首页> 外文会议>China-Japan Symposium on Coal and C1 Chemistry; 20061022-28; Chengdu(CN) >DESIGNING OF HIGHLY-ACTIVE COBALT METAL CLUSTER CATALYST WITH CHELATEVG AGENT FOR THE FISCHER-TROPSCH SYNTHESIS
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DESIGNING OF HIGHLY-ACTIVE COBALT METAL CLUSTER CATALYST WITH CHELATEVG AGENT FOR THE FISCHER-TROPSCH SYNTHESIS

机译:具有螯合剂的高活性钴金属团簇催化剂的FISCHER-TROPSCH合成设计

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The Fischer-Tropsch synthesis (FTS) reaction produces liquid aliphatic hydrocarbons by the hydrogenation of carbon monoxide. Although it has been well known that reduced Co/SiO_2 catalysts show higher activities for this reaction, the activity of this type of catalysts should be improved further in order to establish the compact FTS process that can utilize dispersed carbon resources such as the natural gas from remote gas fields, the coal and the biomass. Co/SiO_2 catalysts are usually prepared as oxide states followed by H_2 reduction to generate FTS active metallic species. The oxide precursor is prepared through various steps, such as impregnating, drying and/or calcination steps. Each step has various parameters, for example, types of solvent and Co source, the pH of the solution, etc. for the impregnating step. It has been generally assumed that the structure of Co species on the calcined catalyst strongly affects the number of surface metallic Co sites after the reduction. Especially, the formation of silicate-like species after the calcination strongly depresses the reducibility of the oxide precursor in the case of Co/SiO_2 catalyst, which results in the smaller number of surface metallic Co sites even after H_2 reduction for long time [1]. In the previous studies, several factors during the preparation of the precursor for Co/SiO_2 catalyst are proposed to affect the structure of Co species after the calcination especially in relation with the formation of silicate-like species, which include the pH of the impregnating solution [1,2], the concentration of oxidizing agents such as NOx during the calcination step [3] and/or the heat flow during the calcination step [4]. However, there is still a lack of information about the effective method for the preparation of the oxide precursor that can create the larger number of the surface metallic sites after the reduction.
机译:费-托合成(FTS)反应通过一氧化碳的氢化产生液态脂族烃。尽管众所周知,还原的Co / SiO_2催化剂对该反应具有更高的活性,但应进一步提高这类催化剂的活性,以建立紧凑的FTS工艺,该工艺可以利用分散的碳资源,例如天然气偏远的气田,煤炭和生物质。通常将Co / SiO_2催化剂制备成氧化物态,然后还原H_2以生成FTS活性金属。通过各种步骤,例如浸渍,干燥和/或煅烧步骤来制备氧化物前体。每个步骤具有各种参数,例如,用于浸渍步骤的溶剂和Co源的类型,溶液的pH等。通常认为,煅烧催化剂上Co物种的结构强烈影响还原后表面金属Co位点的数量。尤其是,在煅烧后形成类似硅酸盐的物种,在Co / SiO_2催化剂的情况下,大大降低了氧化物前体的还原性,即使经过长时间的H_2还原后,表面金属Co的数量也减少了[1]。 。在以前的研究中,提出了在制备Co / SiO_2催化剂前体时会影响煅烧后Co物种结构的几个因素,特别是与硅酸盐样物质的形成有关的因素,其中包括浸渍溶液的pH值。 [1,2]是在煅烧步骤[3]中氧化剂的浓度,例如NO x和/或在煅烧步骤[4]中的热流。但是,仍然缺乏有关制备氧化物前体的有效方法的信息,该方法可在还原后产生大量的表面金属位点。

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