含磷化合物改性氢氧化镁及其在EVA中应用研究

采用钛酸酯偶联剂201、311和含磷有机阻燃剂磷酸甲酚二苯酯、亚磷酸二甲酯对氢氧化镁进行表面改性,以红外光谱、热重、电镜和粒度分析为表征手段考察不同种类的改性剂对氢氧化镁表面改性的影响.结果表明,磷酸甲酚二苯酯改性氢氧化镁能提高10℃分解温度,增加高温下质量保持率;钛酸酯偶联剂311改性氢氧化镁能降低平均粒度,使粒径分...     

茂名乙烯装置长周期运转技术探索

中国石化茂名分公司化工事业部乙烯装置1999年2月完成380 kt/a扩能改造后,长周期运转达79个月。多年来,茂名乙烯装置在长周期运转方面进行了很多技术探索并采取了一系列措施,取得了较好的成绩。     

A kinetic study of the electrochemical hydrogenation of ethylene

In this study, we have examined the kinetics of the electrochemical hydrogenation of ethylene in a PEM reactor. While in itself this reaction is of little industrial interest, this reaction can be looked upon as a model reaction for many of the important hydrogenation processes including the refining of heavy oils and the hydrogenation of vegetable oils.To study the electrochemical hydrogenation of ethylene, several experimental techniques have been used including polarization measurements, measurement of the composition of the exit gases and potential step, transient measurements. The results show that the hydrogenation reaction proceeds rapidly and essentially to completion. By fitting the experimental transient data to the results from a zero-dimensional mathematical model of the process, a set of kinetic parameters for the reactions has been obtained that give generally good agreement with the experimental results. It seems probable that similar experimental techniques could be used to study the electrochemical hydrogenation of other unsaturated organic molecules of more industrial significance.     

Enhanced electrochemical performances of LiNi0.5Mn1.5O4 spinel via ethylene glycol-assisted synthesis

A simple and effective method, ethylene glycol-assisted co-precipitation method, has been employed to synthesize LiNi_0.5Mn_1.5O₄ spinel. As a chelating agent, ethylene glycol can realize the homogenous distributions of metal ions at the atomic scale and prevent the growth of LiNi_0.5Mn_1.5O₄ particles. XRD reveals that the prepared material is a pure-phase cubic spinel structure (Fd3m) without any impurities. SEM images show that it has an agglomerate structure with the primary particle size of less than 100 nm. Electrochemical tests demonstrate that the as-prepared LiNi_0.5Mn_1.5O₄ possesses high capacity and excellent rate capability. At 0.1 C rate, it shows a discharge capacity of 137 mAh g⁻¹ which is about 93.4% of the theoretical capacity (146.7 mAh g⁻¹). At the high rate of 5 C, it can still deliver a discharge capacity of 117 mAh g⁻¹ with excellent capacity retention rate of more than 95% after 50 cycles. These results show that the as-prepared LiNi_0.5Mn_1.5O₄ is a promising cathode material for high power Li-ion batteries.     

Petrochemicals from ethanol over a W-Si-based nanocomposite bidisperse solid acid catalyst

Very high ethylene selectivity values approaching 100% and very high ethanol conversion values approaching 85% were obtained in dehydration of ethanol over a new W-silicate-based nanocomposite catalyst having both meso and macropores and containing a W/Si atomic ratio of 0.85. Silicotungsticacid was successfully incorporated into the catalyst structure following a one-pot hydrothermal synthesis procedure. This catalyst is highly stable and does not loose activity in polar solvents and it has a sufficiently high surface area for catalytic applications. Calcination temperature of the catalyst was found to have a very significant effect on the catalyst structure and also on its catalytic performance in ethanol dehydration. Maximum selectivity of the second major reaction product diethylether was obtained as 0.7 at 200 °C, with the catalyst which was calcined at 400 °C. Very high ethylene and diethylether yield values obtained in this study at different reaction conditions are highly promising for the production of petrochemicals from ethanol.     

Toward a CO2-free ethylene oxide process: Homogeneous ethylene oxide in gas-expanded liquids

Among industrial chemical processes, ethylene oxide manufacture emits the largest amount of CO₂ (∼2-3 million tons/yr), as byproduct from the burning of both the ethylene (feed) and ethylene oxide. Further, the conventional silver-based catalytic process presents safety challenges due to the formation of explosive ethylene oxide/O₂ mixtures in the gas phase. By judicious choice of the catalyst (methyltrioxorhenium), oxidant (H₂O₂) and reaction medium (methanol/water), a homogeneous liquid phase catalytic system has been demonstrated that eliminates CO₂ formation while producing ethylene oxide at >90% selectivity at near-ambient temperatures. Given its high volatility, the ethylene oxide is easily recovered from the reaction phase by distillation. The vicinity of the gaseous ethylene feed to its critical temperature (9 °C) is exploited to significantly increase its solubility in the liquid reaction phase by facile compression beyond the critical pressure of ethylene (∼50 bar). Since H₂O₂ is stable at typical reaction temperatures (40 °C or less), potentially explosive ethylene oxide/O₂ mixtures are avoided in the gas phase. In addition to the potential of arresting the carbon footprint of a large-scale industrial process, the demonstrated process concept shows how gas-expanded liquids can be generally exploited in homogeneous catalysis to enhance productivity.     

无卤阻燃EVA复合材料研究进展

分别介绍了采用无机阻燃剂、氮系阻燃剂、膨胀型阻燃剂和辐射交联技术制备的无卤阻燃乙烯-乙酸乙烯共聚物(EVA)复合材料的研究开发现状,并展望了无卤阻燃EVA复合材料的发展趋势。     

乙烷-氧-水氧化裂解制乙烯反应的研究

研究了不同反应体系组成的乙烷造反然的反应性能,考究了乙烷－氧－水反应体系氧化裂解制乙烯的反应条件。结果表明,在不同反应体系中,以Ｃ２Ｈ６－Ｏ２－Ｈ２Ｏ氧化裂解制乙烯反应性能最佳,８００℃的乙烷转化率为８５．１％,乙烯选择性为６８．１％,乙烯收率可达５８％,Ｃ２Ｈ６－Ｏ２－Ｈ２Ｏ氧化裂解帛乙烯体系最佳工艺参数;反应温度为８５０℃,原料气组成为５０．５％,Ｃ２Ｈ６＋２５．２％Ｏ２＋２４．３％Ｈ２Ｏ停留     

热成像技术在乙烯裂解炉热故障诊断中的应用

概述了红外热成像技术应用于石化设备检测的基本原理和方法,着重阐明了在乙烯装置裂解炉热故障识别与诊断方面的应用,分析了故障成因。     

乙撑胺的市场分析及生产工艺技术比较

对乙撑胺系列产品的国内外市场进行了分析,并对不同生产工艺技术进行了比较。认为应引进国外先进生产技术,优化产品结构,开拓新的应用领域