CA2608051C - A burner with tiltable nozzles - Google Patents
A burner with tiltable nozzles Download PDFInfo
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- CA2608051C CA2608051C CA2608051A CA2608051A CA2608051C CA 2608051 C CA2608051 C CA 2608051C CA 2608051 A CA2608051 A CA 2608051A CA 2608051 A CA2608051 A CA 2608051A CA 2608051 C CA2608051 C CA 2608051C
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- Prior art keywords
- low
- portion nozzle
- concentration gas
- particle
- separator
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D1/00—Burners for combustion of pulverulent fuel
- F23D1/04—Burners producing cylindrical flames without centrifugal action
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D1/00—Burners for combustion of pulverulent fuel
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K3/00—Feeding or distributing of lump or pulverulent fuel to combustion apparatus
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K3/00—Feeding or distributing of lump or pulverulent fuel to combustion apparatus
- F23K3/02—Pneumatic feeding arrangements, i.e. by air blast
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D2201/00—Burners adapted for particulate solid or pulverulent fuels
- F23D2201/20—Fuel flow guiding devices
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
Abstract
To provide a low combustibility fuel firing burner that can ensure high ignition performance and combustion stability even if a gas flow rate is changed along with changes in boiler load or the like. A low combustibility fuel firing burner separates a pulverized low combustibility fuel supplied together with an air with a separator, distributing the separated fuel to a rich portion nozzle and a lean portion nozzle provided in a furnace, and burning the fuel, in which a variable control part such as a core or a flow adjusting/blocking valve is provided in at least one of a high-particle-concentration gas pipe extending from a downstream side of the separator and communicating with the rich portion nozzle and a low-particle-concentration gas pipe extending from the downstream side of the separator and communicating with the lean portion nozzle.
Description
A BURNER WITH TILTABLE NOZZLES
BACKGROUND OF THE INVENTION
1. FIELD OF THE INVENTION
The present invention relates to a low combustibility fuel firing burner applicable to various types of combustion apparatuses that burn a low combustibility fuel such as a pulverized coal boiler.
This application is based on Japanese Patent Application No. 2006-286692.
BACKGROUND OF THE INVENTION
1. FIELD OF THE INVENTION
The present invention relates to a low combustibility fuel firing burner applicable to various types of combustion apparatuses that burn a low combustibility fuel such as a pulverized coal boiler.
This application is based on Japanese Patent Application No. 2006-286692.
2. DESCRIPTION OF RELATED ART
Hitherto, a low combustibility fuel firing burner that burns a pulverized low combustibility fuel (hereinafter referred to as "burner") has been used in pulverized coal boilers fired with a low combustibility fuel such as anthracite or petroleum coke in a fine powder form.
For example, as shown in Figs. 4 and 5, a burner 10A of the related art, which burns a fuel that is pulverized coal obtained by pulverizing anthracite in a furnace 1 of a boiler is composed of a pulverized coal-air mixture system provided in the burner center and supplying a mixture of pulverized coal and a primary air set to about 100 C, and a secondary air system provided around the pulverized coal-air mixture system and supplying a secondary air set to about 300 to 350 C.
The primary air system includes a separator 20A provided upstream of a burner portion for the purpose of improving an ignition performance. The separator 20A is based on the principle of a cyclone. Thus, a portion with many fuel particles (rich portion) and a portion with few fuel particles (lean portion) can be obtained.
On the downstream side of the separator, the primary air system is branched to a rich portion nozzle 24 for introducing and burning a high-particle-concentration gas containing fuel particles in a high concentration and a lean portion nozzle 26 for introducing and burning a low-particle-concentration gas containing fuel particles in a low concentration. In general, in the case of using a low combustibility fuel, the whole burner 10A is inclined downwardly to improve the ignition performance.
Further, the lean portion nozzle 26 is provided on the side of a furnace wall 2 that forms a furnace 1 and is thus put under an oxygen atmosphere to prevent slagging.
