Controllable Condensation of Aromatics and Its Mechanisms in Carbonization

In order to obtain liquefied products with higher yields of aromatic molecules to produce mesophase pitch,a good understanding of the relevant reaction mechanisms is required.Reactive molecular dynamics simulations were used to study the thermal reactions of pyrene,1-methylpyrene,7,8,9,10-tetrahydrobenzopyrene,and mixtures of pyrene with 1-octene,cyclohexene,or styrene.The reactant conversion rates,reaction rates,and product distributions were calculated and compared,and the mechanisms were analyzed and discussed.The results demonstrated that methyl and naphthenic structures in aromatics might improve the conversion rates of reactants in hydrogen transfer processes,but their steric hindrances prohibited the generation of high polymers.The naphthenic structures could generate more free radicals and presented a more obvious inhibition effect on the condensation of polymers compared with the methyl side chains.It was discovered that when different olefins were mixed with pyrene,1-octene primarily underwent pyrolysis reactions,whereas cyclohexene mainly underwent hydrogen transfer reactions with pyrene and styrene,mostly producing superconjugated biradicals through condensation reactions with pyrene.In the mixture systems,the olefins scattered aromatic molecules,hindering the formation of pyrene trimers and higher polymers.According to the reactive molecular dynamics simulations,styrene may enhance the yield of dimer and enable the controlled polycondensation of pyrene.

Highly selective extraction of aromatics from aliphatics by using metal chloride-based ionic liquids

The separation of aromatics from aliphatics is essential for achieving maximum exploitation of oil resources in the petrochemical industry.In this study,a series of metal chloride-based ionic liquids were prepared and their performances in the separation of 1,2,3,4-tetrahydronaphthalene(tetralin)/dodecane and tetralin/decalin systems were studied.Among these ionic liquids,1-ethyl-3-methylimidazolium tetrachloroferrate([EMIM][FeCl_(4)])with the highest selectivity was used as the extractant.Density functional theory calculations showed that[EMIM][FeCl_(4)]interacted more strongly with tetralin than with dodecane and decalin.Energy decomposition analysis of[EMIM][FeCl_(4)]-tetralin indicated that electrostatics and dispersion played essential roles,and induction cannot be neglected.The van der Waals forces was a main effect in[EMIM][FeCl_(4)]-tetralin by independent gradient model analysis.The tetralin distribution coefficient and selectivity were 0.8 and 110,respectively,with 10%(mol)tetralin in the initial tetralin/dodecane system,and 0.67 and 19.5,respectively,with 10%(mol)tetralin in the initial tetralin/decalin system.The selectivity increased with decreasing alkyl chain length of the extractant.The influence of the extraction temperature,extractant dosage,and initial concentrations of the system components on the separation performance were studied.Recycling experiments showed that the regenerated[EMIM][FeCl_(4)]could be used repeatedly.

Morphology,Nanostructure,and Oxidation Reactivity of Particulate Matter Emitted by Diesel Blending with Various Aromatics

This study aims to analyze the influence of the polycyclic aromatic hydrocarbon(PAH)content in diesel on the physical and chemical properties of diesel soot particles.Four diesel fuels with different PAH content were tested on a 11.6 L direct-injection diesel engine.The raw particulate matter(PM)before the after-treatment devices was collected using the thermophoresis sampling system and the filter sampling system.A transmission electron microscope and Raman spectrometer are used to analyze the physical properties of the soot particles,including morphology,primary particle size distribution,and graphitization degree.A Fourier transform infrared spectrometer and thermogravimetric analyzer are used to characterize the surface chemical composition and oxidation reactivity of soot particles,respectively.The results show that as the PAH content in the fuel decreases,the size of the primary soot particles decreases from 29.58 to 26.70 nm.The graphitization degree of soot particles first increases and then decreases,and the relative content of the aliphatic hydrocarbon functional groups of soot particles first decreases and then increases.The T_(10),T_(50),and T_(90) of soot from high-PAH fuel are 505.3,589.3,and 623.5℃,while those from low-PAH fuel are 480.1,557.5,and 599.2℃,respectively.This indicates that exhaust PM generated by the low-PAH fuel has poor oxidation reactivity.However,as the PAH content in fuel is further decreased,the excessively high cetane number may cause uneven mixing and incomplete combustion,leading to enhanced oxidation reactivity.

