Gasification system

• US 4,493,636 A
• Filed: 03/11/1983
• Issued: 01/15/1985
• Est. Priority Date: 03/05/1981
• Status: Expired due to Term

• Current Assignee: United States Of America As Represented By The Department Of Energy
• Original Assignee: United States Department of Energy
• Inventors: Cherish, Peter, Haldipur, Gaurang B., Anderson, Richard G.
• Primary Examiner(s): Dority, Jr., Carroll B.
• Application Number:
  US06/474,360
• Time in Patent Office: 676 Days
• Field of Search: 110/245, 122/4 D, 48/73, 48/77, 48/63, 422/145, 239/422, 239/424, 431/170, 431/187, 431/188
• US Class Current: 431/170
• CPC Class Codes: B01J 8/1827 the fluidising gas being a reactant
• CPC Class Codes: C10J 2200/152 Nozzles or lances for introducing gas, liquids or suspensions
• CPC Class Codes: C10J 2300/093 Coal
• CPC Class Codes: C10J 2300/0976 as steam
• CPC Class Codes: C10J 2300/1823 for synthesis gas
• CPC Class Codes: C10J 3/482 Gasifiers with stationary fluidised bed
• CPC Class Codes: C10J 3/503 for gasifiers with stationary fluidised bed
• CPC Class Codes: C10J 3/723 Controlling or regulating the gasification process

Abstract

A method and system for injecting coal and process fluids into a fluidized bed gasification reactor. Three concentric tubes extend vertically upward into the fluidized bed. Coal particulates in a transport gas are injected through an inner tube, and an oxygen rich mixture of oxygen and steam are injected through an inner annulus about the inner tube. A gaseous medium relatively lean in oxygen content, such as steam, is injected through an annulus surrounding the inner annulus.

Claims

1. A fluidized bed gasification reactor of the type wherein particulate carbonaceous material is fed into a vertically disposed vessel housing a combusting fluidized bed to produce a combustible product gas and ash, comprising:

a first vertical cylindrical tube extending upwardly into said vessel and having an open upper end;

means for flowing a first fluid upwardly through said first tube and into said vessel;

a second vertical tube, having an open upper end, and concentric with and spaced about said first tube so as to form an inner annulus therebetween;

said first and second tubes forming an annular passage of substantially constant cross-section over a substantial portion at their ends, said passage extending radially outwardly and at an angle of greater than 0° and

less than 71/2°

;

means for flowing a second fluid upwardly through said inner annulus and into said vessel;

a third vertical tube, having an open upper end, and concentric with and spaced about said second tube so as to form a second annulus;

means for flowing a third fluid upwardly through said second annulus and into said vessel; and

wherein said second and third tubes are tapered to form narrowed upper ends.

2. In a fluidized bed gasification reactor of the type wherein particulate carbonaceous material is fed into a vertically disposed vessel housing a combusting fluidized bed to produce a combustible product gas and ash, the improvement comprising:

a first vertical cylindrical tube extending upwardly into said vessel and having an open upper end;

means for flowing a first fluid upwardly through said first tube and into said vessel;

a second vertical tube, having an open upper end, and concentric with and spaced about said first tube so as to form an inner annulus therebetween;

means for flowing a second fluid upwardly through said inner annulus and into said vessel;

a third vertical tube, having an open upper end, and concentric with and spaced about said second tube so as to form a second annulus;

means for flowing a third fluid upwardly through said second annulus and into said vessel; and

wherein the upper portions of said first tube and said second tube are substantially equally spaced apart and shaped such that the upper portion of said inner annulus extends radially outwardly at an angle of greater than 0° and

less than or equal to 71/2°

from vertical.

3. The reactor of claim 2 wherein said angle is approximately 5°

.

4. The reactor of claim 2 wherein the upper portion of said inner tube is shaped as an inverted, truncated, annular cone.

5. In a fluidized bed gasification reactor of the type wherein particulate carbonaceous material is fed into a vertically disposed vessel housing a combusting fluidized bed to produce a combustible product gas and ash, the improvement comprising:

a first vertical cylindrical tube extending upwardly into said vessel and having an open upper end;

means for flowing a first fluid upwardly through said first tube and into said vessel;

second vertical tube, having an open upper end, and concentric with and spaced about said first tube so as to form an inner annulus therebetween;

said first and second tubes forming an annular passage of substantially constant cross-section over a substantial portion of their ends, said passage extending radially outwardly and at an angle of greater than 0° and

less than 71/2°

;

means for flowing a second fluid upwardly through said inner annulus and into said vessel;

a third vertical tube, having an open upper end, and concentric with and spaced about said second tube so as to form a second annulus;

means for flowing a third fluid upwardly through said second annulus and into said vessel; and

means for pulsing said third fluid flowing through said second annulus.

6. The reactor of claim 5 wherein said pulsing means comprise plugs affixed about the exterior of said second tube.

7. In an injection system for injecting process mediums into a fluidized bed gasification reactor the improvement comprising:

upwardly disposed outlet means located at an upper end of said system;

a first tube, open at said outlet means;

a second tube, open at said outlet means, concentric to and disposed about said first tube, said second tube having a tube wall thickness which decreases towards said outlet means;

the first and second tubes being substantially equally spaced apart at their upper ends to form a first annulus defined by said first and second tubes, said first annulus expanding radially outwardly from said first tube at an angle greater than 0° and

less than or equal to 71/2°

;

a third tube, open at said outlet means, concentric to and disposed about said second tube, said third tube having a tube wall thickness which decreases towards said outlet means; and

a second annulus defined by said second and third tubes.

8. The injection system in accordance with claim 7 wherein said first tube has an outside diameter which increases towards said outlet means.

9. The injection system in accordance with claim 7 wherein said first tube has a constant inside diameter.