Fluidized bed combustion of carbonaceous fuels

Patent metadata

Field	Value
Publication number	US-10113740-B2
Application number	US-201615235619-A
Country	US
Kind code	B2
Filing date	Aug 12, 2016
Priority date	Aug 12, 2016
Publication date	Oct 30, 2018
Grant date	Oct 30, 2018

Abstract

Methods and devices for combusting a carbonaceous fuel in an oxy-combustion fluidized bed reactor involving controlling the local oxygen content within the oxy-combustion reactor to specified levels. The carbonaceous fuel and an oxygen-containing gas are introduced into a fluidized bed reactor and eluted through a fluidized bed of an inert material, dolomite or a combination thereof to combust the fuel and oxygen to produce at least CO2 and steam. The oxygen-containing gas is a mixture of oxygen, recycled CO2 and steam and has sufficient oxygen added to the recycled CO2 and steam that the mixture contains 7-20 mole % oxygen. The carbonaceous fuel and the oxygen-containing gas are introduced into the fluidized bed at a location in sufficiently close proximity to each other to avoid producing a reducing atmosphere at the location. At least a portion of the produced CO2 and steam are recycled to the reactor.

First claim

What is claimed is:

1. A method of combusting a carbonaceous fuel, said method comprising:
introducing the carbonaceous fuel and an oxygen-containing gas into a staged fluidized bed reactor wherein the carbonaceous fuel comprises a solid selected from the group consisting of coal, petroleum coke, biomass and combinations thereof and wherein the carbonaceous fuel and the oxygen-containing gas are eluted through a fluidized bed comprising an inert material, dolomite or a combination thereof;
wherein the oxygen-containing gas comprises a mixture of oxygen, recycled CO 2 and steam having sufficient oxygen added to the recycled CO 2 and steam that the mixture in each stage contains 7-20 mole % oxygen, and
wherein the carbonaceous fuel and the oxygen-containing gas are introduced into the fluidized bed at a location in sufficiently close proximity to each other to avoid producing a reducing atmosphere at the location;
combusting the carbonaceous fuel and with at least a portion of the oxygen-containing to produce at least CO 2 and steam; and
recycling to the fluidized bed reactor at least a portion of the produced CO 2 and steam as a portion of the oxygen-containing gas such that the total quantity of oxygen supplied to the reactor is greater than 20% but the quantity of oxygen supplied in each stage is no more than 20%.

2. The method of claim 1 wherein the carbonaceous fuel comprises natural gas.

3. The method of claim 1 wherein each stage has a beginning having an oxygen mole percent content of at least 7% up to 20% and an end, with the end of each stage prior to the last stage having an end oxygen content of no more than 3 mole % and the end of the last stage having an oxygen content of no more than 0.7-1.0 mole %.

4. The method of claim 1 wherein the fluidized bed reactor comprises at least one in-bed heat exchanger.

5. The method of claim 4 wherein the fluidized bed reactor comprises a plurality of in-bed heat exchangers and the plurality of in-bed heat exchangers occupy 20-35% by volume of the fluidized bed reactor.

6. The method of claim 5 wherein the fluidized bed reactor comprises a plurality of vertically separated stages, wherein at least one pair of adjacent vertically separated stages are separated by internal heat exchanger surfaces.

7. The method of claim 1 wherein said introducing of the carbonaceous fuel and the oxygen-containing gas into the fluidized bed reactor achieves desired mixing of the carbonaceous fuel and oxygen.

8. The method of claim 7 wherein said introducing of the carbonaceous fuel and the oxygen-containing gas into the fluidized bed reactor comprises introducing the carbonaceous fuel and the oxygen-containing gas into the fluidized bed reactor via an unlike doublet in which a fuel injector is paired with an oxygen-containing gas injector wherein the fuel injector and the oxygen-containing gas injector produce plumes of matched momentums and the plumes interact to form a sheet of uniform mixing.

9. The method of claim 7 wherein said introducing of the carbonaceous fuel and the oxygen-containing gas into the fluidized bed reactor comprises introducing the carbonaceous fuel and the oxygen-containing gas into the fluidized bed reactor via a coaxial splash plate injector wherein the carbonaceous fuel is fed through a central tube to impact a first splash plate and to be redirected to initially flow outwardly generally perpendicular to the central tube and the oxygen-containing gas is fed through an annular flow path disposed about the central tube to impact a second splash plate and to be redirected to initially flow outwardly generally perpendicular to the central tube and parallel the redirected initial flow of the carbonaceous fuel.

