Relative reactivities of alkanes in multi-component catalytic cracking reactions

An experimental technique is discussed for measuring relative reactivities of alkanes in the catalytic cracking of multi-component hydrocarbon mixtures over a heterogeneous, Y-zeolitebased catalyst at 250–350 °C. With the technique, ca. 0.1 l of an alkane mixture is evaporated and contacted with a catalyst, after which the mixture of reaction products and the unreacted feed enters the chromatographic column and is immediately analyzed. The technique is used to measure relative reactivities of 21 alkanes in a single experiment. The principal results of these experiments are similar to the results of single-component cracking: alkane reactivity rapidly increases with the increase of the carbon number, and methyl-branched alkanes are more reactive than linear alkanes. However, the variations in alkane reactivities as a function of their molecular weight and skeleton structure differ very significantly between single- and multicomponent experiments.     

阳离子交换树脂催化合成十三碳二元酸二乙酯

以强酸性阳离子交换树脂为催化剂,十三碳二元酸与乙醇为原料合成十三碳二元酸二乙酯,考察了影响反应的因素。结果表明:醇酸摩尔比为4∶1,催化剂用量为酸质量的2%,在3分子筛脱水的情况下反应7 h,酯化率达98.4%,并且催化剂可重复使用3次。     

Effect of pressure on three catalytic partial oxidation reactions at millisecond contact times

The effects of pressure on reactant conversion and product selectivities in three catalytic oxidation systems have been examined at pressures between 1 and > 5 atm. Reaction was sustained autothermally near adiabatic operating conditions at temperatures of 1000°C with residence times over the noble metal catalysts between 10^–4 and 10^–2 s. The three systems investigated were (1) HCN synthesis over Pt-10% Rh gauze catalysts, (2) methane oxidation to synthesis gas (CO and H₂) over rhodium-coated monoliths, and (3) ethane conversion to ethylene over platinum-coated monoliths. We find that selectivities in all three reactions do not change dramatically with approximately a five-fold increase in pressure. This strongly suggests that free radical homogeneous chain reactions are not significant in these processes and that they can be operated reliably above atmospheric pressure. For the synthesis of HCN over Pt-10% Rh gauzes, the selectivity to HCN can be maintained above 0.75 at pressures up to 5.5 atm. Selectivities to synthesis gas (CO and H₂) from a methane-air mixture over a Rh-coated foam monolith at pressures up to 5.5 atm were maintained above 0.90. Over a Pt-coated foam monolith, the selectivity to ethylene from ethane-air and ethane-O₂ mixtures was independent of pressure up to 6.5 atm and conversion rose slightly although it was necessary to maintain constant velocity and residence time over the catalyst to avoid carbon formation.This research was supported by DOE under Grant No. DE-FG02-88ER13878.     

车用尾气催化转化器结构的计算辅助设计与分析系统

采用ＡｕｔｏＬＩＳＰ语言,编制了运行于ＡｕｔｏＣＡＤ平台上的车用尾催化转化器结构的计算辅助设计与分析系统。该系统结合了参数化设计与性能分析功能,并采用对话框驱动执行的方式,使系统的使用具有直观、方便的特点,可为车用尾气催化转化器的研制工作提供有益帮助。,     

LOSA-1增产轻烯烃FCC助催化剂的开发及工业应用

在中国石化济南分公司800 kt·a^－1催化裂化装置上试应用了岳阳三生化工有限公司生产的LOSA-1增产轻烯烃FCC助催化剂，考察了该助催化剂催化裂化性能及其对汽油和柴油质量的影响。工业应用表明，增产轻烯烃助剂占系统催化剂总藏量4.0％时，丙烯（对催化进料）增加了1.19％，系统总液收及焦炭产率基本保持不变。     

燃料乙醇发展现状和前景展望

介绍了国内外燃料乙醇的发展现状以及我国对于发展燃料乙醇的相关政策,从成本、原料、粮食安全、市场及经济性方面进行了分析,建议应借助人大立法,保证燃料乙醇推广的顺利进行;政府应制定补贴、免征税收等政策并及时落实;积极推进燃料乙醇新技术的开发工作;扩大燃料乙醇应用范围,推进燃料乙醇的应用进程;开展乙醇化工的研究。     

葫芦岛蒙脱土的特征与催化活性

研究了葫芦岛蒙脱土的某些特征与催化活性。该蒙脱石的离子交换能力与层间距分别是７５ｍｅｑ／１００ｇ和１．５２９ｎｍ，对偏三甲苯的歧化、异构化以及偏四甲苯的脱甲基、异构化都具有催化活性。这些数据表明葫芦岛蒙脱土是一种有用的催化材料。     

电控汽油机怠速模糊RBF神经网络控制

针对电控汽油机怠速控制要求,提出了一种模糊径向基函数(RBF)神经网络控制方案,在MATLAB环境下进行了控制仿真,获得了比PID、模糊、模糊BP神经网络更好的控制性能。     

汽油在线优化调合系统实践

为了保证汽油调合辛烷值的准确性,在减少辛烷值浪费的同时应避免因辛烷值低于标准值而造成质量事故。参考国内外汽油在线优化调合的各种技术方案,设计了一种适合中国国情的汽油在线优化调合控制系统。经中石化天津和洛阳炼油厂应用证明,系统很好地解决了调合过程中的辛烷值控制及优化问题,取得了较好的经济效益。     

我国推行无铅汽油情况的研究

车用含铅汽油对人体有极大的危害,本文通过对汽车排放新标准、企业技术改造及有关政策的分析,阐明了我国推行无铅汽油政策的可行性。