共查询到19条相似文献,搜索用时 406 毫秒
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研究开发出了适于FCC汽油加氢改质的选择性加氢脱硫催化剂和辛烷值恢复催化剂,并在300 mL绝热装置上,分别以全馏分FCC汽油或切割后的重馏分FCC汽油为原料,进行了FCC汽油加氢改质工艺的系统研究,结果表明:单独采用辛烷值恢复工艺或辛烷值恢复-选择性加氢脱硫组合工艺不能完全满足FCC汽油加氢改质的要求;而单独采用选择性加氢脱硫工艺或选择性加氢脱硫-辛烷值恢复组合工艺可以满足全馏分FCC汽油或切割后重馏分FCC汽油加氢改质的要求。将全馏分FCC汽油切割后进行加氢改质可以得到硫含量更低的改质产品或直接生产符合国Ⅳ标准的清洁汽油。 相似文献
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加氢脱硫降烯烃技术在FCC汽油加氢脱硫及烯烃饱和的同时,很好地减少汽油辛烷值损失问题。介绍了采用HDDO-01催化剂与HDDO-02催化剂组合工艺,对催化裂化汽油进行加氢处理,w(硫)〈50μg/g,汽油辛烷值损失〈2。 相似文献
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介绍了具有代表性的选择性和结合辛烷值恢复的催化裂化(FCC)汽油精制脱硫加氢工艺。而加氢工艺中的结合辛烷值恢复的加氢工艺更适合我国国情,并提出以辛烷值恢复技术中的异构化和芳构化为主线.研制脱硫能力强和辛烷值保持能力高的脱硫催化剂.适度增强催化剂的酸位疏通孔道,提高其芳构化活性及稳定性。针对反应吸附脱硫工艺,通过寻找硫容量高、吸附性能强的新材料、深度研究脱硫反应机理、简化工艺流程来开展脱硫效果更好、汽油辛烷值维持高的反应吸附脱硫工艺。 相似文献
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Science and technology of novel processes for deep desulfurization of oil refinery streams: a review 总被引:11,自引:0,他引:11
Oil refinery related catalysis, particularly hydrodesulfurization (HDS) processes, is viewed as a mature technology and it is often stated that break-throughs are not to be expected. Although this could be a justified compliment to those who developed this area, at the same time it could also stifle potential new ideas.The applicability and perspectives of various desulfurization technologies are evaluated taking into account the requirements of the produced fuels. The progress achieved during recent years in catalysis-based HDS technologies (synthesis of improved catalysts, advanced reactor design, combination of distillation and HDS) and in ‘non-HDS’ processes of sulfur removal (alkylation, extraction, precipitation, oxidation, and adsorption) is illustrated through a number of examples.The discussed technologies of sulfur removal from the refinery streams lead to a wealth of research topics. Only an integrated approach (catalyst selection, reactor design, process configuration) will lead to novel, efficient desulfurization processes producing fuels with zero sulfur emissions. 相似文献
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Increasingly stringent regulations on the removal of aromatic and sulfur compounds in diesel fuel require the development of new catalysts and processes. Here, control of hydrodesulfurization (HDS) and hydrodearomatization (HDA) properties was studied by preparing bimetallic Pd-Pt catalysts supported on ytterbium-modified ultrastable Y (USY) zeolite by impregnation and subsequent calcination under different temperatures. Catalytic performances of the prepared catalysts, such as HDS of 4,6-dimethyldibenzothiophene (4,6-DMDBT) and HDA of tetralin, were investigated in a high-pressure continuous-flow reactor. With changing calcination temperature, the HDS activity is only slightly affected, although the maximum HDS conversion was obtained at 300°C. In contrast, the HDA activity decreased significantly, with hydrogenation selectivity remaining relatively constant as confirmed by the weak variation of the trans-decalin to cis-decalin ratio. A low calcination temperature of 200°C simultaneously favored both deep HDS and deep HDA, whereas a high calcination temperature of 500°C favored selective HDS reactions with minimal HDA reactions (i.e. saving of expensive hydrogen). These results clearly indicate that the selectivity of HDS to HDA can be controlled by simply changing the calcination temperature of Pd-Pt/Yb/USY zeolite catalysts. 相似文献
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Colin E. Snape William R. Ladner Leonidas Petrakis Bruce C. Gates 《Fuel Processing Technology》1984,8(2):155-168
