1
Robert F Millar, Paul J Persico, Robert H Jensen: Moving-bed radial flow solids-fluid contacting apparatus. UOP, James R Hoatson Jr, John F Spears Jr, William H Page II, August 29, 1978: US04110081 (20 worldwide citation)

An improved radial flow moving bed reactor, or other type of fluid-solid contacting vessel, in which stagnant catalyst volumes are reduced. The improvement results from the placement of a plurality of catalyst collection scoops or a single discoid cover plate just above the catalyst withdrawal condu ...


2
Millar Robert Fredrick, Jensen Robert Hugh: Moving bed radial flow solids-fluid contacting apparatus.. UOP, December 20, 1978: EP0000094-A1

The invention concerns an improved radial flow solids-fluid contacting apparatus (1) in which radial flow of fluid (liquid or gas) coacts with downward flow of the solids in particle form. The invention concerns the design and placement of particle collection scoops (8) close to the bottom of the be ...


3
Millar Robert F, Jensen Robert H, Persico Paul J: Traduction non-disponible, Moving bed radial flow solids-fluid contacting apparatus. UOP, MACRAE & CO, May 19, 1981: CA1101195

* * ABSTRACT * * An improved radial flow moving bed reactor, or other type of fluid-solid contacting vessel, in which stagnant catalyst volumes are reduced. The improvement results from the placement of a plurality of catalyst collection scoops which are attached to and extend above catalyst withdra ...


4
Moving-bed radial flow solids-fluid contacting apparatus. UOP, September 7, 1979: FR2416726-A1

{PG,1 An improved radial flow moving bed reactor, or other type of fluid-solid contacting vessel, in which stagnant catalyst volumes are reduced. The improvement results from the placement of a plurality of catalyst collection scoops or a single discoid cover plate just above the catalyst withdrawal ...


5
Moving bed radial flow solids-fluid contacting apparatus. UOP, September 3, 1980: GB2040718-A

{PG,1 An improved radial flow moving bed reactor, or other type of fluid-solid contacting vessel, in which stagnant catalyst volumes are reduced. The improvement results from the placement of a plurality of catalyst collection scoops or a single discoid cover plate just above the catalyst withdrawal ...