[EN] Alkali metal-doped MoVSbO catalysts have been prepared by impregnation of a MoVSbO-mixed oxide (prepared previously by a hydrothermal synthesis) and finally activated at 500 or 600 degrees C in N-2. The catalysts have been characterized and tested for the selective oxidation of propane and propylene. Alkali-doped catalysts improved in general the catalytic performance of MoVSbO, resulting more selective to acrylic acid and less selective to acetic acid than the corresponding alkali-free MoVSbO catalysts. However, the specific behaviour strongly depends on both the alkali metal added and/or the final activation temperature. At isoconversion conditions, catalysts activated at 600 degrees C present selectivity to acrylic acid higher than ...
Since the metal oxide catalysts used in many chemical processes show very high selectivity for the p...
Mixed oxides composed of the four metals Mo, V, Te, and Nb are known to be efficient catalysts in se...
Several parameters involved in preparing the modified Mo1V0.3Te0.23Nb0.12Ox catalysts system for the...
[EN] Alkali metal-doped MoVSbO catalysts have been prepared by impregnation of a MoVSbO-mixed oxide ...
Nb-free (SbO)(2)M(20)O(56) catalysts (M = Mo, V) presenting pure M1 phase have been prepared by a po...
The effects of preparation conditions (calcination mode, calcination atmosphere and calcination temp...
An effective Mo-1 V(0.3)Te(0.23)Nb(0.12)Ox catalysts for the selective oxidation of propane to acryl...
MoV(0.3)Te(0.23)Nb(0.12)O(x) catalysts were prepared by the slurry method in a rotary evaporator and...
Manganese promoted catalysts has been prepared at a fixed composition of Mo1V0.3Te0.23Nb0.125Mn≤nOx ...
The formation of phases during activation of MoVTeNb mixed oxides and transition metal doped MoVTeNb...
Acrylic acid synthesis is currently based on propylene generated mainly by high-temperature processe...
The selective oxidation of propane to acrylic acid is potential to replace the current manufacture o...
Hydrothermal synthesis of MoVTeNbOx catalysts has been investigated. It has been shown that the phas...
[EN] MoVTeO and MoVTeNbO catalysts have been prepared, characterized (by XRD, Raman, IR. XPS, oxygen...
[EN] The effect of activation treatments of K-free and K-MoVSbO bronzes on either their physico-chem...
Since the metal oxide catalysts used in many chemical processes show very high selectivity for the p...
Mixed oxides composed of the four metals Mo, V, Te, and Nb are known to be efficient catalysts in se...
Several parameters involved in preparing the modified Mo1V0.3Te0.23Nb0.12Ox catalysts system for the...
[EN] Alkali metal-doped MoVSbO catalysts have been prepared by impregnation of a MoVSbO-mixed oxide ...
Nb-free (SbO)(2)M(20)O(56) catalysts (M = Mo, V) presenting pure M1 phase have been prepared by a po...
The effects of preparation conditions (calcination mode, calcination atmosphere and calcination temp...
An effective Mo-1 V(0.3)Te(0.23)Nb(0.12)Ox catalysts for the selective oxidation of propane to acryl...
MoV(0.3)Te(0.23)Nb(0.12)O(x) catalysts were prepared by the slurry method in a rotary evaporator and...
Manganese promoted catalysts has been prepared at a fixed composition of Mo1V0.3Te0.23Nb0.125Mn≤nOx ...
The formation of phases during activation of MoVTeNb mixed oxides and transition metal doped MoVTeNb...
Acrylic acid synthesis is currently based on propylene generated mainly by high-temperature processe...
The selective oxidation of propane to acrylic acid is potential to replace the current manufacture o...
Hydrothermal synthesis of MoVTeNbOx catalysts has been investigated. It has been shown that the phas...
[EN] MoVTeO and MoVTeNbO catalysts have been prepared, characterized (by XRD, Raman, IR. XPS, oxygen...
[EN] The effect of activation treatments of K-free and K-MoVSbO bronzes on either their physico-chem...
Since the metal oxide catalysts used in many chemical processes show very high selectivity for the p...
Mixed oxides composed of the four metals Mo, V, Te, and Nb are known to be efficient catalysts in se...
Several parameters involved in preparing the modified Mo1V0.3Te0.23Nb0.12Ox catalysts system for the...