Average chemical structures of asphaltenes from three coal liquefaction processes, namely hydroliquefaction (SRC-II), hydrogen-donor solvent extraction (HDS) and supercritical gas extraction (SCG), have been deduced using a structural analysis scheme in which data from 1H and 13C NMR are combined with those from elemental, molecular weight and functional group analyses. Compared with SRC-II and HDS asphaltenes, SCG asphaltenes contain less-condensed aromatic nuclei which can be largely represented by 1- and 2-ring structures. They also contain more oxygen groups and slightly larger aliphatic substituents. CH3 accounts for between 30 and 40% of the aliphatic carbon in all the asphaltenes investigated. Small amounts of long alkyl chains are present in the SCG asphaltenes but not in the SRC-II and HDS asphaltenes. SCG extraction is chemically less severe than the SRC process and HDS extraction since neither hydrogen nor HDS are employed and, as a result, SCG extracts are considered to be much more representative of the organic matter in the parent coals. 相似文献
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炼油厂产品深度脱硫工艺的研究进展 总被引:4,自引:2,他引:2
综述了国内外开发和应用的脱硫技术,通过一系列实例阐述了近年来催化加氢脱硫及非加氢脱硫的工艺进展。该技术主要有催化加氢脱硫(改进催化剂的合成、先进的反应器设计、蒸馏与加氢脱硫组合等)及非加氢脱硫技术(烷基化脱硫、溶剂萃取脱硫、沉淀脱硫、吸附脱硫、氧化脱硫和膜分离脱硫等);评述了催化加氢脱硫、烷基化脱硫、吸附脱硫和氧化脱硫等脱硫技术的特点和研究应用前景。 相似文献
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焦炉气加氢催化剂及净化工艺的开发 总被引:1,自引:0,他引:1
介绍了适合于焦炉气加氢催化剂及净化工艺的研究实验结果,实验表明,JT-1及JT-8型加氢催化剂均可适用于含高浓度CO和CO2气氛下原料气的加氢净化,且净化度高,副反应小,并满足以焦炉气为原料的甲醇厂的原料净化要求,可将原料气中硫化物脱除至总硫体积分数<0.1×10-6。 相似文献
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《Applied Catalysis A: General》2005,278(2):143-172
The possible origins of sulfur impurities in FCC gasoline are reviewed and discussed. Their mechanism of formation during the FCC process as well as their mechanism of transformation on hydrotreating catalysts are also examined.The article focuses on the desulfurization of FCC gasoline by means of catalytic processes considering the fact that deep desulfurization must be achieved (in accordance with new regulations) while preserving octane rating of the fraction. The various parameters (presence of a promoter, nature and modification of the support, additives and poisons) which may influence the selectivity in hydrodesulfurization (HDS) versus olefin hydrogenation are also discussed. Existing and potential processes for the HDS of FCC gasoline with octane preservation are described. 相似文献
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Biomimetic sequestration of carbon dioxide (CO2) is one of the methods proposed to reduce the CO2 released into the atmosphere. In this study, we compared soluble protein of hemocyte from diseased shell (HDS) and extrapallial fluid (EPF) extracted from Crassostrea gigas with bovine carbonic anhydrase II in terms of their ability to promote CO2 hydration and the production of calcium precipitates. On the basis of the experiments of CO2 hydration, the key role of HDS was identified. Moreover, mass‐spectroscopic analysis (MALDI‐TOF) and circular dichroism (CD) analysis were used for understanding molecular weight and secondary protein structure. From the amino acid sequence and secondary protein structure, the different processes of CO2 hydration by bovine carbonic anhydrase II and HDS could be assessed. 相似文献
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Whasik Min 《Korean Journal of Chemical Engineering》2002,19(4):601-606
SK Corporation has developed a new process, SK HDS Pretreatment process that enables the refiners to produce economically
ultra-low-sulfur-diesel of below 10 ppm. This technology is based on the adsorptive removal of nitrogen containing compounds
(NCC) from the feedstock to conventional hydrodesulfurization (HDS) units. The NCC is known to interfere with the activity
of HDS catalysts. In the SK HDS Pretreatment Process, the feedstock to the HDS unit is pretreated, and 90% or more of NCC
in the feedstock is removed, resulting in higher desulfurization in a conventional HDS unit. It was found that the degree
of improvement in HDS is proportional to the degree of NCC removal. SK HDS Pretreatment Process is a cost-effective method
for refineries to choose for 10 ppm ULSD production.
This paper is dedicated to Professor Wha Young Lee on the occasion of his retirement from Seoul National University. 相似文献