Add to ORKGA process is described for separating paraxylene from a multicomponent fluid mixture of C8 aromatics. A mixture of C8 aromatics is fed to a simulated moving-bed adsorptive apparatus. The location of the feed to the apparatus is moved at set intervals. The rate of flow of feed to the apparatus is varied during each interval to enhance the separation of paraxylene from the multicomponent mixture.Exxonmobil Chemical Patents Inc.Georgia Tech Research Corporatio
A simulated moving-bed (SMB) pilot plant, characterized by two unique features, the number of ports ...
Process intensification in distillation led to major developments, such as reactive distillation, he...
This design project explores the economic viability of a novel technology for the production of para...
A process to separate paraxylene from a mixture of paraxylene, metaxylene, orthoxylene, and ethylben...
Para-xylene is separated from a mixture of C8 aromatics using a simulated moving bed (SMB) adsorptio...
The process involves the use of two rotary valves to implement Varicol operation of a simulated movi...
Multifunctional reactors, which combine a reaction step and a separation step in one singl...
This work analyzes the use of process intensification in the production of p-xylene. Both separation...
A new hybrid process for the production of o- and p-xylene is proposed to replace the traditional pl...
A dual-bed Simulated Moving Bed Reactor (SMBR) is developed under the framework of a proposed aromat...
Multifunctional reactors, which combine a reaction step and a separation step in one single unit, c...
Dead volume classified as bed head, bed tail, and bed line affects the purity and recovery in indust...
Adsorptive separations are becoming increasingly important in chemical industry. The simulated movin...
The search for new adsorbents with enhanced capacity and selectivity, suitable for application on la...
Dead volume classified as bed head, bed tail, and bed line affects the purity and recovery in indust...
A simulated moving-bed (SMB) pilot plant, characterized by two unique features, the number of ports ...
Process intensification in distillation led to major developments, such as reactive distillation, he...
This design project explores the economic viability of a novel technology for the production of para...
A process to separate paraxylene from a mixture of paraxylene, metaxylene, orthoxylene, and ethylben...
Para-xylene is separated from a mixture of C8 aromatics using a simulated moving bed (SMB) adsorptio...
The process involves the use of two rotary valves to implement Varicol operation of a simulated movi...
Multifunctional reactors, which combine a reaction step and a separation step in one singl...
This work analyzes the use of process intensification in the production of p-xylene. Both separation...
A new hybrid process for the production of o- and p-xylene is proposed to replace the traditional pl...
A dual-bed Simulated Moving Bed Reactor (SMBR) is developed under the framework of a proposed aromat...
Multifunctional reactors, which combine a reaction step and a separation step in one single unit, c...
Dead volume classified as bed head, bed tail, and bed line affects the purity and recovery in indust...
Adsorptive separations are becoming increasingly important in chemical industry. The simulated movin...
The search for new adsorbents with enhanced capacity and selectivity, suitable for application on la...
Dead volume classified as bed head, bed tail, and bed line affects the purity and recovery in indust...
A simulated moving-bed (SMB) pilot plant, characterized by two unique features, the number of ports ...
Process intensification in distillation led to major developments, such as reactive distillation, he...
This design project explores the economic viability of a novel technology for the production of para...