This paper explores the thermal and catalytic pyrolysis of HFC-134a over γ-Al2O3 calcined at temperatures of 550 °C (A550), 650 °C (A650), 750 °C (A750), and 850 °C (A850). The physicochemical properties of catalysts were studied through thermogravimetric analysis (TGA), Brunauer–Emmett–Teller equation for nitrogen physisorption analysis (BET), X-ray diffraction (XRD), and temperature-programmed desorption of ammonia (NH3-TPD). The non-catalytic pyrolysis of HFC-134a showed less than 15% decomposition of HFC-134a. Catalysts increased the decomposition as A650 revealed the highest decomposition efficiency by decomposing more than 95% HFC-134a for 8 h followed by A750, A850, and A550. The larger surface area and pore volume paired with a low ...
The activity of γ-alumina and γ-alumina promoted with transition metal chlorides for the hydrolytic ...
Thermal pyrolysis of halon 1211 (CBrClF2). diluted in nitrogen, in a tubular alumina reactor, has be...
The crystal and pore structures of a microspherical alumina-chromium catalyst calcined at 800-1100 C...
This paper evaluated the effect of calcination temperature and the use of Mg/Al2O3 on the decomposit...
In this study, the catalytic activity of γ-Al2O3 was investigated for the decomposition of NF3. Reac...
The catalytic activity of K₂-xO/AC for the decomposition of CHF₃ was investigated at temperatures be...
The catalytic activity of activated carbon (AC) and activated carbon supported potassium for the dec...
A series of alpha-Mo2C/gamma-Al2O3 catalysts with different Mo loadings were prepared by temperature...
This is an extension study of the thermal decomposition of 2H-heptafluoropropane (HFP), mainly aimin...
AbstractThe effect of calcination temperatures on dry reforming catalysts supported on high surface ...
The effect of calcination temperatures on dry reforming catalysts supported on high surface area alu...
The crystal and pore structures of a microspherical alumina-chromium catalyst calcined at 800-1100 C...
The effect of calcination temperatures on dry reforming catalysts supported on high surface area alu...
The catalytic activity of activated carbon (AC) and activated carbon supported potassium for the dec...
The effect of calcination temperature for the support and catalyst on the catalytic properties of th...
The activity of γ-alumina and γ-alumina promoted with transition metal chlorides for the hydrolytic ...
Thermal pyrolysis of halon 1211 (CBrClF2). diluted in nitrogen, in a tubular alumina reactor, has be...
The crystal and pore structures of a microspherical alumina-chromium catalyst calcined at 800-1100 C...
This paper evaluated the effect of calcination temperature and the use of Mg/Al2O3 on the decomposit...
In this study, the catalytic activity of γ-Al2O3 was investigated for the decomposition of NF3. Reac...
The catalytic activity of K₂-xO/AC for the decomposition of CHF₃ was investigated at temperatures be...
The catalytic activity of activated carbon (AC) and activated carbon supported potassium for the dec...
A series of alpha-Mo2C/gamma-Al2O3 catalysts with different Mo loadings were prepared by temperature...
This is an extension study of the thermal decomposition of 2H-heptafluoropropane (HFP), mainly aimin...
AbstractThe effect of calcination temperatures on dry reforming catalysts supported on high surface ...
The effect of calcination temperatures on dry reforming catalysts supported on high surface area alu...
The crystal and pore structures of a microspherical alumina-chromium catalyst calcined at 800-1100 C...
The effect of calcination temperatures on dry reforming catalysts supported on high surface area alu...
The catalytic activity of activated carbon (AC) and activated carbon supported potassium for the dec...
The effect of calcination temperature for the support and catalyst on the catalytic properties of th...
The activity of γ-alumina and γ-alumina promoted with transition metal chlorides for the hydrolytic ...
Thermal pyrolysis of halon 1211 (CBrClF2). diluted in nitrogen, in a tubular alumina reactor, has be...
The crystal and pore structures of a microspherical alumina-chromium catalyst calcined at 800-1100 C...