Effect of carbon dioxide pressure on 4-t-butylphenol hydrogenation activity of supported rhodium catalyst
| Title | Effect of carbon dioxide pressure on 4-t-butylphenol hydrogenation activity of supported rhodium catalyst | 
| Publication Type | Journal Article | 
| Year of Publication | 2013 | 
| Authors | Hiyoshi, N, Sato, O, Yamaguchi, A, Rode, CV, Shirai, M | 
| Journal | Journal of the Japan Petroleum Institute | 
| Volume | 56 | 
| Issue | 3 | 
| Pagination | 165-170 | 
| Date Published | MAY | 
| ISSN | 1346-8804 | 
| Keywords | 4-t-Butylphenol hydrogenation, Carbon dioxide solvent, Peng-Robinson equation, Rhodium catalyst, Supercritical fluid | 
| Abstract | Hydrogenation of 4-t-butylphenol over an activated carbon-supported rhodium catalyst in carbon dioxide solvent was analyzed based on phase observation with a view cell and calculations of the solubility of 4-t-butylphenol using the Peng-Robinson equation of state as a function of carbon dioxide pressure. The reaction experiments showed that the initial reaction rate of 4-t-butylphenol at 313 K under 2 MPa of hydrogen pressure was increased by the addition of carbon dioxide, especially above a total pressure of 11 MPa. Direct visual observation showed that the solubility of 4-t-butylphenol increased with higher carbon dioxide pressure. The calculations based on the Peng-Robinson equation of state also showed that the solubility of 4-t-butylphenol in the 4-t-butylphenol carbon dioxide hydrogen (2 MPa) system at 313 K significantly increased by addition of carbon dioxide above a total pressure of 11 MPa. We concluded that the increase in the hydrogenation rates was caused by the increased concentration of 4-t-butylphenol substrate in the carbon dioxide solvent.  |  
| Type of Journal (Indian or Foreign) | Foreign | 
| Impact Factor (IF) | 0.58 | 
