃、TPAOH和TPA⁺/CO₃^2-混合碱分别处理HZSM-5分子筛,采用FT-IR、XRD、XRF、N₂吸附脱附、SEM、NH₃-TPD及Py-FTIR表征手段对各类碱处理前后的HZSM-5分子筛进行表征。结果表明,3种类型的碱处理HZSM-5分子筛后,均能形成微孔-介孔多级孔道的HZSM-5(A)催化剂,并能调变催化剂的酸性,其中,TPA⁺/CO₃^2-混合碱处理得到的HZSM-5(TPA⁺/CO₃^2-)催化剂,比表面积最大,介孔数量最多。在小型固定床反应器上,考察了HZSM-5和HZSM-5(A)催化剂的噻吩烷基化性能,结果表明,HZSM-5(TPA⁺/CO₃^2-)催化剂因为具有适当的多级孔孔道和较多的B酸中心而表现出较高的噻吩转化率和1-己烯对噻吩的选择性。     

氢氧化钠-氟硅酸铵改性HZSM-5催化甲醇制丙烯

首次将氢氧化钠-氟硅酸铵复合改性应用于甲醇制丙烯(MTP)催化剂的制备中. 采用X射线衍射(XRD)、X 射线荧光光谱(XRF)、N₂吸附-脱附、透射电镜(TEM)、NH₃程序升温脱附(NH₃-TPD)等测试技术对改性前后HZSM-5分子筛催化剂的晶体结构、元素组成、织构性质、酸性质等进行了表征. 结果表明, 采用氢氧化钠-氟硅酸铵复合改性不仅可以提高催化剂的介孔孔容, 还能有效调变催化剂的酸性. 复合改性方法成功克服了单纯碱处理容易破坏分子筛的骨架结构、单纯氟硅酸铵改性因受扩散限制仅限于修饰分子筛外表面的缺点. 改性后HZSM-5 分子筛催化剂在MTP反应中的诱导期大大缩短, 在常压、反应温度为470 ℃、甲醇质量空速(WHSV)为2 h^-1的条件下, 初始丙烯选择性高达43%. 此外, 复合改性后HZSM-5分子筛在MTP反应中的稳定性大幅改善, 催化寿命延长至本体样品的3倍.     

HZSM-5分子筛在甲醇制丙烯反应中的失活与再生

研究了甲醇制丙烯(MTP)催化剂经过多周期反应后失活的本质原因,据此提出了一种简便易行的催化剂再生方法,即二次晶化法,并将其应用到失活MTP催化剂的再生中。采用X射线衍射(XRD)、X射线荧光光谱(XRF)、X射线光电子能谱(XPS)、N₂吸附、²⁷Al魔角旋转固体核磁共振(²⁷Al MAS NMR)、NH₃程序升温脱附(NH₃-TPD)、吡啶吸附红外(Py-IR)光谱等测试技术对再生前后HZSM-5分子筛催化剂的晶体结构、硅铝比、织构性质、酸性质等进行了表征。并在常压(甲醇分压为30 kPa)、反应温度为470 ℃、甲醇质量空速(WHSV)为1 h^-1的条件下,研究了再生前后HZSM-5分子筛催化剂的催化性能。结果表明,分子筛晶体结构被破坏、活性位流失是多周期反应后HZSM-5分子筛催化剂活性下降的主要原因。经过二次晶化再生后,催化剂的相对结晶度、比表面积、孔容和酸量都明显提高,晶体结构和活性位得到了有效修复,再生催化剂在MTP反应中重新表现出优异的甲醇转化能力和丙烯选择性。     

Pd/PMO-SBA-15 催化剂催化苯甲醇选择氧化反应性能

 研究了 PMO-SBA-15 材料负载的金属钯纳米粒子 (Pd/PMO-SBA-15) 在水相中催化苯甲醇选择氧化制苯甲醛的反应. 考察了纳米粒子种类、氧化剂用量、反应时间和反应温度等对苯甲醇转化率及苯甲醛选择性的影响. 结果表明, 以水为溶剂, 以 H2O2 (30%) 为氧化剂时, 可得到较高的苯甲醇转化率和苯甲醛选择性. 当以 0.05 g 的 2%Pd/PMO-SBA-15 为催化剂, H2O2 用量为 1.5 ml, 反应温度为 80 oC, 反应 4 h 时, 苯甲醇转化率和苯甲醛选择性分别达到 97.1% 和 100.0%. 对该催化体系的重复使用性能进行了考察. 结果发现, 随着使用次数的增加, 苯甲醇转化率有所下降, 但苯甲醛选择性保持不变.     

