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Direct Conversion of Syngas into Light Olefins with Low CO2 Emission
ACS Catalysis ( IF 11.3 ) Pub Date : 2020-01-21 , DOI: 10.1021/acscatal.9b04629 Sen Wang 1 , Pengfei Wang 1 , Dezhi Shi 1, 2 , Shipei He 1, 2 , Li Zhang 1, 2 , Wenjun Yan 1 , Zhangfeng Qin 1 , Junfen Li 1 , Mei Dong 1 , Jianguo Wang 1, 2 , Unni Olsbye 3 , Weibin Fan 1
ACS Catalysis ( IF 11.3 ) Pub Date : 2020-01-21 , DOI: 10.1021/acscatal.9b04629 Sen Wang 1 , Pengfei Wang 1 , Dezhi Shi 1, 2 , Shipei He 1, 2 , Li Zhang 1, 2 , Wenjun Yan 1 , Zhangfeng Qin 1 , Junfen Li 1 , Mei Dong 1 , Jianguo Wang 1, 2 , Unni Olsbye 3 , Weibin Fan 1
Affiliation
Direct conversion of syngas into light olefins over bifunctional catalysts has made significant progress; the C2=–C4= selectivity in hydrocarbons reaches >80%. Nevertheless, a relatively harsh reaction condition (>380 °C, 1.0 MPa) led to producing large amounts of CO2 (>40%) and gave a low olefin/paraffin (O/P) ratio (<10) as a result of significant promotion of water–gas shift (WGS) reaction and overhydrogenation of olefins. In this context, attempts are made here to develop a highly active low-temperature composite catalyst. It was found that a zinc–cerium–zirconium solid solution (ZnxCe2–yZryO4) and a SAPO-34 mixture showed CO conversion, light olefin selectivity in hydrocarbons, and O/P ratios of about 7%, 83%, and 23, respectively, at 300 °C and 1 atm. More interestingly, this catalyst showed CH4 selectivity and CO2 emission lower than 5 and 6%, respectively. A combination of experimental, in situ spectroscopy, and theoretical calculation results reveals that doping Ce in ZnxZr2.0O4 greatly inhibits the WGS reaction by increasing the formation energy barrier of carboxylate intermediate species, but increases surface oxygen vacancy concentration of the composite through formation of a solid solution, and as a consequence, improving the catalytic activity for conversion of syngas at mild conditions by enhancing the interaction of CO with the catalyst, which elongates the C–O bond of the HCO* species.
中文翻译:
将合成气直接转化为低CO 2排放的轻烯烃
通过双功能催化剂将合成气直接转化为轻质烯烃已取得重大进展。C 2 = –C 4 =在烃中的选择性达到> 80%。但是,相对苛刻的反应条件(> 380°C,1.0 MPa)导致产生大量的CO 2(> 40%),并且由于以下原因导致了较低的烯烃/石蜡(O / P)比(<10)。大大促进了水煤气变换(WGS)反应和烯烃的过度氢化。在这种情况下,这里尝试开发高活性的低温复合催化剂。发现锌-铈-锆固溶体(Zn x Ce 2- y Zr y O 4)和SAPO-34混合物在300°C和1个大气压下分别显示出CO转化率,在烃中的轻烯烃选择性以及O / P比分别约为7%,83%和23。更有趣的是,该催化剂的CH 4选择性和CO 2排放分别低于5和6%。实验,原位光谱和理论计算结果的结合表明,Zn x Zr 2.0 O 4中掺杂铈 通过增加羧酸盐中间体物种的形成能垒极大地抑制了WGS反应,但通过形成固溶体而增加了复合材料的表面氧空位浓度,因此,通过提高温度提高了在温和条件下转化合成气的催化活性CO与催化剂的相互作用,延长了HCO *物种的C–O键。
更新日期:2020-01-22
中文翻译:
将合成气直接转化为低CO 2排放的轻烯烃
通过双功能催化剂将合成气直接转化为轻质烯烃已取得重大进展。C 2 = –C 4 =在烃中的选择性达到> 80%。但是,相对苛刻的反应条件(> 380°C,1.0 MPa)导致产生大量的CO 2(> 40%),并且由于以下原因导致了较低的烯烃/石蜡(O / P)比(<10)。大大促进了水煤气变换(WGS)反应和烯烃的过度氢化。在这种情况下,这里尝试开发高活性的低温复合催化剂。发现锌-铈-锆固溶体(Zn x Ce 2- y Zr y O 4)和SAPO-34混合物在300°C和1个大气压下分别显示出CO转化率,在烃中的轻烯烃选择性以及O / P比分别约为7%,83%和23。更有趣的是,该催化剂的CH 4选择性和CO 2排放分别低于5和6%。实验,原位光谱和理论计算结果的结合表明,Zn x Zr 2.0 O 4中掺杂铈 通过增加羧酸盐中间体物种的形成能垒极大地抑制了WGS反应,但通过形成固溶体而增加了复合材料的表面氧空位浓度,因此,通过提高温度提高了在温和条件下转化合成气的催化活性CO与催化剂的相互作用,延长了HCO *物种的C–O键。