WO2016179824A1 - A system for burning pulverized solid fuel and a method thereof - Google Patents

A system for burning pulverized solid fuel and a method thereof Download PDF

Info

Publication number
WO2016179824A1
WO2016179824A1 PCT/CN2015/078948 CN2015078948W WO2016179824A1 WO 2016179824 A1 WO2016179824 A1 WO 2016179824A1 CN 2015078948 W CN2015078948 W CN 2015078948W WO 2016179824 A1 WO2016179824 A1 WO 2016179824A1
Authority
WO
WIPO (PCT)
Prior art keywords
zone
combustor
combustion
solid fuel
pulverized solid
Prior art date
Application number
PCT/CN2015/078948
Other languages
French (fr)
Inventor
Zheng Shi
Original Assignee
Zheng Shi
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Zheng Shi filed Critical Zheng Shi
Priority to PCT/CN2015/078948 priority Critical patent/WO2016179824A1/en
Priority to PCT/CN2015/085735 priority patent/WO2016179909A1/en
Publication of WO2016179824A1 publication Critical patent/WO2016179824A1/en

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23MCASINGS, LININGS, WALLS OR DOORS SPECIALLY ADAPTED FOR COMBUSTION CHAMBERS, e.g. FIREBRIDGES; DEVICES FOR DEFLECTING AIR, FLAMES OR COMBUSTION PRODUCTS IN COMBUSTION CHAMBERS; SAFETY ARRANGEMENTS SPECIALLY ADAPTED FOR COMBUSTION APPARATUS; DETAILS OF COMBUSTION CHAMBERS, NOT OTHERWISE PROVIDED FOR
    • F23M9/00Baffles or deflectors for air or combustion products; Flame shields
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C9/00Combustion apparatus characterised by arrangements for returning combustion products or flue gases to the combustion chamber
    • F23C9/006Combustion apparatus characterised by arrangements for returning combustion products or flue gases to the combustion chamber the recirculation taking place in the combustion chamber

Definitions

  • the present invention relates to the field of combustors for small to medium sized combustors and furnaces using pulverized solid fuel.
  • Combustors wherein a single or a plurality of fuel nozzles are arranged to project a mixture of air and solid fuel, into the combustor are well known.
  • the powdered solid fuel and pressurized air are blown into a combustor as an air-fuel mixture.
  • air-fuel mixture might have been pre-ignited before entering the combustor, or might be entering the combustor to be ignited.
  • One of the important tasks of the abovementioned systems is to provide the proper conditions for the near-complete combustion of the fuel. This is mainly achieved by projecting the fuel supply fed into the combustor at an appropriate rate, angle and rotation, and keeping the fuel in the combustor for a sufficient time.
  • the present invention discloses a system and method for combustion of solid fuels, such as pulverized coal in small and medium boilers.
  • the system includes a combustor having a first zone, a second zone and an exit that connects the two zones, and one or a plurality of pre-combustors where the fuel is heated up, ignited, and/or combusted to a certain extent.
  • a combustion mixture of pulverized solid fuel, combustion air and flame is projected by the pre-combustor (s) , at a high velocity, into the first zone in a first direction that is away from the exit, and then forced to flow in the opposite direction of the first direction in order to enter the second zone, creating a turbulent reflux flow in the first zone.
  • the velocity of the combustion mixture is between 50 meters per second and 100 meters per second for a combustor of 10 meters in length along the traveling direction of the combustion mixture.
  • FIG. 1 graphically illustrates the cross-sectional view of one of the embodiments of the invention.
  • FIG. 1 is a cross-sectional view of the combustor according to one of the embodiments of the invention.
  • the combustor 101 is fitted with a pre-combustor (or fuel/air nozzle) 102 that projects a high velocity combustion mixture of pulverized solid fuel, combustion air and flame into the first zone 103 in a first direction that is away from the exit 109.
  • the flue gas is forced to flow in the opposite direction of the first direction in order to move into the second zone 104 of the combustor 101 and then travels into the third zone 105 before exiting at outlet 106.
  • the pre-combustor (or fuel/air nozzle) 102 is placed at or near the same side as the exit 109 of the first zone 103, the high power flame jet capable of creating an effective turbulent reflux dynamic occurring within the first zone 103.
  • the velocity of the combustion mixture is between 50 meters per second and 100 meters per second along the traveling direction of the combustion mixture, and should cover the whole length of the combustor without making direct contact with the opposite wall so as to avoid slag formation.
  • the method of the present invention can be described as follows.
  • the pre-combustor 102 projects a high velocity combustion mixture of pulverized solid fuel, combustion air and flame against the wall 107 of the first zone 103 (but is designed in such a manner that the flame is not in contact with the wall) .
  • the stream of combustion mixture projected by the pre-combustor 102 is depicted by the arrows labeled 1° in FIG. 1.
  • the reflux stream mainly moves backwards in the periphery of the strong stream 1°, depicted by the arrows labeled 2°.
  • a certain portion of the reflux stream 2° gradually loses its backward speed while moving in the opposite direction of the powerful stream 1°, and thus is redirected back and joins stream 1°, which is depicted by the arrows labeled 4°.
  • the remainder of stream 2° will keep on moving towards the opposite wall 108 and then exit into the second zone 104, as labeled by arrow 3°.
  • Steam 3° will go through the second zone 104 and the third zone 105 before eventually exiting the combustor at the outlet 106.
  • the invention described above effectively enables more thorough mix of the fuel and combustion air, prolongs the amount of time that the fuel stream spends within the combustor, and improves the overall efficiency of combustion of the fuel in a cost effective manner since it allows a smaller combustor to burn a larger amount of fuel.

