加氢釜搅拌型式的探讨

通过对加氢釜的搅拌型式的探讨,找到解决实际生产问题的方法,改良了搅拌效果,提高了加氢釜的产能。     

国内外加氢石油树脂的技术进展

介绍了国内外石油树脂的生产和技术发展状况，并对加氢催化剂的最新进展了作了较详细的论述，提出了发展我国加氢石油树脂的建议。     

选择加氢法改进豆油下脚料制油酸酰胺的稳定性

为改进豆油下脚料生产的润滑剂油酸酰胺碘值高、放置一段时间后迅速变黄等稳定性差的缺点．采用骨架镍催化剂选择性加氢油酸酰胺。使其中的亚油酸酰胺、亚麻酸酰胺等不饱和组分大部分转化力油酸酰胺而被除去，提高油酸酰胺的含量和使用性能。最佳反应条件为：反应温度160℃。反应压力0．4MPa，反应时间3．0h，催化剂用量3％。采用碘值结合放置后目测的方法进行了产品分析和评估。     

二氧化碳催化加氢研究进展

介绍了近年来由 CO2 催化加氢制取甲醇、烃类、醛类、甲酸和二甲醚等反应的研究进展     

6-羟基色满的合成

以2′,5′-二羟基苯乙酮和原甲酸三乙酯缩合得到6-羟基-4-色酮,再经催化氢化得到标题化合物。这是合成6-羟基色满的新路线,收率能达到47%。     

In situ observation of methoxide hydrogenation on the Ni(111) surface

The surface chemistry of methoxide (CH₃O-) on the Ni(111) surface has been studied in the presence of hydrogen pressures up to 2 Torr. During heating in vacuum methoxide decomposes to H₂ and CO, which desorb at 380 and 445 K, respectively. The CH₃O-decomposition process is rate limited by CH bond breaking and exhibits a strong deuterium kinetic isotope effect in CD₃O-. In the presence of ambient hydrogen pressures of 0.02–2.0 Torr both CH₃O- and CD₃O-are hydrogenated directly to methanol at 310 K. Methoxide is hydrogenated by adsorbed hydrogen, which nearly saturates the surface at these pressures and temperatures.     

硝基苯加氢制备对氨基苯酚的工艺要素研究

在稀硫酸介质中,Pt/C催化,硝基苯加氢还原、转位得到目标化合物对氨基苯酚。工艺要素研究表明:硝基苯20mL,氢气压力为1kPa的水封压力,温度85～90℃,十六烷基三甲基溴化铵用量为0.1g,2%Pt/C催化剂0.5g,反应时间为5h时,所得产品质量达到并优于日本JISK4144 1986标准要求。     

在役加氢反应器材料损伤分析

基于随加氢反应器运行 5a的试验试块 ,研究了加氢反应器运行 5a后筒体材料 2 .2 5Cr 1Mo钢的损伤。进行了化学成分分析、拉伸和冲击试验、脱氢和脱脆试验以及断口形貌分析。结果表明 :反应器运行 5a后筒体母材及其焊缝金属的拉伸性能未发生明显变化 ,而冲击韧性明显降低 ,且焊缝金属损伤程度较母材严重。经分析 ,材料的损伤主要是加氢反应器长期使用过程中高温回火所致     

Determination of effectiveness factor of a partial internal wetting catalyst from adsorption measurement

The effect of partial internal wetting of catalyst pellets on apparent reaction kinetics at elevated temperatures and pressures is investigated experimentally and by modeling for benzene hydrogenation. A new method that combines adsorption and chemical reaction is introduced to study the kinetics influenced by capillary condensation of reagents at steady-state conditions. It is shown that the extent of liquid filling in the pellet interior has a critical effect on the global kinetics, and the current state of the catalyst depends on the history. Under certain conditions two steady states of the effectiveness factor exist. Moreover, either a decrease in temperature or increase in total pressure can increase the effectiveness factor. The model exhibits good agreement with experimental results.     

Reaction Coupling of Ethylbenzene Dehydrogenation with Nitrobenzene Hydrogenation

The chemical equilibrium for the coupling of ethylbenzene dehydrogenation with nitrobenzene hydrogenation, to produce styrene and aniline simultaneously, has been calculated on the basis of the Soave–Redlich–Kwong equation of state. The dehydrogenation of ethylbenzene in the presence of nitrobenzene over the catalysts -Al₂O₃, ZSM-5, activated carbon and platinum supported on activated carbon has been carried out at 400 °C. The effects of Pt loading and the pretreatment of the catalysts have been investigated. It has been revealed that the conversion of ethylbenzene can be greatly improved by the reaction coupling due to the elimination of the hydrogen produced in the reaction by the hydrogenation of nitrobenzene. Platinum supported on the activated carbon has been suggested as a suitable catalyst. The best results with ethylbenzene conversion of 33.8% and styrene selectivity of 99.2% were obtained over Pt(0.02 wt%)/AC at 400 °C. Moreover, such process is also energetically favored since the necessary process heat to drive the ethylbenzene dehydrogenation can be provided by the coupling with the exothermic nitrobenzene hydrogenation reaction.