甲苯氧化制苯甲酸的新催化体系

以分子氧为氧化剂,探索了甲苯氧化制苯甲酸的新催化体系,第一次把N-羟基邻苯二甲酰亚胺(NHPI)与钴盐组成的催化剂用于甲苯氧化反应.实验揭示:以NHPI/Co(acac)2(乙酰丙酮酸钴)和NHPI/Co(OAc)2(醋酸钴)为催化剂时,苯甲酸的收率可分别为55.5%与41.2%,文中还对氧气压力、反应温度与时间等对反应的影响进行了讨论,同时提出了可能的反应机理.     

对硝基邻苯二乙醚合成技术研究

以邻苯二酚与溴乙烷为原料、聚乙二醇为相转移催化剂合成邻苯二乙醚,再经过冰醋酸和硝酸硝化得到对硝基邻苯二乙醚。研究了反应温度、反应时间、原料摩尔比和催化剂用量等对反应收率的影响,获得了合成邻苯二乙醚的优化工艺条件:n(C6H4(OH)2)∶n(NaO H)∶n(C2H5Br)=1∶2.6∶2.4,反应温度80℃,反应时间4h,催化剂用量2g,该反应条件下邻苯二乙醚平均收率88%。混酸硝化条件下合成对硝基邻苯二乙醚的较佳工艺条件为n(C10H14O2)∶n(HNO3)=1∶1.2,乙酸25mL,反应时间30min,反应温度20℃,该反应条件下对硝基邻苯二乙醚平均收率为99%。     

季铵盐催化氧化法合成硝基苯甲酸

研究了季铵盐A－1催化KMnO4分别氧化邻、对硝基甲苯合成邻、对硝基苯甲酸的反应。考察了不同相转移催化剂的催化活性及催化剂用量、反应温度、反应时间、KMnO4用量和反应体系酸碱性对反应的影响。在优化反应条件下，即以季铵盐A－1为相转移催化剂，KMnO4与硝基甲苯摩尔比为2．5：1，反应温度为95℃，反应时间为3h，在中性条件下进行反应，邻位、对位产物收率分别可达95%和92%。实验表明，季铵盐A－1对于KMnO4氧化硝基甲苯合成硝基苯甲酸的反应是一种优良的相转移催化剂。     

NHPI/Co(Salen)催化氧化取代甲苯

以分子氧为氧化剂,N-羟基邻苯二甲酰亚胺(NHPI)为引发剂,Co(Salen)配合物[NHPI/Co(Salen)]为催化剂,偶氮二异丁腈(AIBN)为助引发剂,AcOH为溶剂,催化氧化取代甲苯制备取代苯甲酸。最佳反应条件为:甲苯6mmol,q(NHPI)=10%,q[Co(Salen)]=0.5%,q(AIBN)=1%,O2(0.1MPa),AcOH10mL,于80℃反应20h,甲苯转化率92.7%,苯甲酸选择性88.9%。     

对硝基甲苯的液相催化氧化研究

本文报道了用乙酰丙酮钴催化对硝基甲苯氧化制备对硝基苯甲酸,以氧气的氧化剂,在3.0MPa压力下,60℃时反应4h可达到83.5%的产率,经过纯化可以制得纯度大于99%的对硝基苯甲酸。文中对各种反应条件的影响进行了研究,并得出其最佳反应条件。同时,文中也探讨了中心金属离子Co^2 和NaOH在此反应中起的重要催化作用及水对反应的影响。     

聚合物微球固载的N-羟基邻苯二甲酰亚胺在分子氧氧化甲苯过程中的催化性能

以交联聚苯乙烯(CPS)微球为基质,经过几步大分子反应在微球表面合成与固载了N-羟基邻苯二甲酰亚胺(NHPI),形成固载有NHPI的聚合物微球CPS-NHPI。本文主要将CPS-NHPI与过渡金属盐组成共催化体系,用于分子氧氧化甲苯的反应,考察了该非均相催化剂的催化特性与催化氧化机理。结果表明,几种过渡金属盐中,Co(OAc)2的助催化效果最好;微球CPS-NHPI与Co(OAc)2所构成的共催化体系,在温和条件(80℃和常压氧气)下可有效地将甲苯深度氧化为苯甲酸,显现出高的催化活性(甲苯转化率达到57%)与优良的选择性(苯甲酸的选择性达到84%)。催化氧化反应遵循自由基链式反应机理。主催化剂CPS-NHPI固载的NHPI与助催化剂Co(OAc)2适宜的摩尔比为14∶1,主催化剂所含NHPI为底物的12(mol)%时,催化剂用量较为合适。固体催化剂CPS-NHPI具有良好的再循环使用性能。     

