锗钨酸催化合成水杨酸异戊酯

Isoamyl salicylate was synthesized by using germanotungtic acid as catalyst.The effects of the amaunt of catalyst,the molar ratio of salicycic acid of isoamy l alcohol,the reaction temperature and the reaction time on the yield of ester w ere studied.The optimum reaction conditions were 1.3∶100 (mass ratio) of cataly st to reactants,1∶2.5 (molar ratio) of acid to alcohol,135～153℃ being satisfa ctary reaction temperature and reaction time suitable being 3h.Under such condit ion,the yield of ester was up to 94%.Germanotungtic acid catalyst can be used re peatedly.     

加热与超声辐照条件下4-(丁二酰亚胺基)-1-丁烷磺酸Brnsted酸催化剂催化吡喃并[4,3-b]吡喃衍生物合成(英文)

4-(Succinimido)-1-butane sulfonic acid was shown to be an efficient and reusable Brnsted acid catalyst for the synthesis of pyrano[4,3-b]pyran derivatives using thermal and ultrasonic conditions. The catalyst was prepared by mixing succinimide and 1,4-butanesultone, which is simpler and safer than the preparation of succinimide sulfonic acid. This method has the advantages of high yield, clean reaction, simple methodology, and short reaction time. The catalyst can be recycled without loss of activity.     

固体酸Fe2(SO4)3催化合成丙酸异戊酯

Solid acid ferric sulphate Fe2(SO4)3 was prepared and used for the study of the catalytic synthesis of iso-amyl propionate. The optimun reaction conditions were follows: the ratio of amount of substance n(iso-amylalcohol) : n(propionic acid) = 1.5, the reaction time 2h, the catalyst quantity 1.5g, and dewatering solvent toluene 10ml. The yield was 97.2% under the optimum reaction conditions. The catalyst being of high catalytic activity for the esterification reactions was prepared very easily and could be used repeatedly.     

磺化碳催化Biginelli反应一锅法合成3,4-二氢-2(1H)-酮和硫酮(英文)

A sulfonated carbon material was shown to be a highly efficient,eco-friendly,and recyclable solid acid catalyst for the Biginelli reaction of β-ketoester,aldehyde,and urea or thiourea under solvent-free conditions.It gave 3,4-dihydropyrimidin-2(1H)-ones and-thiones in good to excellent yields.This method has the advantages of a simple procedure with easy work-up,short reaction time,and high yields.The catalyst can be recycled after a simple work-up and was reused four times without substantial reduction in activity.     

高效可回收催化剂In(OTf)_3用于无溶剂条件下Pechmann缩合反应(英文)

In(OTf)3 plays the role of a Lewis acid catalyst in the Pechmann condensation of phenols with β-ketoesters under solvent-free conditions to give coumarin derivatives. This novel and inexpensive method has advantages such as short reaction time, excellent product yields, and avoids the use of organic solvents in agreement with green chemistry principles. Catalyst loadings can be as low as 1 mol% to give high yields of the corresponding coumarins at 80 °C. The catalyst can be recovered after the reaction, and reused with only a slight decrease in the yield.     

Effect of diluent and reaction parameter on selective oxidation of propane over MoVTeNb catalyst using nanoflow catalytic reactor

The selective oxidation of propane to acrylic acid over an MoVTeNb mixed oxide catalyst, dried and calcined before reaction has been studied using high-throughput instrumentation, which is called nanoflow catalytic reactor. The effects of catalyst dilution on the catalytic performance of the MoVTeNb mixed oxide catalyst in selective oxidation of propane to acrylic acid were also investigated. The effects of some reaction parameters, such as gas hourly space velocity （GHSV） and reaction temperature, for selective oxidation of propane to acrylic acid over diluted MoVTeNb catalyst have also been studied. The configuration of the nanoflow is shown to be suitable for screen catalytic performance, and its operating conditions were mimicked closely to conventional laboratory as well as to industrial conditions. The results obtained provided very good reproducibility and it showed that preparation methods as well as reaction parameters can play significant roles in catalytic performance of these catalysts.     

