Khanindra Kalita
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Khanindra Kalita has a total of 4 co-authors. Here are the top co-authors by number of shared publications:
- Jayashree Parthiban
Catalysis Group Department of Chemistry Indian Institute of Technology Indore Indore Madhya Pradesh India
2 shared publications - Sanjay Kumar Singh
Catalysis Group, Department of Chemistry, Indian Institute of Technology Indore, Khandwa Road, Simrol, Indore 453552, Madhya Pradesh, India
2 shared publications - Mahendra Kumar Awasthi
Catalysis Group, Department of Chemistry, Indian Institute of Technology Indore, Simrol, Indore 453552, Madhya Pradesh, India
1 shared publication - Tushar A. Kharde
Catalysis Group, Department of Chemistry, Indian Institute of Technology Indore, Khandwa Road, Simrol, Indore, 453552, M.P., India
1 shared publication
Latest Publications
- 26 July 2026
- Published by Wiley in Chemistry – An Asian Journal
- Vol. 21 (14) , e70908
Diruthenium Catalyst for CO 2 and (Bi)carbonate Hydrogenation to Formate in Aqueous media
Highly efficient CO 2 and (bi)carbonate hydrogenation to formate in water was achieved by exploiting the cooperative interaction of the two ruthenium centers in a series of water‐soluble diruthenium complexes [{( η 6 ‐arene)RuCl} 2 ( μ ‐ κ 2 : κ 2 ‐benztetraimd)] 2+ containing the bridging meta ‐/ para ‐bis‐imidazole methane‐based ligands ( m ‐/ p ‐benztetraimd). Our findings revealed the pivotal role of the ligand structure in tuning the catalytic activity, where the catalyst p ‐C3 [{( η 6 ‐ p ‐cymene)RuCl} 2 ( μ ‐ κ 2 : κ 2 ‐ p ‐benztetraimd)] 2+ outperformed others. Consequently, a high formate yield (2.73 mmol) with a turnover number (TON) of 1092 (1524 in 24 h) and a turnover frequency (TOF) of 137 h −1 was achieved over the catalyst p ‐C3 at 40 bar p CO 2 / p H 2 (1:3) at 80°C. Advantageously, the catalyst p ‐C3 also efficiently hydrogenated potassium bicarbonate and potassium carbonate to formate. We further utilized the optimized process for demonstrating the conversion of CO 2 captured (via direct air capture) to formate through an integrated carbon capture and CO 2 hydrogenation process. Moreover, the catalyst p ‐C3 exhibited appreciable recyclability over multiple catalytic cycles for the reversible CO 2 /(bi)carbonate hydrogenation and formate dehydrogenation process. The key reaction intermediates, such as hydride species formed by treating the complex p ‐C3 with H 2 gas, revealed the role of such intermediates in achieving high catalytic activity for CO 2 hydrogenation over the diruthenium catalysts.
- 26 July 2026
- Published by Wiley in Chemistry – An Asian Journal
- Vol. 21 (14) , e70908
Diruthenium Catalyst for CO 2 and (Bi)carbonate Hydrogenation to Formate in Aqueous media
Highly efficient CO 2 and (bi)carbonate hydrogenation to formate in water was achieved by exploiting the cooperative interaction of the two ruthenium centers in a series of water‐soluble diruthenium complexes [{( η 6 ‐arene)RuCl} 2 ( μ ‐ κ 2 : κ 2 ‐benztetraimd)] 2+ containing the bridging meta ‐/ para ‐bis‐imidazole methane‐based ligands ( m ‐/ p ‐benztetraimd). Our findings revealed the pivotal role of the ligand structure in tuning the catalytic activity, where the catalyst p ‐C3 [{( η 6 ‐ p ‐cymene)RuCl} 2 ( μ ‐ κ 2 : κ 2 ‐ p ‐benztetraimd)] 2+ outperformed others. Consequently, a high formate yield (2.73 mmol) with a turnover number (TON) of 1092 (1524 in 24 h) and a turnover frequency (TOF) of 137 h −1 was achieved over the catalyst p ‐C3 at 40 bar p CO 2 / p H 2 (1:3) at 80°C. Advantageously, the catalyst p ‐C3 also efficiently hydrogenated potassium bicarbonate and potassium carbonate to formate. We further utilized the optimized process for demonstrating the conversion of CO 2 captured (via direct air capture) to formate through an integrated carbon capture and CO 2 hydrogenation process. Moreover, the catalyst p ‐C3 exhibited appreciable recyclability over multiple catalytic cycles for the reversible CO 2 /(bi)carbonate hydrogenation and formate dehydrogenation process. The key reaction intermediates, such as hydride species formed by treating the complex p ‐C3 with H 2 gas, revealed the role of such intermediates in achieving high catalytic activity for CO 2 hydrogenation over the diruthenium catalysts.
- 30 January 2024
- Published by Royal Society of Chemistry (RSC) in Dalton Transactions
- Vol. 53 (10) , 4363-4389
Recent progress in molecular transition metal catalysts for hydrogen production from methanol and formaldehyde
Hydrogen is considered as a potential alternative and sustainable energy carrier, but its safe storage and transportation are still challenging due to its low volumetric energy density. Notably, C1-based substrates, methanol and formaldehyde, containing high hydrogen contents of 12.5 wt% and 6.7 wt%, respectively, can release hydrogen on demand in the presence of a suitable catalyst. Advantageously, both methanol and aqueous formaldehyde are liquid at room temperature, and hence can be stored and transported considerably more safely than hydrogen gas. Moreover, these C1-based substrates can be produced from biomass waste and can also be regenerated from CO2, a greenhouse gas. In this review, the recent progress in hydrogen production from methanol and formaldehyde over noble to non-noble metal complex-based molecular transition metal catalysts is extensively reviewed. This review also focuses on the critical role of the structure–activity relationship of the catalyst in the dehydrogenation pathway.
- 30 January 2024
- Published by Royal Society of Chemistry (RSC) in Dalton Transactions
- Vol. 53 (10) , 4363-4389
Recent progress in molecular transition metal catalysts for hydrogen production from methanol and formaldehyde
Hydrogen is considered as a potential alternative and sustainable energy carrier, but its safe storage and transportation are still challenging due to its low volumetric energy density. Notably, C1-based substrates, methanol and formaldehyde, containing high hydrogen contents of 12.5 wt% and 6.7 wt%, respectively, can release hydrogen on demand in the presence of a suitable catalyst. Advantageously, both methanol and aqueous formaldehyde are liquid at room temperature, and hence can be stored and transported considerably more safely than hydrogen gas. Moreover, these C1-based substrates can be produced from biomass waste and can also be regenerated from CO2, a greenhouse gas. In this review, the recent progress in hydrogen production from methanol and formaldehyde over noble to non-noble metal complex-based molecular transition metal catalysts is extensively reviewed. This review also focuses on the critical role of the structure–activity relationship of the catalyst in the dehydrogenation pathway.