Coated sulfated zirconia/SAPO-34 for the direct conversion of CO2 to light olefins

被引:35
|
作者
Ramirez, Adrian [1 ]
Chowdhury, Abhishek Dutta [1 ]
Caglayan, Mustafa [1 ]
Rodriguez-Gomez, Alberto [1 ]
Wehbe, Nimer [2 ]
Abou-Hamad, Edy [2 ]
Gevers, Lieven [1 ]
Ould-Chikh, Samy [1 ]
Gascon, Jorge [1 ]
机构
[1] King Abdullah Univ Sci & Technol, KAUST Catalysis Ctr KCC, Adv Catalyt Mat, Thuwal 23955, Saudi Arabia
[2] King Abdullah Univ Sci & Technol, Core Labs, Thuwal 23955, Saudi Arabia
关键词
HIGHLY SELECTIVE CONVERSION; CATALYTIC CRACKING; CARBON-DIOXIDE; HYDROGENATION; ACID; HYDROCARBONS; METHANOL; ZIRCONIUM; PROPENE; ALKANES;
D O I
10.1039/c9cy02532d
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The conversion of CO2 to light olefins via bifunctional catalysts (i.e. metal oxides/zeolites) is a promising approach to tackle CO2 emissions and, at the same time, reduce fossil-fuel dependence by closing the carbon cycle. However, designing a catalyst, especially a zeolite, that can operate at mid-low temperatures (where the selective CO2 conversion is favored) is still a challenge for the scientific community. Herein, we report the synthesis of a novel coated ZrS/SAPO-34 in combination with an iron catalyst (Fe2O3@KO2) that successfully fills this temperature gap. While making use of the properties of the zeolite to maximize light olefin selectivity, the unique nature of the sulfated zircona (ZrS) layer allows the cracking of C5+ heavy hydrocarbons produced on the Fe component at temperatures where conventional zeolites fall short. In particular, total short olefin yields per pass over 20% at CO2 conversions near 50% (total C-2-C-4 olefin selectivity = 40-45) can be achieved at T = 375 degrees C, P = 30 bar, H-2/CO2 = 3 and 5000 mL g(-1) h(-1). Light olefin space-time yields here reported (10.4 mmol gcat(-1) h(-1)) clearly outperform conventional zeolite based bifunctional systems for CO2 conversion.
引用
收藏
页码:1507 / 1517
页数:11
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