A mild,simple and efficient method for selectiveα-monobromination of 1,3-diketones and β-ketoesters using pyridinium bromochromate

Pyridinium bromochromate has been found to be a highly efficient and selective reagent for theα-monobromination of 1,3-diketones andβ-keto-esters in the absence of base,Lewis acid,or other catalyst.The products were formed in high to excellent yields under mild reaction conditions and in short reaction times.     

Selective Oxidation of Propane by Lattice Oxygen of Vanadium-Phosphorous Oxide in a Pulse Reactor

Selective oxidation of propane by lattice oxygen of vanadium-phosphorus oxide (VPO) catalysts was investigated with a pulse reactor in which the oxidation of propane and the re-oxidation of catalyst were implemented alternately in the presence of water vapor. The principal products are acrylic acid (AA),acetic acid (HAc), and carbon oxides. In addition, small amounts of C1 and C2 hydrocarbons were also found, molar ratio of AA to HAc is 1.4-2.2. The active oxygen species are those adsorbed on catalyst surface firmly and/or bound to catalyst lattice, i.e. lattice oxygen; the selective oxidation of propane on VPO catalysts can be carried out in a circulating fluidized bed (CFB) riser reactor. For propane oxidation over VPO catalysts, the effects of reaction temperature in a pulse reactor were found almost the same as in a steady-state flow reactor. That is, as the reaction temperature increases, propane conversion and the amount of C1 C2 hydrocarbons in the product increase steadily, while selectivity to acrylic acid and to acetic acid increase prior to 350℃ then begin to drop at temperatures higher than 350℃, and yields of acrylic acid and of acetic acid attained maximum at about 400℃. The maximum yields of acrylic acid and of acetic acid for a single-pass are 7.50% and 4.59% respectively, with 38.2% propane conversion. When theamount of propane pulsed decreases or the amount of catalyst loaded increases, the conversion increases but the selectivity decreases. Increasing the flow rate of carrier gases causes the conversion pass through a minimum but selectivity and yields pass through a maximum. In a fixed bed reactor, it is hard to obtainhigh selectivity at a high reaction conversion due to the further degradation of acrylic acid and acetic acid even though propane was oxidized by the lattice oxygen. The catalytic performance can be improved inthe presence of excess propane. Propylene can be oxidized by lattice oxygen of VPO catalyst at 250℃, nevertheless, selectivity to AA and to HAc are even lower, much more acetic acid was produced (molar ratio of AA to HAc is 0.19:1-0.83:1) though the oxidation products are the same as from propane.     

High-yield production of 2,5-dimethylfuran from 5-hydroxymethylfurfural over carbon supported Ni–Co bimetallic catalyst

The catalytic conversion of 5-hydroxymethylfurfural(HMF) to 2,5-dimethylfuran(DMF) has attracted extensive research interests because DMF can be used as potential and competitive renewable transportation fuel or additives. Here we report a non-noble bimetallic catalyst with improved activity for hydrogenation and hydrogenolysis by introducing active carbon as support into a nickel–cobalt catalyst. The characterizations of the catalyst indicate that the Ni and Co species are uniformly dispersed on the active carbon through the wetness impregnation method. The influences of reaction temperature and hydrogen pressure are systematically investigated and an excellent yield(up to 95%) of DMF can be obtained at relatively mild conditions, 130 °C and 1 MPa H_2, over the carbon supported Ni–Co bimetallic catalyst. The high catalytic activity originates from the synergistic effect between Ni and CoO xspecies, the high BET surface area of the catalyst, and the uniform dispersion of Ni and Co species on the active carbon. The catalyst could be reused for 5 times without loss of activity in a batch reactor. Futhermore, the conversion of HMF to DMF on a fixed-bed reactor was also investigated and the 2%Ni–20%Co/C catalyst exhibited an excellent yield to DMF(90%) for 71 h time on stream, indicating the high activity and stability of the catalyst.     

