Unraveling high alkene selectivity at full conversion in alkyne hydrogenation over Ni under continuous flow conditions

被引:13
作者
Bakuru, Vasudeva Rao [1 ,6 ]
Fazl-Ur-Rahman, Kashifa [2 ]
Periyasamy, Ganga [2 ]
Velaga, Bharath [3 ]
Peela, Nageswara Rao [3 ]
DMello, Marilyn Esclance [1 ]
Kanakikodi, Kempanna S. [1 ]
Maradur, Sanjeev P. [1 ]
Maji, Tapas Kumar [4 ]
Kalidindi, Suresh Babu [5 ]
机构
[1] Poornaprajna Inst Sci Res, Mat Sci & Catalysis Div, Bangalore 562164, Karnataka, India
[2] Bangalore Univ, Dept Chem, Bangalore 56, Karnataka, India
[3] Indian Inst Technol, Dept Chem Engn, Gauhati 781039, Assam, India
[4] Jawaharlal Nehru Ctr Adv Sci Res, CPMU, Mat Mol Lab, Bangalore 560064, India
[5] Andhra Univ, Sch Chem, Dept Inorgan & Analyt Chem, Visakhapatnam 530003, Andhra Pradesh, India
[6] Catholic Univ Louvain, Inst Matiere Condense & Nanosci, B-1348 Louvainla La Neuve, Belgium
关键词
CATALYZED TRANSFER HYDROGENATION; METAL-SUPPORT INTERACTION; PD CATALYSTS; CHEMOSELECTIVE HYDROGENATION; PALLADIUM SULFIDE; NICKEL; SEMIHYDROGENATION; CARBON; PHENYLACETYLENE; NANOCATALYSTS;
D O I
10.1039/d2cy00875k
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
Selective hydrogenation of alkynes into alkenes under continuous flow conditions over non-precious metal catalysts is an attractive prospect for the chemical industry, especially for the petrochemical and polymer industry. Achieving high alkene selectivity at full alkyne conversions is an ongoing challenge. To address this, we dissolved carbon into Ni lattices by treating Ni@C material derived from MOF-74(Ni) with H-2 at 300 degrees C and the resultant material is explored as a catalyst for selective styrene synthesis from phenylacetylene (PA) under fixed bed flow conditions. The designed catalyst exhibited a rare combination of sustained high styrene (ST) selectivity (92 +/- 1%) and full phenylacetylene (PA) conversion (>99%). Density functional theory (DFT) calculations predict that the carbon incorporation decreases the interaction energy between ST and the catalyst surface, and this increased the reaction barrier for further hydrogenation. Time on stream data showed a 13 h stable performance and the catalyst is regenerable for 4 cycles without a loss of activity. Further, PA is completely removed (by semi-hydrogenation) from the styrene stream even when it is present in low quantities (1.8%).
引用
收藏
页码:5265 / 5273
页数:10
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