Green ethylene production from bio-ethanol with acidity controlled Barium exchanged zeolite Y catalyst

被引:0
|
作者
Oluokun, Tolulope [1 ,6 ]
Saini, Swati [1 ,2 ]
Verma, Akash [1 ,2 ]
Sharma, Bhawna [1 ,2 ]
Konathala, Sivakumar [3 ]
Vorontsov, Alexander [4 ]
Smirniotis, Panagiotis G. [5 ]
Babalola, Jonathan O. [6 ]
Kumar, Umesh [1 ,2 ]
机构
[1] CSIR Indian Inst Petr, Chem & Mat Sci Div, Polymer Mat Area, Haridwar Rd, Dehra Dun 248005, India
[2] Acad Sci & Innovat Res AcSIR, Ghaziabad 201002, India
[3] CSIR Indian Inst Petr, Analyt Sci Div, Analyt Sci Div, Haridwar Rd, Dehra Dun 248005, India
[4] Ariel Univ, Dept Chem Engn, IL-407000 Ariel, Israel
[5] Univ Cincinnati, Dept Chem & Environm Engn, Cincinnati, OH 45221 USA
[6] Univ Ibadan, Dept Chem, Ibadan 200005, Nigeria
来源
MOLECULAR CATALYSIS | 2024年 / 566卷
关键词
Barium; Bioethanol conversion; Catalytic dehydration; Ethylene selectivity; Zeolite Y; H-ZSM-5; CATALYSTS; DIETHYL-ETHER; DEHYDRATION; CONVERSION; BIOETHANOL; PROPYLENE; HYDROCARBONS; PHOSPHORUS; ALUMINAS; BASICITY;
D O I
10.1016/j.mcat.2024.114415
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
Considering the environmental concern and public legislation, the current focus has been shifted to utilizing renewable resources to produce valuable chemicals. Here in, we synthesized a series of Ba-Y zeolite catalysts by incorporating different amounts of Ba (2-7 wt.%) into H-Y zeolite via an ion-exchanged method and subsequently studied these catalysts for the selective bio-ethanol conversion to ethylene. The synthesized catalysts were characterized in detail using PXRD, FTIR, NH3-TPD, CO2-TPD, Pyridine IR, BET, ICP-OES, XPS, TEM, SEM-EDX, UV-Vis, Al-27-NMR, and TGA. The catalytic conversion was executed by using 50-95 % bio-ethanol feed in a fixed bed flow reactor. The prepared Ba-Y catalysts had improved catalytic performance in relation to the parent Y zeolite within the range (200 - 350 degrees C). The maximum ethylene yield of >98 % was achieved at low reaction temperature of 280 degrees C and 10 g/ml/min contact time with 5 wt.% incorporation of Ba in HY catalyst after 15 h TOS. The modification in acidic sites of the H-Y zeolites catalyst by Ba addition is responsible for the high conversion and selectivity, controlling the side reactions and improved anti-coke capacity.
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页数:12
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