STUDIES ON THE RING-OPENING POLYMERIZATION OF TETRAHYDROFURAN Ⅳ. COPOLYMERIZATION OF TETRAHYDROFURAN AND PROPYLENE OXIDE INITIATED BY FUMING SULFURIC ACID AND PERCHLORIC ACID CATALYST SYSTEM

The yield of copolymerization of tetrahydrofuran and propylene oxide (THF:PO=100:5—15, by wt.) using a binary catalyst of fuming sulfuric acid (21% or 28%) and perchloric acid is around 50—60%, and the loss of THF in the reaction is below 10—15%. The average molecular weight of the product can be controlled in the range of 1000—2000 by varying the binary catalyst system. The present method, which is different from the usual copolymerization initiated by BF_3-diol or SbCl_5-diol system, shows the pecularities i.e. the yield of copolymerization with the low PO feed is not decreased, the hydroxyl functionality is equal to 2, and the end-groups are predominantly primary hydroxyls (around 65—70%).     

纤维素乙二胺负载钯配合物的制备及其对Heck反应的催化性能

合成了纤维素乙二胺负载钯（CE—Pd）配合物,用IR、XPS、TG／DTA等手段对其进行了表征．该配合物在室温至280oC范围内有很好的稳定性,在空气氛围水相中能有效地催化丙烯酸与芳基碘、苯乙烯与芳基碘的Heck芳基化反应,立体选择性地生成取代的反式肉桂酸、1,2-二苯乙烯．在80℃时反应6h,反式肉桂酸的产率达89．7％．纤维素乙二胺负载钯（CE—Pd）配合物还具有较好的重复使用性能,连续使用4次,反式肉桂酸的产率仍可达到63．5％．     

纤维素二乙烯三胺负载钯配合物的制备及对Heck反应的催化性能

通过较简单的方法合成了纤维素二乙烯三胺负载钯(0)配合物,并利用XPS、TG、DTA等手段对其进行了表征。该配合物在室温至230℃范围内有很好的稳定性,在空气氛围、DMSO中能有效地催化丙烯酸、苯乙烯与芳基碘的Heck反应,立体选择性地生成取代的反式肉桂酸、1,2-二苯乙烯,在70℃时反应6h,产率≥66%(丙烯酸、苯乙烯与带取代基芳基碘的Heck反应产率接近100%)。催化剂中起催化作用的是金属态的钯。     

田菁胶负载钯催化Heck反应的研究

通过较简单的方法合成了田菁胶负载钯化合物,利用XPS、IR、TG、DTA和TEM等手段对其进行了表征.该化合物在空气氛围中就能很好地催化丙烯酸、苯乙烯和丙烯酰胺与芳基碘的Heck反应,高产率(≥85 % )且立体选择性地生成取代的反式肉桂酸、1,2- 二苯乙烯和肉桂酰胺.化合物具有较好的重复使用性能.催化剂中起催化作用的是金属态的钯.     

壳聚糖基聚合物负载钯配合物的制备及对Heck反应催化性能

以壳聚糖为基本原料制得壳聚糖缩水杨醛负载钯配合物(S-CTS-Pd)和交联壳聚糖缩水杨醛负载钯配合物(CL-S-CTS-Pd)两种催化剂,利用XPS、TG、DTA等手段对其进行了表征.两种催化剂不需在惰性气体氛围中就能有效地催化芳基碘与丙烯酸、苯乙烯的Heck反应,高产率地得到反式肉桂酸、1,2二苯乙烯,芳基碘上吸电子和供电子取代基的存在对反应没有明显影响.与S-CTS-Pd相比,CL-S-CTS-Pd在较低的温度或较少的催化剂用量下,对Heck反应仍有较高的催化活性.负载催化剂CL-S-CTS-Pd重复使用性能的研究表明,在催化碘苯与丙烯酸反应重复10次后,肉桂酸的产率仍达75.3%.     

