大功率CO_2激光器非平衡态合成WO_3／Fe_2O_3新型陶瓷催化剂──Ⅱ．WO_3／Fe_2O_3烯烃歧化反应催化剂的催化活性

用大功率ＣＯ２激光器熔制ＷＯ３／Ｆｅ２Ｏ３新型烯烃歧化反应催化剂。考查了催化剂组成、激光功率及熔炼时间与丙烯歧化反应催化活性之间的关系。     

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。     

哈尔滨炼油厂MTBE装置试生产

介绍了哈尔滨炼油厂ＭＴＢＥ装置的工艺路线、新技术的应用及特点；催化剂的装填及应用情况；总结了生产过程中遇到的一系列问题及解决办法；探索了平稳生产的新徐径，以保证装置安全、平稳、长周期运行；同时对反应器操作温度、催化蒸馏塔操作压力、原料中醇烯比等因素对异丁烯转化率及ＭＴＢＥ产品的影响做了简单的总结。     

我国车用汽油的发展概况及发展方向探讨

介绍了我国车用汽油的发展轨迹 ,通过与国外先进标准的对比分析了我国车用汽油存在的不足 .指出我国在加入WTO后 ,更应不断升级车用汽油质量标准 ,需要从标准制定、炼油技术等多方面追赶世界先进水平 ,积极研制生产清洁型无污染汽油 ,从根本上消除汽车尾气对环境的污染 .     

Study of direct and indirect naphtha recycling to a resid FCC unit for maximum propylene production

To satisfy the increasing propylene demand, direct and indirect naphtha recycling schemes around an existing resid fluid catalytic cracking (FCC) unit were investigated. To this aim, light cracked naphtha (LCN), heavy cracked naphtha (HCN) and a PolyNaphtha (PN) oligomerisation product were cracked under a wide range of operating conditions over a commercial Y zeolite based equilibrium catalyst. Experimental data were acquired in three different units: a fixed bed bench scale unit, a fixed fluidised bed unit and an adiabatic circulating fluidised bed pilot plant. It was shown that FCC naphthas require high operating severities to crack, and that even then their conversion remains relatively moderate. Hence, direct recycling to the main riser does not seem a viable pathway to increase propylene product. Feeding FCC naphthas to a second reaction zone operating at high severity allows to increase the propylene yield in a significant manner. Increasing conversion, however, not only leads to higher LPG and propylene yields, but also results in very high dry gas yields. An alternative scheme was proposed, in which the olefinic C₄ and C₅ fractions are converted into a naphtha fraction through oligomerisation in a dedicated unit before being recracked in the secondary riser. As the highly olefinic oligomerised effluent mainly consist of dimerised and trimerised butenes and pentenes, this feed is more easily cracked and high conversions can be achieved. This indirect interconversion of butenes and pentenes into propylene therefore effectively allows to convert these butenes and pentenes into propylene, resulting in a significant increase in propylene yield. Each of the three main naphtha recycle options (directly to the main riser, directly to a secondary riser or indirectly via a light olefin oligomerisation unit) have been analysed and compared to a base case. In the evaluation of each of these schemes, all heat balance effects, both on the riser and the regenerator side, have been accounted for. The proposed process scheme with an indirect recycle via an oligomerisation unit enhances the already inherent flexibility of the FCC unit. The naphtha recycle can be turned on or off, the second reaction zone can be used to crack naphtha or to crack resid feed to maximise throughput, while the effluent of the oligomerisation unit can be recycled to the FCC unit for propylene production or hydrogenated and sent to gasoline and kerosene pool.     

Development and Commercial Application of a Novel Catalyst DVR—1 for Catalytic Cracking of Daqing Vacuum Residue

A newly developed catalyst type DVR-1 for catalytic cracking of Daqing vacuum resid was put into use in a commercial VRFCC unit,This catalyst features uniquely active matrix and modified ultra-stable zeolite.The commercial application results show that the DVR-1 type catalyst has the advantage of high heavy oil conversion,good metal tolerance nd gooed stability for catalyst regeneration,The FCC tests have shown Favorable product distribution,acceptable product quality and enormaous economic benefits whe processing the feedstock containin 75%-100% Daqing VR.     

RFCC汽油质量波动因素分析及对策

随着RFCC掺渣比的提高和原料碳含量的增加,原脱臭工艺技术无法满足产品的质量要求。通过分析RFCC脱臭汽油质量波动的原因,提出了从优化原料性质、操作参数和改变工艺方法等方面改进汽油质量,认为Merox抽提塔与固定床无碱脱臭技术相结合可提高硫醇脱除率,提高产品质量,满足汽油产品的质量指标,并具有显著的经济效益。     

催化裂化原位降硫助剂的制备及其性能研究

采用溶胶-凝胶法制备具有介孔结构的降硫基质材料，选择具有降硫选择性的活性元素对合成的基质材料进行改性处理，考察不同的改性方法对制得的催化裂化原位降硫助剂性能的影响，并对基质材料和降硫助剂的结构进行表征。采用美国进口的ACE-R小型催化裂化评价装置将降硫助剂与催化裂化催化剂匹配进行性能评价，在不改变原催化裂化产品分布和产品性质的同时，降低原料的总硫含量，总硫降低可达40％以上。     

催化裂化技术现状及发展趋势

详述了国内外最新渣油催化裂化、多产柴油催化裂化、低碳烯烃催化裂化、生产清洁燃料催化裂化及催化剂的技术进展，同时根据我国实际情况对今后催化裂化技术的发展提出了建议。     

多维气相色谱快速测定汽油中的烯烃、芳烃和苯含量

针对车用无铅汽油国家标准GB17930-1999中对烯烃，芳烃和苯含量提出的明确限值要求，以及现有标准方法和其它分析技术在分析汽油组成时存在的问题，结合国外汽油分析的发展趋势及我国汽油生产的工艺和汽油组成分布特点，提出了一套新的多维气相色谱技术测定汽油中烯烃。芳烃和苯含量的方法。并研制了新的烯烃捕集阱，可捕集汽油中高达70%的烯烃，且具有良好的可逆性和使用寿命，提出的方法可以在12min内通过一次色谱进样实现汽油中烯烃总量，芳烃总量和苯含量的测定。试验结果与荧光指示剂吸附法（FIA，GB/T11132-1989）相比具有很好的一致性。但分析速度和方法的再现性得到明显改善。试验成本也大大降低。