Abstract

A system for burning pulverized solid fuel and a method thereof are provided. A high velocity flame jet is projected within a first zone (103) of a combustor (101) where most of combustion occurs and forced to create a powerful turbulent reflux within the first zone (103) of the combustor (101). The pulverized solid fuel entering the reflux consequently spends a prolonged time in the first zone (103) of the combustor (101) before exiting into a second zone (104), thus allowing for more complete combustion given the same volume of combustion space in the first zone (103).

Description

SYSTEM AND METHOD TO IMPROVE EFFICIENCY OF COMBUSTION IN SMALL TO MEDIUM SIZED COMBUSTORS TECHNICAL FIELD
The present invention relates to the field of combustors for small to medium sized combustors and furnaces using pulverized solid fuel.
BACKGROUND
Combustors wherein a single or a plurality of fuel nozzles are arranged to project a mixture of air and solid fuel, into the combustor are well known. In this type of systems, the powdered solid fuel and pressurized air are blown into a combustor as an air-fuel mixture. Such air-fuel mixture might have been pre-ignited before entering the combustor, or might be entering the combustor to be ignited.
One of the important tasks of the abovementioned systems is to provide the proper conditions for the near-complete combustion of the fuel. This is mainly achieved by projecting the fuel supply fed into the combustor at an appropriate rate, angle and rotation, and keeping the fuel in the combustor for a sufficient time.
In large-scale industrial coal-fired combustors, near-complete combustion of the pulverized solid fuel is always assured as these combustors have large combustors and sophisticated fuel preheating and delivery systems. Typically, in these large combustors, preheating arrangements and the design of the combustor itself is made in such a way that the coal dust thoroughly mixes with combustion air, and spends a protracted amount of time in the combustor and thus assures adequate combustion of the coal dust. For example, elaborate systems such as tangentially-fired combustors are designed in such a way that the coal dust is projected into a virtual vortex flow which protracts the time the fuel spends within the chamber.
Unfortunately, the above is not applicable to small or medium-scale combustors fired by pulverized solid fuel such as powdered coal whereby a small  installation is utilized and arrangements for fuel preheating are limited.
Accordingly, there is a need to improve fuel combustion in small to medium-scaled combustors, while simultaneously providing a system that is simple to construct and inexpensive to produce.
SUMMARY OF INVENTION
The present invention discloses a system and method for combustion of solid fuels, such as pulverized coal in small and medium boilers.
In accordance with one embodiment of the present invention, the system includes a combustor having a first zone, a second zone and an exit that connects the two zones, and one or a plurality of pre-combustors where the fuel is heated up, ignited, and/or combusted to a certain extent. A combustion mixture of pulverized solid fuel, combustion air and flame is projected by the pre-combustor (s) , at a high velocity, into the first zone in a first direction that is away from the exit, and then forced to flow in the opposite direction of the first direction in order to enter the second zone, creating a turbulent reflux flow in the first zone.
In accordance with one embodiment of the present invention, the velocity of the combustion mixture is between 50 meters per second and 100 meters per second for a combustor of 10 meters in length along the traveling direction of the combustion mixture.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 graphically illustrates the cross-sectional view of one of the embodiments of the invention.
DETAILED DESCRIPTION OF THE INVENTION
The present invention may be better understood and its many objects and advantages will become apparent to those skilled in the art by reference to the accompanying drawing.
FIG. 1 is a cross-sectional view of the combustor according to one of the embodiments of the invention. The combustor 101 is fitted with a pre-combustor (or fuel/air nozzle) 102 that projects a high velocity combustion mixture of pulverized  solid fuel, combustion air and flame into the first zone 103 in a first direction that is away from the exit 109. The flue gas is forced to flow in the opposite direction of the first direction in order to move into the second zone 104 of the combustor 101 and then travels into the third zone 105 before exiting at outlet 106. Since the pre-combustor (or fuel/air nozzle) 102 is placed at or near the same side as the exit 109 of the first zone 103, the high power flame jet capable of creating an effective turbulent reflux dynamic occurring within the first zone 103.
For a combustor of around 10 meters in length, the velocity of the combustion mixture is between 50 meters per second and 100 meters per second along the traveling direction of the combustion mixture, and should cover the whole length of the combustor without making direct contact with the opposite wall so as to avoid slag formation.
