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综述了不同吸附剂脱硫和选择性吸附两方面的机理及研究进展。在燃料油选择性吸附脱硫研究的吸附剂中,使用最多的是金属阳离子改性的Y型分子筛,以Cu、Ni和Ce改性的Y型分子筛最为成熟。其吸附脱硫机理主要包括π-络合吸附和金属S—M键作用。燃料油(以汽油和柴油为主)组成复杂,含大量烯烃、芳烃、烷烃及少量的氮化物、氧化物、水及胶质,影响吸附剂的吸附脱硫效果,而烯烃和芳烃严重影响吸附剂的选择性吸附脱硫性能。各种吸附剂对富含烯烃或芳烃的燃料油中的硫化物选择性和硫容量不同,但都不高。研究吸附剂与燃料中的硫化物的选择性吸附机理,对研发具有高选择性和高吸附容量的吸附剂起推动作用。 相似文献
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综述了吸附脱硫过程中涉及的各种吸附机理,如物理吸附和化学吸附中的π配合吸附、直接M—S键吸附和电荷转移配合吸附,介绍了相应的吸附剂开发进展。对物理吸附和不同化学吸附方法进行了评述。 相似文献
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我国焦化苯粗品中噻吩含量普遍偏高,脱除焦化苯中的噻吩类硫化物,可提高焦化苯的质量,有利于其进一步的深加工利用。目前,焦化苯中噻吩类硫化物脱除技术主要有萃取精馏法、选择吸附法、选择氧化法、催化加氢法、酸洗精制法等;另外,Friedel-Crafts反应脱硫法和氯甲基化脱硫法也可将焦化苯中纯苯与噻吩类硫化物分离。选择吸附法脱硫技术具备硫酸酸洗精制法操作简单和催化加氢法脱硫精度高、以及萃取精馏法可回收噻吩的优点,具有较大的工业化推广应用价值,提高吸附剂吸附容量以及吸附剂的稳定性将是选择吸附法今后研究的重点。近年来,离子液体已用于催化裂化汽油中硫化物的脱除,这对将来采用离子液体脱除焦化苯中噻吩的技术研究具有重要的借鉴意义。 相似文献
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Sheng‐Qiang Wang Li Zhou Wei Su Yan Sun Yaping Zhou 《American Institute of Chemical Engineers》2009,55(7):1872-1881
A method for deep desulfurization of transportation fuels was presented. Reactive conversion of sulfur compounds and the following adsorption occurred inside adsorbents. The condensation reaction with formaldehyde catalyzed by phosphomolybdic acid was shown effective for the removal of thiophenic and benzothiophenic compounds. Thiophene or benzothiophene of model fuels was completely removed. Coupling with an oxidation reaction, the total sulfur content of commercial fuels was dropped to below 15 ppm. Appropriate desulfur condition was at 70–80°C and ambient pressure without consumption of hydrogen. Saturated adsorbent was regenerated with heating in air at 400°C, and the sulfur capacity was almost fully recovered. Fuel quality was not negatively affected by the desulfur operation. © 2009 American Institute of Chemical Engineers AIChE J, 2009 相似文献
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采用液相离子交换法制备一系列AgY和AgMgY吸附剂。以噻吩的正辛烷溶液为模型化合物,在小型固定床上考察不同浓度硝酸银和硝酸镁制备的AgY单金属吸附剂和AgMgY双金属吸附剂的吸附脱硫性能。结果表明:当Ag+为0.30 mol/L、Mg2+为0.15 mol/L时,吸附剂的脱硫能力最佳。从穿透曲线可看出:每克AgY、AgMgY吸附剂的最大处理量分别为72、120mL汽油,AgMgY双金属吸附剂的脱硫性能明显好于AgY单金属吸附剂。通过X射线衍射仪(XRD)、X射线荧光光谱仪(XRF)、程序升温还原(TPR)和傅里叶变换红外光谱仪(FT-IR)等对吸附剂进行表征,发现Mg2+的存在(作为一种助剂)提高了吸附剂的L酸含量并使其还原性增强,更有利于吸附。经过再生后的吸附剂,其脱硫能力较新鲜吸附剂相比没有明显的下降。 相似文献
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吸附脱硫技术具有操作条件温和、节能、不改变燃油品质和成本低等特点而备受关注。针对噻吩类难脱除硫化物的深度脱除和转化问题,综述了近年来应用多孔吸附材料选择性吸附超深度脱除燃油中噻吩类硫化物的作用机理及最新研究进展。重点分析了分子筛、金属有机骨架、多孔炭材料、复合材料等不同吸附剂的研究现状,并探讨了各种吸附材料的吸附机理、改性方式和优缺点。本文指出分子筛因优异的热稳定性、高比表面积、均一的孔道结构、低成本和易于工业化等特点,是目前最具优势的吸附剂材料。未来研究应着重阐明吸附机理、提高合成便捷性、脱硫性能以及再生能力,更全面系统的研究将为开发具有理想选择性和再生能力的高效吸附剂奠定基础。 相似文献
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J.M. Campos‐Martin M.C. Capel‐Sanchez P. Perez‐Presas J.L.G. Fierro 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》2010,85(7):879-890
Environmental concerns have introduced a need to remove sulfur‐containing compounds from light oil. As oxidative desulfurization is conducted under very mild reaction conditions, much attention has recently been devoted to this process. In this contribution, the developments in selective removal of organosulfur compounds present in liquid fuels via oxidative desulfurization, including both chemical oxidation and biodesulfurization, are reviewed. At the end of each section, a brief account of the research directions needed in this field is also included. Copyright © 2010 Society of Chemical Industry 相似文献
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Wenshuai ZhuWangli Huang Huaming Li Ming ZhangWei Jiang Guangying ChenChangri Han 《Fuel Processing Technology》2011,92(10):1842-1848
In order to obtain the ultra low-sulfur diesel, deep desulfurization of diesel oil has become a vital subject of environmental catalysis studies. Extraction and catalytic oxidation desulfurization (ECODS) system is one of the most promising desulfurization processes. A series of Keggin-type POM-based ionic liquids hybrid materials [MIMPS]3PW12O40·2H2O (1-(3-sulfonic group) propyl-3-methyl imidazolium phosphotungstate), [Bmim]3PW12O40 (1-butyl 3-methyl imidazolium phosphotungstate), [Bmim]3PMo12O40 (1-butyl 3-methyl imidazolium phosphomolybdate) and [Bmim]4SiW12O40 (1-butyl-3-methyl imidazolium silicotungstate) have been developed in this study, and the reaction has performed using the POM-ILs materials as catalysts, H2O2 as oxidant, and ionic liquid (IL) as solvent. Through experimental evaluations, [MIMPS]3PW12O40·2H2O was found to be the best catalyst, with an S-removal of 100% at 30 °C for 1 h. The main factors affecting the process including temperature, catalyst dosage, and O/S (H2O2/DBT) molar ratio were investigated in detail. Under the optimal conditions, DBT (dibenzothiophene) and 4,6-DMDBT (4,6-dimethyl-dibenzothiophene) could achieve high desulfurization efficiency. Moreover, the reaction system also exhibited high activity in actual diesel oil, which could be reduced from 1113 ppm to 198 ppm. The reaction system could recycle 8-times with a slight decrease in activity. 相似文献