Method and a system for maintaining steam temperature with decreased loads of a steam turbine power plant comprising a fluidized bed boiler

Patent metadata

Field	Value
Publication number	US-11300288-B2
Application number	US-201816754681-A
Country	US
Kind code	B2
Filing date	Oct 17, 2018
Priority date	Nov 2, 2017
Publication date	Apr 12, 2022
Grant date	Apr 12, 2022

Abstract

The solution comprises a method of and a system for maintaining steam temperature and therefore electricity production efficiency with decreased loads of a steam turbine power plant comprising a fluidized bed boiler (12) and a fluidized bed superheater (2) adapted to superheat steam supplied to a steam turbine (3). According to the solution, the steam temperature may be maintained by providing, outside a furnace (10), additional heating to the fluidized bed material in its outer circulation, thereby increasing the amount of thermal energy available in the fluidized bed material to be transferred in the fluidized bed superheater (2) to the steam supplied to the steam turbine (3). Such additional heating may be performed by selectably supplying combustible gas with nozzles (111) into and/or burned with a burner in or in the vicinity of the fluidized bed material outside the furnace (10). As an additional aspect of the disclosed solution, the combustible gas may be produced with a gasifier (4).

First claim

The invention claimed is:

1. A method of maintaining the temperature of steam supplied to a steam turbine of a steam turbine power plant, which power plant further comprises a circulating fluidized bed boiler comprising a furnace and a fluidized bed superheater configured to superheat steam supplied to the steam turbine by transferring thermal energy to said steam from fluidized bed material, the method comprising:
selecting a trigger load for the power plant, which trigger load is less than the full rated load of the power plant and greater than the minimum rated viable load of the power plant,
determining the load of the power plant,
when the load of the power plant is at or above the trigger load, superheating steam with the fluidized bed superheater such that the temperature of the superheated steam entering the steam turbine is at or near its maximum temperature, and
when the load of the power plant is below the trigger load:
injecting combustible gas into the fluidized bed material outside the furnace, the combustible gas being ignited by the fluidized bed material when the combustible gas comes into contact with the fluidized bed material having a temperature at or above a minimum temperature required to ignite the combustible gas,
superheating steam with the fluidized bed superheater,
additionally heating the fluidized bed material outside the furnace such that the temperature of the superheated steam entering the steam turbine is at or near its maximum temperature, wherein the additional heating of the fluidized bed material is brought about by combustion of the injected combustible gas, and
conveying the superheated steam from the fluidized bed superheater to the steam turbine.

2. The method according to claim 1 , wherein the additional heating of the fluidized bed material occurs, with respect to an outer circulation of the fluidized bed material, at or before the fluidized bed superheater and after the fluidized bed material has exited the furnace.

3. The method according to claim 1 , wherein the additional heating of the fluidized bed material occurs, with respect to an outer circulation of the fluidized bed material, at or before the fluidized bed superheater but not earlier than the entrance of the fluidized bed material into a loop seal heat exchanger chamber.

4. The method according to claim 3 , wherein the additional heating of the fluidized bed material occurs in the loop seal heat exchanger chamber.

5. The method according to claim 4 , wherein the combustible gas is injected into the fluidized bed material by means of gas injection nozzles in the loop seal heat exchanger chamber.

6. The method according to claim 3 , wherein the additional heating of the fluidized bed material occurs in a combustion chamber, which combustion chamber is arranged adjacent to the loop seal heat exchanger chamber such that there is a circulation of fluidized bed material between the loop seal heat exchanger chamber and the combustion chamber.

7. The method according to claim 6 , wherein the combustible gas is injected into the fluidized bed material by means of gas injection nozzles in the combustion chamber ( 16 ).

8. The method according to claim 2 , wherein the additional heating of the fluidized bed material occurs in a heat exchanger chamber which heat exchanger chamber houses the fluidized bed superheater and is arranged adjacent to the furnace, and wherein the combustible gas is injected into the fluidized bed material by means of gas injection nozzles in the heat exchanger chamber.

