共查询到19条相似文献,搜索用时 109 毫秒
1.
In recent years, the catalytic dehydroaromatization of methane to benzene has been a challenging and intriguing research subject in heterogeneous catalysis and natural gas chemical industry. Since the first report on non-oxidative conversion of methane to benzene on Mo/HZSM-5[1], many attractive studies regarding the development of new catalyst, the catalyst characterization[2~4], the reaction mechanism and the bifunctional role of Mo carbide and HZSM-5 have been reported. However, Mo/HZSM-5 catalyst was thought to have the best catalytic performance for CH4 dehydroaromatization to benzene. Recently, another kind of zeolite, MCM-22, was found to be a promising catalyst support for formation of benzene from methane[5]. Xu et al[6] studied the catalytic performance of MoO3/MCM-49 for this reaction without accounting for coke formation. In this paper, we present MCM-49 as a support, and the catalyst Mo/MCM-49 shows high ratio of benzene to aromatics in selective dehydroaromatization of methane. 相似文献
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Dehydrogenation and aromatization of methane over Mo/HZSM-5 catalyst without adding oxygen were widely studied[1~3]. However, the existing problem of this route is the low yield of aromatics, owing to the high stability of methane. Recently, the introduction of the second metal species was believed to be a promising route to improve non-oxidative transformation of methane over Mo/HZSM-5 catalyst[4-7]. 相似文献
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HuiyingChen YonggangLi WenjieShen YideXu XinheBao 《天然气化学杂志》2004,13(3):160-166
The effect of dimethyl ether (DME) co-feed on the catalytic performance of methane dehydroaxomatization (MDA) over 6Mo/HZSM-5 catalyst was investigated as a function of DME concentration under reaction conditions of T=1023 K, p=101 kPa and SV=1500 ml/(g.h). A high benzene yield wasobtained and the stability of the catalyst was improved by adding 1.5%DME to the CH4 feed. The C6H6 yield was as high as ca. 10% even after reaction for 6 h. The stability of the catalyst was further improved when DME concentration in the co-feed gas was increased to an appropriate value. TGA and TPO results of the used 6Mo/HZSM-5 catalyst showed that the amount of coke on the used catalyst was reduced and the chemical nature of the coke was changed. When 1.5%DME was added to the CH4 feed, the coke formed on the catalyst could be burned off more easily than that when only CH4 was used as reactant. It is supposed that the oxygen in DME may play a role in preventing the coke burnt off at lower temperature from transforming into the coke burnt off at higher temperature, which results in the improvement of the stability of the catalyst. 相似文献
4.
QunDong XiaofeiZhao JianWang M.Ichikawa 《天然气化学杂志》2004,13(1):36-40
The influence of adding Fe,Cr,Co,and Ga into 3%Mo/HZSM-5 catalyst on methane aromatization,and the influence of additives ratio on methane conversion,selectivity to hydrocarbons and coke,as well as distribution of aromatics were investigated.The experimental results showed that the addition of Fe,Cr,Co and Ga promoted the dehydrogenation and dissociation of methane.The results of NH3-TPD indicated that the acidity of HZSM-5 was changed by adding Fe and Co components,consequently the catalytic properties of Mo/HZSM-5 were changed.It was also revealed that strong acid sites were the center of methane aromatization.The results of XRD characterization showed that the crystallinity of Mo on ZSM-5 zeolite was increased after adding Fe,Co additives. 相似文献
5.
Junwei Wang Maoqing Kang Zhixin Zhang Xinkui WangInstitute of Coal Chemistry Chinese Academy of Sciences Taiyuan China Manuscript received December revised March 《天然气化学杂志》2002,(Z1)
Impregnation, mechanical mixing and hydrothermal treatment methods were used to introduce molybdenum species into the HZSM-5 zeolite. The structure and surface acidity of the catalysts were studied by means of XRD, FT-IR, NH3-TPD, TPR and XPS. The effects of Mo content and reaction time on stream on the aromatization of propane were investigated. It was found that the performance of the Mo/HZSM-5 catalyst prepared by the hydrothermal treatment method was much better than that of the other two catalysts. For example, under the reaction conditions of 823 K and 600 h-1, propane conversion and aromatics selectivity over the catalyst prepared by hydrothermal pretreatment could reach 89.17% and 78.56%, respectively. XRD and XPS results showed that the Mo species in the catalysts prepared by hydrothermal treatment were highly dispersed on the surface of the HZSM-5, and larger amounts of them could penetrate into the HZSM-5 channel, as compared with the other two kinds of catalysts. These factors may be responsi 相似文献
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The effect of steam-treatment to HZSM-5 zeolite and Mo/HZSM-5 with a steaming time range of 0.5-1 h on the catalytic performance of methane dehydro-aromatization (MDA) over Mo/HZSM-5 catalyst prepared with impregnation has been studied in detail in combination with the characterization of 1H MAS NMR technique. Both the deactivation rate constant (kd) and the Brnsted acid sites per unit cell were calculated to quantitatively evaluate the stability of Mo/HZSM-5 catalysts treated with steam at 813 K before and after impregnation of molybdenum species, and the corresponding variation of their Brnsted acid sites. The results reveal that a V-shape relationship between kd and the number of B1 acid sites per unit cell is presented on Mo/HZSM-5 catalyst under the tested steam-treatment and reaction conditions. 相似文献
7.
