A systematic physical and chemical analysis of different industrial microspherical supports based on thermochemically activated aluminum trihydrate (TCA-ATH) has been performed in order to improve and optimize supports for the production of isobutane dehydrogenation alumina-chromia catalysts. It has been demonstrated that the phase composition of TCA-ATH products and their structure plays an important role in their synthesis of catalysts on their basis. According to results of physical and chemical research of supports supplied by different producers, an improvement of the industrial technology has been proposed. Preliminary thermal treatment of industrial microspheric products of thermochemical activation of aluminum trihydrate at 550°C un...
This publication continues a series of our reports on the optimization of preparation conditions for...
This publication continues a series of our reports on the optimization of preparation conditions for...
We analyze the effects of fluidized bed height, circulation ratio, and pressure drop in a reactor on...
A systematic physical and chemical analysis of different industrial microspherical supports based on...
A systematic physical and chemical analysis of different industrial microspherical supports based on...
For the purpose of improving the mechanical strength and reducing the abrasive activity of micro-sph...
For the purpose of improving the mechanical strength and reducing the abrasive activity of micro-sph...
For the purpose of improving the mechanical strength and reducing the abrasive activity of micro-sph...
The crystal and pore structures of a microspherical alumina-chromium catalyst calcined at 800-1100 C...
The crystal and pore structures of a microspherical alumina-chromium catalyst calcined at 800-1100 C...
For the purpose of improving the mechanical strength and reducing the abrasive activity of micro-sph...
The crystal and pore structures of a microspherical alumina-chromium catalyst calcined at 800-1100 C...
The crystal and pore structures of a microspherical alumina-chromium catalyst calcined at 800-1100 C...
This publication continues a series of our reports on the optimization of preparation conditions for...
This publication continues a series of our reports on the optimization of preparation conditions for...
This publication continues a series of our reports on the optimization of preparation conditions for...
This publication continues a series of our reports on the optimization of preparation conditions for...
We analyze the effects of fluidized bed height, circulation ratio, and pressure drop in a reactor on...
A systematic physical and chemical analysis of different industrial microspherical supports based on...
A systematic physical and chemical analysis of different industrial microspherical supports based on...
For the purpose of improving the mechanical strength and reducing the abrasive activity of micro-sph...
For the purpose of improving the mechanical strength and reducing the abrasive activity of micro-sph...
For the purpose of improving the mechanical strength and reducing the abrasive activity of micro-sph...
The crystal and pore structures of a microspherical alumina-chromium catalyst calcined at 800-1100 C...
The crystal and pore structures of a microspherical alumina-chromium catalyst calcined at 800-1100 C...
For the purpose of improving the mechanical strength and reducing the abrasive activity of micro-sph...
The crystal and pore structures of a microspherical alumina-chromium catalyst calcined at 800-1100 C...
The crystal and pore structures of a microspherical alumina-chromium catalyst calcined at 800-1100 C...
This publication continues a series of our reports on the optimization of preparation conditions for...
This publication continues a series of our reports on the optimization of preparation conditions for...
This publication continues a series of our reports on the optimization of preparation conditions for...
This publication continues a series of our reports on the optimization of preparation conditions for...
We analyze the effects of fluidized bed height, circulation ratio, and pressure drop in a reactor on...