焦化汽油加氢试生产重整原料的技术分析

在0.6Mt/a柴油加氢精制装置上利用焦化汽油为原料进行重整原料油的试生产，改善了焦化汽油的性质，降低了硫，氮和可导致重整催化剂中毒的金属含量及烯烃含量，提高了饱和烃的含量，生产出了合格的重整原料，该技术拓宽了重整原料来源，较好地解决了焦化汽油的出路问题。     

对我国催化重整工艺专利市场的思考

根据我国专利法的原则，在对我国催化重整和芳烃生产专利检索过程和结果进行分析的基础上，阐述了对目前我国催化重整工艺专利市场的几点看法并提出对策。     

催化重整装置的几点设计改进

以一套500kt/a规模的催化重整装置的设计为例进行分析和讨论，提出对今后催化重整装置设计的几点改进建议，包括原料的加氢预处理流程，提纯重整产氢，优化预分馏塔及稳定塔的塔盘层数，选择合适的预加氢进料换热器及甲苯塔、二甲苯塔的加压操作等。     

低压组合床重整工艺工业试验

介绍了国产500kt／a低压组合床催化重整装置首次在中国石化股份有限公司长岭分公司的工业试验情况。近两年的运转及标定结果表明试验是成功的，该技术达到了国外连续重整技术第一代与第二代之间的水平，并且投资小，适于小型固定床重整装置的改造。     

多孔纤维型重整微反应器的等效电阻网络建模

针对应用于重整制氢微反应器的复杂多孔金属纤维载体（PFS）的流速场高效分析难题,建立载体中随机微通道的等效电阻网络分析模型. 基于复杂随机纤维结构的统计网络模型,将纤维载体中三维联通的随机微通道结构及与之相连的进出口腔简化为规则的网络通道结构.借鉴基尔霍夫定律,建立纤维载体的等效电阻网络模型,并确定求解方法. 纤维载体流速场实例分析的结果表明,基于等效电阻网络模型求解的纤维载体流速场与计算流体力学(CFD)方法的结果之间的皮尔森相关系数约为98%,且求解效率约为CFD方法的2.9×10⁴倍. 研究成果为多孔纤维型重整制氢微反应器的设计制造提供了新的支撑方案.     

Stable NiO–CeO2 nanoparticles with improved carbon resistance for methane dry reforming

High surface area mixed oxide 8.7% NiO-CeO₂ nanoparticles (122 m²/g; 6–7 nm) were prepared using a reversed microemulsion method, and were tested for dry methane reforming (DRM). The catalytic activity of these nanoparticles remains stable under the severe conditions of DRM (700 °C), and they show better carbon resistance than conventional NiO-CeO₂ catalysts prepared without control of the size. The activity and selectivity of nanoparticles and reference catalyst are similar, but nanoparticles reduce the accumulation of carbon by 63% during the DRM tests, which is a key feature for this reaction. XPS and H₂-TPR suggest that the improved carbon resistance of the nanoparticles is due to the better interaction and cooperation between NiO and CeO₂ mixed phases. In nanoparticles, the participation of cerium cations in the redox processes taking place during DRM stabilizes cationic species of nickel. On the contrary, the catalyst prepared without control of the size suffers segregation of Ni during DRM reaction, and segregated Ni explains the higher catalytic formation of carbon.     

热轧窄带钢车间改造设计实践

介绍了将串列式、横列式热带生产线改造成半连续、３／４连续式生产线的设计实践。改造后可以连铸坯为原料，实现一火成材，并使卷重增加，产量和成材率提高。     

改善操作延长转化炉炉管寿命

分析转化炉炉管不正常原因及对炉管造成的危害，确定通过改善工艺操作来延长转化炉炉管寿命，实践证明效果明显。     

Sintering of Pt/Al2O3 reforming catalysts: EXAFS study of the behavior of metal particles under oxidizing atmosphere

The effect of an oxidative atmosphere (300 °C) is studied on fresh and sintered unchlorinated naphtha reforming catalysts containing 0.6–1% Pt. The TPR profiles show that only one species is formed using our experimental conditions, regardless of the mean crystallite size of the metal particles. The structural information supplied by EXAFS compared with cuboctahedral particle modeling, implies that such species is a surface platinum oxide, the structure of which is close to that of PtO₂, but largely distorted. This is true whether the catalyst is sintered or not.     

A paraffin-fueled SOFC system design and integration

This paper addresses an integrated design of paraffin-reformer, gas separations and the electricity production with a solid oxide fuel cell (SOFC). The overall design consists of three modules. First module is a system of paraffin reformer. In this module, the paraffin feed stream is to send to a steam-reformer. In the second module, the gas separations method illustrated is the combination of a methane-permeable membrane with a pressure-swing adsorption (PSA). In the third module, the purified hydrogen is fed to the SOFC unit. To be energy efficient, this paraffin-fueled SOFC system is designed with the consideration of heat integration. The intent of this paper is to provide a possible, alternative way of cogeneration systems for refinery and petrochemical plants.