10. The method of claim 7 wherein said introducing of the carbonaceous fuel and the oxygen-containing gas into the fluidized bed reactor comprises introducing the carbonaceous fuel and the oxygen-containing gas into the fluidized bed reactor via a coaxial arrangement wherein the carbonaceous fuel is fed through a central tube and the oxygen-containing gas is fed through an annular flow path disposed about the central tube, the coaxial arrangement further comprising a plurality of side discharge outlets that centrally side discharge a portion of the carbonaceous fuel with an annular plume of the oxygen-containing gas.

11. The method of claim 7 wherein said introducing of the carbonaceous fuel and the oxygen-containing gas into the fluidized bed reactor comprises introducing the carbonaceous fuel and the oxygen-containing gas into the fluidized bed reactor in parallel and vertically spaced apart.

12. In a process for combusting a carbonaceous fuel in an oxy-combustion reactor, the improvement comprising:
controlling local oxygen content within the oxy-combustion reactor to less than 20 mole %.

13. A processing system comprising:
a staged fluidized bed reactor wherein a carbonaceous fuel and an oxygen-containing gas are eluted through a fluidized bed comprising an inert material, dolomite or a combination thereof, wherein the carbonaceous fuel comprises natural gas;
wherein the oxygen-containing gas comprises a mixture of oxygen, recycled CO 2 and steam having sufficient oxygen added to the recycled CO 2 and steam that the mixture in each stage contains 7-20 mole % oxygen; and
wherein the carbonaceous fuel and the oxygen-containing are injected into the fluidized bed at a location in sufficiently close proximity to each other to avoid producing a reducing atmosphere at the location.

14. The processing system of claim 13 wherein each stage has a beginning having an oxygen mole percent content of at least 7% up to 20% and an end, with the end of each stage prior to the last stage having an end oxygen content of no more than 3 mole % and the end of the last stage having an oxygen content of no more than 0.7-1.0 mole %.

15. The processing system of claim 13 wherein the carbonaceous fuel comprises a solid selected from the group consisting of coal, petroleum coke, biomass and combinations thereof.

16. The processing system of claim 13 wherein the fluidized bed reactor comprises at least one in-bed heat exchanger.

17. The processing system of claim 16 wherein the fluidized bed reactor comprises a plurality of in-bed heat exchangers and the plurality of heat exchangers occupy 20-35% by volume of the fluidized bed reactor.

18. A method of combusting a carbonaceous fuel, said method comprising:
introducing the carbonaceous fuel and an oxygen-containing gas into a staged fluidized bed reactor, wherein the carbonaceous fuel comprises natural gas and wherein the carbonaceous fuel and the oxygen-containing gas are eluted through a fluidized bed comprising an inert material, dolomite or a combination thereof;
wherein the oxygen-containing gas comprises a mixture of oxygen, recycled CO 2 and steam having sufficient oxygen added to the recycled CO 2 and steam that the mixture in each stage contains 7-20 mole % oxygen, and
wherein the carbonaceous fuel and the oxygen-containing gas are introduced into the fluidized bed at a location in sufficiently close proximity to each other to avoid producing a reducing atmosphere at the location;
combusting the carbonaceous fuel and with at least a portion of the oxygen-containing to produce at least CO 2 and steam; and
recycling to the fluidized bed reactor at least a portion of the produced CO 2 and steam as a portion of the oxygen-containing gas such that the total quantity of oxygen supplied to the reactor is greater than 20% but the quantity of oxygen suppl

Assignees

• Gas Technology Inst

Inventors

• Fitzsimmons Mark

Classifications

• Y02E20/34

  Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery · CPC title

• F23C2202/00

  Fluegas recirculation · CPC title

• C10L5/04

  Raw material {of mineral origin} to be used; Pretreatment thereof {(pretreatment of fuels of non-mineral origin C10L5/40)} · CPC title

• F23C10/002 Primary

  for pulverulent solid fuel (F23C10/005 - F23C10/32 take precedence) · CPC title

• F23C10/00

  Fluidised bed combustion apparatus · CPC title