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31篇 您的检索式:作者名="Vitidsant"
    题名 作者 年代 出处 被引量
1Sputtered nano-cobalt on H-USY zeolite for selectively converting syngas to gasoline显示文摘Selectively converting CO and H2 to gasoline product(isoparaffin and olefin) in one step still remains a great challenge. We demonstrate effective H-USY zeolite supported nano-cobalt bifunctional catalysts for this catalytic reaction, which are prepared by the novel physical sputtering process. Particles of the sputtered cobalt exist in nano-level and are well-dispersed on acid USY zeolite. Easy activation of the loaded nano-cobalt is also achieved in a low-temperature hydrogen reduction atmosphere. In the tandem catalytic reaction, the sputtered bifunctional Co/USY catalyst exhibits a much higher CO conversion and higher isoparaffin selectivity than the conventional impregnated one. Compared with H-Mor, H-Beta and other zeolites supported catalysts, H-USY zeolite supported cobalt catalyst shows the clearest promotional effect on the activity of FischerTropsch synthesis. The described synthesis herein provides a new pathway to solve the problem caused by the strong metal-support interaction(MSI) in heterogeneous catalysis.Peng Lu Jian Sun Pengfei Zhu Takayuki Abe Ruiqin Yang Akira Taguchi Tharapong Vitidsant Noritatsu Tsubaki 2015Journal of Energy Chemistry2015,24,5:2
2Catalytic cracking reaction of used lubricating oil to liquid fuels catalyzed by sulfated zirconia 显示文摘Permsubscul A Vitidsant T Damronglerd S 2007Korean J Chem Eng2007,24,:1
3Highly active Fischer-Tropsch synthesis Co/SiO2 catalysts prepared from microwave irradiation显示文摘Reubroyeharoen P Vitidsant T Liu Y 2007Catalysis Communications2007,8,3:1
4Continuous Low-temperature Methanol Synthesis from Syngas Using Alcohol Promoters 显示文摘Reubroycharoen P Yamagami T Vitidsant T 2003Energy Fuels2003,17,4:1
5Highly active Fischer-Tropsch synthesis Co/SiO2 catalysts prepared from microwave irradiation显示文摘Reubroycharoen Prasert Vitidsant Tharapong Liu Yong 2007Catalysis Communications2007,8,3:1
6Production of activated carbon from palm oil shell by pyrolysis and steam activation in a fixed bed reactor 显示文摘VITIDSANT T SURAVATTANASAKUL T DAMRONGLERD S 1999Science Asia1999,25,4:1
7Highly efficient sulfur and coking resistance catalysts for tar gasification with steam显示文摘SRINAKRUANG J SATO K VITIDSANT T 2006Fuel2006,85,17:1
8Iso-butanol direct synthesis from syngas over the alkali metals modified Cr/ZnO catalysts显示文摘TAN L YANG G H YONEYAMA Y KOU Y L TAN Y H VITIDSANT T TSUBAKI N 2015Appl Catal A: Gen2015,505,:1
9A highly efficient catalyst for tar gasification with steam显示文摘SRINAKRUANG J SATO K VITIDSANT T 2005Catalysis communications2005,6,6:1
10A highly efficient catalyst for tar gasification with steam显示文摘SRINAKRUANG J SATO K VITIDSANT T 2005Catalysis communications2005,6,6:1
11Highly active Fischer-Tropsch synthesis Co/SiO2 catalysts prepared from microwave irradiation显示文摘Vitidsant T Liu Y Yang G H 2007Catalysis Communications2007,8,3:1
12Highly efficient sulfur and eoking resistanee catalysts for tar gasification with steam显示文摘Srinakruang J Sato K Vitidsant T 2006Fuel2006,,85:1
13Highly active Fischer-Tropsch synthesis Co/Si O2catalysts prepared from microwave irradiation显示文摘REUBROYCHAROEN P VITIDSANT T LIU Y 2007Catalysis Communications2007,8,3:1
14Development of a new low-temperature methanol synthesis process 显示文摘Reubroycharoen P Vitidsant T Yoneyama Y Tsubaki N 2004Catalysis Today2004,89,4:1
15A new method of low temperature methanol synthesis 显示文摘Xu B L Yang R Meng F Z Reubroycharoen P Vitidsant T Zhang Y Yoneyama Y Tsubaki N 2009Catalysis Surveys from Asia2009,13,3:1
16A highly efficient catalyst for tar gasification with steam 显示文摘SRINAKRUANG J SATO K VITIDSANT T 2005Catalysis Communications2005,6,6:1
17Active Fischer-Tropsch synthesis Fe-Cu-K/SiO_2 catalysts prepared by autocombustion method without a reduction step显示文摘The purpose of this study was to prepare iron-based catalysts supported on silica by autocombustion method for directly using for Fischer-Tropsch synthesis(FTS) without a reduction step. The effect of different citric acid(CA):iron nitrate(N) molar ratios and acid types on the FTS performance of catalysts were investigated. The CA:N molar ratios had an important influence on the formation of iron active phases and FTS activity. The iron carbide(Fe_xC), which is known to be one of the iron active phases, was demonstrated by the X-ray diffraction and X-ray photoelectron spectroscopy. Increasing the CA:N molar ratios up to 0.1 increased CO conversion of catalyst to 86.5%, which was then decreased markedly at higher CA:N molar ratios. An excess of CA resulted in carbon residues covering the catalyst surface and declined FTS activity. The optimal catalyst(CA:N molar ratio = 0.1) achieved the highest CO conversion when compared with other autocombustion catalysts as well as reference catalyst prepared by impregnation method, followed by a reduction step. The autocombustion method had the advantage to synthesize more efficient catalysts without a reduction step. More interestingly, iron-based FTS catalysts need induction duration at the initial stage of FTS reaction even after reduction, because metallic iron species need time to be transformed to Fe_xC. But here, even if without reduction, Fe_xC was formed directly by autocombustion and induction period was eliminated during FTS reaction.Suthasinee Pengnarapat Peipei Ai Prasert Reubroycharoen Tharapong Vitidsant Yoshiharu Yoneyama Noritatsu Tsubaki 2018Journal of Energy Chemistry2018,27,2:1
18Highly efficient sulfur and coking resistance catalysts for tar gasification with steam显示文摘Srinakruang J Sato K Vitidsant T 2006Fuel2006,85,1718:1
19Highly Efficient Sulfur and Coking Resistance Catalysts for Tar Gasification with Steam显示文摘Srinakruang J Sato K Vitidsant T 2006Fuel2006,85,1718:1
20An active and selective production of gasoline-range hydrocarbons over bifunctional Co-based catalysts显示文摘NGAMCHARUSSRIVICHAI C LIU X LI X VITIDSANT T FUJIMOTO K 2007Fuel2007,86,12:1
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