12．5×10^4 m3储油罐底板阴极保护方案比选

对国内外储油罐底板内外侧各种阴极保护方法进行了分析对比。重点介绍了茂名分公司12.5×10~4m~3储油罐底板内外侧阴极保护方案:内侧为涂料加铝合金牺牲阳极阴极保护;外侧为涂料加混合金属氢化物网状阳极阴极保护。     

低压合成甲醇催化剂的工业侧线试验

在0 25m3反应釜中,对QCM-01低压合成甲醇催化剂进行了工业放大试验。试验结果表明,产品性能达到了小试试样的水平。在此基础上进行了1000h的原粒度工业侧线试验,试验结果表明,中试产品的性能达到了国外MK101催化剂的水平。     

中间馏分油型加氢裂化催化剂用沸石的研究

通过水热处理法制备了3个不同脱铝深度的改性Y沸石，再经浸渍法制成中间馏分油型加氢裂化催化剂，在200mL小型加氢裂化装置上进行了催化性能评价。试验结果表明，除了沸石的酸性外，其孔结构和比表面积对催化剂的活性、中间馏分油选择性和液体收率都有很大的影响，为最大幅度提高催化剂的中间馏分油选择性并保持较好活性，要求沸石具有较低的酸量、较高的比表面积和较多的二次孔及适量的L酸量。     

烯烃均相茂金属催化技术的工艺条件

烯烃均相茂金属催化技术的工艺条件潘智达孙俊全杨士林（浙江大学高分子科学与工程系，杭州３１００２７）ＰａｎＺｈｉｄａ，ＳｕｎＪｕｎｑｕａｎａｎｄＹａｎｇＳｈｉｌｉｎ（ＤｅｐａｒｔｍｅｎｔｏｆＰｏｌｙｍｅｒＳｃｉｅｎｃｅａｎｄＥｎｇｉｎｅｅｒｉｎｇ，Ｚｈ...     

茂金属催化剂气相法聚乙烯中试研究

我国自行开发的茂金属催化剂在气相法聚乙烯中试装置上进行了运行试验和性能试验。考察了茂金属催化剂ＡＰＥ－１的运行稳定性和适应性以及聚合反应条件与催化剂活性、产品熔融流动性能和产品密度的关联性。经过测定，试验所得产品的相对分子质量分布特性与国外同类产品相近。     

Kelogg合成氨工艺进展

综述了以先进合成氨工艺和转化换热系统技术为代表的Ｋｅｌｏｇｇ第二代合成氨工艺。较详细介绍了钌基催化剂和转化换热器     

Effect of phase transfer catalysts on the interfacial tension of water/toluene system

The effect on the interfacial tension of the water toluene system has been studied at 25 °C in the presence of four phase-transfer catalysts i.e. tricaprylmethyl ammonium chloride, hexadecyltrimethyl ammonium chloride, hex-adecytrimethyl ammonium bromide and hexadecyltributyl phosphonium bromide. The interfacial tension of aqueous phenol/resorcinol-toluene in the presence and absence of tricaprylmethyl ammonium chloride has also been reported. Attempt has been made to elucidate the change in volumetric rate of extraction with different catalysts for two phase reactions, on the basis of interfacial tension.     

连续重整装置仿真系统的设计开发

为提高操作人员对连续重整装置开停工及事故处理的熟练程度，并对生产进行指导，采用半机理模型结合设计和现场数据介发的连续重整装置仿真系统已在现场成功投用。介绍了该仿真系统的软硬件结构、动态模型及仿真功能。     

Probing the early stages of polymerization of ethylene on a model chromium/silica catalyst by Fourier transform infrared spectroscopy

The nature of the interaction of monomer, and the early stages of growth of oligomers of ethylene on a rather more uniform surface of Cr/SiO₂ catalyst than hitherto studied has been investigated by differenceFTIR spectroscopy using C₂D₄ and C₂H₄ as reactants both with and without subsequent treatment of the catalyst with CO andTHF. The active catalyst was prepared by reaction of vapour phase CrO₂Cl₂ with the vicinal hydroxyls of the silica surface. Three distinct kinds of methylene groups were detected. Arguments are given for assigning the peaks at 2935 and 2860 cm^–1 to CH₂ groups directly bound to the active site and those at 2920 and 2850 to CH₂s in the growing chain well removed from the Cr. The peaks at 2160 and 2165 cm^–1 are attributed to CD₂ groups hydrogen bonded to surface hydroxyls.     

吸附精制提高催化裂化柴油的安定性

用卸出的催化裂化平衡催化剂对催化裂化柴油进行吸附精制，取得了很好的效果。精制油收率99％以上，其安定性达到了优级轻柴油的标准（沉渣＜2．0mg／100mL，色号≤16）。精制后柴油的胶质下降约1个百分点，对吸附物的组成分析表明，其氮含量是柴油的17倍以上。对精制油的分析表明，吸附精制可明显降低柴油的酸度和碱性氮化物的含量。