The method of the present invention can be described as follows. The pre-combustor 102 projects a high velocity combustion mixture of pulverized solid fuel, combustion air and flame against the wall 107 of the first zone 103 (but is designed in such a manner that the flame is not in contact with the wall) . The stream of combustion mixture projected by the pre-combustor 102 is depicted by the arrows labeled 1° in FIG. 1. As the flame steam propagates towards the opposite wall where it consequently reverses back towards to its original direction, forming a turbulent reflux stream. The reflux stream mainly moves backwards in the periphery of the strong stream 1°, depicted by the arrows labeled 2°. A certain portion of the reflux stream 2° gradually loses its backward speed while moving in the opposite direction of the powerful stream 1°, and thus is redirected back and joins stream 1°, which is depicted by the arrows labeled 4°. The remainder of stream 2° will keep on moving towards the opposite wall 108 and then exit into the second zone 104, as labeled by arrow 3°. Steam 3° will go through the second zone 104 and the third zone 105 before eventually exiting the combustor at the outlet 106.
People skilled in the art will recognize the obvious advantage of the system and method described above. Through a simple system of projecting a high-speed combustion mixture inside the confines of the first zone 103 of the combustor 101, a powerful and turbulent reflux effect is created. This turbulent reflux effectively causes the stream of combustion mixture to circulate back and forth from one wall 107 to another wall 108 until it finally exits the first zone 103 at the exit 109. Typically, there  is a steep temperature drop from the combustor to the second zone 104 of the combustor 101 due to extensive heat transfer, and consequently, there is little further combustion once the fuel/air/flame has exited the combustor. The fact that the majority of the stream of combustion mixture does not simply pass through the first zone 103 and leave it at the exit 109 as is usually the case in these types of combustor is the premise of the present invention. The powerful turbulent reflux effect within the combustor effectively allows for a much better combustion of the fuel given that the air and fuel mixes well and that the fuel spends a prolonged amount of time within the combustor.
The invention described above effectively enables more thorough mix of the fuel and combustion air, prolongs the amount of time that the fuel stream spends within the combustor, and improves the overall efficiency of combustion of the fuel in a cost effective manner since it allows a smaller combustor to burn a larger amount of fuel.

Claims (4)

  1. A system for burning pulverized solid fuel, comprising:
    -a combustor comprising a first zone and a second zone, and an exit that connects the two zones,
    -a pre-combustor that is positioned in proximity to the exit,
    wherein a combustion mixture of pulverized solid fuel, combustion air and flame is projected by the pre-combustor, at a high velocity, into the first zone in a first direction that is away from the exit, and then forced to flow in the opposite direction of the first direction in order to enter the second zone, creating a turbulent reflux flow in the first zone.
  2. The system of claim 1, wherein the velocity of the combustion mixture is between 50 meters per second and 100 meters per second for a combustor of around 10 meters in length along the traveling direction of the combustion mixture.
  3. A method for burning pulverized solid fuel, comprising:
    -projecting, by a pre-combustor and at a high velocity, a combustion mixture of pulverized solid fuel, combustion air and flame into a first zone of a combustor in a first direction, wherein the combustor comprises a first zone and a second zone, and an exit that connects the two zones, and wherein the first direction is moving away from the exit,
    -forcing the combustion mixture to flow in the opposite direction of the first direction in order to enter the second zone via the exit, creating a turbulent reflux flow in the first zone.
  4. The method of claim 3, further comprising, wherein the velocity of the combustion mixture is between 50 meters per second and 100 meters per second for a combustor of around 10 meters in length along the traveling direction of the combustion mixture.
PCT/CN2015/078948 2015-05-14 2015-05-14 A system for burning pulverized solid fuel and a method thereof WO2016179824A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
PCT/CN2015/078948 WO2016179824A1 (en) 2015-05-14 2015-05-14 A system for burning pulverized solid fuel and a method thereof
PCT/CN2015/085735 WO2016179909A1 (en) 2015-05-14 2015-07-31 Burner design for pulverized coal-fired boilers using minimal ignition fuel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/CN2015/078948 WO2016179824A1 (en) 2015-05-14 2015-05-14 A system for burning pulverized solid fuel and a method thereof

