Fluid sand falling type circulating fluidized bed boiler with a plurality of risers and method of operating the same

Patent metadata

Field	Value
Publication number	US-11333349-B2
Application number	US-201916401465-A
Country	US
Kind code	B2
Filing date	May 2, 2019
Priority date	Jul 19, 2018
Publication date	May 17, 2022
Grant date	May 17, 2022

Abstract

Disclosed herein are a fluid sand falling type circulating fluidized bed boiler with a plurality of risers for preventing erosion and corrosion of water tubes and increasing combustion efficiency, and a method of operating the same. The fluid sand falling type circulating fluidized bed boiler with a plurality of risers includes a boiler section into which fuel and oxidizer are injected, a riser section connected to the boiler section so that the fuel and fluid sand supplied from the boiler section are introduced from the bottom of the riser section and flow up, and a relay section provided on the boiler section to supply the fluid sand having passed through the riser section to the boiler section, wherein the fuel is injected from the top of the boiler section and burned while flowing down therein.

First claim

What is claimed is:

1. A fluid sand falling type circulating fluidized bed boiler with a plurality of risers, comprising:
a boiler section into which fuel is injected through a fuel injection section on one side of an upper portion of the boiler and combusted while flowing down therein, and into which oxidizer is injected through a plurality of oxidizer injection sections on a side wall of the boiler section in a height direction of the boiler section;
a riser section connected to the boiler section so that the combusted fuel and fluid sand supplied from the boiler section are introduced from a bottom of the riser section and flow up;
a relay section provided on the boiler section to supply the fluid sand having passed through the riser section to the boiler section; and
a plurality of water tube sections provided on an outer wall and in an internal space of the boiler section and extending in the height direction of the boiler section.

2. The fluid sand falling type circulating fluidized bed boiler according to claim 1 ,
wherein each output of the plurality of oxidizer injection sections is individually controlled to control descending rates of the fluid sand and the fuel and combustion of the fuel, and
wherein the plurality of oxidizer injection sections provided in a lower portion of the riser section includes a nozzle configured to decrease an injection amount of oxidizer when an amount of flow and a flow rate are increased in the riser section and to increase the injection amount of oxidizer when the amount of flow and the flow rate are decreased in the riser section.

3. The fluid sand falling type circulating fluidized bed boiler according to claim 1 , further comprising a second fuel injection section provided at one side of a lower portion of the riser section to inject fuel, having a combustion rate higher than the fuel supplied into the boiler section, to the riser section.

4. The fluid sand falling type circulating fluidized bed boiler according to claim 1 , wherein the riser section includes a plurality of riser sections arranged along a circumference of the boiler section or in an inner portion of the boiler section.

5. The fluid sand falling type circulating fluidized bed boiler according to claim 1 , further comprising a heat exchange section connected to the boiler section and the riser section to perform heat exchange using combustion gas produced by burning fuel.

6. The fluid sand falling type circulating fluidized bed boiler according to claim 5 , further comprising a first cyclone section provided between the riser section and the relay section,
wherein the first cyclone section is provided to transfer the combustion gas, the combustion gas being heated while passing through the riser section, to a final superheater or a reheater of the heat exchange section.

7. The fluid sand falling type circulating fluidized bed boiler according to claim 5 , further comprising a second cyclone section connected to an upper portion of the boiler section,
wherein the second cyclone section serves to transfer the combustion gas produced in the boiler section to a convection heat exchanger of the heat exchange section.

