Biomass-mixed, pulverized coal-fired burner and fuel combustion method

Patent metadata

Field	Value
Publication number	US-10281148-B2
Application number	US-201314386951-A
Country	US
Kind code	B2
Filing date	Mar 21, 2013
Priority date	Mar 21, 2012
Publication date	May 7, 2019
Grant date	May 7, 2019

Abstract

A biomass-mixed, pulverized coal-fired burner is provided. The biomass-mixed, pulverized coal-fired burner is capable of burning biomass fuel as auxiliary fuel in large quantities and burning only pulverized coal when the biomass fuel is not sufficiently available. The biomass-mixed, pulverized coal-fired burner includes: a biomass fuel jet nozzle that extends axially along the biomass-mixed, pulverized coal-fired burner; a pulverized coal fuel jet nozzle that surrounds the biomass fuel jet nozzle; a secondary air nozzle that surrounds the pulverized coal fuel jet nozzle; and a tertiary air nozzle that surrounds the secondary air nozzle. A biomass fuel stream is jetted into an inside of a pulverized coal fuel flame formed in a furnace, the flame offering favorable ignition and flame holding performance.

First claim

The invention claimed is:

1. A biomass-mixed, pulverized coal-fired burner, comprising:
a biomass fuel jet nozzle having a biomass fuel jet port that jets biomass fuel conveyed by biomass fuel primary air as a biomass fuel stream;
a pulverized coal fuel jet nozzle having a pulverized coal fuel jet port that surrounds an opening in the biomass fuel jet port, the pulverized coal fuel jet nozzle jetting pulverized coal fuel conveyed by pulverized coal fuel primary air as a pulverized coal fuel stream;
a secondary air nozzle having a secondary air jet port that surrounds an opening in the pulverized coal fuel jet port, the secondary air jet port jetting secondary air; and
a tertiary air nozzle having a tertiary air jet port that surrounds the secondary air jet port, the tertiary air jet port jetting a tertiary air swirl flow, wherein
the biomass fuel jet nozzle includes a biomass fuel conveying pipe that forms a flow path for the biomass fuel stream, and includes a biomass fuel swirl vane that converts the biomass fuel stream to a swirl flow whirling around an axis of the biomass fuel conveying pipe to thereby make a fuel concentration lower on an axis side of the biomass fuel conveying pipe and higher on an outer circumferential wall side of the biomass fuel conveying pipe,
the biomass fuel jet port has a pipe end extending in parallel with a pipe axis,
the biomass fuel jet nozzle further includes a biomass fuel baffle plate disposed on a pipe inner wall upstream of the pipe end, the biomass fuel baffle plate reducing a swirl of the biomass fuel stream jetted from the biomass fuel jet port,
the pulverized coal fuel jet nozzle includes a pulverized coal fuel conveying pipe that forms a flow path for the pulverized coal fuel stream, a pulverized coal fuel swirl vane that converts the pulverized coal fuel stream to a swirl flow whirling around an outer circumference of the biomass fuel jet nozzle to thereby make a fuel concentration higher on an outer circumferential wall side of the pulverized coal fuel conveying pipe, a flame stabilizer disposed at a pipe end of the pulverized coal fuel jet port and having a funnel-shaped widening ring including an inner face having an inner diameter larger than an inner diameter of the pulverized coal fuel convening pipe and a stepped part formed at the inner face of the widening ring and continuously extending around the entire circumference of the pulverized coal fuel jet port, and a pulverized coal fuel baffle plate disposed on a pipe inner wall upstream of the flame stabilizer, the pulverized coal fuel baffle plate reducing a swirl of the pulverized coal fuel stream jetted from the pulverized coal fuel jet port,
a spread angle of the pulverized coal fuel stream jetted from the pulverized coal fuel jet port is reduced by the flame stabilizer having the stepped part and the pulverized coal fuel baffle plate,
the stepped part includes a lateral face having an inner diameter larger than an inner diameter of the pulverized coal fuel conveying pipe,
the secondary air jetted from the secondary air jet port forms a buffer stream between the pulverized coal fuel stream and the tertiary air swirl flow, and
the pulverized coal fuel stream is formed such that the biomass fuel stream jetted from the biomass fuel jet port is enveloped by the pulverized coal fuel stream jetted from the pulverized coal fuel jet port.

2. The biomass-mixed, pulverized coal-fired burner according to claim 1 , wherein
the biomass fuel jet nozzle includes a biomass fuel bent section disposed upstream of the biomass fuel swirl vane, and
the pulverized coal fuel jet nozzle includes a pulverized coal fuel bent section disposed upstream of the pulverized coal fuel swirl vane.

