首页> 外文会议>International Conference on Environment >Exploring Transition Metal (Cr, Mn, Fe, Co, Ni) Promoted Copper-Catalyst for Carbon Dioxide Hydrogenation to Methanol
【24h】

Exploring Transition Metal (Cr, Mn, Fe, Co, Ni) Promoted Copper-Catalyst for Carbon Dioxide Hydrogenation to Methanol

机译:探索过渡金属(Cr,Mn,Fe,Co,Ni)促进了二氧化碳氢化铜催化剂与甲醇

获取原文

摘要

Methanol production from direct CO2 hydrogenation has been widely envisaged to have key role in promoting CO2 utilization. The approach is a serious option in alleviating global warming, thus, contributing to sustainable development. However, the efficiency of methanol production from direct CO2 hydrogenation is highly dependent on the reactivity of catalyst. In this study, the structure-activity relationships of transition metal (Cr, Mn, Fe, Co, Ni) promoted copper-catalyst in direct CO2 hydrogenation to methanol were established by a systematic comparison between the synthesized catalysts. The copper-catalyst used in the study was Cu/ZnO/SBA-15 (CZ/SBA-15). Catalytic performance of all the synthesized catalysts was evaluated in a continuous-flow fixed-bed micro-reactor under kinetic-controlled conditions. Overall, the manganese promoted copper-catalyst (Mn-CZ/SBA-15) was determined as the most active catalyst. The outstanding performance of Mn-CZ/SBA-15 was due to the jointly presence of small copper crystallites and strong interaction between copper oxide and other oxide species in the catalyst. At reaction temperature of 180° C, under reaction pressure of 4.0 MPa, WHSV of 60 L/gcat.h, and H_2:CO_2 mole ratio of 3:1, the catalyst presented the highest methanol yield of 10.4%. The CO2 conversion achieved was 10.5% and the methanol selectivity was 98.6%.
机译:广泛设想从直接CO2氢化的甲醇生产在促进CO2利用方面具有关键作用。该方法是减轻全球变暖的认真选择,从而有助于可持续发展。然而,从直接CO 2氢化甲醇产生的效率高度依赖于催化剂的反应性。在该研究中,通过合成催化剂之间的系统比较建立了在合成催化剂之间的系统比较建立了在直接CO 2氢化到甲醇中的过渡金属(Cr,Mn,Fe,Fe,Co,Ni)的结构 - 活性关系。该研究中使用的铜催化剂是Cu / ZnO / SBA-15(CZ / SBA-15)。在动力学控制条件下,在连续流动固定床微反应器中评价所有合成催化剂的催化性能。总的来说,锰促进的铜催化剂(Mn-CZ / SBA-15)被确定为最活性催化剂。 Mn-CZ / SBA-15的出色性能是由于催化剂中的小铜微晶和氧化铜和其他氧化物物种之间的强相互作用。在反应温度为180℃的温度下,在4.0MPa的反应压力下,WHSV为60L / gcat.h,H_2:CO_2摩尔比为3:1,催化剂呈列最高甲醇产率为10.4%。实现的CO 2转化为10.5%,甲醇选择性为98.6%。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号