Cr改性USY分子筛提高裂化催化剂的异构化性能

在催化裂化过程中,烷烃分子在酸性催化剂表面进行一系列的反应,其中氢转移反应能导致汽油中的烯烃质量分数降低,而异构化、环化、芳构化反应则改善裂化产品的分布,对提高裂化汽油的辛烷值有明显的效果。为了解决我国裂化汽油中烯烃质量分数过高的问题,目前大多数催化裂化装置都采用了降烯烃裂化催化剂,以氢转移反应活性高的REUSY分子筛作为裂化催化剂的活性组分。但由于REUSY分子筛的异构化活性较低,因此裂化汽油的辛烷值有所下降,需要对裂化汽油进行加氢异构化处理。若直接对裂化催化剂进行改性,提高其异构化反应活性,     

NiOd USY分子筛,γ—Al2O3及其混合载体上的NO吸附行为和分？…

运用红外技术和高斯函数对红外谱图进行分峰拟合,研究了对ＮｉＯ在ＵＳＹ分子筛,γ－Ａｌ２Ｏ３和混合载体上的对ＮＯ吸附规律,并推出不同ＮｉＯ含量时,Ｎｉ＾２＋在这些载体上的分布,结果表明,位于γ－Ａｌ２Ｏ３表面,ＵＳＹ分筛ＳＩ、Ｓ１位和ＳＩ位的Ｎｉ＾２＋离子吸附ＮＯ时,它们的吸附分别为１８５５－１８７５、１９００和１９０５ｃｍ＾－１,ＮｉＯ在γ－Ａｌ２Ｏ３的体相和表面间存在分布平衡,久有７５％ＮｉＯ存     

用FT—IR技术研究Mo／HZSM—5分子筛的骨架结构

在两种不同硅铝比的ＨＺＳＭ－５分子筛上担载不同量的钼物种后，对甲烷地氧脱氢芳构化反应呈现出不同的催化活性，使用ＦＴ－ＩＲ技术测定了催化剂样品的骨架结构，结果表明，在两种族中分子筛载体上，钼物处的存在状态及其与载全校是的相互作用各不同相；分子筛载的酸性环境决定了浸渍时钼物种的可能存在状态。     

W-Ni/Al2O3-USY催化剂中USY的作用

采用ＥＳＣＡ，ＴＰＲ及高压连续流动反应色谱等技术研究了在Ｗ－Ｎｉ／Ａｌ２Ｏ３中引入超稳Ｙ型分子筛对载体表面性质及催化剂加氢脱氮活性的影响。结果表明：ＵＳＹ可明显改善Ｗ和Ｎｉ的分散状态，提高催化剂的总酸，并可调变Ｂ酸和Ｌ酸的分布；加入ＵＳＹ可提高催化剂的比表面积，但不利于发挥Ｎｉ的助剂作用；加入适宜量的ＵＳＹ，可明显提高催化剂的加氢脱氮活性。     

甲烷在Mo／HZSM—5催化剂上的高温活化

高温下,甲烷在Ｍｏ／ＨＺＳＭ－５分子筛上可直接生成苯［１］．虽然低温下甲烷能被Ｍｏ／ＨＺＳＭ－５催化剂表面的—ＯＨ所活化［２］,但对甲烷在高温下的活化过程知之甚少,然而这却是很重要的．我们采用原位红外光谱技术,研究了甲烷在高温下Ｍｏ／ＨＺＳＭ－５催化...     

MoO3／HBZSM—5催化剂上甲烷的无氧芳构化反应

以含硼杂原子分子筛ＨＢＺＳＭ－５为载体,考察了其担载ＭｏＯ３后催化甲烷无氧芳构化反应的性能,并结合ＸＲＤ,ＩＲ,ＴＧ和ＳＥＭ等手段对催化剂进行了表征。实验结果表明,ＭｏＯ３／ＨＢＺＳＭ－５催化剂具有较高的甲烷芳构化活性,但稳定性较差,随着引入分子筛骨架中硼量的增大,甲烷的极值转化率增高;随着反应温度的升高,ＭｏＯ３／ＨＢＺＳＭ－５催化剂的甲烷芳构化活性升高。从产物分布的变化来看,硼的引入对于催化剂     

超声辅助制备Ni-Mo/USY催化剂上正庚烷异构化性能研究

以USY分子筛作为载体,Ni和Mo作为活性组分,利用超声辅助浸渍法（US-IM）和常规浸渍法（C-IM）制备了Ni/USY（US-IM）和Ni-Mo/USY催化剂.采用X射线衍射（XRD）、吡啶-红外光谱分析（Py-IR）和N₂吸附-脱附等对催化剂进行理化性质表征,综合考察了不同改性方法以及单金属和双金属改性前后分子筛酸性和孔结构性质等的变化及其对正庚烷异构化性能的影响.实验结果表明：Mo对于Ni在USY分子筛上的均匀分布以及异构化催化性能具有协同促进作用;超声条件对双金属改性的USY结构基本无影响;超声空化作用降低了催化剂金属粒子的团聚,使其在USY表面均匀分散,增加了催化反应中所需的金属活性位点.超声辅助浸渍制备的Ni-Mo/USY中较高的金属分散度导致了较强的金属-载体相互作用,使其活性和稳定性高于常规浸渍法.在优化超声条件下,反应温度和反应时间分别为250℃和3 h,还原温度和还原时间分别为550℃和5 h,H₂/C₇摩尔比为0.14时,正庚烷的转化率和异构化选择性分别可以达到65.7%和74.1%.     