In Figs. 4 and 5, reference numeral 23 denotes a high-particle-concentration gas pipe for introducing a high-particle-concentration gas to the rich portion nozzle 24; and from the separator 20A, a low-particle-concentration gas pipe for introducing a low-particle-concentration gas to the lean portion nozzle 26 from the separator 20A (see Japanese 25 Unexamined Patent Application, Publication No. Hei 8-178210
Hitherto, a low combustibility fuel firing burner that burns a pulverized low combustibility fuel (hereinafter referred to as "burner") has been used in pulverized coal boilers fired with a low combustibility fuel such as anthracite or petroleum coke in a fine powder form.
For example, as shown in Figs. 4 and 5, a burner 10A of the related art, which burns a fuel that is pulverized coal obtained by pulverizing anthracite in a furnace 1 of a boiler is composed of a pulverized coal-air mixture system provided in the burner center and supplying a mixture of pulverized coal and a primary air set to about 100 C, and a secondary air system provided around the pulverized coal-air mixture system and supplying a secondary air set to about 300 to 350 C.
The primary air system includes a separator 20A provided upstream of a burner portion for the purpose of improving an ignition performance. The separator 20A is based on the principle of a cyclone. Thus, a portion with many fuel particles (rich portion) and a portion with few fuel particles (lean portion) can be obtained.
On the downstream side of the separator, the primary air system is branched to a rich portion nozzle 24 for introducing and burning a high-particle-concentration gas containing fuel particles in a high concentration and a lean portion nozzle 26 for introducing and burning a low-particle-concentration gas containing fuel particles in a low concentration. In general, in the case of using a low combustibility fuel, the whole burner 10A is inclined downwardly to improve the ignition performance.
Further, the lean portion nozzle 26 is provided on the side of a furnace wall 2 that forms a furnace 1 and is thus put under an oxygen atmosphere to prevent slagging.
In Figs. 4 and 5, reference numeral 23 denotes a high-particle-concentration gas pipe for introducing a high-particle-concentration gas to the rich portion nozzle 24; and from the separator 20A, a low-particle-concentration gas pipe for introducing a low-particle-concentration gas to the lean portion nozzle 26 from the separator 20A (see Japanese 25 Unexamined Patent Application, Publication No. Hei 8-178210
3 (Fig. 5), for instance).
However, according to the above related art, when a gas flow rate is changed along with change in boiler load or the like, an ignition performance or combustion stability might be affected thereby. In particular, in the case of using a low combustibility fuel, an ignition performance or combustion stability is affected also by interference of flames of adjacent nozzles.
To be specific, a distribution rate of fuel particles is determined in accordance with a separation efficiency of the separator 20A. Thus, during partial load operations that cause reduction in gas supply, the separation efficiency of the separator 20A is accordingly lowered due to a decrease in centrifugal force. Therefore, it is difficult to attain a desired distribution rate for the rich portion nozzle 24 and the lean portion nozzle 26.
Further, if a burner is not used during partial load operations or a spare burner is used, there is a fear of backflow of a gas from the lean nozzle pipe 25 to a direction of the separator 20A due to a negative pressure.
The above change in distribution rate and gas backflow, or the interference of flames of adjacent nozzles affects the ignition performance or combustion stability of the low combustibility fuel firing burner 10A designed to distribute particles of a low combustibility fuel with the separator 20A,
However, according to the above related art, when a gas flow rate is changed along with change in boiler load or the like, an ignition performance or combustion stability might be affected thereby. In particular, in the case of using a low combustibility fuel, an ignition performance or combustion stability is affected also by interference of flames of adjacent nozzles.
To be specific, a distribution rate of fuel particles is determined in accordance with a separation efficiency of the separator 20A. Thus, during partial load operations that cause reduction in gas supply, the separation efficiency of the separator 20A is accordingly lowered due to a decrease in centrifugal force. Therefore, it is difficult to attain a desired distribution rate for the rich portion nozzle 24 and the lean portion nozzle 26.