《催化学报》1995,(1)
We have studied the methane activation in non-oxidative condition[1,2],and have shown the possibility of direct methane conversion to aromaticsover Mo/HZSM-5.Ethene is regarded as the initial product of the reaction.We thus pay attention to the selective production of ethene and low hydro-carbons from methane directly.The molecular sieve HSAPO-34(SP) waschosen as catalyst support,which has the framework topology of naturalchabazite,and has been shown to convert methanol selectively to Cl~ C3 hy-drocarbons[3].The framework Of SP contains a three-dimensional channel 相似文献
8.
NorAishahSaidinaAmin Kusmiyati 《天然气化学杂志》2004,13(3):148-159
The dehydroaramatization of methane over W-supported ZSM-5 with varying degrees of Li^ ion-exchanged catalysts was studied with and without oxygen at 1073 K and atmospheric pressure.Catalyst activity and stability were found to be influenced by the catalyst acidity related to BrSnsted acid sites and by the presence of oxygen in the feed. The NH3-TPD and FTIR-pyridine results demonstrated that partially exchanged of H^ ions by Li^ into the W/HZSM-5 catalysts could be used to control the amount of strong acid sites on the catalyst surface. Without oxygen, the 3WHLi-Z (5:1) catalyst that has strong acid sites equal to nearly 74% of the original strong acid sites in the parent HZSM-5 exhibited the highest methane conversion and selectivity towards aromatics. However, the catalyst deactivated in a five hour period. In the presence of oxygen, the catalyst activity and stability could be improved further.The results of this study revealed that a suitable amount of strong Bronsted acid sites as well as oxygen addition in the feed increased the catalyst activity and stability. The 3WHLi-Z(5:1) catalyst exhibited improved performance in the dehydroaromatization of methane. 相似文献
9.
《天然气化学杂志》1992,(4)
The behavior of HZSM-5 was investigated as catalysts for esteri-fication of n-butyl alcohol and glacial acetic acid in liquid phase.The con-version of acetic acid remained higher than 93% in a continuous reaction for60 h under the reaction conditions:weight ratio of HZSM-5 catalyst to reac-tant,0.04;mole ratio of alcohol to acid,1.10;the reaction time for eachbatch,5 h;reaction temperature,135℃ and mole ratio of SiO_2 to Al_2O_3 inthe catalyst,50. 相似文献
10.
Study on Bifunctionality of Mo/HZSM-5 Catalysts for Methane Dehydro-Aromatization under Non-oxidative Condition 下载免费PDF全文
Lingling Su Yide Xu Xinhe BaoState Key Laboratory of Catalysis Dalian Institute of Chemical Physics Chinese Academy of Sciences Zhongshan Road P. O. Box Dalian ChinaManuscript received June revised July 《天然气化学杂志》2002,(Z1)
The optimum Mo/[H~+] ratio per unit cell of the active precursors in Mo/HZSM-5 catalysts for methane dehydro-aromatization, measured by 1H MAS NMR, was found to be about 1 when adjusting the acid sites by altering either the SiO2/Al2O3 ratios or the Mo loading. This implies that a concerted interaction between the Mo species and the Bronsted acid sites probably features the bifunctionality of the Mo/HZSM-5 catalyst. On the other hand, it was found that the driving force for Mo species to move into the HSZM-5 zeolite channels and the interaction between the Mo species and the Bronsted acid sites are closely and proportionably related with the amount of Bronsted acid sites per unit cell. 相似文献
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甲烷脱氢芳构化Mo/HZSM-5基催化剂表征 总被引:1,自引:0,他引:1
利用H2-TPR、XPS、EPR等谱学方法,对Mo/HZSM-5基催化剂的可还原性以及工作态催化剂上钼物种的价态进行了表征研究.结果表明,随着焙烧温度的升高,前驱态催化剂中可还原钢物种在总钼量中所占比率明显下降;工作态催化剂表面存在混合价态的Mo物种:以Mo4 为主,Mo5 为次;673K焙烧制备并经DHAM反应操作的催化剂上检测到Mo5 的EPR讯号相当弱,而973K焙烧制备并经同样反应操作的催化剂,其Mo5 EPR讯号却强得多;酸促进的Mo/HZSM-5基催化剂上高的甲烷转化活性与工作态催化剂表面Mo5 物种的浓度并不存在顺变关系,而与表面酸位(尤其是B酸位)及Mo4 物种的浓度密切相关. 相似文献
14.
