共查询到18条相似文献,搜索用时 125 毫秒
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目前我国的3-氰基吡啶主要依赖进口,为了缓解国内供需矛盾,寻找合理的3-氰基吡啶工业化生产路线已经迫在眉睫。综述了3-氰基吡啶的合成路线,包括烟酰胺法,2-甲基戊二腈氧化法以及3-甲基哌啶,3-甲基吡啶氨氧化法。着重介绍了氨氧化法的反应机理及其催化剂的催化活性。在对几类钒系以及非钒系催化剂进行探讨的基础上,提出了一种新型的纳米分子筛催化剂,并对其工业应用前景进行了展望。 相似文献
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丙烯醛水合加氢法制备1,3-丙二醇 总被引:3,自引:1,他引:3
简述了聚对苯二甲酸丙二酯 ( PTT)的特性、我国 PTT的发展状况 ,阐述了纤维级 1,3-丙二醇的研制、开发与生产对 PTT发展的重要性。着重介绍丙烯醛水合加氢法生产 1,3-丙二醇的工艺 ,并对丙烯醛水合反应、3-羟基丙醛加氢反应、4-氧代 -1,7-庚二醇水解反应、1,3-丙二醇提纯方法以及反应催化剂和反应条件进行了探讨 相似文献
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Dehydration of glycerol to acrolein was performed on WO3/ZrO2 solid heterogeneous catalysts in a continuous flow fixed bed reactor. A maximum of 75% acrolein selectivity was achieved at 100% conversion of glycerol. The acrolein selectivity correlates with the concentration of weak acidic sites of the WO3/ZrO2 catalysts that were free of basic sites. 相似文献
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Mudassir K. Munshi Samadhan T. Lomate Raj M. Deshpande Vilas H. Rane Ashutosh A. Kelkar 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》2010,85(10):1319-1324
BACKGROUND: Glycerol has become readily available as a byproduct from the biodiesel industry. High functionality and relatively low price make it a potential building block to produce value‐added derivatives such as acrolein. RESULTS: Dehydration of glycerol to acrolein was performed over several silica supported Brønsted acidic ionic liquids as catalysts. All the catalysts prepared were active for the synthesis of acrolein (conversion of glycerol was observed in the range 35–90% with selectivity to acrolein in the range 29–58%). CONCLUSIONS: Catalyst prepared from triphenyl (3‐sulfopropyl) phosphonium 4‐methylbenzenesulfonate gave good activity and selectivity at 4 h reaction time. The conversion of glycerol decreased with increase in glycerol concentration. Higher temperature (325 °C) resulted in significantly lower conversion as well as selectivity to acrolein. With the use of two additional traps cooled to ? 7 °C, the selectivity to acrolein increased significantly for good catalysts. Copyright © 2010 Society of Chemical Industry 相似文献
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The purpose of this study is to increase acrolein yield and capability of coking resistance in the reaction of glycerol dehydration to acrolein by assembling metal phosphate supported on HZSM-5 catalyst.The as-prepared catalysts were characterized by XRD,SEM,EDS,BET,NH3-TPD,CO2-TPD and Py-IR techniques.It was found that metal phosphate species were incorporated into the porous structure of HZSM-5 zeolites,thus influencing the surface and textural physico-chemical properties of the supporters.The alkaline-treated HZSM-5 catalyst promoted the dispersion of phosphate species on the carriers.Moreover,the amount of strong aridity was tremendously improved by adding the different metal hydrophosphates and the catalysts show high catalytic activity.In this present work,the Sn1/4H2PO4/HZSM-5 catalyst exhibited good performance in the catalytic activity and coking resistant ability,which resulted in a high acrolein yield of 83% initially and acrolein yield of 68% after 30 h.The aridity,especially the ratio of strong to weak acid,plays an important role in promoting acrolein yield and stability simultaneously. 相似文献
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《Applied Catalysis A: General》1999,176(1):11-16
Silica-supported bismuth molybdate catalysts were prepared by impregnation in a highly dispersed state and by coprecipitation in a largely crystallized state. Their catalytic behavior was investigated in the oxidation of propene to acrolein. The highly dispersed bismuth molybdate catalysts on silica were found to be intrinsically active but poorly selective to acrolein. When we increased the loading amount the oxidation activity drastically increased. The poor acrolein selectivity of this catalyst was improved by continuous use in the catalytic oxidation for making the particle size of the dispersed bismuth molybdate larger. The catalytic activity and selectivity were little influenced by the loading amount in the cases of the coprecipitated catalysts. The results demonstrate that, for the activity and selectivity, bismuth molybdate catalysts need to be of a certain particle size which can provide sufficient lattice oxide ions during the catalytic redox cycle. 相似文献
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用生物柴油副产物粗甘油催化氧化脱水制丙烯酸,该过程耦合了甘油脱水制丙烯醛和丙烯醛选择性氧化制备丙烯酸两步反应。结果表明,在甘油脱水反应中,使用Cs3PW12O40, P-ZSM-5和Co0.5H2PO4/SiO2等固体酸催化剂,可得到较高的丙烯醛收率(最高86.9%)。利用上述催化剂和MoVW基氧化催化剂,在脱水/氧化双催化剂床层构型反应器中,以甘油为原料合成丙烯酸的收率达50%~80%,直接加入粗甘油可获得相似的丙烯酸收率。 相似文献
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Gas-phase dehydration of glycerol to produce acrolein was investigated over commercial catalysts based onγ-Al2O3, viz. A-64, A-56, I-62, AP-10, AP-56, AP-64 and KR-104. To understand the effect of Cl?anions, HCl-impregnated sup-ports have been investigated in the dehydration reaction of glycerol at 375 °C. For comparison, various H-zeolites were also examined. It was found that the glycerol conversion over the solid acid catalysts was strongly dependent on their acidity and surface area. And the relationship between the catalytic activity and the acidity of the catalysts was discussed. The outstanding properties of Pt/γ-Al2O3 catalyst systems for the dehydration of glycerol were revealed. Pt/γ-Al2O3 catalyst (AP-64) showed the highest catalytic activity after 50 h of reaction with an acrolein selectivity of 65%at a conversion of glycerol of 90%. Based on these results, catalysts based onγ-Al2O3 appear to be most promising for gas phase dehydration of glycerol. 相似文献
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A series of aluminophosphates (APO) catalysts with Ce, Cu, Cr, Fe, Mn, Mo, V, and W oxide loading at a constant ratio M: Al = 1: 10 and PO4: Al = 1: 12 were prepared and characterized by N2 physisorption, XRD and NH3-TPD. Gas-phase dehydration of glycerol to produce acrolein and acetol was investigated at 280°C in presence of water. Conversion
and product distribution depended on the intrinsic acidity and the type of transition metal oxide. Best selectivity to acrolein
(52–58%) was obtained for W- und Mo-APO catalysts. Cr-, Mn- and W- oxide containing catalysts enhanced the formation of phenol,
acetaldehyde and CO
x
. The catalysts containing V- and Fe-oxide promoted the formation of allyl alcohol. All catalysts showed long term stability,
which can be attributed to the redox ability of the metal oxides that enhances the removal of coke deposits. The investigated
catalyst a specially W-APO and Mo-APO can be recommended for further controlled trials on a pilot plant for selective conversion
of water solution of glycerol to acrolein and/or acetol. 相似文献