Gas distributors for circulating fluidized bed reactors
Abstract
A distributor for a circulating dry scrubber reactor includes a venturi section with a venturi section wall extending from a venturi section inlet to a venturi section outlet along a longitudinal axis, with the venturi section inlet connected to an inlet plenum and the venturi section outlet connected to a circulating dry scrubber reactor. A hub is mounted within the venturi section wall with an annular converging-diverging flow path defined between the venturi section wall and the hub for distribution of gas flow from the venturi section outlet into a circulating dry scrubber reactor space and for maintaining stable bed fluidization in a CDS system at a comparatively low system pressure loss.
Claims
exact text as granted — not AI-modified1 . A distributor for a circulating dry scrubber reactor comprising:
a venturi section including a venturi section wall extending from a venturi section inlet to a venturi section outlet along a longitudinal axis, wherein the venturi section outlet is configured and adapted to be connected to a circulating dry scrubber reactor; a hub mounted within the venturi section wall with an annular converging-diverging flow path defined between the venturi section wall and the hub for distribution of gas flow from the venturi section outlet into a circulating dry scrubber reactor space and for maintaining stable bed fluidization; an inlet plenum connected upstream of the venturi section inlet to supply a flow of gas to the annular converging-diverging flow path, wherein the inlet plenum includes an elbow section; and at least one ladder vane mounted inside the elbow section, wherein the at least one ladder vane and the elbow section are configured to turn a flow of gas from the inlet plenum toward the venturi section inlet.
2 . (canceled)
3 . A distributor as recited in claim 1 , wherein at least one portion of the venturi section wall defines a frustoconical wall and the frustoconical wall tapers inward toward the hub.
4 . A distributor as recited in claim 3 , wherein the frustoconical wall and a corresponding part of the hub define a converging area of the converging-diverging flow path.
5 . A distributor as recited in claim 3 , wherein the frustoconical wall and a corresponding part of the hub define a diverging area of the converging-diverging flow path.
6 . A distributor as recited in claim 1 , wherein a portion of the venturi section wall defines a cylindrical wall.
7 . A distributor as recited in claim 6 , wherein the cylindrical wall and a corresponding part of the hub define a diverging area of the converging-diverging flow path.
8 . A distributor as recited in claim 1 , wherein the hub includes an inlet section that defines a converging portion of the flow path in a direction from the venturi section inlet to the venturi section outlet, and wherein the hub includes an outlet section that defines a diverging portion of the flow path in the direction from the venturi section inlet to the venturi section outlet.
9 . A distributor as recited in claim 8 , wherein the inlet section of the hub is substantially conical.
10 . A distributor as recited in claim 9 , wherein the inlet section cone has a conical angle of about 60° to about 90°.
11 . A distributor as recited in claim 8 , wherein the outlet section of the hub is substantially conical.
12 . A distributor as recited in claim 11 , wherein the outlet section cone has a conical angle of about 40° to about 90°.
13 . A distributor as recited in claim 8 , wherein the inlet section of the hub is substantially hemispherical.
14 . A distributor as recited in claim 8 , wherein the outlet section of the hub is frustoconical.
15 . A distributor as recited in claim 11 , wherein a tip portion of the outlet section cone defines a frustocone truncated about 7% to about 12% short of a full cone.
16 . A distributor as recited in claim 14 , wherein a lifting ring is mounted to the truncated tip portion of the hub outlet section.
17 . A distributor as recited in claim 8 , wherein the hub includes a cylindrical section connecting the inlet and outlet sections of the hub.
18 . A distributor as recited in claim 8 , wherein the inlet section of the hub has a vertex with an axial position at or below the venturi section inlet of the venturi section wall relative to the longitudinal axis.
19 . A distributor as recited in claim 8 , wherein the outlet section of the hub has a high axial point at a common axial position with the venturi section outlet of the venturi section wall relative to the longitudinal axis.
20 . A distributor as recited in claim 1 , wherein the hub has a diameter of at least about 58% that of the venturi section wall.
21 . A distributor as recited in claim 1 , wherein the hub has a diameter of about 40% to about 90% of that of the venturi section wall.
22 . A distributor as recited in claim 1 , wherein the venturi section wall has a diameter and a length in an axial direction with respect to the longitudinal axis, wherein the length of the venturi section wall is at least about 70% to about 140% as long as the diameter of the cylindrical wall.
23 . A distributor as recited in claim 1 , further comprising a plurality of supports, each mounting the hub to the venturi section wall.
24 . A distributor as recited in claim 1 , further comprising at least one support at an end of the hub, mounting the hub to the venturi section wall.
25 . A circulating dry scrubber comprising:
a circulating dry scrubber reactor with an inlet for introducing flue gas and a reactor space for circulating particles for treating flue gas within the reactor space; and a distributor as recited in claim 1 , wherein the venturi section outlet of the distributor is in fluid communication with the inlet of the reactor to supply flue gas thereto.
26 . A distributor for a circulating dry scrubber reactor comprising:
a venturi section including a venturi section wall extending from a venturi section inlet to a venturi section outlet along a longitudinal axis, wherein the venturi section outlet is configured and adapted to be connected to a circulating dry scrubber reactor; a hub mounted within the venturi section wall with an annular converging-diverging flow path defined between the venturi section wall and the hub for distribution of gas flow from the venturi section outlet into a circulating dry scrubber reactor space and for maintaining stable bed fluidization, wherein the hub includes an outlet section that defines a diverging portion of the flow path in the direction from the venturi section inlet to the venturi section outlet, wherein at least a portion of the outlet section of the hub is below the venturi section outlet of the venturi section wall relative to the longitudinal axis; an inlet plenum connected upstream of the venturi section inlet to supply a flow of gas to the annular converging-diverging flow path, wherein the inlet plenum includes an elbow section; and at least one ladder vane mounted inside the elbow section, wherein the at least one ladder vane and the elbow section are configured to turn a flow of gas from the inlet plenum toward the venturi section inlet.Cited by (0)
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