2001
DOI: 10.1016/s1566-7367(01)00043-7
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Titania supported ruthenium as a coking-resistant catalyst for high pressure dry reforming of methane

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Cited by 97 publications
(47 citation statements)
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“…As the estimation indicates that the temperature range from 700 to 835 °C is appropriate for the CH 4 dry reforming, the reaction temperature was decided on 780°C in the present study. This temperature is consistent with those reported by a lot of researches [4,5,7,8,14]. Figure 4 shows the CH 4 conversion over NiO prepared from the anode material as a function of reaction time.…”
Section: Ch 4 Dry Reformingsupporting
confidence: 90%
See 1 more Smart Citation
“…As the estimation indicates that the temperature range from 700 to 835 °C is appropriate for the CH 4 dry reforming, the reaction temperature was decided on 780°C in the present study. This temperature is consistent with those reported by a lot of researches [4,5,7,8,14]. Figure 4 shows the CH 4 conversion over NiO prepared from the anode material as a function of reaction time.…”
Section: Ch 4 Dry Reformingsupporting
confidence: 90%
“…It has been known that noble metal (Pt, Rh, Ru, Pd and Ir) supported catalysts had good catalytic performance for the CH 4 dry reforming [1][2][3][4][5][6][7][8][9]. However, the development of cheap metal catalyst has been desired, because the noble metal catalyst is not suitable for utilizing on a large scale.…”
Section: Introductionmentioning
confidence: 99%
“…10). The conversion of reactants and selectivity of the products was dependent on number of active sites, size of the active metal (Ni) and the reducibility of the active (Ni) species [59,60,66,[73][74][75][76]. With increasing wt% of Ni loading Ni dispersion was increased upto 3.0 wt% Ni but above that the Ni dispersion was found to be decreasing.…”
Section: Effect Of Ni Loadingmentioning
confidence: 99%
“…A number of studies have claimed that the nature of the support strongly affects the catalytic behavior and carbon deposition during methane dry reforming [15][16][17][18][19][20]. The supports that have been explored in an effort to enhance catalyst performance and control carbon deposition are alumina, SiO 2 , ZrO 2 , and TiO 2 .…”
Section: Introductionmentioning
confidence: 99%
“…The supports that have been explored in an effort to enhance catalyst performance and control carbon deposition are alumina, SiO 2 , ZrO 2 , and TiO 2 . Among these, TiO 2 has been reported to be an excellent support for suppressing carbon deposition [15][16][17][19][20][21][22][23][24][25][26]. The TiO x species partially reduced by H 2 treatment, the pre-treatment for catalyst activation, migrate to metal particles, and then provide Me-O v -Ti 3+ sites.…”
Section: Introductionmentioning
confidence: 99%