负载型铼催化剂体系与甲醇选择氧化性能的关系

以铼酸铵为前驱体,制备了氧化物负载型铼催化剂并研究其甲醇选择氧化反应的催化性能.结果表明,Fe₂O₃和V₂O₅等氧化物负载型铼催化剂表现出很高的甲醇选择氧化制备二甲氧基甲烷的催化性能,选择性可达90%～94%(摩尔分数).选择氧化反应活性与铼担载量有关.在α－Fe₂O₃担载的铼催化剂中,以担载质量分数为1%～3%铼的催化剂活性最高[450mmol/(h·gRe)],而高于3%的铼担载量,单位铼催化活性逐渐下降.XRD,XPS和脉冲反应等结果表明,铼酸铰负载于α-Fe₂O₃载体上,并于He气氛中焙烧后,所得表面铼物种与担载量有关,当低于单层担载量时以Re⁶⁺占主导,而高于单层担载量时则Re⁶⁺与Re⁴⁺物种共存.     

纳米氧化锰负载钛基电催化膜制备及其苯甲醇催化氧化性能

利用乳液法制备出MnO_x纳米颗粒,将其负载于微孔管式钛膜制得MnO_x负载钛基电催化膜(MnO_x/Ti).运用X射线衍射(XRD)、X射线光电子能谱(XPS)、扫描电子显微镜(SEM)、循环伏安法(CV)和计时电流法(CA)等表征方法系统考察了不同焙烧温度下MnO_x晶型结构、MnO_x/Ti催化膜电化学性能以及催化氧化苯甲醇的变化规律.结果表明:随着焙烧温度的升高, MnO_x的晶型由初始的Birnessite-MnO₂逐渐转变为K_0.27MnO₂,再由Mn3O4最终转变为α-MnO₂.所得MnO_x/Ti膜中, α-MnO₂晶粒尺寸小于30 nm,结晶度较高,颗粒分布均匀.同时,由于其含有不饱和配位的锰原子和氧空位以及与基体Ti之间存在键合作用,表现出优异的电化学性能和催化性能.以450 ℃焙烧所得的α-MnO₂/Ti为阳极构建电催化膜反应器催化氧化苯甲醇.在反应温度为25 ℃, 50mmol·L^-1苯甲醇水溶液,电流密度为2 mA·cm^-2,停留时间为15 min的条件下,膜反应器苯甲醇转化率达64%,苯甲醛选择性为79%.     

ZnZr/HZSM-5复合催化剂上CO2加氢制备C5+异构烷烃

本研究将锌锆氧化物(ZnZr)与HZSM-5分子筛有效耦合制得系列ZnZr/HZSM-5复合催化剂,考察了HZSM-5硅铝比及Zn/Zr比对复合催化剂上CO₂加氢制备C₅₊异构烷烃性能的影响。结果表明,SiO₂/Al₂O₃=130,Zn/Zr=1∶5制得的ZnZr-4/HZSM-5复合催化剂表现出最优的CO₂加氢制C₅₊异构烷烃性能,CO₂转化率为17%,CO选择性抑制到25%,C₅₊烃及C₅₊烃中异构烷烃选择性分别达60%及89%。该复合催化剂稳定性良好,连续运转120 h未出现失活现象。ZnZr氧化物与HZSM-5分子筛的良好匹配对CO₂加氢高选择性合成C₅₊异构烷烃至关重要。     

