2004
DOI: 10.1016/j.matlet.2003.08.006
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Catalytic conversion of isopropanol over NiO/MgO system doped with Li2O

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Cited by 23 publications
(10 citation statements)
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References 34 publications
(34 reference statements)
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“…(b) The induced decrease in the surface area of 0.045FeAlO sample due to increasing the amount of Fe 2 O 3 loading from 4.5 to 6.5 mol % may be ascribed to the aggregation of small iron species into larger bulk particles of iron in preparation process [42]. (c) The slight increase in S BET value due to Ag 2 O-doping precalcined at 500˚C can be attributed to creation of new pores due to liberation of nitrogen oxides gases during the thermal decomposition of AgNO 3 dopant added [43]. (d) The observed significant decrease in S BET of the investigated samples as result of increasing the calcination temperature from 500 to 800˚C could be attributed to the sintering process.…”
Section: Surface Propertiesmentioning
confidence: 99%
“…(b) The induced decrease in the surface area of 0.045FeAlO sample due to increasing the amount of Fe 2 O 3 loading from 4.5 to 6.5 mol % may be ascribed to the aggregation of small iron species into larger bulk particles of iron in preparation process [42]. (c) The slight increase in S BET value due to Ag 2 O-doping precalcined at 500˚C can be attributed to creation of new pores due to liberation of nitrogen oxides gases during the thermal decomposition of AgNO 3 dopant added [43]. (d) The observed significant decrease in S BET of the investigated samples as result of increasing the calcination temperature from 500 to 800˚C could be attributed to the sintering process.…”
Section: Surface Propertiesmentioning
confidence: 99%
“…The interaction between the support and transition metal oxides can take place via the formation of metal aluminate in case of alumina support, or solid solution in case of MgO support [3,4] that having small catalytic activity if compared to metal oxide-supported solid. For this reason it is important to study the possibility of obtaining membranes which can not react with the catalytically active phase (transition metal oxide) and with low cost to be economic.…”
Section: Introductionmentioning
confidence: 99%
“…The catalytic activity and selectivity of the oxide catalyst can be modified by loading on different support materials [5,6]. The interaction between the support and transition metal oxide can take place via of formation metal aluminate in case of alumina-support, or solid solution in case of MgO support [7,8] having small catalytic activity if compared to metal oxide-supported solid. For this reason it is important to study the possibility of obtaining membranes which can not react with the catalytically active phase (transition metal oxide) and with low cost to be economic.…”
Section: Introductionmentioning
confidence: 99%