N-杂环卡宾催化对硝基苯甲醛的氧化酯化

以空气为氧化剂,研究了在N-杂环卡宾催化下,对硝基苯甲醛与9种醇的氧化酯化反应。考察了不同卡宾前体、卡宾前体的用量以及溶剂对收率和反应速率的影响。结果表明,当以对硝基苯甲醛摩尔分数10%的溴化3-乙基-4-甲基-5-羟乙基噻唑鎓盐为催化剂,过量的原料醇为溶剂时,可以有效地催化氧化对硝基苯甲醛进行酯化反应,收率为36%~64%,但当使用与对硝基苯甲醛等摩尔比的醇时,收率仅为9%~29%。     

N-杂环卡宾催化下对硝基苯甲醛的氧化酯化

以空气为氧化剂,研究了在N- 杂环卡宾催化下,对硝基苯甲醛与9种醇的氧化酯化反应。 考察了不同卡宾前体、卡宾前体的用量以及溶剂对收率和反应速率的影响。 结果表明,当以对硝基苯甲醛摩尔分数10%的溴化3-乙基-4-甲基-5-羟乙基噻唑鎓盐为催化剂,过量的原料醇为溶剂时,可以有效地催化氧化对硝基苯甲醛进行酯化反应,收率为36%~64%,但当使用与对硝基苯甲醛等摩尔比的醇时,收率仅为9%~29%。     

对硝基苯甲酸的的合成研究进展

综述了以对硝基甲苯为原料，合成对硝基苯甲酸的近期研究进展，并从技术和经济角度讨论了各种合成方法的优点与不足。     

对硝基苯甲酸制备实验的改进

对硝基苯甲酸的制备实验是有机化学实验教学中氧化反应的典型代表。为了提高对硝基苯甲酸的产率、简化后处理步骤,对对硝基苯甲酸的合成条件进行了改进。探究了反应时间、反应温度和相转移催化剂对对硝基苯甲酸产率的影响。通过改变氧化剂种类、加入相转移催化剂、改变加料方式等措施有效地提高了产率。改进后产物的产率比教材中的重铬酸钠-硫酸氧化法提高了16.8%。     

Alkane Oxidation with Molecular Oxygen Using a New Efficient Catalytic System: N-Hydroxyphthalimide (NHPI) Combined with Co(acac)(n)() (n = 2 or 3)

A novel class of catalysts for alkane oxidation with molecular oxygen was examined. N-Hydroxyphthalimide (NHPI) combined with Co(acac)(n)() (n = 2 or 3) was found to be an efficient catalytic system for the aerobic oxidation of cycloalkanes and alkylbenzenes under mild conditions. Cycloalkanes were successfully oxidized with molecular oxygen in the presence of a catalytic amount of NHPI and Co(acac)(2) in acetic acid at 100 degrees C to give the corresponding cycloalkanones and dicarboxylic acids. Alkylbenzenes were also oxidized with dioxygen using this catalytic system. For example, toluene was converted into benzoic acid in excellent yield under these conditions. Ethyl- and butylbenzenes were selectively oxidized at their alpha-positions to form the corresponding ketones, acetophenone, and 1-phenyl-1-butanone, respectively, in good yields. A key intermediate in this oxidation is believed to be the phthalimide N-oxyl radical generated from NHPI and molecular oxygen using a Co(II) species. The isotope effect (k(H)/k(D)) in the oxidation of ethylbenzene and ethylbenzene-d(10) with dioxygen using NHPI/Co(acac)(2) was 3.8.     

