DEVELOPMENT AND INDUSTRIAL APPROBATION OF TECHNOLOGIES OF COBALT CATALYSTS FOR SYNTHESIS OF LONG CHAIN HYDROCARBONS FROM SYNTHESIS GAS

A. Savost’yanov, R. Yakovenko, Grigory B. Narochny, V. G. Bakun, A. A. Merkin
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Abstract

The compositions, methods of preparation and specific technological parameters of the production processes of cobalt catalysts for the synthesis of long chain hydrocarbons from synthesis gas were justified. To obtain C35+ selective catalysts by coprecipitation of active components, the carrier must provide a polydisperse distribution of the pore volume along the radii. This is achieved by hydrothermal treatment of the aluminosilicate carrier. To increase the strength of catalysts, it is possible to incorporate natural bentonites and diatomite of Roctov region deposits into the composition of coprecipitated catalysts. Effective catalytic systems are impregnated catalysts on Al2O3 and SiO2 supports with aluminum oxide promotion. The insertion of 5% - Al2O3 of cobalt metal mass allows to form crystallites of Co-CoO system with a size of 8 nm on the SiO2 surface, which provides high activity and selectivity for ceresin. Aluminum oxide is stabilized with Co3O4 in a structure with a high degree of ordering, without hindering its reduction, with the formation of cobalt predominantly with the crystalline structure of hexagonal close packing. Catalyst technologies are implemented in industry. The catalysts underwent continuous continuous testing (1000 h) in laboratory and industrial conditions, showed high stability of operation. During the entire operation, the yield of C5+ hydrocarbons was 159-171 g/Nm3 based on the processed synthesis gas. The long-chain hydrocarbons C35+ (ceresin) obtained are of high quality: the dropping point was 114-116 °C (37-40% ceresin content). Operation during the year of two industrial reactors at the Novocherkassk plant of synthetic products with a total volume of catalyst loading of 18 m3 confirmed the results of laboratory tests. For citation: Savostyanov A.P., Yakovenko R.E., Narochny G.B., Bakun V.G., Merkin A.A. Development and industrial approbation of technologies of cobalt catalysts for synthesis of long chain hydrocarbons from synthesis gas. Izv. Vyssh. Uchebn. Zaved. Khim. Khim. Tekhnol. 2018. V. 61. N 9-10. P. 53-58
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合成气合成长链烃用钴催化剂技术的开发与产业化评价
对合成气合成长链烃用钴催化剂的组成、制备方法和具体工艺参数进行了论证。为了通过活性组分的共沉淀获得C35+选择性催化剂,载体必须沿半径提供多分散的孔体积分布。这是通过水热处理铝硅酸盐载体来实现的。为了提高催化剂的强度,可以将罗克托夫地区沉积物的天然膨润土和硅藻土加入共沉淀催化剂的组成中。有效的催化体系是在Al2O3和SiO2载体上浸渍催化剂,并由氧化铝促进。加入5% - Al2O3的钴金属质量可以在SiO2表面形成尺寸为8 nm的Co-CoO体系,具有较高的树脂活性和选择性。氧化铝与Co3O4稳定在一个高度有序的结构中,而不妨碍其还原,形成的钴主要是六方紧密堆积的晶体结构。催化剂技术在工业上得到了应用。催化剂在实验室和工业条件下连续测试(1000 h),表现出较高的运行稳定性。在整个操作过程中,以加工的合成气为基准,C5+烃的产率为159 ~ 171 g/Nm3。得到了高质量的长链烃C35+(蜡质),其落点为114-116℃(蜡质含量为37-40%)。在新切尔卡斯克合成产品工厂的两个工业反应器(催化剂装载总量为18立方米)一年内的运行证实了实验室测试的结果。引用本文:Savostyanov a.p., Yakovenko R.E, Narochny g.b., Bakun v.g., Merkin A.A.。合成气合成长链烃用钴催化剂技术的开发与工业认可。Izv。Vyssh。Uchebn。Zaved。Khim。Khim。Tekhnol》2018。v . 61。N 9。p . 53-58
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来源期刊
CiteScore
1.40
自引率
44.40%
发文量
83
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