TY - JOUR
T1 - Recent advances in light olefins production from catalytic hydrogenation of carbon dioxide
AU - Numpilai, Thanapha
AU - Cheng, Chin Kui
AU - Limtrakul, Jumras
AU - Witoon, Thongthai
N1 - Funding Information:
This research was supported in part by the Thailand Research Fund and the Kasetsart University (grant no. RSA6280007 ), the Center of Excellence on Petrochemical and Materials Technology (PETROMAT) , the Nanotechnology Center (NANOTEC) , NSTDA, the Ministry of Science and Technology, Thailand , through its program of Research Network of NANOTEC (RNN), the Postdoctoral Fellowship from Vidyasirimedhi Institute of Science and Technology , the Kasetsart University Research and Development Institute (KURDI) through its program of Development of Advance Researcher Competence System for Competitiveness in Agriculture and Food (FF(KU) 25.64) and the Program Management Unit for Human Resources & Institutional Development, Research and Innovation ( B05F630097 ).
Publisher Copyright:
© 2021 Institution of Chemical Engineers
PY - 2021/7
Y1 - 2021/7
N2 - Increasing concerns of global warming problems caused by rising CO2 concentration in the atmosphere have driven many activities and researches for the reduction of CO2 emission. A huge CO2 emission has been discharged from industrial sectors arising from materials processing. Therefore, the development of efficient processes for the reduction of CO2 emission in the industry sector is vital. One of promising ways is to utilize CO2 as a carbon source for the production of high value-added chemicals including light olefins. In order to make the CO2-to-light olefin process feasibility in terms of economic point of view, efficient catalysts are essential for maximizing selectivity and yield of light olefins. This review summarizes recent progresses in rational design of catalytic system for CO2 conversion to light olefins. Two different paths for CO2 hydrogenation to light olefins, including the CO2−Fischer−Tropsch (CO2-FT) and oxygenate-mediated (like methanol, dimethyl ether, etc.), are compared in terms of catalytic performance and C2–C4 olefins productivity. In the CO2-FT route, the selective production of the desired C2–C4 olefins is the key goal of development with an emphasis on synergy control between active metals, promoters and supports for tuning the surface H/C ratio which significant relevance to the C2–C4 olefins formation. While, an improvement in activity with suppressing secondary reaction is imperative for achieving a high C2–C4 olefins productivity in oxygenate-mediated. Besides optimizing the catalyst components (i.e., metal oxide/zeolite mass ratios and zeolite acidity) as well as operating conditions, the distance control of the two active components is another crucial to reach the satisfactory performance. Recently, a novel catalytic system using multifunctional catalysts composed of In2O3/SAPO-34 and Fe-Co/K-Al2O3 catalysts provides an unprecedented high C2–C4 olefins productivity, shedding light on the prospects for economic competitiveness and growth in the market economy.
AB - Increasing concerns of global warming problems caused by rising CO2 concentration in the atmosphere have driven many activities and researches for the reduction of CO2 emission. A huge CO2 emission has been discharged from industrial sectors arising from materials processing. Therefore, the development of efficient processes for the reduction of CO2 emission in the industry sector is vital. One of promising ways is to utilize CO2 as a carbon source for the production of high value-added chemicals including light olefins. In order to make the CO2-to-light olefin process feasibility in terms of economic point of view, efficient catalysts are essential for maximizing selectivity and yield of light olefins. This review summarizes recent progresses in rational design of catalytic system for CO2 conversion to light olefins. Two different paths for CO2 hydrogenation to light olefins, including the CO2−Fischer−Tropsch (CO2-FT) and oxygenate-mediated (like methanol, dimethyl ether, etc.), are compared in terms of catalytic performance and C2–C4 olefins productivity. In the CO2-FT route, the selective production of the desired C2–C4 olefins is the key goal of development with an emphasis on synergy control between active metals, promoters and supports for tuning the surface H/C ratio which significant relevance to the C2–C4 olefins formation. While, an improvement in activity with suppressing secondary reaction is imperative for achieving a high C2–C4 olefins productivity in oxygenate-mediated. Besides optimizing the catalyst components (i.e., metal oxide/zeolite mass ratios and zeolite acidity) as well as operating conditions, the distance control of the two active components is another crucial to reach the satisfactory performance. Recently, a novel catalytic system using multifunctional catalysts composed of In2O3/SAPO-34 and Fe-Co/K-Al2O3 catalysts provides an unprecedented high C2–C4 olefins productivity, shedding light on the prospects for economic competitiveness and growth in the market economy.
KW - CO hydrogenation
KW - CO−Fischer−Tropsch route
KW - Light olefins
KW - Oxygenate-mediated route
UR - http://www.scopus.com/inward/record.url?scp=85107022916&partnerID=8YFLogxK
U2 - 10.1016/j.psep.2021.05.025
DO - 10.1016/j.psep.2021.05.025
M3 - Review article
AN - SCOPUS:85107022916
SN - 0957-5820
VL - 151
SP - 401
EP - 427
JO - Process Safety and Environmental Protection
JF - Process Safety and Environmental Protection
ER -