Selective Hydrogenation of Polycyclic Aromatics to Monocyclic Aromatics over NiMoC/HβCatalysts in a Methane and Hydrogen Environment

To obtain high yields of monocyclic aromatic hydrocarbons with methyl side chains,such as toluene and xylene,methane(CH_(4))can be introduced into the hydrocracking of polycyclic aromatic hydrocarbons.CH_(4)can participate in the reaction,supply methyl side chains to the product,and improve product distribution.In this study,the hydrogenation reaction of polycyclic aromatic hydrocarbons over a carbonized NiMo/Hβcatalyst in a CH_(4)and hydrogen(H_(2))environment was investigated to study the promotional effect of CH_(4)on the hydrocracking of polycyclic aromatics.Under conditions of 3.5 MPa,380℃,volume air velocity of 4 h^(-1),gas-oil volume ratio of 800,and H_(2):CH_(4)molar ratio of 1:1,the conversion rate of naphthalene was 99.97%,the liquid phase yield was 93.62%,and the selectivity of BTX were 17.76%,25.17%,and 20.47%,respectively.In comparison to the use of a H_(2)atmosphere,the selectivity of benzene was significantly decreased,whereas the selectivity of toluene and xylene were increased.It was shown that CH_(4)can participate in the hydrocracking of naphthalene and improve the selectivity of toluene and xylene in the liquid product.The carbonized NiMo/Hβcatalyst was characterized by a range of analytical methods(such as X-ray diffraction(XRD),ammonia-temperature-programmed desorption(NH3-TPD),hydrogen-temperature-programmed reduction(H_(2)-TPR),and X-ray photoelectron spectroscopy(XPS)).The results indicated that Ni and Mo carbides were the major species in the carbonized NiMo/Hβcatalyst and were considered to be active sites for the activation of CH_(4)and H_(2).After loading the metal components,the catalyst displayed prominent weak acidic sites,which may be suitable locations for cracking,alkylation,and other related reactions.Therefore,the carbonized NiMo/Hβcatalyst displayed multiple functions during the hydrocracking of polycyclic aromatic hydrocarbons in a CH_(4)and H_(2)environment.These results could be used to develop a new way to efficiently utilize polycyclic aromatic hydrocarbons and natural gas resources.

CO_(2)utilization in syngas conversion to dimethyl ether and aromatics:Roles and challenges of zeolites-based catalysts

Several studies have proven a strong correlation between global warming and CO_(2)emissions.Annually,38 billion tons of CO_(2)are approximately emitted into the atmosphere.Utilizing CO_(2)via chemical conversion to clean fuels and value-added aromatics can substantially contribute to controlling the problem.Considering the thermodynamic and environmental limitations of hydrogenation of CO_(2)alone to value-added aromatics and fuels,CO_(2)utilization has currently emerged as a promising and practical approach for the production of fuels and aromatics with simultaneous utilization of both CO and CO_(2)wastes.As such,the approach is economically preferable.CO_(2)could be converted directly to fuels by the hydrogenation process or as a part of a syngas mixture.Dimethyl ether(DME)is a clean fuel with a higher energy density,which could be used as a substituent for several fuels such as diesel.In the same vein,value-added aromatics such as benzene,toluene,and xylene(BTX)can be produced from a similar process.Herein,we report a review that collects the most recent studies for the conversion of CO_(2)to DME and aromatics via zeolite-based bifunctional catalysts.We highlighted the main routes for producing DME and aromatics,as well as thoroughly discussed the conducted studies on CO_(2)hydrogenation and CO_(2)-rich syngas utilized as feedstock for conversion to DME and aromatics.The CO_(2)hydrogenation mostly occurs through the methanol-mediated reaction route but is most often limited by low selectivity and catalyst deactivation,particularly in the utilization of CO_(2)alone for the reduction reaction.The review takes an overview of the progress made so far and concluded by identifying the roles and challenges of zeolite-based catalysts for CO_(2)utilization and conversion to DME and aromatics.Accordingly,despite the incredible growth the field received in the last couple of years,however,many research challenges and opportunities associated with this process are still abounded and required to be addressed.Special attention is required for the development of approaches to block diffusion of H2O through zeolite to suppress the excess formation of CO_(2)in CO_(2)-rich syngas hydrogenation to DME and aromatics,exceed the product distribution limits,and suppress catalysts deactivation.

