Low-temperature water-gas shift reaction over supported Cu catalysts

Renewable Energy

Volumn 65, Issue , 2014, Pages 102-107

  Jeong, Dae Woon ^a   Jang, Won Jun ^a   Shim, Jae Oh ^a   Han, Won Bi ^a   Roh, Hyun Seog ^a   Jung, Un Ho ^b   Yoon, Wang Lai ^b  

^a Yonsei University Wonju   (South Korea)

^b Korea Institute of Energy Research (KIER)   (South Korea)

Author keywords

Co precipitated; Cu; Easier reducibility; Low temperature water gas shift reaction; Nano sized CeO2; Preparation method

Indexed keywords

CO-PRECIPITATED; EASIER REDUCIBILITY; LOW-TEMPERATURE WATER-GAS SHIFT; NANO-SIZED CEO2; PREPARATION METHOD;

CARBON DIOXIDE; CATALYST ACTIVITY; COPPER; WATER GAS SHIFT;

CATALYST SUPPORTS;

CARBON DIOXIDE; CATALYSIS; CATALYST; CERIUM; COPPER; LOW TEMPERATURE; PRECIPITATION (CHEMISTRY); REDUCTION; RENEWABLE RESOURCE; SURFACE AREA;

EID: 84892807061     PISSN: 09601481     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.renene.2013.07.035     Document Type: Article

References (37)

1. Rodriguez J.A., Liu P., Wang X., Wen W., Hanson J., Hrbek J., et al. Water-gas shift activity of Cu surfaces and Cu nanoparticles supported on metal oxides. Catal Today 2009, 143:45-50.
2. Subramanian V., Potdar H.S., Jeong D.-W., Shim J.-O., Jang W.-J., Roh H.-S., et al. Synthesis of a novel nano-sized Pt/ZnO catalyst for water gas shift reaction in medium temperature application. Catal Lett 2012, 142:1075-1091.
3. Rostrup-Nielsen J.R. Catalytic steam reforming. Catalysis, science and technology 1984, Springer, Berlin. J.R. Anderson, M. Boudart (Eds.).
4. 2 production from methane. JMol Catal A: Chem 2002, 181:137-142.
5. Liu Z.-W., Jun K.-W., Roh H.-S., Park S.-E. Hydrogen production for fuel cells through methane reforming at low temperatures. JPower Sources 2002, 111:283-287.
6. Liu Z.-W., Roh H.-S., Jun K.-W. Important factors on carbon dioxide reforming of methane over nickel-based catalysts. JInd Eng Chem 2003, 9:753-761.
7. Yahiro H., Murawaki K., Saiki K., Yamamoto T., Yamaura H. Study on the supported Cu-based catalysts for the low-temperature water-gas shift reaction. Catal Today 2007, 126:436-440.
8. Fu Q., Saltsburg H., Flytzani-Stephanopoulos M. Active nonmetallic Au and Pt species on ceria-based water-gas shift catalysts. Science 2003, 301:935-938.
9. Trimm D.L., Önsan Z.I. Onboard fuel conversion for hydrogen-fuel-cell-driven vehicles. Catal Rev Sci Eng 2001, 43:30-84.
10. Thomas J.M., Thomas W.J. Principles and practice of heterogeneous catalysis 1997, VCH, New York.
11. Burch R. Gold catalysts for pure hydrogen production in the water-gas shift reaction: activity, structure and reaction mechanism. Phys Chem Chem Phys 2006, 8:5483-5500.
12. Marino F., Descorme C., Duprez D. Supported base metal catalysts for the preferential oxidation of carbon monoxide in the presence of excess hydrogen (PROX). Appl Catal B: Environ 2005, 58:175-183.
13. 2 catalyst activity for water-gas shift reaction. Appl Catal A: Gen 2008, 347:23-33.
14. Liu X., Guo P., Xie S., Pei Y., Qiao M., Fan K. Effect of Cu loading on Cu/ZnO water-gas shift catalysts for shut-down/start-up operation. Int J Hydrogen Energy 2012, 37:6381-6388.
15. Ma Z.-Y., Yang C., Wei W., Li W.-H., Sun Y.-H. Catalytic performance of copper supported on zirconia polymorphs for CO hydrogenation. JMol Catal A: Chem 2005, 231:75-81.
16. Figueiredo R.T., Ramos A.L.D., De Andrade H.M.C., Fierro J.L.G. Effect of low steam/carbon ratio on water gas shift reaction. Catal Today 2005, 107-108:671-675.
17. 2(111) and ZnO(0001): intrinsic activity and importance of support interactions. Angew Chem Int Ed 2007, 46:1329-1332.
18. 2 catalysts. Catal Lett 2002, 84:95-100.
19. Dell R.M., Stone F.S., Tiley P.F. The adsorption of oxygen and other gases on copper. Trans Faraday Soc 1953, 49:195-201.
20. 3 catalyst prepared by a homogeneous precipitation method using urea for direct internal reforming (DIR) in a molten carbonate fuel cell (MCFC). Chem Lett 2009, 38:1162-1163.
21. 2 catalysts for a single stage water gas shift reaction. Catal Lett 2012, 142:439-444.
22. Roh H.-S., Koo K.Y., Jung U.H., Yoon W.L. Hydrogen production from natural gas steam reforming over Ni catalysts supported on metal substrates. Curr Appl Phys 2010, 10:S37-S39.
23. 2 catalyst for water gas shift reaction at low temperature. Bull Kor Chem Soc 2011, 32:3557-3558.
24. Roh H.-S., Lee D.K., Koo K.Y., Jung U.H., Yoon W.L. Natural gas steam reforming for hydrogen production over metal monolith catalyst with efficient heat-transfer. Int J Hydrogen Energy 2010, 35:1613-1619.
25. 2 catalyst via a cerium hydroxy carbonate precursor for water gas shift reaction. Catal Lett 2011, 141:1268-1274.
26. 2 catalysts: redox features and catalytic behaviors. Appl Catal A: Gen 2005, 288:116-125.
27. 2 catalysts under severe conditions. Renew Energy 2012, 42:212-216.
28. 2) catalyst for water gas shift reaction in medium temperature application. Catal Today 2012, 185:113-118.
29. Roh H.-S., Jeong D.-W., Kim K.-S., Eum I.-H., Koo K.Y., Yoon W.L. Single stage water-gas shift reaction over supported Pt catalysts. Catal Lett 2011, 141:95-99.
30. 3 catalyst in combined steam and carbon dioxide reforming of methane for gas to liquid (GTL) process. Catal Lett 2009, 130:217-221.
31. 2) powders by microwave-hydrothermal (MH) route. Mater Chem Phys 2002, 74:306-312.
32. 2 catalysts. Catal Today 2004, 93-95:39-44.
33. Chuah G.K., Jaenicke S. The preparation of high surface area zirconia - influence of precipitating agent and digestion. Appl Catal A: Gen 1997, 163:261-273.
34. Trovarelli A., De Leitenburg C., Dolcetti G. Design better cerium-based oxidation catalysts. Chemtech 1997, 27:32-37.
35. 2 mixed oxide catalysts prepared via sol-gel technique: CO oxidation. Catal Today 2001, 68:53-61.
36. Kubacka A., Si R., Michorczyk P., Martínez-Aria A., Xu W., Hanson J.C., et al. Tungsten as an interface agent leading to highly active and stable copper-ceria water gas shift catalyst. Appl Catal B: Environ 2013, 132-133:423-432.
37. 3 for low temperature water-gas shift reaction. Fuel Process Technol 2010, 91:1438-1445.