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Hydrodesulfurization of selective catalytic cracked gasoline

机译:选择性催化裂化汽油的加氢脱硫

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Hydrodesulfurization (HDS) reaction of catalytic cracked gasoline (CCG) on Co-MO/γ-Al_2O_3 was investigated in detail to make clear the important factors for deep HDS of CCG. A CCG containing 229 ppm sulfur and 30.4 vol% olefins was used in this study. Eleven alkylthiophenes and 2 alkylbenzothiophenes, 3 alkylthiacyclopentanes, and 2 disulfides were identified in this CCG by means of GC-AED analyses. In the reaction at 220℃ and 1.6 MPa using a conventional flow reactor of bench pilot scale, these sulfur compounds were hydrodesulfurized, whereas thiols were produced from H_2S and olefins. The reactions of thiophene HDS, isoolefin and n-olefin hydrogenation (HG) were studied to clarify the active sites on the catalyst. First, the effect of H_2S on the reaction was examined. The HG of n-olefin as well as thiophene HDS was inhibited by H_2S, while the HG of isoolefin was promoted. The effects of Co on these three reactions were also examined over the catalysts with different Co/(Co + Mo) ratios. Thiophene HDS was promoted by Co, while isoolefin HG was little affected and n-olefin HG was largely retarded. From these examinations, three types of active sites for thiophene HDS, isoolefin HG and n-olefin HG were proposed. Oligomers of isoolefins were found in the isoolefin hydrotreated product. The possibility of improving the HDS selectivity by carbonaceous deposit was investigated for HDS reactions of CCG and model compounds. The coking pretreatment was carried out on the catalyst and each reaction was examined. HDS selectivity (higher activity for HDS and lower activity for olefin HG) on CCGHDS was improved. Relative deactivation was in the following order, isoolefin HG > thiophene HDS > n-olefin HG. Pyridine modification (i.e. pyridine injection at 150℃ and partial pyridine desorption at 300℃) was investigated on thiophene and olefins reaction. Thiophene HDS was little affected. Olefin HG and thiol production reaction were strongly inhibited. Improvement of HDS selectivity was observed in the reactions of CCG after pyridine modification. Improvement of HDS selectivity by pyridine modification was considered to result from the selective deactivation of the active sites for olefin reactions (hydrogenation and thiol production).
机译:详细研究了催化裂化汽油(CCG)在Co-MO /γ-Al_2O_3上的加氢脱硫(HDS)反应,以明确影响CCG深层HDS的重要因素。在这项研究中使用了含有229 ppm硫和30.4体积%烯烃的CCG。在该CCG中,通过GC-AED分析鉴定出11个烷基噻吩和2个烷基苯并噻吩,3个烷基噻吩环戊烷和2个二硫键。使用台式试验规模的常规流动反应器在220℃和1.6 MPa的反应中,这些硫化合物被加氢脱硫,而硫醇则由H_2S和烯烃生成。研究了噻吩HDS,异烯烃和正烯烃加氢(HG)的反应,以阐明催化剂上的活性位。首先,检查了H_2S对反应的影响。 H_2S抑制了正烯烃和噻吩HDS的HG,同时促进了异烯烃的HG。在具有不同Co /(Co + Mo)比的催化剂上,还研究了Co对这三个反应的影响。 Co促进了噻吩HDS,而异烯烃HG受的影响很小,而正烯烃HG的阻滞作用很大。通过这些检查,提出了噻吩HDS,异烯烃HG和正烯烃HG的三种活性位点。在异烯烃加氢处理的产物中发现了异烯烃的低聚物。对于CCG和模型化合物的HDS反应,研究了通过含碳沉积物改善HDS选择性的可能性。在催化剂上进行焦化预处理,并检查每个反应。在CCGHDS上的HDS选择性(HDS的较高活性和烯烃HG的较低活性)得到改善。相对失活的顺序如下:异烯烃HG>噻吩HDS>正烯烃HG。在噻吩与烯烃的反应中研究了吡啶的修饰(即在150℃下注入吡啶,在300℃下部分吡啶解吸)。噻吩HDS影响不大。强烈抑制烯烃HG和硫醇的生成反应。在吡啶修饰后CCG的反应中观察到HDS选择性的提高。认为通过吡啶修饰改善的HDS选择性是由于烯烃反应(氢化和硫醇生产)的活性位点的选择性失活而导致的。

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