Fabrication of a sinter-resistant Fe-MFI zeolite dragonfruit-like catalyst for syngas to aromatics conversion

Direct conversion of syngas to aromatics has great potential to decrease fossil fuel dependence.Here,a unique structured hybrid catalyst composed of Fe_(3)O_(4) nanoparticles intimately dispersed inside an acidic zeolite is developed.1 to 4 nm sized Fe_(3)O_(4) nanoparticles end up evenly dispersed in an acidic and slightly mesoporous Al-ZSM-5 based on Fe_(3)O_(4) restructuring during co-hydro thermal synthesis using organosilane modification.A very high aromatic productivity of 214 mmolaromatics h^(-1) gFe^(-1) can be obtained with a remarkable 62%aromatic selectivity in hydrocarbons.This catalyst has excellent sintering resistance ability and maintains stable aromatics production over 570 h.The synthetic insights that postulate a mechanism for the metastable oxide-zeolite reorganization during hydrothermal synthesis could serve as a generic route to sinter-resistant oxide-zeolite composite materials with uniform,well-dispersed oxide nanoparticles in close intimacy with-and partially confined in-a zeolite matrix.

Molecular Characterization of C_(9+)Aromatics in Gasoline by Gas Chromatography-Mass Spectrometry

The comprehensive characterization of heavy aromatic hydrocarbons in gasoline is important to optimize the blending process and understand the correlation between aromatics content and engine particulate emissions.However,most current analysis methods can only provide the composition of C_(8)/C_(8-) aromatics.In this study,a simple and fast gas chromatography-mass spectrometry(GC-MS)method to identify and quantify C_(9+)aromatics in gasoline was developed.A selected ion monitoring model was employed to eliminate interference from non-aromatic compounds in the detection of target compounds,as well as that between target compounds with different molecular formulas.The identification of C_(9+)aromatics was based on the retention time of model compounds,combined with characteristic mass fragment ions,boiling points,and retention indexes.Seventy-nine C_(9)–C_(12)aromatic compounds were quantified based on the calibration of representative model compounds,and the method demonstrated good linearity,and high accuracy and precision.Furthermore,the developed methodology was successfully applied to the analysis of gasoline fractions from the reforming,pyrolysis,straight-run,delayed coking,and catalytic cracking processes,as well as commercial gasolines.The results showed that C_(9)aromatics were the predominant aromatics in all gasoline samples,followed by C10 aromatics.Alkylbenzenes such as C_(9)H_(12)and C_(10)H_(14)were the main components in the reforming,straight-run,delayed coking,and catalytic cracking gasoline fractions,as well as in the commercial gasolines,in which 1,2,4-trimethylbenzene and 3-ethyltoluene were dominant;in contrast,aromatics with higher degrees of unsaturation such as indene were the most abundant aromatics in the pyrolysis gasoline fraction.

Carbon isotopic compositions of mono-, di-, tri-aromatics provide insights into the source of sulfur-rich crude oils in the Huanghekou Depression, Bohai Bay Basin

The stable carbon isotope compositions (δ13C) of individual aromatic hydrocarbons have been analyzed in sulfur-rich and sulfur-lean crude oils from the Huanghekou Depression, Bohai Bay Basin. The δ13C values of individual aromatic hydrocarbons, including alkylbenzenes, alkylnaphthalenes, alkylphenanthrenes, alkylfluorenes and alkyldibenzothiophenes, are reported. The main aims are to find out the origin of these oils and their relationship to paleoclimate. The distribution of aromatic hydrocarbons and maturity parameters show the oils all stay in the low-mature to mature stage. Meanwhile, aromatic hydrocarbons are mainly derived from the diagenetic/catagenetic origin. The δ13C values for 1,2,4-trimethylbenzene (−30.7‰ to −28.8‰) and 1,2,3,4-tetramethylbenzene (−32.4‰ to −26.3‰) indicate the algae-derived organic matter for alkylbenzenes. Some isomers, such as 1,7-+1,3-+1,6-dimethylnaphthalene, 1,2,5-trimethylnaphthalene, 1,2,5,6-+1,2,3,5-tetramethylnaphthalene, 1,10-+1,3-+3,10-+3,9-dimethylphenanthrenes, 1,6-+2,9-+2,5-dimethylphenanthrenes and 4,9-+4,10-+1,9- dimethylphenanthrenes show isotopic depletion (−34.9‰ to −25.2‰), indicating the major contribution of algae for these compounds. Meanwhile, isotopically depleted (−33.6‰ to −26.7‰) alkyldibenzothiophenes represent the algae input. δ13C values for mainly algae-derived naphthalene to trimethylnaphthalenes of sulfur-rich oils are more enriched than those of sulfur-lean oil, with the most significant difference of 4.4‰, indicating that the aridity of the environment and stratified water column result in the enrichment in 13C.