Further, if a burner is not used during partial load operations or a spare burner is used, there is a fear of backflow of a gas from the lean nozzle pipe 25 to a direction of the separator 20A due to a negative pressure.
The above change in distribution rate and gas backflow, or the interference of flames of adjacent nozzles affects the ignition performance or combustion stability of the low combustibility fuel firing burner 10A designed to distribute particles of a low combustibility fuel with the separator 20A,
4 so there is an increasing demand to develop a low combustibility fuel firing burner that overcomes the above problems.
BRIEF SUMMARY OF THE INVENTION
The present invention has been accomplished in view of the above circumstances, and it is an object of the present invention to provide a low combustibility fuel firing burner that can ensure high ignition performance and combustion stability even if a gas flow rate is changed along with changes in boiler load or the like.
The present invention adopts the following solutions with a view to attaining the above object.
A low combustibility fuel firing burner according to an aspect of the present invention separates a pulverized low combustibility fuel supplied together with an air with a separator, distributes the separated fuel to a rich portion nozzle and a lean portion nozzle provided in a furnace, and burns the fuel, wherein a variable control part for changing a flow path sectional area is provided in at least one of a gas flow path extending from a downstream side of the separator and communicating with the rich portion nozzle and a gas flow path extending from the downstream side of the separator and communicating with the lean portion nozzle.
According to the low combustibility fuel firing burner of the present invention, the variable control part for changing a flow path sectional area is provided in at least one of the gas flow path communicating with the rich portion nozzle and the gas flow path communicating with the lean portion nozzle.
BRIEF SUMMARY OF THE INVENTION
The present invention has been accomplished in view of the above circumstances, and it is an object of the present invention to provide a low combustibility fuel firing burner that can ensure high ignition performance and combustion stability even if a gas flow rate is changed along with changes in boiler load or the like.
The present invention adopts the following solutions with a view to attaining the above object.
A low combustibility fuel firing burner according to an aspect of the present invention separates a pulverized low combustibility fuel supplied together with an air with a separator, distributes the separated fuel to a rich portion nozzle and a lean portion nozzle provided in a furnace, and burns the fuel, wherein a variable control part for changing a flow path sectional area is provided in at least one of a gas flow path extending from a downstream side of the separator and communicating with the rich portion nozzle and a gas flow path extending from the downstream side of the separator and communicating with the lean portion nozzle.
According to the low combustibility fuel firing burner of the present invention, the variable control part for changing a flow path sectional area is provided in at least one of the gas flow path communicating with the rich portion nozzle and the gas flow path communicating with the lean portion nozzle.
5 Hence, a sectional area of a gas flow path is appropriately changed and adjusted to the optimum value in accordance with operation conditions such as partial load operations.
In the low combustibility fuel firing burner, it is preferred that the variable control part be a movable resistor provided in a gas flow path for supplying a high-particle-concentration gas from the separator to the rich portion nozzle. Thus, a sectional area of a gas flow path for supplying a high-particle-concentration gas to the rich portion nozzle can be changed as appropriate. Hence, a gas flow rate in the gas flow path for supplying a high-particle-concentration gas is adjusted in accordance with operation conditions, and a separation efficiency of the separator can be optimized in accordance with operation conditions such as partial load operations.
In the low combustibility fuel firing burner, it is preferred that the variable control part be a flow adjusting/blocking valve provided in a gas flow path for supplying a low-particle-concentration gas from the separator to the lean portion nozzle. Thus, a sectional area of a gas flow path for supplying a low-particle-concentration gas to
In the low combustibility fuel firing burner, it is preferred that the variable control part be a movable resistor provided in a gas flow path for supplying a high-particle-concentration gas from the separator to the rich portion nozzle. Thus, a sectional area of a gas flow path for supplying a high-particle-concentration gas to the rich portion nozzle can be changed as appropriate. Hence, a gas flow rate in the gas flow path for supplying a high-particle-concentration gas is adjusted in accordance with operation conditions, and a separation efficiency of the separator can be optimized in accordance with operation conditions such as partial load operations.