9. The method according to claim 2 , wherein the additional heating of the fluidized bed material occurs in a gas lock located between a dip leg and a heat exchanger chamber which heat exchanger chamber houses the fluidized bed superheater and is arranged adjacent to the furnace.

10. The method according to claim 9 , wherein the combustible gas is injected into the fluidized bed material by means of gas injection nozzles in the gas lock.

11. The method according to claim 2 , wherein the additional heating of the fluidized bed material occurs in a heat exchanger chamber housing at least one superheater and arranged adjacent to a loop seal chamber devoid of any superheater(s).

12. The method according to claim 11 , wherein the combustible gas is injected into the fluidized bed material by means of gas injection nozzles in the heat exchanger chamber.

13. The method according to claim 1 , wherein the combustion of the combustible gas is brought about by providing oxygen with fluidization gas which is required for bringing about fluidization of the fluidized bed material.

14. The method according to claim 1 , wherein the additional heating of the fluidized bed material is brought about by additionally burning combustible gas with a burner within or in the vicinity of the fluidized bed material.

15. The method according to claim 14 , wherein the burner is configured to burn the combustible gas in at least one of: a loop seal heat exchanger chamber, a combustion chamber, a heat exchanger chamber, a gas lock, or a heat exchanger chamber.

16. The method according to claim 1 , the method further comprising generating product gas by gasification with a gasifier and using said product gas as the combustible gas.

17. A system, comprising:
a steam turbine,
a circulating fluidized bed boiler comprising a furnace and a fluidized bed superheater configured to superheat steam supplied to the steam turbine by transferring thermal energy to said steam from fluidized bed material, and
a control unit configured to:
receive a set value for a trigger load for a power plant comprising the system which trigger load is less than the full rated load of the power plant and greater than the minimum rated viable load of the power plant,
determine the load of the power plant, and
when the load of the power plant is below the trigger load, control injection of combustible gas into the fluidized bed material outside the furnace such that the temperature of steam entering the steam turbine is maintained at or near its maximum temperature, wherein additional heating of the fluidized bed material is brought about by combustion of the combustible gas which is injected into the fluidized bed material and ignited by the fluidized bed material when the combustible gas comes into contact with the fluidized bed material having a temperature at or above a minimum temperature required to ignite the combustible gas.

18. The system according to claim 17 , the system further comprising a loop seal heat exchanger chamber provided with gas injection nozzles configured to inject the combustible gas into the fluidized bed material.

19. The system according to claim 17 , the system further comprising:
a combustion chamber arranged adjacent to a loop seal heat exchanger chamber such that there is a circulation of fluidized bed material between the loop seal heat exchanger chamber and the combustion chamber, and
gas injection nozzles in the combustion chamber configured to inject the combustible gas into the fluidized bed material.

20. The system according to claim 17 , the system further comprising:
a heat exchanger chamber housing the fluidized bed superheater and arranged adjacent to the boiler, and
gas injection nozzles in the heat exchanger chamber configured to inject the combustible gas into the fluidized bed material.

21. The system according to claim 17 , the system further comprising:
a heat exchanger chamber housing the fluidized bed superhe

Assignees

• Valmet Technologies Oy

Inventors

• Varonen Mikko
• Nieminen Matti

Classifications

• F22B31/04

  Heat supply by installation of two or more combustion apparatus, e.g. of separate combustion apparatus for the boiler and the superheater respectively · CPC title

• F22G1/16 Primary

  by using a separate heat source independent from heat supply of the steam boiler, e.g. by electricity, by auxiliary combustion of fuel oil · CPC title

• F01K3/24

  with heating by separately-fired heaters · CPC title

• F22B31/0084 Primary

  with recirculation of separated solids or with cooling of the bed particles outside the combustion bed · CPC title

• F22G3/00 Primary

  Steam superheaters characterised by constructional features; Details or component parts thereof · CPC title