Insights into the size effect of ZnCr_(2)O_(4)spinel oxide in composite catalysts for conversion of syngas to aromatics

Direct conversion of syngas to aromatics(STA)over oxide-zeolite composite catalysts is promising as an alternative method for aromatics production.However,the structural effect of the oxide component in composite catalysts is still ambiguous.Herein,we investigate the size effect by selecting ZnCr_(2)O_(4)spinel,as a probe oxide,mixing with H-ZSM-5 zeolite as a composite catalyst for STA reaction.The CO conversion,aromatics selectivity and space-time yield(STY)of aromatics are all significantly improved with the crystal size of ZnCr_(2)O_(4)oxide decreases,which can mainly attribute to the higher oxygen vacancy concentration and thus the rapid generation of more C1oxygenated intermediate species.Based on the understanding of the size-performance relationship,ZnCr_(2)O_(4)-400 with a smaller size mixing with H-ZSM-5 can achieve32.6%CO conversion with 76%aromatics selectivity.The STY of aromatics reaches as high as 4.79 mmol g_(cat)^(-1)h^(-1),which outperforms the previously reported some typical catalysts.This study elucidates the importance of regulating the size of oxide to design more efficient oxidezeolite composite catalysts for conversion of syngas to value-added chemicals.

食品中多环芳烃的来源、污染状况与检测分析

多环芳烃(polycyclic aromatic hydrocarbons,PAHs)是一类持久性的有机污染物,具有致癌、致畸、致突变等毒性,广泛存在于食品、特别是烟熏食品中,过量摄入将严重危害人体健康。许多国家通过制定严格的限量标准、加强检验检测等措施对食品中的PAHs进行防控,但随着工业化的快速发展,煤、石油等燃料的大量使用,食品中PAHs污染的问题依然突出,其在食品中仍普遍被检出,已成为影响食品安全的主要风险来源之一,关于食品中PAHs的污染来源、监测分析和检测技术等方面的研究也日益增多。本文概述了PAHs对农作物的影响,分析了食品中PAHs的主要来源和污染状况,从样品前处理和测定分析两个方面,综述了食品中PAHs的主要检测技术,评述了其优缺点,并提出了今后研究工作的建议,以期为食品中PAHs的监测分析、预防控制和深入研究提供参考。

国内首套ORP除烯烃装置的工艺及应用研究

美国UOP公司新研制的ORP除烯烃装置首次在中国石油广东石化公司260万t/a芳烃联合装置进行了工业应用。该装置用于脱除重整上游重整生成油中的烯烃,在45~110℃工作温度､2.1 MPa操作压力､5.0质量空速条件下,可满足下游吸附分离单元对进料中溴指数低于20×10^(-6)的进料要求。通过与传统的酸性白土吸附工艺的对比,分析其工艺､操作､参数和配备设施等情况,研究表明,该ORP除烯烃装置具有低生产成本､催化剂可在线再生､大幅降低固废产生､可根据不同生产状况及时进行调整等优点。

环保橡胶填充油的研究与应用进展

概述了橡胶填充油(简称橡胶油)的分类、发展现状及国内外环保橡胶油的生产工艺和研究进展。环保橡胶油主要有处理芳烃油、重质环烷基油、浅度溶剂抽提油、残余芳烃抽提油以及调合油5大类。以润滑油精制装置副产抽出油、催化裂化油浆、渣油等为原料,环保橡胶油的生产工艺主要有溶剂精制工艺、复合溶剂抽提工艺、加氢精制-溶剂抽提复合工艺、加氢精制工艺等,这些工艺通过选择性脱除原料中的多环芳烃、保留低环芳烃和烷基芳烃来生产环保橡胶油,国内目前存在产能低、产品芳碳率低等问题,影响了环保橡胶油在国内的大规模应用,也影响环保型橡胶轮胎质量的提高。在原有技术方案上开发新的环保橡胶油生产工艺,探索新的加工路线迫在眉睫。