In the low combustibility fuel firing burner, it is preferred that the variable control part be a flow adjusting/blocking valve provided in a gas flow path for supplying a low-particle-concentration gas from the separator to the lean portion nozzle. Thus, a sectional area of a gas flow path for supplying a low-particle-concentration gas to
6 the lean portion nozzle can be changed from a full-open position to a totally-closed position as appropriate. Hence, a gas flow rate in the gas flow path for supplying a low-particle-concentration gas can be adjusted in accordance with operation conditions, or the gas flow path can be closed when the burner is not used.
In the low combustibility fuel firing burner, it is preferred that a wall against which a low combustibility fuel supplied into the separator collides be given a hardwearing finish. Thus, a wear resistance of the wall against which slag, melted ash, and unburnt carbon collide is improved.
A low combustibility fuel firing burner according to another aspect of the present invention separates a pulverized low combustibility fuel supplied together with an air with a separator, distributes the separated fuel to a rich portion nozzle and a lean portion nozzle provided in a furnace, and burns the fuel, wherein a blowoff angle of the rich portion nozzle and a blowoff angle of the lean portion nozzle are offset in a vertical direction.
According to the low combustibility fuel firing burner, a blowoff angle of the rich portion nozzle and a blowoff angle of the lean portion nozzle are offset in a vertical direction, so interference of flames of nozzles can be prevented.
A low combustibility fuel firing burner according to another aspect of the present invention separates a pulverized
In the low combustibility fuel firing burner, it is preferred that a wall against which a low combustibility fuel supplied into the separator collides be given a hardwearing finish. Thus, a wear resistance of the wall against which slag, melted ash, and unburnt carbon collide is improved.
A low combustibility fuel firing burner according to another aspect of the present invention separates a pulverized low combustibility fuel supplied together with an air with a separator, distributes the separated fuel to a rich portion nozzle and a lean portion nozzle provided in a furnace, and burns the fuel, wherein a blowoff angle of the rich portion nozzle and a blowoff angle of the lean portion nozzle are offset in a vertical direction.
According to the low combustibility fuel firing burner, a blowoff angle of the rich portion nozzle and a blowoff angle of the lean portion nozzle are offset in a vertical direction, so interference of flames of nozzles can be prevented.
A low combustibility fuel firing burner according to another aspect of the present invention separates a pulverized
7 low combustibility fuel supplied together with an air with a separator, distributes the separated fuel to a rich portion nozzle and a lean portion nozzle provided in a furnace, and burns the fuel, wherein a blowoff angle of the lean portion nozzle is offset to a furnace wall side in a horizontal direction.
According to the low combustibility fuel firing burner, a blowoff angle of the lean portion nozzle is offset to a furnace wall side in a horizontal direction, so it is possible to prevent slagging on a furnace wall as well as interference of flames of nozzles.
According to the present invention, in the low combustibility fuel firing burner structured to distribute fuel particles of a low combustibility fuel with a separator, it is possible to prevent changes in distribution rate in accordance with operation conditions or gas backflow, so high ignition performance and combustion stability can be ensured.
Further, high ignition performance and combustion stability can be ensured by preventing interference of flames of adjacent nozzles as well.
BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWINGS
Fig. 1 is a cross-sectional view of a low combustibility fuel firing burner according to an embodiment of the present invention;
According to the low combustibility fuel firing burner, a blowoff angle of the lean portion nozzle is offset to a furnace wall side in a horizontal direction, so it is possible to prevent slagging on a furnace wall as well as interference of flames of nozzles.
According to the present invention, in the low combustibility fuel firing burner structured to distribute fuel particles of a low combustibility fuel with a separator, it is possible to prevent changes in distribution rate in accordance with operation conditions or gas backflow, so high ignition performance and combustion stability can be ensured.