YipingZhang DongjieWang JinhuaFei XiaomingZheng 《天然气化学杂志》2003,12(2):145-149
Mo/HZSM-5 is a good catalyst for methane aromatization, and the reaction performance of Mo/HZSM-5 and Cu modified Mo/HZSM-5 catalysts under various pretreatment conditions has been studied. The results indicate that the catalyst presented a distinguished catalytic activity, benzene selectivity and a high stability when the bed temperature was raised in N2 atmosphere. 相似文献
15.
Aromatization of methane over different Mo-supported catalysts in the absence of oxygen 总被引:2,自引:0,他引:2
Tan Pinglian Xu Zhusheng Zhang Tao Chen Liayuan Lin Liwu 《Reaction Kinetics and Catalysis Letters》1997,61(2):391-396
Both acidity and structure of the support are important factors in converting methane to aromatics. Lower SiO2/Al2O3 ratio seems to favor the aromatization of methane over the Mo/HZSM-5 catalyst. When Pt is added as a modifier the activity
of Mo/HZSM-5 catalyst will decrease slightly, but coke formation will enhanced. 相似文献
16.
W掺杂对Mo/HZSM催化甲烷无氧芳构化性能的影响 《燃料化学学报》2017,45(11):1384-1391
采用浸渍法制备了Mo/HZSM-5、Mo-W/HZSM-5和W/HZSM-5三种催化剂。通过XRD、BET、Py-FTIR、H2-TPR、XPS、TEM、NH3-TPD、TPO、TG和Raman等技术对催化剂的物化性质进行表征,并考察其在甲烷无氧芳构化反应中的催化性能。结果表明,相比于Mo/HZSM-5,Mo-W/HZSM-5催化剂表现出更高的CH_4转化率、芳烃收率以及催化稳定性。H_2-TPR和XPS结果表明,Mo-W/HZSM-5中存在更易被还原为W~(4+)的正八面体(WO_6)~(n-)前驱体,反应过程中W4+的形成有助于提高CH_4转化率。同时,积炭表征结果表明,石墨型积炭是导致Mo/HZSM-5催化剂快速失活的主要原因,W掺杂可以抑制MoW/HZSM-5催化剂上石墨型积炭的形成,进而提高催化剂的稳定性。 相似文献
17.
DEHYDROGENATION AND AROMATIZATION OF METHANE IN THE ABSENCE OF OXYGEN OVER DOPED Mo/HZSM-5 CATALYSTS 下载免费PDF全文
研究了在Mo/HZSM-5催化剂上添加助剂以及不同的反应预处理温度对甲烷无氧脱氢芳构化反应的影响。实验结果表明,由于第二组分的添加,Mo/HZSM-5催化剂的活性和选择性都得到了较大程度的改善。预处理温度是影响催化剂反应性能的关键因素。Mo-Ru/HZSM-5催化剂经过873K空气预处理后,甲烷在973K的转化率约为10%,催化剂的稳定性也得到较大程度的提高。TPSR实验结果表明,Ru的加入降低了芳烃生成的温度。TPO和DTA实验结果表明,在Mo-Ru/HZSM-5催化剂上可生成较多的碳物种,结合反应结果,可以认为反应过程中生成的碳物种对甲烷的无氧脱氢芳构化反应是起积极作用的 相似文献
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Impregnation,mechanical mixing and hydrothermal treatment methods were used to introduce molybdenum species into the HZSM-5 zeolite ,the structure and surface acidity of the catalysts were studied by means of XRD,FT-IR ,NH3-TPD,TPR and XPS,The effects of Mo content and reaction time on stream on the aromatization of propane were investigated,It was found that the performance of the Mo/HZSM-5 catalst prepared by the hydrothermal treatment method was much better than that of the other two catalysts,For example ,under the reaction conditions of 823 K and 600h^-1, propance conversion and aromatics selectivity over the catalyst prepared by hydrothermal pretreatment could reach 89.17% and 78.56%,respectively,XRD and XPS results showed that the Mo species in the catalysts prepared by hydrothermal treatment were highly dispersed on the surface of the HZSM-5,and lartger amounts of them could penetrate into the HZSM-5 channel ,as compared with the other two kinds of catalysts,These factors may be responsibled for their high activities for propane aromatization,IR and NH3-TPD studies indicated that the number of Broensted acid centers decreased and the Lewis acid centers increased after Mo was introduced into the HZSM-5 zeolite. 相似文献