芳香中药在动物健康养殖中的研究与应用

多年来,动物生产中滥用抗生素等药物给人类健康带来了严重威胁,着眼于提高动物机体健康水平或将成为未来畜禽水产业可持续发展的方向。芳香中药通常指以挥发性物质为主要有效成分具有芳香气味的中药材及其提取物,具有抗菌、抗炎、增强免疫等作用。近年来,很多研究都在探讨芳香中药作为饲用替抗产品的潜力,文章综述了芳香中药的作用机制及其动物生产中的研究进展,并分析了芳香中药与动物健康养殖的关系及芳香中药当前存在的问题,对其发展前景进行了展望。文章旨在总结芳香中药目前的研究状况,为芳香中药在畜禽、水产健康养殖及饲料工业等方面的研究提供参考意见。

不同氮肥处理对香稻和非香稻品种籽粒灌浆和叶片光合特性的影响

在大田条件下,通过对香稻和非香稻品种的籽粒灌浆、叶片光合特性进行研究,明确香稻和非香稻品种产量和品质形成的生理机制。结果表明:在籽粒灌浆期,相对于非香稻品种,香稻品种在不施氮处理下表现为较高的籽粒灌浆速率,在施氮处理下表现为较低的籽粒灌浆速率;对于剑叶光合速率,无论在施氮还是非施氮条件下均表现为香稻品种高于非香稻品种,说明香稻品种更具有高光效特性。对2品种的产量性状分析表明,香稻品种较非香稻品种粒多,穗大;而非香稻品种相对于香稻品种则穗小,穗数多,这说明,香稻品种主要表现为大穗型,而非香稻品种主要表现为多穗型。对2品种的品质性状进行分析,加工品质2品种差异较小,外观品质表现为非香稻品种明显优于香稻品种,食味值2品种相差相对较小,且均表现为不施氮处理的食味值较高。综合以上分析表明,相对于非香稻品种,香稻品种在不施氮处理下主要表现为较高的籽粒灌浆速率,较高的剑叶光合速率,较高的产量及较高的食味品质;在施氮处理下,除光合速率香稻高于非香稻品种外,其他性状稍低于非香稻品种,这说明,在水稻提优栽培中,在确保产量不降低的情况下,不施或适当少施氮肥,有利于增加香稻品种的籽粒灌浆速率和剑叶光合速率,从而提高香稻的品质。

香型优质高产杂交稻新品种野香优669的选育与应用

【目的】选育产量、米质和抗性相协调的香型优质水稻新品种。【方法】利用亲本间的遗传多样性和农艺性状的互补性,以高产、高配合力的父本福恢669与香型、优质、抗病的不育系野香A杂交,结合多生态点抗性鉴定、高温逼熟后品质分析、多年多点品比试验等相结合。【结果】选育出优质、高产、抗病,株叶态协调的杂交稻品种野香优669。2019–2020年参加福建省中稻区域试验,全生育期两年平均139.8 d,比对照II优3301早熟1.1d,产量平均9363 kg·hm^(-2),比对照增产2.24%,未达显著水平。两年稻瘟病抗性鉴定综合评价为抗稻瘟病,稻米品质达部颁一等优质食用稻品种品质标准,2021年通过福建省农作物审定委员会审定(闽审稻20210014)。野香优669聚合了来自双亲的22个有利基因,其中6个为单方携带,16个为双亲均携带。【结论】野香优669产量高、抗性强、品质好、口感佳,在生产上大面积推广应用,是福建省农业主推品种之一。

木质素氧化解聚衍生芳香族化合物的研究进展

木质素作为自然界最丰富的可再生芳香族资源,由于具有复杂的三维网状结构和顽固的抗性,难以高值化利用。全球约有90%的工业木质素被直接用于燃烧发电,造成了极大的资源浪费。木质素氧化解聚转化为芳香族化合物是对其高值化利用的重要手段,本文在介绍木质素结构和种类的基础上,综述了木质素氧化解聚的研究进展,主要从化学催化氧化、电化学氧化、生物催化氧化解聚木质素的方法和氧化解聚产物4个方面进行总结,分析了各种氧化解聚方法的优缺点和适用范围,以及不同氧化解聚方法对木质素衍生产物的选择性影响。

伊立替康药物中间体7-乙基喜树碱合成的课程思政设计

抗癌药物伊立替康中间体7-乙基喜树碱的合成是杂环芳烃的烷基化反应。本案例通过将实验过程与药物合成和“健康中国”相关联,对实验进行了创新性的思政融入设计。师生全员在案例的导入、研讨、实施、反思与考核的全过程进行全方位的课程思政教育,解决了实验课只注重实验内容而忽略思政教育的问题,实现了“三全育人”。在此过程中不仅激发了学生的学习兴趣,有效地进行了科学思维和创新思维的训练,培养了学生的探索精神和创新意识,而且强化了学生提高原子利用率的绿色化学意识、环保意识和可持续发展意识,提升了学生为健康中国贡献力量的责任感和使命感,坚定了学生运用所学专业知识服务国家的决心和信心。

