IP Library › Granted Patent US 9,707,533
Granted Patent B2
US 9,707,533 · App. 14/955,344 · Granted Jul 18, 2017

Fluidized catalyst stripping unit for displacing entrained gas from catalyst particles

Inventor: Matthew T. Pretz (Lake Jackson, TX)
Assignee: Dow Global Technologies LLC
B01J8/34B01J2208/00991
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Quick Facts
Patent No.
US 9,707,533
App. No.
14/955,344
Granted
Jul 18, 2017
Kind
B2
Abstract

A fluidized catalyst stripping unit for displacing entrained gas from catalyst particles comprising: a vessel housing a two stage cyclonic separation section which comprises one or more primary cyclonic separation devices and one or more secondary cyclones; a stripping section which comprises internals; and an inlet in fluid communication with a catalytic reactor to feed a particulate-fluid suspension to the two stage cyclonic separation section; wherein each primary cyclonic separation device comprises an internal cylindrical surface to separate a major fraction of the particulates from the suspension and form a vortex of reduced particulate content; a particulate discharge outlet from each secondary cyclone to the stripping section; wherein the particulate discharge outlet of the secondary cyclone is submerged in a catalyst bed located above the stripper internals, and wherein the stripping section comprises one or more bubble breaking grids within the catalyst bed and above the stripping internals is provided.

Claims (12)

1. A fluidized catalyst stripping unit for displacing entrained gas from catalyst particles comprising:

a vessel which houses

a two stage cyclonic separation section which comprises one or more primary cyclonic separation devices and one or more secondary cyclones;

a stripping section which comprises internals and one or more bubble breaking grids supported by a hinged support system;

an inlet in fluid communication with a catalytic reactor to feed a particulate-fluid suspension to the two stage cyclonic separation section; and

a particulate discharge outlet from each secondary cyclone to the stripping section;

wherein:

each primary cyclonic separation device comprises an internal cylindrical surface to separate a major fraction of the particulates from the suspension and form a vortex of reduced particulate content;

the particulate discharge outlet of the secondary cyclone is submerged in a catalyst bed which is located above the stripper internals within the stripping section; and

the one or more bubble breaking grids are located within the catalyst bed and above the stripping internals.

2. The fluidized catalyst stripping unit according to claim 1 , wherein the one or more bubble breaking grids are selected from the group consisting of subway grating, chevrons, packing, round bars, pipes, flat bars, and angle irons.

3. The fluidized catalyst stripping unit according to claim 1 , wherein the one or more bubble breaking grids are supported by a cantilevered support system.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 15, 2017
From: PRETZ, MATTHEW T.
To: DOW GLOBAL TECHNOLOGIES LLC
Reel/Frame 041584/0087 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 24, 2016
From: PRETZ, MATTHEW T.
To: DOW GLOBAL TECHNOLOGIES LLC
Reel/Frame 037813/0134 →
Continuity (1)
Related Publication 20170151544A1 · Jun 1, 2017