一种无机-有机高分子杂化催化剂Pd(0)-CS/MCM-41的制备及其性能研究

将天然高分子聚合物壳聚糖负载到MCM-41介孔分子筛上,再在室温与氯化钯乙醇溶液作用,制得了一种无机-有机天然高分子杂化催化剂Pd(0)-CS/MCM-41,并利用XPS、FTIR、XRD、热重等手段对其进行了表征。以碘代苯与丙烯酸的Heck芳基化反应考察了所得催化剂的催化性能。结果表明,催化剂具有较高的催化活性和良好的重复使用性能,催化剂在氮气保护下能有效地催化碘代苯与丙烯酸的Heck反应,高产率地得到反式肉桂酸。经8次重复使用后,肉桂酸的产率仍达80%以上。     

煤酸异构化制对苯二甲酸

进行了煤氧化产物煤酸（水溶酸WSA）钾在催化剂碳酸镉的存在下，异构化制对苯二甲酸(TPA)的研究。主要考察了催化剂用量、二氧化碳初压、反应温度和反应时间对TPA产率的影响。结果表明，在催化剂存在下煤酸可以转化成TPA。单独煤酸钾异构化时，较佳反应条件：温度430 ℃～450 ℃，压力4.0 MPa，催化剂CdCO3用量4%，反应时间2 h。煤酸钾与苯甲酸（BA）钾混合异构化时，较佳反应条件与单独煤酸钾时基本相同。单独煤酸钾在较佳条件下异构化时，粗TPA产率达34%左右，相当于根据其中有效成分苯多羧酸（BPCA）计算的理论产率的75%左右，选择性较好。煤酸钾加苯甲酸钾在较佳条件下异构化时,粗TPA产率可达68%，扣除假定BA自身岐化生成TPA理论产量之后，则煤酸的TPA产率高达70%，比煤酸单独异构化TPA产率(34%)高1倍。粗TPA经精制可得纯度99%以上的精TPA。     

乙酸选择性加氢制乙醇反应性能研究

在固定床反应器上考察了反应温度、反应压力、乙酸(HAC)液体进料空速、H_2/HAC(总气体空速GHSV或H_2流量)对乙酸选择性加氢制乙醇反应的影响,研究了乙酸转化率、产物选择性、乙醇时空收率的变化规律,验证了自主开发催化剂的稳定性。结果表明,副产物的选择性受反应条件的影响,选择合适的反应条件可以抑制乙酸乙酯和丙酮的生成。原料与催化剂床层接触时间小于5s时,可以避免发生乙酸加氢分解脱羰反应生成甲烷气相产物,也避免了乙醇的进一步反应生成乙烷。在反应温度为280℃,反应压力为2.5 MPa,乙酸进料液时空速为0.72 h~(-1),H_2/HAC(mol ratio)为16的条件下,乙酸乙酯选择性为6%。900 h长周期实验表明,自主开发催化剂具有较好的工业应用前景。     

硫酸高铈催化合成丙酸苄酯

以结晶硫酸高铈为催化剂对丙酸苄酯的合成进行了研究，考察了反应时间、催化剂用量、醇酸摩尔比和带水剂等因素对反应的影响，结果表明，在最佳反应条件下，酯化率在85％以上。     

腐植酸负载Pd/Ni双金属催化剂对Heck反应催化性能的研究

制备了腐植酸负载Pd/Ni双金属催化剂, 该催化剂能够成功催化溴苯与丙烯酸、苯乙烯等乙烯基化合物的Heck反应, 产率均在85%以上; 催化剂能够不同程度地重复使用, 在催化溴苯与丙烯酸反应中, 催化剂重复使用3次后仍可得到42.9%的产率, 而在催化溴苯与苯乙烯反应中, 催化剂重复使用7次后也可得到26.7%的产率; 并且对不同取代基芳基卤与丙烯酸的反应也有很好的催化活性.