富油煤焦油中多环芳烃加氢饱和反应研究进展

【意义】多环芳烃(polycyclic aromatic hydrocarbons,PAHs)是煤焦油中最主要的成分之一,通过加氢饱和可制取具有高能量密度和高热稳定性的喷气燃料。通过分析PAHs加氢过程特点,指出PAHs自身的共振能和加氢中间产物的空间位阻,以及原料和中间产物在催化剂活性位上的竞争吸附是PAHs加氢饱和的关键难题。【进展】综述了近年来PAHs加氢饱和催化剂的研究进展,分析了影响催化剂性能的本质原因,指出提高催化剂活性金属组分的分散度、减小催化剂金属颗粒尺寸可以使催化剂具有更多的加氢活性位点,活性金属适宜的缺电子状态能促进PAHs分子在活性位点上的吸附活化,抑制竞争吸附带来的不利影响。具有丰富孔道和介孔(6~8 nm)结构的催化剂载体有利于PAHs和加氢中间产物的扩散,降低加氢中间产物的空间位阻对加氢反应的不利影响,同时可提供更多的反应表面,促进深度加氢反应进行。酸性适宜的载体可以与活性组分产生相互作用,促进活性组分形成适宜的缺电子状态。总结了PAHs加氢饱和过程的热力学和动力学特征,PAHs加氢反应为放热可逆反应,平衡常数和平衡转化率随反应温度降低而增大,随反应压力的升高而增大,PAHs的扩散性随反应温度的升高而增强,吸附常数随饱和环数的增加而减小。【展望】最后,从催化剂活性组分和载体的设计及调控、PAHs加氢饱和过程热力学和动力学研究等方面提出了研究建议。对煤焦油中PAHs加氢饱和过程及其催化剂的分析和讨论将为富油煤资源高效开发利用提供有益指导。

晶种法直接水热合成含磷ZSM-5分子筛及其芳构化性能研究

费托合成油品向高辛烷值汽油转化的流化床体系中,水蒸气的存在极易导致ZSM-5分子筛发生不可逆的水热失活,而磷的引入能提高ZSM-5分子筛的水热稳定性。采用晶种法在无胺体系下直接水热合成了含磷ZSM-5分子筛(HS-P-Z5),并与常规浸渍法得到的含磷ZSM-5分子筛(IM-P-Z5)进行了对比。通过XRD、SEM和N2吸/脱附等对水热处理前后的ZSM-5分子筛进行了表征,通过水洗实验考察了磷元素的流失情况,并以1-辛烯为探针分子评价了ZSM-5分子筛的芳构化性能。结果表明,HS-P-Z5比IM-P-Z5具有更高强度的特征衍射峰、更多的微孔结构和酸量。水洗实验和NMR表征结果表明,HS-P-Z5具有更加稳定的磷铝结构,磷物种不易被洗掉,故其具有更好的水热稳定性,在水热处理后能够保留更多分子筛的微孔结构以及强酸位点。HS-P-Z5-ST(ST表示水热处理)具有最高的芳烃选择性,在反应时间730 min时,其芳烃选择性为23.1%,高于IMP-Z5-ST(18.4%)以及Z5-ST(11.2%)。

果糖酸处理HZSM-5己烯芳构化催化剂的结构及性能

为提高HZSM-5己烯芳构化催化剂的BTX(苯、甲苯、二甲苯)选择性和寿命,利用果糖酸对HZSM-5进行处理(F-HZS),并与磷酸和硝酸处理的HZSM-5(P-HZS和N-HZS)进行对比,采用XRD、XRF、N_(2)吸附-脱附、NH_(3)-TPD、Py-FTIR等方法对催化剂结构进行表征,考察了催化剂己烯芳构化的催化性能。实验结果表明,酸处理后催化剂的MFI结构保留完整,且出现了介孔结构。催化剂的孔体积、硅铝比及B酸量和L酸量比值(B/L)增加,但酸量及酸强度下降,F-HZS的B/L最高,BTX选择性和寿命也明显高于P-HZS和N-HZS。在0.2 MPa、405℃,质量空速2 h-1条件下,F-HZS的BTX选择性为61.34%,寿命为60 h。