燕化200kt/a气相法聚丙烯装置技术改造设计

从设计角度对燕化200kt/a气相法聚丙烯装置的技术改造进行了详细分析和说明。装置改造获得了最大的经济效益，为国内同类装置进行技术改造提供了经验。     

偶联剂对地砖用PVC填充材料相态结构和力学性能的影响

研究了钛酸酯类偶联剂和硅烷类偶联剂对钙矿、硅酸盐填充的PVC填允材料力学性能、相态结构、密度、热失重率及吸水伸长率和耐热阻燃性能的影响。结果表明,偶联剂可改善填充PVC的抗冲性能,降低其拉伸强度,扫描电镜分析表明,填料越细,分散越均匀,越易被PVC树脂所包覆,力学性能越好,研究得到了比重大、热失重率低、吸水伸长率小、阻燃耐烧灼性好的高填充PVC硬质塑料地板砖。     

裂解炉横跨管的设计

裂解炉横跨管的设计对辐射段炉管的变形有较大的影响，通过对己建成投产的裂解炉横跨管的设计及使用情况进行总结，以及对横跨管设计的几个方案进行比较，对横跨管设计提出了比较合理的方案，此方案已在中原，天津等裂解炉的设计中采用，并取得良好效果。     

不同混合材掺量对低碱水泥适应性的试验研究

对不同种类及掺量的混合材对低碱水泥流动洼能进行试验研究，结果为：低碱硅酸盐水泥中掺入矿渣粉、粉煤灰、石灰石等混合材有利于改善浆体流动性能，目双掺效果较单掺好；外加剂掺入量对流动性能的改善随着掺量的增加而增加，但掺入量应适宜、经济；石灰石为非活洼混合材，本试验研究结果表明它能显著增大水泥流动性且保持较小的经时损失，但其掺量不宜过大。     

过氧化二碳酸双（2-乙基）己酯的合成研究

以氯甲酸(2-乙基)己酯为原料制备过氧化二碳酸双(2-乙基)己酯(EHP)，研究了加料方式、反应温度、反应时间、投料比等因素对产品的影响。结果表明：氯甲酸(2-乙基)己酯与过氧化钠的摩尔比为1：0．58～0．62，反应温度为15℃～20℃，反应时间为3～4小时，以异十二烷为溶剂，可以得到高效、无毒的EHP溶液。     

数码辅助方法在毛细管流变仪测量粘度的应用

讨论了传统流变仪测量粘度上存在的问题，提出了改进的方案测量粘度，以减少误差。试验方案主要体现在用数码方法采集数据。     

燕化660 kt/a乙烯冷区设备布置

主要介绍了大型乙烯改扩建的冷区设备布置的主要特点，分析了设备布置的思路，及与土建等各专业的关系，强调了设备布置方案利旧的方法。     

Measurement and Correlation for Solubility of (S)-(+)-2,2-Dimethyl-cyclopropane Carbox Amide in Different Solvents

1 INTRODUCTION (S)-(+)-2,2-dimethylcyclopropane carbox amide [(+)-DMCPCA, Fig.1] is a key intermediate of Cilas- tatin, an inhibitor of dehydropeptidase-I. As the syner- gist of imipenem (an antibiotic drug), cilastatin is widely used in clinical applications and has prosper- ous prospects[1]. In industrial manufacture[2―6], as the optical intermediate, the chemical and optical purity of (+)-DMCPCA would affect the quality of cilastatin. So, the separation and purification are impo…     

An Investigation of Error Sources in Computational Fluid Dynamics Modelling of a Co-current Spray Dryer

The paper is focused on identifying error sources in computational fluid dynamics(CFD) predictions of a spray drying process. Seven groups of drying and atomisation parameters were selected for analysis and 13 simulation trials were performed. The theoretical results were compared with experimental data and sensitivity of the simulation results to the analysed factors was determined. The following parameters affecting the accuracy of CFD spray modelling were found: gas turbulence model, particle dispersion, atomising air, initial parameters of atomisation and heat losses to the environment. A major difference in the errors committed during modelling of spray drying process for fine and coarse sprays was observed.