CO Selective Oxidation in Hydrogen-Rich Gas over Copper-Series Catalysts

The performances of CO selective oxidation in hydrogen-rich gas over four catalytic systems of CuO/ZrO2, CuO/MnO2, CuO/CoO and CuO/CeO2 were compared. The reducibility of these catalysts and the effect of CuO and CeO2 molar ratio of CuO/CeO2 catalysts on the activity of selective CO oxidation are investigated by XRD and TPR methods. The results show that the catalysts with the exception of CuO/ZrO2 have the interactions between CuO and CoO, CeO2 or MnO2, which result in a decrease in the reduction temperature. Among the catalysts studied, CuO/ZrO2 catalyst shows the lowest catalytic activity while CuO/CeO2 catalyst exhibits the best catalytic performance. The CuO(10%)/CeO2 catalyst attains the highest CO conversion and selectivity at 140 and 160℃. The addition of 9% H2O in the reactant feed decreases the activity of CuO/CeO2 catalyst but increases its CO selectivity.     

2,3,5-三甲基氢醌的绿色合成工艺研究

以偏三甲苯(TMB)为原料,冰醋酸为溶剂,过氧化氢(50%)为氧化剂,通过直接氧化合成了2,3,5-三甲基氢醌(TMHQ);考察了反应温度、反应时间以及氧化剂和溶剂用量等对TMHQ收率的影响,确定了优化的氧化反应条件.结果表明,最优的氧化反应条件为:反应温度85℃,反应时间3h,TMB与冰醋酸的物质的量之比1∶12,TMB与过氧化氢的物质的量之比1∶11.     

低浓度甲烷甲醇深度氧化Ag/La0.6Sr0.4MnO3催化剂

用柠檬酸溶胶－凝胶法制备钙钛矿型Ｌａ０．６Ｓｒ０．４ＭｎＯ３氧化物,并用Ａｇ对其进行修饰,制得Ａｇ／Ｌａ０．６Ｓｒ０．４ＭｎＯ３系列催化剂。结果表明,６％Ａｇ／Ｌａ０．６Ｓｒ０．４ＭｎＯ３催化剂上甲烷或甲醇氧化转化９５％时的反应温度Ｔ９５可低至７３５Ｋ（对ＣＨ４）或４２１Ｋ（对ＣＨ３ＯＨ）;适量Ａｇ的负载修饰并不改变催化剂基质氧化物Ｌａ０．６Ｓｒ０．４ＭｎＯ３的纳米级钙钛矿型结构;Ａｇ的掺杂诱使催     

Efficient oxidation of alcohols to carbonyl compounds with molecular oxygen catalyzed by N-hydroxyphthalimide combined with a Co species

Highly efficient catalytic oxidation of alcohols with molecular oxygen by N-hydroxyphthalimide (NHPI) combined with a Co species was developed. The oxidation of 2-octanol in the presence of catalytic amounts of NHPI and Co(OAc)2 under atmospheric dioxygen in AcOEt at 70 degrees C gave 2-octanone in 93% yield. The oxidation was significantly enhanced by adding a small amount of benzoic acid to proceed smoothly even at room temperature. Primary alcohols were oxidized by NHPI in the absence of any metal catalyst to form the corresponding carboxylic acids in good yields. In the oxidation of terminal vic-diols such as 1,2-butanediol, carbon-carbon bond cleavage was induced to give one carbon less carboxylic acids such as propionic acid, while internal vic-diols were selectively oxidized to 1,2-diketones.     

低浓度甲烷甲醇深度氧化Ag/La0.6Sr0.4MnO3催化剂

Ag-modified La0.6Sr0.4MnO3 catalysts were prepared and their catalytic performance for deep oxidation of CH4 and CH3OH at low concentrations were investigated. The results showed that the La0.6Sr0.4MnO3 host catalyst with the perovskite-type nano-crystallite structure displayed considerably high catalytic activity for deep oxidation of CH4 and CH3OH at low concentrations. Ag modification to the La0.6Sr0.4MnO3 host catalyst resulted in significant enhancement of the catalyst activity, making the T95 (the reaction temperature needed for conversion of 95%of CH4 or CH3OH) lowered down to 735K (for CH4) and 421K (for CH3OH) from 813 and 465 K over the Ag-free system under the reaction conditions:0.1MPa,CH4/O2/N2=2/12/86(molar ratio),GHSV=45000 h-1 and CH3OH/O2/N2= 0.2/1.0/98.8 (molar ratio),GHSV=58000 h-1,respectively.The carbon containing product was almost CO2 and the contents of HCHO and CO in the reaction exit gas were both under GC detectable limit in both cases.
The results of spectroscopic characterization indicated that modification by proper amount of Ag-dopant did not change the perovskite structure of the La0.6Sr0.4MnO3 host catalyst as a whole. Interaction of Ag-dopant with the surface of the host catalyst,La0.6Sr0.4MnO3,was in favor of high dispersion of the Ag component at the catalyst surface and led to the oxidation of part of the Mn3+species to Mn4+,resulting in an increase of amounts of the reducible Mnn+ species and a decrease of their reduction temperature. On the other hand, this interaction led also to enhancement of adsorption ability of the catalyst toward O2 at relatively low temperature. High activity of the Ag modified La0.6Sr0.4MnO3 catalyst for CH4 and CH3OH complete oxidation was closely related to high redox-activity of the catalyst and its prominent adsorption-activation ability to O2 at relatively low temperatures.     

