| 1 |
Increase in stability of BaCo/CeO2 catalyst by optimizing the loading amount of Ba promoter for high-temperature water-gas shift reaction using waste-derived synthesis gas
Lee YL, Kim KJ, Jang WJ, Shim JO, Jeon KW, Na HS, Kim HM, Bae JW, Nam SC, Jeon BH, Roh HS
Renewable Energy, 145, 2715, 2020 |
| 2 |
Design and scale-up of a Cr-free Fe-Al-Cu catalyst for hydrogen production from waste-derived synthesis gas
Jang WJ, Shim JO, Jeon KW, Na HS, Kim HM, Lee YL, Roh HS, Jeong DW
Applied Catalysis B: Environmental, 249, 72, 2019 |
| 3 |
Effect of alkali and alkaline earth metal on Co/CeO2 catalyst for the water gas shift reaction of waste derived synthesis gas
Lee YL, Jha A, Jang WJ, Shim JO, Rode CV, Jeon BH, Bae JW, Roh HS
Applied Catalysis A: General, 551, 63, 2018 |
| 4 |
High-Temperature Water Gas Shift Reaction Over Fe/Al/Cu Oxide Based Catalysts Using Simulated Waste-Derived Synthesis Gas
Jeong DW, Subramanian V, Shim JO, Jang WJ, Seo YC, Roh HS, Gu JH, Lim YT
Catalysis Letters, 143(5), 438, 2013 |
| 5 |
H-2 production from high temperature shift of the simulated waste derived synthesis gas over magnetite catalysts prepared by citric acid assisted direct synthesis method
Subramanian V, Jeong DW, Han WB, Jang WJ, Shim JO, Roh HS
International Journal of Hydrogen Energy, 38(21), 8699, 2013 |