Pd2X2(dpm)2(X＝NCO-,CH3CO2-,SCN-,NO3-;dpm＝Ph2PCH2PPh2配合物与H2S反应的NMR研究

采用NMR方法考察了室温和低温(-78～60℃)下Pd₂X₂(dpm)₂(X=NCO^-,CH₃CO₂^-,SCN^-和NO₃^-,dpm=Ph₂PCH₂PPh₂)与H₂S在CD₂Cl₂或CDCl₃中的反应。结果表明,在X=NCO^-和CH₃CO₂^-的情况下,H₂S优先与这些Pd配合物的阴离子作用生成相应的共轭酸HX和Pd₂(SH)₂(dpm)₂,后者在H₂S存在下又进一步转化为Pd₂(SH)₂(dpm)₂(μ-S);当X=SCN^-和NO₃^-时,反应则生成结构可能为[Pd₂(H)(SH)(μ-SH)(dpm)₂]⁺的双核Pd配合物。     

聚苯并噁嗪固载钯基纳米催化剂在芳香醇氧化反应中的应用

以球状聚苯并噁嗪为载体, 采用浸渍热解法合成了钯炭纳米催化剂. 通过透射电子显微镜观察发现, 钯纳米粒子几乎全部均匀分布在载体上, 且尺寸均一, 平均直径约为3.5 nm. 结果表明, 载体表面含有丰富的含氮含氧官能团, 氮和氧原子与钯之间存在相互作用, 从而使聚苯并噁嗪能够有效固载钯纳米粒子. 采用相同的方法进一步合成Pd-Au/C和Pd-Pt/C双金属催化剂, Pd-Au和Pd-Pt纳米粒子也展现出良好的分散性, 无明显团聚现象, 平均直径分别为4.3和4.2 nm, 进一步说明聚苯并噁嗪对金属活性组分的有效固载. 将催化剂应用于苯甲醇氧化反应, 其中Pd₁-Au₁/C在2 h的转化率为98%, 对产物苯甲醛的选择性大于99%, 该催化剂经过焙烧可恢复催化活性, 表现出良好的循环稳定性, 并能将不同取代基的芳香醇氧化为相应的醛, 是一种良好的醇氧化催化剂.     

CuI/2,2'-联吡啶/2,2,6,6-四甲基哌啶氧化物催化氧化醇生成腈的工艺

以高压反应釜为反应装置,采用CuI/Bipy(2,2'-联吡啶)/TEMPO(2,2,6,6-四甲基哌啶氧化物)催化体系,以氨水作氮源,分子氧作氧化剂,对醇催化氧化生成相应腈的方法进行了优化。 以苯甲醇的催化氧化反应为模型反应,考察了催化剂及其用量、溶剂、反应温度以及时间对催化性能的影响。 实验表明:在高压釜中,120 ℃、40×10⁵ Pa的氮氧混合气(φ(O₂)=8%)条件下,将催化剂摩尔分数降低至1%(脂肪醇催化剂摩尔分数为5%),反应时间缩短至8 h时,催化效果最佳。同时,该反应系统对于不同的芳香醇和脂肪醇的氧化均取得了90%以上的转化率和90%以上的产品收率。     

Bimetallic Au/Pd catalyzed aerobic oxidation of alcohols in the poly(ethylene glycol)/CO2 system

Bimetallic Au/Pd nanoparticles were prepared and used to catalyze oxidation of alcohols in the poly(ethylene glycol) (PEG)/CO₂ biphasic system using O₂ as the oxidant without adding any base. The catalytic activity of Au/Pd bimetal with different mole ratios was studied using benzyl alcohol as the substrate. It was found that bimetallic Au/Pd nanoparticles with Au:Pd=1:3.5 had higher catalytic activity than monometallic Au, Pd and the bimetallic Au/Pd nanoparticles with other molar ratios. The effect of CO₂ pressure on the oxidation of benzyl alcohol and 1-phenylethanol in PEG/CO₂ was investigated. It was demonstrated that CO₂ pressure could be used to tune the conversion and selectivity of the reactions effectively. α,β,-Unsaturated alcohols were also studied and found to be more reactive than benzyl alcohol and 1-phenylethanol. Recycling experiments showed that the Au/Pd/PEG/CO₂ catalytic system could be recycled at least four times without reducing the activity. In addition, the catalytic system is clean and the products can be separated easily.     