离子液体中芳烃侧链分子氧催化氧化反应研究

分别以离子液体[Hex-mim]BF4, [Bmim]BF4, [Bmim]PF6和[Omim]BF4为溶剂, Co(Ⅱ), Mn(Ⅱ)或Ni(Ⅱ)/NHPI(AIBN)为复合催化剂, 考察了不同离子液体-催化剂体系中常压分子氧氧化芳烃侧链烷基的反应. 在[Hex-mim]BF4中, Co(Ⅱ)或Mn(Ⅱ)/NHPI可有效地催化芳烃侧链烷基的分子氧氧化. 在优化条件下, 乙苯、正丙苯和正丁苯分别以高达90%, 94%和93%的收率得到相应的芳香酮; 甲苯和对位取代甲苯以32%~47%的收率被氧化为相应的芳香酸. 离子液体及金属催化剂体系在减压下除水后, 可循环使用.     

Liquid-phase oxidation of 2-methoxy-p-cresol to vanillin with oxygen catalyzed by a combination of CoCl2 and N-hydroxyphthalimide

Liquid-phase oxidation of 2-methoxy-p-cresol to vanillin (4-hydroxy-3-methoxybenzaldehyde), in methanol, with molecular oxygen at atmospheric pressure as oxidant and a combination of cobaltous chloride and N-hydroxyphthalimide (NHPI) as catalyst, has been investigated. The effect of reaction conditions on conversion and selectivity for vanillin was studied systematically. Selectivity for vanillin could be enhanced by optimizing the molar ratio of 2-methoxy-p-cresol to NHPI, the amount of sodium hydroxide, reaction time, reaction temperature, and the volume of methanol, which determined the concentration of the reactants. Under the optimized conditions the yield of vanillin was 90.1 %.     

磷酸钛固载磷钨酸非均相催化合成异戊酸己酯

通过在300℃下焙烧2h制备了磷酸钛固载15%磷钨酸H3PW12O40(简记为HPW)非均相酯化催化剂HPW/Ti3(PO4)4;采用红外光谱仪分析了催化剂的结构;基于异戊酸与正己醇的酯化反应考察了催化剂用量、n(正己醇)∶n(异戊酸)、反应时间、带水剂种类和催化剂重复使用性能等因素对酯化率的影响.结果表明,该催化剂催化合成异戊酸己酯的适宜反应条件为:0.2mol异戊酸,催化剂用量0.6g,n(正己醇)∶n(异戊酸)=1.6∶1,反应时间4.5h,环己烷10mL;相应的酯化率达95.1%.与此同时,该催化剂循环利用6次后酯化率不低于84%.     

室温MnO_x上O_3氧化脱除空气中甲醛

采用氧化还原法制备了MnOx催化剂,X射线衍射结果表明其主要为无定形结构.在甲醛和臭氧浓度分别为137和642mg/m3,相对湿度为56%(25oC),GHSV为2×105h-1条件下,MnOx催化剂上O3可将甲醛全部氧化为CO2,反应150min内甲醛转化率和CO2选择性一直保持在～100%.另外,当臭氧与甲醛的摩尔比约为2:3,即显著低于化学计量比时,CO2选择性仍可达～100%.采用傅里叶变换红外光谱仪在线分析了甲醛氧化反应产物,未检测到任何副产物,从而确认了MnOx催化剂上O3对甲醛的完全氧化.