正庚烷在超稳Y沸石(USY)负载超强酸催化剂上加氢异构化

The Pt-bearing SO₄^2-/ZrO₂ superacid catalysts supported on ultra stable Y (USY) zeolite were prepared by impregnation and characterized by X-ray diffraction, nitrogen adsorption and Hammett indicators. Their catalytic activities were evaluated in the hydroisomerization of n-heptane with an atmospheric fixed-bed reactor. The catalysts possessed a high surface area, superacidity and well maintained pore structure of USY support. The supported catalysts with a suitable SO₄^2-/ZrO₂ loading exhibited a higher catalytic activity and selectivity than the unsupported SO₄^2-/ZrO₂ catalyst or the Pt supported on USY catalyst without superacid. At the reaction temperature of 220 ℃, over the catalyst with a Pt loading of 0.8wt% and ZrO₂ loading of 10wt%, the conversion of n-heptane could be as high as 35.2% with a selectivity of 87.9% for isomerization products.     

USY分子筛催化FCC汽油的烷基化脱硫反应研究

以USY分子筛催化FCC汽油中噻吩类硫化物与烯烃的烷基化反应,采用DL-2B-EE微库仑仪测定反应前后硫分布的变化,考察了USY分子筛的制备条件和烷基化反应温度对其催化性能的影响.实验结果表明,水蒸汽处理温度350℃、水蒸汽处理时间5h,反应温度120℃时,USY分子筛催化剂的比表面积为613m2/g,催化活性最佳,使得FCC汽油中<100℃馏分的硫含量减少至16.92mg/L.水蒸汽流速对USY分子筛催化烷基化反应影响不大.不同处理方法所得USY分子筛的吡啶吸附红外光谱结果表明,具有较多的酸中心的USY分子筛更有利于催化FCC汽油的烷基化脱硫反应.     

NiO在USY分子筛、γ-Al2O3及其 混合载体上的NO吸附行为和分布规律

运用红外技术和高斯函数对红外谱图进行分峰拟合,研究了对NiO在USY分子筛、γ-Al     

脱铝超稳Y沸石催化合成乙酸正丁酯研究

研究了脱铝超稳Y沸石催化乙酸与正丁醇的酯化反应。考察了催化剂硅铝比，催化剂用量，反应物配比，反应时间等因素对反应的影响。在适宜的反应条件下乙酸酯化率可达98．0％，且催化剂可重复使用。     

用正电子谱学研究USY沸石中二次孔的脱水

超稳Ｙ型沸石（ＵＳＹ）分子筛是石油催化裂化中的优异催化剂,它是由ＨＹ型沸石经高温水热处理制备的,它的特点之一是具有良好的热稳定性．因而,对ＵＳＹ的改性研究一直受到关注［１-５］,尤其是在制备ＵＳＹ过程中由于水热处理所产生大量二次孔,它与ＵＳＹ的结构与?..     

掺杂Cr助剂的Pt/USY催化剂上正庚烷异构化反应研究

The Pt-supported USY zeolite catalysts doped with Cr, Al or Zn were prepared by impregnation, and characterized by XRD, low temperature nitrogen physisorption, H2-chemisorption and IR spectroscopy of the pyridine adsorption. Catalytic activities were evaluated via the hydroisomerization of n-heptane with an atmospheric fixed-bed reactor. The Pt dispersion and acidity of the Pt-supported USY catalyst were influenced by the addition of the promoters. The Pt-supported catalysts promoted by Cr, Al or Zn, especially by Cr, were catalytically much more stable and exhibited much higher catalytic activity and selectivity for isomerization of n-heptane than the catalysts without the dopant. Both the conversion and selectivity are discussed in relation with the physicochemical properties of catalysts.     

Fe Promotion Effect in Mn/USY for Low-temperature Selective Catalytic Reduction of NO with NH3

SCR of NO with NH3 is considered to be the most effective process for the treatment of stack gases from stationary sources1. The commercial catalysts for NH3-SCR are V2O5/TiO2 (anatase) promoted with either WO3 or MoO32-5. Although the vanadium- based cat…     

FCC汽油在Ni-Mo-P/USY催化剂上的降烯烃工艺研究

制备了Ni-Mo-P/USY催化剂,采用透射电镜(TEM)及选区电子衍射(SAED)等手段对催化剂进行表征,证实了Ni、Mo活性组分可以较好聚合于USY载体中,并以抚顺石油二厂FCC汽油为原料,考察在该催化剂上进行的烯烃异构化及芳构化反应,探讨了工艺条件对催化性能的影响,结果表明,P改性后的Ni-Mo-P/USY催化剂比改性前性能大为提高,在反应温度320℃、反应压力2.0MPa、质量空速(WHSV)4.0h-1、氢油比(VH2/VOil)400∶1的条件下,汽油烯烃转化率、液体收率、产品异构化选择性和芳构化选择性分别可以达到62.1%、78.4%、47.2%和14.1%.     

Propane Aromatization over Mo／HZSM—5 Catalysts

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.