Unraveling the surface reactions during liquid-phase oxidation of benzyl alcohol on Pd/Al2O3: an in situ ATR-IR study

The palladium-catalyzed liquid-phase reaction of benzyl alcohol to benzaldehyde was investigated in the presence and absence of oxygen by attenuated total reflection infrared (ATR-IR) spectroscopy. The 5 wt % Pd/Al2O3 catalyst was fixed in a flow-through ATR-IR cell serving as a continuous-flow reactor. The reaction conditions (cyclohexane solvent, 323 K, 1 bar) were set in the range commonly applied in the heterogeneous catalytic aerobic oxidation of alcohols. The in situ ATR-IR study of the solid-liquid interface revealed a complex reaction network, including dehydrogenation of benzyl alcohol to benzaldehyde, decarbonylation of benzaldehyde, oxidation of hydrogen and CO on Pd, and formation of benzoic acid catalyzed by both Pd and Al2O3. Continuous formation of CO and its oxidative removal by air resulted in significant steady-state CO coverage of Pd during oxidation of benzyl alcohol. Unexpectedly, benzoic acid formed already in the early stage of the reaction and adsorbed strongly (irreversibly) on the basic sites of Al2O3 and thus remained undetectable in the effluent. This observation questions the reliability of product distributions conventionally determined from the liquid phase. The occurrence of the hydrogenolysis of the C-O bond of benzyl alcohol and formation of toluene indicates that Pd was present in a reduced state (Pd0) even in the presence of oxygen, in agreement with the dehydrogenation mechanism of alcohol oxidation.     

HZSM-5分子筛用于合成聚甲醛二甲基醚

以磷酸二氢铵为前驱体,使用浸渍法制备了一系列不同磷含量改性的HZSM-5分子筛,并结合X射线衍射、N2吸附和氨程序升温脱附等表征结果探讨了催化剂硅/铝比、粒径尺寸、晶体结构、孔结构及表面酸性对其催化甲醇和三聚甲缩反应生成聚甲醛二甲基醚(PODEn)反应性能的影响,同时与商业催化剂进行了比较.结果表明,硅铝比为50,粒径尺寸为5μm,P2O5含量较低(0～6%)的HZSM-5分子筛表现出较高的催化活性和PODEn选择性.在130℃,原料甲醇和三聚甲醛的质量比为2:1的优化条件下反应时,三聚甲醛转化率可达到95.2%,PODEn(n=2～5)的选择性为62.9%,略好于商业催化剂.     

Zn-P复合改性HZSM-5在线催化热解获取生物油的研究

为进一步提高精制生物油的制取效率和燃料品质,采用Zn和P对HZSM-5分子筛进行复合改性,使用XRD、SEM EDS、ICP-AES、BET等方法表征改性HZSM-5分子筛,考察了Zn、P改性对精制生物油理化特性和液相产物的化学组成以及对HZSM-5抗结焦性能的影响。结果表明,Zn、P在HZSM-5表面负载均匀,Zn、P改性未影响HZSM-5的晶体骨架结构,改性HZSM-5的比表面积随着Zn负载量的上升而减少;Zn负载量为3%时,催化热解得到的精制生物油含氧量为10.67%,热值为36.76 MJ/kg,pH值为5.85,精制生物油品质得到显著提升;液相产物中酸类、醛类和酮类等不期望物质相对含量显著下降,芳香族化合物相对含量显著增加,芳香族化合物相对含量为91.93%,其中,芳香烃为74.63%;HZSM-5因负载P使得其相对结焦量明显降低,显著增强了HZSM-5的稳定性;Zn改性促进了氢原子转移和碳正离子的形成,有利于提高HZSM-5分子筛的芳构化性能。     

Synthesis and properties of α-substituted benzylpyridinium salts as cationic initiators

α-Methylbenzylpyridinium SbF₆ (1a) and α,α-dimethylbenzylpyridinium SbF₆ (1b) were prepared and the effect of α-methyl groups on the active species and the activity of 1a, 1b during the cationic polymerization of glycidyl phenyl ether (GPE) was evaluated. 1b was prepared by the reaction of α,α-dimethylbenzyl alcohol with pyridinium hexafluoroantimonate (2) in several solvents, and the yield depended on the dipole moment of the solvents, although it was poor for the reaction of α,α-dimethylbenzyl chloride with pyridine for the steric hindrance of the α-methyl groups followed by exchange with NaSbF₆. Both 1a and 1b acted as a latent thermal initiator during the cationic polymerization of GPE and 1b showed higher activity during cationic polymerization with the higher steric effect of the α-methyl groups than 1a. The ¹H-NMR analysis of the obtained poly GPE indicated that the active species of 1b changed from the benzyl cation to H⁺, depending on the reaction temperature, although 1a released benzyl cations as active species in the cationic polymerization of GPE. © 1996 John Wiley & Sons, Inc.     