3. The biomass-mixed, pulverized coal-fired burner according to claim 1 , wherein the biomass fuel primary air is supplied in such a quantity that a velocity of a fuel conveying stream in the biomass fuel jet nozzle falls within a range between 14.5 m/s and 30 m/s.

4. The biomass-mixed, pulverized coal-fired burner according to claim 2 , wherein the biomass fuel primary air is supplied in such a quantity that a velocity of a fuel conveying stream in the biomass fuel jet nozzle falls within a range between 14.5 m/s and 30 m/s.

5. The biomass-mixed, pulverized coal-fired burner according to claim 1 , wherein the biomass fuel primary air is supplied such that the biomass-mixed, pulverized coal-fired burner is operated in a range that, with fuel containing 60% by weight of biomass fuel, is sandwiched between a first straight line and a second straight line as follows: the first straight line extending from A/C 0.5 relating to the biomass fuel to A/C 1.6 relating to the biomass fuel at a load factor of 100% of the biomass-mixed, pulverized coal-fired burner; and the second straight line extending from A/C 0.5 relating to the biomass fuel to A/C 2.4 relating to the biomass fuel at a load factor of 50% of the biomass-mixed, pulverized coal-fired burner,
wherein the A/C relating to the biomass fuel is a ratio of biomass fuel primary air flow rate (Nm 3 /h) to biomass fuel (kg/h).

6. The biomass-mixed, pulverized coal-fired burner according to claim 2 , wherein the biomass fuel primary air is supplied such that the biomass-mixed, pulverized coal-fired burner is operated in a range that, with fuel containing 60% by weight of biomass fuel, is sandwiched between a first straight line and a second straight line as follows: the first straight line extending from A/C 0.5 relating to the biomass fuel to A/C 1.6 relating to the biomass fuel at a load factor of 100% of the biomass-mixed, pulverized coal-fired burner; and the second straight line extending from A/C 0.5 relating to the biomass fuel to A/C 2.4 relating to the biomass fuel at a load factor of 50% of the biomass-mixed, pulverized coal-fired burner,
wherein the A/C relating to the biomass fuel is a ratio of biomass fuel primary air flow rate (Nm 3 /h) to biomass fuel (kg/h).

7. The biomass-mixed, pulverized coal-fired burner according to claim 3 , wherein the biomass fuel primary air is supplied such that the biomass-mixed, pulverized coal-fired burner is operated in a range that, with fuel containing 60% by weight of biomass fuel, is sandwiched between a first straight line and a second straight line as follows: the first straight line extending from A/C 0.5 relating to the biomass fuel to A/C 1.6 relating to the biomass fuel at a load factor of 100% of the biomass-mixed, pulverized coal-fired burner; and the second straight line extending from A/C 0.5 relating to the biomass fuel to A/C 2.4 relating to the biomass fuel at a load factor of 50% of the biomass-mixed, pulverized coal-fired burner,
wherein the A/C relating to the biomass fuel is a ratio of biomass fuel primary air flow rate (Nm 3 /h) to biomass fuel (kg/h).

8. The biomass-mixed, pulverized coal-fired burner according to claim 4 , wherein the biomass fuel primary air is supplied such that the biomass-mixed, pulverized coal-fired burner is operated in a range that, with fuel containing 60% by weight of biomass fuel, is sandwiched between a first straight line and a second straight line as follows: the first straight line extending from A/C 0.5 relating to the biomass fuel to A/C 1.6 relating to the biomass fuel at a load factor of 100% of the biomass-mixed, pulverized coal-fired burner; and the second straight line extending from A/C 0.5 relating to the biomass fuel to A/C 2.4 relating to the biomass fuel at a load factor of 50% of the biomass-mixed, pulverized coal-fired burner,
wherein the A/C relating to the biomass fuel is a ratio of biomass fuel primary air flow rate (Nm 3 /h) to biomass fuel (kg/h).

9. A fuel combustion method comprising:
burning biomas

Assignees

• Kawasaki Heavy Ind Ltd

Inventors

• Taniguchi Koji
• Kato Atsunori
• YABARA Suguru
• Tanabe Yutaka

Classifications

• F23D2201/10

  Nozzle tips · CPC title

• F23C2900/06041

  Staged supply of oxidant · CPC title

• F23D2201/20

  Fuel flow guiding devices · CPC title

• F23C7/004

  using vanes · CPC title

• F23G7/10 Primary

  of field or garden waste {or biomasses} · CPC title