Methanation of Syngas over Ni-Based Catalysts with Different Supports

• 作者: Buyan-Ulzii Battulga Enkhsaruul Byambajav Munkhdelger Chuluunsukh
• 来源期刊: 化学工程与科学期刊(英文)
• 学科: 化学
• 关键词: CO HYDROGENATION Water-Gas Shift Reaction Nano-γ-Al2O3 METHANE PRODUCTIVITY
• 年，卷（期）: 2020,（2）
• 页码范围: 113-122
• 页数: 10页
• 分类号: O64

摘要

CO methanation over the 20% nickel catalyst prepared by impregnation-precipitation method on different supports of commercial γ-Al2O3, TiO2, SiO2 and nano-γ-Al2O3* was investigated. The nano-γ-Al2O3* support was pulverized using a ball milling method. Catalyst characterization was done using the methods of BET, XRD, SEM, ICP-OES methods. Carbon monoxide methanation process was carried out at the temperature of 350&#176C in pressure of 3 bar of H2:CO syngas with the molar ratio of 3:1 and with the GHSV of 3000 h-1 in a fixed bed reactor. The initial temperature of methane formation increased according to the order of Ni/γ-Al2O3* 2 γ-TiO2 γ-Al2O3. The Ni/γ-Al2O3*, which was prepared on the surface of nano milled γ-Al2O3 support, produced methane from the lowest temperature of 178&#176C to 350&#176C in CO methanation. The Ni/γ-Al2O3* catalyst gave the highest amount of methane (0.1224 mmol/g-cat) for 1 h methanation among other catalysts. XRD and SEM analysis proved that NiO particles in the Ni/γ-Al2O3* were finely distributed, and their sizes were smaller compared to those in the traditional one. The pulverization of γ-Al2O3 improved the dispersion of catalytic active nickel species inside porosity of the support leading to the improvement of its catalytic performance for CO methanation.