Publications (1)

Publication Number Publication Date
WO2016179824A1 true WO2016179824A1 (en) 2016-11-17

Family

ID=57247636

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2015/078948 WO2016179824A1 (en) 2015-05-14 2015-05-14 A system for burning pulverized solid fuel and a method thereof

Country Status (1)

Country Link
WO (1) WO2016179824A1 (en)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1349971A (en) * 1919-09-15 1920-08-17 Mcdonald John Urban Furnace
DE3340107A1 (en) * 1983-11-05 1985-05-15 Franz X. 6200 Wiesbaden Wittek Process for the operation of heating boilers with atomisable fuels and heating boiler for carrying out the process
JPS6131812A (en) * 1984-07-25 1986-02-14 Matsushita Electric Ind Co Ltd Baffle plate of fuel combustion equipment
JPH11201443A (en) * 1998-01-12 1999-07-30 Ishikawajima Harima Heavy Ind Co Ltd Rdf combustion tubular boiler
CN202709089U (en) * 2012-02-22 2013-01-30 崔国培 Biomass powder burner
DE202014105238U1 (en) * 2014-10-31 2014-11-12 Lasco Heutechnik Gmbh Mobile solid fuel firing system

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1349971A (en) * 1919-09-15 1920-08-17 Mcdonald John Urban Furnace
DE3340107A1 (en) * 1983-11-05 1985-05-15 Franz X. 6200 Wiesbaden Wittek Process for the operation of heating boilers with atomisable fuels and heating boiler for carrying out the process
JPS6131812A (en) * 1984-07-25 1986-02-14 Matsushita Electric Ind Co Ltd Baffle plate of fuel combustion equipment
JPH11201443A (en) * 1998-01-12 1999-07-30 Ishikawajima Harima Heavy Ind Co Ltd Rdf combustion tubular boiler
CN202709089U (en) * 2012-02-22 2013-01-30 崔国培 Biomass powder burner
DE202014105238U1 (en) * 2014-10-31 2014-11-12 Lasco Heutechnik Gmbh Mobile solid fuel firing system

Similar Documents

Publication Publication Date Title
JP4969015B2 (en) Solid fuel burner and combustion method using solid fuel burner
JP5386230B2 (en) Fuel burner and swirl combustion boiler
JP6049503B2 (en) Combustion burner and boiler
TWI712761B (en) Solid fuel burner
US20120244479A1 (en) Combustion System Using Recycled Flue Gas to Boost Overfire Air
CN105927969A (en) Combustion system for reducing nitric oxides of front and back wall opposite-combustion boiler
US20040185401A1 (en) Mixing process for combustion furnaces
RU2661993C1 (en) Combustion burner and boiler equipped with such burner
US10948182B2 (en) Combustion system for a boiler
US20090068601A1 (en) Burner Pilot With Virtual Spinner
JP6470383B2 (en) Turbine including flue gas recirculation combustor
KR101737235B1 (en) mixed-combustion burner
WO2016179824A1 (en) A system for burning pulverized solid fuel and a method thereof
RU2364788C1 (en) Burner device
WO2014179956A1 (en) System and method for small-scale combustion of pulverized solid fuels
JP6246709B2 (en) Combustion burner and boiler
JP2000039108A (en) LOW NOx BURNER
CN108700287B (en) Method for injecting particulate solid fuel and oxidant and injector therefor
EP2860447B1 (en) Combustion chamber with air injection systems
WO2016031540A1 (en) Combustion burner and boiler
HUT65491A (en) An advanced overfire air system for nox control and method for controlling nox in fossil fuel furnaces
RU169645U1 (en) VERTICAL PRISMATIC LOW EMISSION HEATER
JPS5843313A (en) Burner for pulverized coal
CN102944009A (en) Arrangement structure of mixing air of circulating fluid bed ignition device
JP6159145B2 (en) Combustor

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 15891527

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 15891527

Country of ref document: EP

Kind code of ref document: A1