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| 1 | Activity enhancement by acetic acid in cyclohexane oxidation using Ti-containing zeolite catalyst 显示文摘 | Limtrakul J | 2002 | Appl Catal A: Gen2002，233，： | 1 |
| 2 | Catalytic deoxygenation ofbenzaldehyde over gallium-modified ZSM-5 zeolite 显示文摘 | Ausavasukhi A Sooknoi T Resasco D E | 2009 | Journal ofCatalysis2009，268，1： | 1 |
| 3 | Activity enhancement by acetic acid in cyclohexane oxidation using Ti - containing zeolite catalyst显示文摘 | SOOKNOI T LIMTRAKUL J | 2002 | Appl Catal A2002，233，： | 1 |
| 4 | Regioselective alkane oxygenation with H2O2 catalyzed by titanosilicalite TS-1显示文摘 | Shul' pin G B Sooknoi T Romakh V B | 2006 | Tetrahedron Letters2006，47，18： | 1 |
| 5 | Kinetics and Mecha- nism of Hydrogenation of Furfural on Cu/SiO2 Catalysts 显示文摘 | Sitthisa S Sooknoi T Ma Yuguang | 2011 | J Catal2011，277，1： | 1 |
| 6 | Regioselective alkane oxygenation with H202 catalyzed by titanosilicalite TS-1 显示文摘 | Shul' pin G B Sooknoi T Romakh V B | 2006 | Tetrahedron Letters2006，47，18： | 1 |
| 7 | Activity enhancement by acetic acid in cyclohexane oxidation using Ti-containing zeolite catalyst显示文摘 | SOOKNOI T LIMTRAKUL J | 2002 | Appl Catal A:Gen2002，233，： | 1 |
| 8 | Direct conversion of glyc- erol to acrylic acid via integrated dehydration-oxidation bed system显示文摘 | Witsuthammakul A Sooknoi T | 2012 | Applied Catalysis A: General2012，，： | 1 |
| 9 | Selective conversion of m-cresol to toluene over bimetallic Ni–Fe catalysts显示文摘 | Lei Nie Priscilla M. de Souza Fabio B. Noronha Wei An Tawan Sooknoi Daniel E. Resasco | 2013 | Journal of Molecular Catalysis. A, Chemical2013，，： | 1 |
| 10 | Activity enhancenent by acetic acid in cyclohexane oxidation using Ti-containing zeolite catalyst显示文摘 | Jumras Limtrakul | 2002 | Applied Catalysis A:General2002，，233： | 1 |
| 11 | Selective Ethylene Permeable Zeolite Composite Double-Layered Film for Novel Modified Atmosphere Packaging显示文摘 | MONPRASIT P RITVIRULH C SOOKNOI T et al | 2011 | Polymer Engineering & Science2011，51，7： | 1 |
| 12 | Additional Brensted acid sites in HZSM-5 formed by the presence of water显示文摘 | AUSAVASUKHI A SOOKNOI T | 2009 | Applied Catalysis A:General2009，361，12： | 1 |
| 13 | Activity enhancement by acetic acid in cyclohexane oxidation using Ti - containing zeolite catalyst 显示文摘 | SOOKNOI T LIMTRAKUL J | 2002 | Appl Catal A : Gen2002，233，： | 1 |
| 14 | Regioselective alkane oxygenation with H2O2 by titanosilicalite TS-1显示文摘 | Georgiy B Shul'pin Tawan Sooknoi Vladimir B Romakh | 2006 | Tetrahedron Letters2006，47，： | 1 |
| 15 | Activity enhancement by acetic acid in cyclohexane oxidation using Ti-containing zeolite catalyst显示文摘 | SOOKNOI TAWAN LIMTRAKUL JUMRAS | 2002 | Appl Cat A:Gen2002，233，12： | 1 |
| 16 | Activity enhancement by acetic acid in cyclohexane oxidation using Ti-containing zeolite catalyst显示文摘 | Sooknoi T Limt rakul J | 2002 | Appl Catal A: Gen2002，233，： | 1 |
| 17 | Ammoximation of Cyclohexanone in Acetic Acid Using Titanium Siliealite-1 Catalyst:Activity and Reaction Pathway 显示文摘 | Sooknoi T Chitranuwatkul V | 2005 | J Mol Catal A-Chem2005，236，1： | 1 |
| 18 | Activity Enhancement by Acetic Acid in Cyclohexane Oxidation using Ti-Containing Zeolite Catalyst显示文摘 | Sooknoi T Limtrakul L | 2002 | J Appl Catal A : Gen2002，233，： | 1 |
| 19 | Reaction mechanism of aqueous-phase conversion of γ-valerolactone(GVL) over a Ru/C catalyst显示文摘The present work explores the reaction pathways of γ-valerolactone(GVL) over a supported ruthenium catalyst. The conversion of GVL in aqueous phase over a 5% Ru/C catalyst was investigated in a batch reactor operating at 463 K under 500–1000 psi of H_2. The main reaction products obtained under these conditions were 2-butanol(2-BuOH), 1,4-pentanediol(1,4-PDO), 2-methyltetrahydrofuran(2-MTHF) and 2-pentanol(2-PeOH). A complete reaction network was developed, identifying the primary and/or secondary products. In this reaction network, production of 2-BuOH via decarbonylation of a ring-opened surface intermediate CH_3CH(O*)–(CH_2)_2–CO*is clearly the dominant pathway. From the evolution of products as a function of reaction time and theoretical(DFT) calculations, a mechanism for the formation of intermediates and products is proposed. The high sensitivity of 2-BuOH production to the presence of CO, compared to a much lower effect on the production of the other products indicates that the sites responsible for decarbonylation are particularly prone to CO adsorption and poisoning. Also, since the decarbonylation rate is not affected by the H2 pressure it is concluded that the direct decarbonylation path of the CH_3CH(O*)–(CH_2)_2–CO*intermediate does not required a previous dehydrogenation step, as is the case in decarbonylation of short alcohols. | Abigail Rozenblit Adam J.Avoian Qiaohua Tan Tawan Sooknoi Daniel E.Resasco | 2016 | Journal of Energy Chemistry2016，25，6： | 0 |
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