A low-temperature regenerable catalyst for stable and selective propylene production from ethylene using Ni and P-supported SSZ-13 zeolite

被引:0
|
作者
Huyen Tran Dang [1 ]
Rajendiran, Senkuttuvan [1 ]
Kim, Chul-Ung [1 ,2 ]
Kim, Youngmin [1 ]
Kim, Jeong-Chul [3 ]
Kim, Tae-Wan [1 ,2 ]
机构
[1] Korea Res Inst Chem Technol, Chem & Proc Technol Div, Daejeon 34114, South Korea
[2] Univ Sci & Technol UST, Dept Adv Mat & Chem Engn, Daejeon 34113, South Korea
[3] Hanbat Natl Univ, Dept Chem & Biol Engn, Daejeon 34158, South Korea
基金
新加坡国家研究基金会;
关键词
Ethylene-to-propylene; Olefin interconversion; NiO-P-SSZ-13; Low-temperature regeneration; Coke hydrocracking; AROMATIC-HYDROCARBONS; REACTION PATHWAYS; PHOSPHORIC-ACID; STEAM CRACKING; HYDROGENATION; HYDROCRACKING; CONVERSION; NICKEL; DEACTIVATION; NAPHTHALENE;
D O I
10.1016/j.apcatb.2024.124421
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
Due to the increasing demand for propylene, highly selective propylene production from ethylene using small pore zeolite has received significant attention. However, rapid catalyst deactivation due to coke deposition on the catalyst impedes effective propylene production in industry. Therefore, it is essential to develop a low-temperature regeneration ethylene-to-propylene (ETP) catalyst with stable catalytic activity. To achieve such a catalyst, various hydrocracking metal species and phosphorus-supported SSZ-13 were prepared and evaluated using a one-pass ETP and ETP-Regen test. The optimized catalyst NiO(1.0)-P(0.6)-SSZ-13 exhibited a constant, excellent propylene yield of over 70 wt% with 90 wt% of propylene selectivity over ETP reaction and consecutive ETP-Regen cycles. The unprecedented catalytic performance of NiO(1.0)-P(0.6)-SSZ-13 was ascribed to the synergistic effect of NiO and P components, where nickel is responsible for catalyst recovery through effective coke removal, while phosphorus plays an essential role in size-selective diffusion.
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页数:18
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