Enantioselective decarboxylation of beta-keto esters with Pd/amino alcohol systems: successive metal catalysis and organocatalysis

The kinetics and mechanisms of one-pot cascade reactions of racemic beta-keto esters to give chiral ketones in the presence of Pd/C-chiral amino alcohol catalyst systems were studied. Transformation of 2-methyl-1-tetralone-2-carboxylic acid benzyl ester (1) into 2-methyl-1-tetralone (4) in the presence of Pd/C and cinchona alkaloids or ephedrine was chosen as a model reaction. After the first reaction step, the Pd-catalysed debenzylation of 1 to afford the corresponding beta-keto acid (2), there are two possible reaction routes that may be catalysed by the chiral amino alcohol in solution or by Pd(0) sites on the metal surface in cooperation with the adsorbed amino alcohol. The reaction intermediate 2 was synthesized, and the kinetics of decarboxylation were followed by NMR, UV and IR spectroscopy. The studies revealed that the role of Pd is to trigger the reaction series by deprotection of 1. The subsequent dominant reaction route from the racemic beta-keto acid 2 to the chiral ketone 4 is catalysed by the chiral amino alcohol in the liquid phase. It is shown that kinetic resolution of the diastereomeric salt of rac-2 and the chiral amino alcohol plays a key role in the enantioselection. High enantioselectivity necessitates an amino alcohol/rac-2 ratio of at least 2. A high ratio favours the formation of 1:1 amino alcohol/acid diastereomeric complexes, and the second amino alcohol molecule may be responsible for the enantioselective protonation of 2 in the diastereomeric complex.     

甘油辅助HZSM-5分子筛的制备及其甲烷无氧芳构化催化性能研究

以正硅酸乙酯(TEOS)为硅源,甘油为辅助剂,在水热条件下合成HZSM-5分子筛。考察甘油添加量、晶化时间对HZSM-5分子筛的晶粒尺寸、相对结晶度和酸性等性质及其甲烷无氧芳构化催化性能的影响。利用X射线衍射(XRD)、扫描电镜(SEM)、氨程序升温脱附(NH_3-TPD)等分析手段对不同条件合成的HZSM-5分子筛样品进行表征。结果表明,在添加一定量的甘油辅助剂的条件下,通过调控晶化时间,可以提升HZSM-5分子筛的相对结晶度,在一定程度上抑制无定型SiO_2的产生,增加其酸量。在甲烷无氧芳构化反应中,甘油辅助合成的HZSM-5分子筛催化剂表现出优良的催化性能,与未添加甘油合成的HZSM-5分子筛催化剂相比,甲烷转化率、苯选择性和芳烃选择性均有较大提高,且具有较强的稳定性与容炭能力。     

氮掺杂碳纳米管负载的Ru和Pd催化剂上异丙醇的转化(英文)

Ru and Pd (2 wt%) loaded on pure and on Ndoped carbon nanotubes (NCNTs) were prepared and tested using the isopropyl alcohol decomposition reaction as probe reaction. The presence of nitrogen functionalities (pyridinic, pyrrolic, and quaternary nitrogen) on the nitrogen doped support induced a higher metal dispersion: Pd/NCNT (1.8 nm) Pd/CNT (4.9 nm), and Ru/NCNT (2.4 nm) Ru/CNT (3.0 nm). The catalytic activity of the supports was determined first. Isopropyl alcohol conversion produces acetone on CNTs while on NCNTs it led to both dehydration and dehydrogenation products. At 210 °C and in the presence of air, the isopropyl alcohol conversion was higher on the NCNTs (25%) than on the CNTs (11%). The Pd loaded catalysts were more active and more selective than the Ru ones. At 115 °C, the Pd catalysts were 100% selective towards acetone for a conversion of 100%, whereas the Ru catalysts led to dehydration and dehydrogenation products. The nitrogen doping induced the appearance of redox properties when oxygen is present in the reaction mixture.