8. A method of operating the fluid sand falling type circulating fluidized bed boiler with the plurality of risers according to claim 1 , comprising:
a) a step of determining an operation mode or operation of each of a plurality of riser sections;
b) a step of injecting the fuel and oxidizer into the boiler section to burn the fuel;
c) a step of transferring the fuel and fluid sand supplied from the boiler section to each of the riser sections to a first cyclone section;
d) a step of transferring heated combustion gas transferred to the first cyclone section to a reheater of a heat exchange section and transferring the fluid sand to the relay section; and
e) a step of resupplying the fluid sand transferred to the relay section to the boiler section,
wherein the fuel is burned while flowing down in the boiler section, and the fuel is burned while flowing up in the riser section,
wherein in the b) step, each output of a plurality of oxidizer injection sections for injecting oxidizer into the boiler section is individually controlled to control descending rates of the fluid sand and the fuel and combustion of the fuel, and
wherein the b) step further includes using an oxidizer injection section provided in a lower portion of at least one riser of the plurality of the risers to decrease an injection amount of oxidizer when an amount of flow and a flow rate are increased in the at least one riser and to increase the injection amount of oxidizer when the amount of flow and the flow rate are decreased in the at least one riser.

9. The method according to claim 8 , wherein in the b) step, the combustion gas, having been produced by burning the fuel in the boiler section, is transferred to a convection heat exchanger of the heat exchange section through a second cyclone section.

10. The method according to claim 8 , wherein in the c) step, fuel, having a combustion rate higher than the fuel supplied into the boiler section, is further supplied to the riser section.

11. The method according to claim 8 , wherein in the a) step, the operation mode is one of: a pure oxygen combustion mode and an air combustion mode.

12. A power generation plant using a fluid sand falling type circulating fluidized bed boiler for oxidizer thermal power generation with a plurality of risers, the fluid sand falling type circulating fluidized bed boiler comprising:
a boiler section into which fuel is injected through a fuel injection section on one side of an upper portion of the boiler and combusted while flowing down therein, and into which oxidizer is injected through a plurality of oxidizer injection sections on a side wall of the boiler section in a height direction of the boiler section;
a riser section connected to the boiler section so that the combusted fuel and fluid sand supplied from the boiler section are introduced from a bottom of the riser section and flow up;
a relay section provided on the boiler section to supply the fluid sand having passed through the riser section to the boiler section; and
a plurality of water tube sections provided on an outer wall and in an internal space of the boiler section and extending in the height direction of the boiler section.

13. A power generation system for oxidizer thermal power generation using a fluid sand falling type circulating fluidized bed boiler with a plurality of risers, the fluid sand falling type circulating fluidized bed boiler comprising:
a boiler section into which fuel is injected through a fuel injection section on one side of an upper portion of the boiler and combusted while flowing down therein, and into which oxidizer is injected through a plurality of oxidizer injection sections on a side wall of the boiler section in a height direction of the boiler section;
a riser section connected to the boiler section so that the combusted fuel and fluid sand supplied from the boiler section are introduced from a bottom of the riser section and flow up;
a relay section provided on the boiler section to supply the fluid sand having passed through the riser section to the boiler section; and
a plurality of water tube sections provided on an outer wall and in an internal space of the boiler section and extending in the height direction of the boiler section.

Assignees

• Korea Inst Ind Tech
• Korea Inst Energy Res
• Korea Inst Mach & Materials

Inventors

• Lee Uen Do
• Bang Byeong Ryeol
• Kim Young Doo
• Jeong Soo Hwa
• Yang Chang Won
• Lee Jae Goo
• Mun Tae Young
• Seo Myung Won
• Moon Ji Hong
• Park Hyun Seol
• Shim Joon Mok
• Park Young Cheol
• Shun Do Won
• Moon Jong Ho
• Bae Dal Hee
• Jo Sung Ho
• Hwang Yun Tae
• Keel Sang In
• Yun Jin Han
• Lee Chungkyu
• Heo Pil Woo

Classifications

• F22B31/0007

  with combustion in a fluidized bed · CPC title

• Y02E20/12

  Heat utilisation in combustion or incineration of waste · CPC title

• F23C10/10 Primary

  the separation apparatus being located outside the combustion chamber · CPC title

• F23C10/12

  the particles being circulated exclusively within the combustion zone · CPC title

• F23C2206/103

  Cooling recirculating particles · CPC title