초록 ▼

The present invention is concerned with the method of regenerating the fluidizable, catalytic, particulate solids in the regenerator section of an FCC process, and RCC process or a metals removal system or “ART”type process. It is directed to the use of a conduit means for charging fluidizing gaseou

The present invention is concerned with the method of regenerating the fluidizable, catalytic, particulate solids in the regenerator section of an FCC process, and RCC process or a metals removal system or “ART”type process. It is directed to the use of a conduit means for charging fluidizing gaseous material to a vertical cylindrical vessel for cooling fluidizable particulate solids flowing through said vertical cylindrical vessel, which conduit means comprises a horizontal header means having suspended therefrom a plurality of vertical and horizontally spaced apart conduits, each conduit having near its open end a restriction orifice. The header means is located near the top of the cylindrical cooling vessel. One portion of the vertical conduits has lower ends located in the upper half of the vessel and a second portion of the vertical conduits has lower ends located in a lower half of the vessel.

대표청구항 ▼

In an improved solid particulate material regeneration system comprising collected fluidized mass(es) of said solid particulate material, the improvement which comprises: A. regenerating the solid particulate material by combustion of deposited hydrocarbonaceous material on said solid particulate ma

In an improved solid particulate material regeneration system comprising collected fluidized mass(es) of said solid particulate material, the improvement which comprises: A. regenerating the solid particulate material by combustion of deposited hydrocarbonaceous material on said solid particulate material in a plurality of separate stages arranged for sequential flow of solid particulate material therethrough under regeneration temperature conditions maintained less than 816°C. (1,500°F.); B. accomplishing said regenerating of solid particulate material in the upper stage of regeneration under conditions providing a flue gas recovered therefrom at an elevated temperature up to about 760°C. (1,400°F.); C. cooling said solid particulate material flowing downwardly counter-current to fluidized gas in a heat-exchange zone to provide partially-cooled solid particulate material, said heat-exchange zone being provided with a plurality of upwardly extending liquid-carrying heat-exchange conduit combinations and a means for charging said fluidizing gas to a lower half and an upper half of said heat-exchange zone, said means comprising a header means located near the upper end of said heat-exchange zone and having suspended from said header means a plurality of vertical aeration conduits, a first portion of said vertical aeration conduits having their lower ends located in said lower half of said heat-exchange zone and a second portion of said vertical aeration conduits having their lower ends located in said upper half of said heat-exchange zone.