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Suspension catalytic distillation (SCD) has been developed recently as an innovative technology in catalytic distillation. In this paper, a brief introduction to SCD is given and an equilibrium stage (EQ) model is developed to simulate this new process for synthesis of linear alkylbenzene (LAB) from benzene and 1-dodecene.Since non-ideality of this reaction system is not strong, EQ model developed could be applied to it successfully.Simulation results agree well with experimental data, and indicate some characteristics of SCD process as an advanced technology for the production of LAB: 100% conversion of olefins, low temperature (90-100℃) and low benzene/olefin mole ratio. 相似文献
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The selective oxidation of n-butane to maleic anhydride(MA) on a vanadium-phosphorus oxide (VPO) catalyst was studied using on-line gas-chromatography combined with mass spectrometry(GC-MS) and transient response technique.The reaction intermediates,butene and furan,were found in the reaction effuent under near industrial feed condition (3% butane 15% O2),while dihydrofuran was detected at high butane concentration (12% butane,5%O2).Some intermediates of MA decomposition were also identified.Detection of these intermediates shows that the vanadium phosphorus oxides are able to dehydrogenate butane to butene,and butene further to form MA.Based on these observations,a modified scheme of reaction network is proposed.The transient experiments show that butane in the gas phase may directly react with oxygen both on the surface and from the metal oxide lattice,without a proceeding adsorption step.Gas phase oxygen can be adsorbed and transformed to surface lattice oxygen but it can not participate in selective oxidation.Adsorbed oxygen leads to deep oxidation,while lattice oxygen leads to selective oxidation. 相似文献
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以BαCO3和不同的镧化合物作为催化剂组分,分别采用干混法和湿混法制备了BαCO3质量含量为2.5%-15%的BαCO3/Lα2O3催化剂,在微型固定床反应器上评价了催化剂的甲烷氧化偶联反应性能,考察了反应条件对催化剂性能的影响,以及催化剂床层中的热点效应,采用XRD和TPR对催化剂的结构和性能进行了表征。结果表明,不同方法制备的BαCO3/Lα2O3催化剂在较低炉温的条件下都具有好的甲烷氧化偶联反应性能,其中湿混法制备的10%BαCO3/Lα2O3催化剂性能最好,在烷氧比为2,反应气体空速为36000mL·g^-1·h^-1的条件下,反应炉温在125℃时甲烷氧化偶联反应仍能平稳进行。存在于催化剂床层的热点是维持甲烷氧化偶联反应的关键。不同方法制备的BαCO3/Lα2O3催化剂其物相和氧化还原性能也有一定的差别。 相似文献
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Adsorption, surface reaction and process dynamics on the surface of a commercial copper-based cata-lyst for methanol synthesis from CO/CO2/H2 were systematically studied by means of temperature programmed desorption (TPD), temperature programmed surface reaction (TPSR), in-situ Fourier transform-inferred spectroecopy(FTIR) and stimulus-response techniques. As a part of results, an elementary step sequence was suggested and a group of ordinary differential equations (ODEs) for describing transient conversations relevant to all species on the catalyst surface and in the gas phase in a micro-fixed-bed reactor was derived. The values of the parameters referred to dynamic kinetics were estimated by fitting the solution of the ODEs with the transient response data obtained by the stimulus-response technique with a FTIR analyzer as an on-line detector. 相似文献
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研究了白钨矿型ABO4(A=碱土金属、过渡金属、镧系金属、主族金属离子等;B=Mo、W)氧化物催化剂的尿素燃烧法制备工艺,考察了燃烧剂尿素的用量、燃烧温度等制备条件与氧化物纯度的关系.结果表明,尿素燃烧法可以获得A位离子为Mg、Ca、Sr、Ba、Cr、Mn、Co、Ni、Zn、Cd、Al的纯AMoO4白钨矿型氧化物催化剂和A位离子为Mg、Ca、Sr、Ba、Mn、Co、Ni、Zn、Cd的纯AWO4白钨矿型氧化物催化剂,A位离子为La、Ce时,得到混合氧化物. 相似文献
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YSBH-02分子筛催化剂上异丙醇与苯气相烷基化反应的研究 总被引:2,自引:0,他引:2
对YSBH-02型分子筛催化剂上异丙醇与苯常压气相烷基化合成异丙苯的工艺过程进行了实验研究。以单因素实验法考察了温度(200~340℃),苯/醇摩尔比(4.5~15.5)和液相空速(5~50h^-1)对烷基化反应的影响,并基于正交实验设计综合考察了温度、苯/醇比和液相空速对烷基化规律和产物分布的影响。结果表明,YSBH-02型分子筛催化剂对异丙醇与苯气相烷基化具有良好的催化活性和选择性;较为适宜的烷基化条件为:温度280℃,苯/醇摩尔比13:1,液相空速9h^-1。 相似文献
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对于放热反应,尤其是气相和气固相强放热反应,定态稳定性和参数敏感性是管式反应器设计、操作中一个十分重要而有趣的课题。本文以若干简单模型为例,简要地说明了管式反应器稳定性和敏感性的基本概念、分析方法与实际应用。 相似文献
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