首页> 外文会议>China-Japan Symposium on Coal and C1 Chemistry; 20061022-28; Chengdu(CN) >INFLUENCE OF LA_2O_3 ADDITION ON COKE RESISTANCE AND REGENERATION OF NI/OLIVINE CATALYST IN STEAM REFORMING OF BENZENE
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INFLUENCE OF LA_2O_3 ADDITION ON COKE RESISTANCE AND REGENERATION OF NI/OLIVINE CATALYST IN STEAM REFORMING OF BENZENE

机译:LA_2O_3的添加对苯蒸汽重整过程中焦炭抗性和镍/橄榄催化剂再生的影响

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The gasification of biomass provides a competitive means of obtaining a clean, hydrogen rich gas for energy and chemicals production. Its industrial feasibility depends mainly on the tar elimination technologies. Tar catalytic reforming is a process to covert the condensable tar into permanent gases at the typical temperatures of 650~900℃. This involves oxidation of the tar components using steam to produce hydrogen and carbon oxides. It has the advantages over a simple scrubbing operation of increasing the gas yield and the overall efficiency of the biomass thermochemical conversion process. Ni-based catalysts are the most common used catalysts in steam reforming of methane and naphtha for its cheapness and high activity. However most of commercial reforming nickel catalysts display a rapid deactivation due to the build-up of surface carbon. These catalysts, which have been essentially designed for paraffinic hydrocarbons reforming, are not well suited for the molecular structures present in tar compounds and heavy feedstocks [1]. Many researchers are therefore devoting to develop novel catalyst formulations to optimize desired catalyst properties [2]. Courson et al. [3] prepared a nickel catalyst supported on olivine calcined at 1100℃. They reported that this catalyst is stable with its strong nickel-olivine interaction, and very active for dry and steam reforming of methane. In our previous study, we tested Ni-olivine catalyst in the steam reforming of benzene [4]. The catalyst was deactivated quickly and lost more than 50% of its initial activity within 20 minutes of treatment. It is possible to improve the anti-deactivation of the catalyst by incorporating oxide of basic rare earth. Present paper deals with the performances of La_2O_3 promoted Ni-olivine catalyst with the aim of reducing the coke formation as well as retrieving activity through regeneration. Benzene was chosen as the model compound because it is the main constituent of tar and also it represents a stable aromatic structure for tar molecules [5].
机译:生物质的气化为获得清洁的,富氢的气体用于能源和化学品生产提供了竞争性手段。其工业可行性主要取决于焦油消除技术。焦油催化重整是在典型的650〜900℃温度下将可冷凝的焦油转化为永久性气体的过程。这涉及使用蒸汽氧化焦油成分以产生氢和碳氧化物。与简单的洗涤操作相比,它具有增加气体产率和生物质热化学转化过程的整体效率的优点。镍基催化剂因其廉价和高活性而成为甲烷和石脑油蒸汽重整中最常用的催化剂。然而,由于表面碳的积累,大多数商业重整镍催化剂显示出快速的失活。这些已经设计用于链烷烃重整的催化剂并不十分适合焦油化合物和重质原料中的分子结构[1]。因此,许多研究人员致力于开发新型催化剂配方,以优化所需的催化剂性能[2]。 Courson等。 [3]制备了在1100℃煅烧的橄榄石上负载的镍催化剂。他们报告说,该催化剂具有很强的镍-橄榄石相互作用,因此非常稳定,并且对甲烷的干燥和蒸汽重整非常活跃。在我们以前的研究中,我们在苯的蒸汽重整中测试了镍橄榄石催化剂[4]。催化剂迅速失活,在20分钟内失去了超过50%的初始活性。通过掺入碱性稀土氧化物可以改善催化剂的抗失活性。本文研究了La_2O_3助催化的Ni-橄榄石催化剂的性能,目的是减少焦炭的形成以及通过再生获得活性。选择苯作为模型化合物是因为它是焦油的主要成分,并且它代表了焦油分子的稳定芳香结构[5]。

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