Further, high ignition performance and combustion stability can be ensured by preventing interference of flames of adjacent nozzles as well.
BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWINGS
Fig. 1 is a cross-sectional view of a low combustibility fuel firing burner according to an embodiment of the present invention;
8 Fig. 2 is a longitudinal sectional view of a structural example of a separator and a primary air pipe of Fig. 1;
Fig. 3 is a longitudinal sectional view showing an example of a blowoff angle of a rich portion nozzle and a lean portion nozzle;
Fig. 4 is a cross-sectional view of a low combustibility fuel firing burner of the related art; and Fig. 5 is a longitudinal sectional view showing a blowoff angle of a rich portion nozzle and a lean portion nozzle of Fig. 4.
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, an embodiment of a low combustibility fuel firing burner according to the present invention will be described with reference to the accompanying drawings.
A low combustibility fuel firing burner (hereinafter simply referred to as "burner") 10 of Figs. 1 to 3 is provided in, for example, a furnace 1 of a pulverized coal boiler or the like. The burner 10 burns a powder (fine powder) of a low combustibility fuel supplied together with an air in the furnace 1. Specific examples of the low combustibility fuel include anthracite and petroleum coke.
The following description is directed to the burner 10 supplied with a fuel that is pulverized coal obtained by pulverizing anthracite as a low combustibility fuel.
Fig. 3 is a longitudinal sectional view showing an example of a blowoff angle of a rich portion nozzle and a lean portion nozzle;
Fig. 4 is a cross-sectional view of a low combustibility fuel firing burner of the related art; and Fig. 5 is a longitudinal sectional view showing a blowoff angle of a rich portion nozzle and a lean portion nozzle of Fig. 4.
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, an embodiment of a low combustibility fuel firing burner according to the present invention will be described with reference to the accompanying drawings.
A low combustibility fuel firing burner (hereinafter simply referred to as "burner") 10 of Figs. 1 to 3 is provided in, for example, a furnace 1 of a pulverized coal boiler or the like. The burner 10 burns a powder (fine powder) of a low combustibility fuel supplied together with an air in the furnace 1. Specific examples of the low combustibility fuel include anthracite and petroleum coke.
The following description is directed to the burner 10 supplied with a fuel that is pulverized coal obtained by pulverizing anthracite as a low combustibility fuel.
9 The burner 10 is composed of a pulverized coal supply system supplied with pulverized coal together with a primary air at a relatively low temperature, about 100 C, and a secondary air system supplied with a secondary air at a relatively high temperature, about 300 to 350 C.
The pulverized coal supply system is positioned at almost the center of the burner 10 and provided with a separator 20 for distributing a mixture of a primary air and pulverized coal to a rich portion and a lean portion as described later for the purpose of improving an ignition performance. The separator 20 has a cyclone structure that is based on centrifugal separation. A primary air pipe 22 for supplying a mixed gas from a tangent line direction is connected to a side wall of an external cylinder 21. A high-particle-concentration gas pipe 23 is connected to a small diameter portion 21a obtained by tapering the external cylinder 21 into a cone shape, and a rich portion nozzle 24 that is open to the furnace 1 is provided at its tip end.
Further, a low-particle-concentration gas pipe 25 is concentrically inserted into the external cylinder 21. The low-particle-concentration gas pipe 25 extends from the external cylinder 21 to the opposite side to the high-particle-concentration gas pipe 23 and makes a U-turn. A lean nozzle 26 is provided adjacent to the rich portion nozzle 24 at substantially the same level, at a tip end of the low-particle-concentration gas pipe 25. Incidentally, an opening 25a of the low-particle-concentration gas pipe 25 is positioned on the downstream side (rich portion nozzle 24 side) of a joint of the primary air pipe 22 in a flow 5 direction of the mixed gas.
As for a positional relationship between the rich portion nozzle 24 and the lean portion nozzle 26, the lean portion nozzle 26 for burning a low-particle-concentration gas is provided on the side of a furnace wall 2 that forms the
The pulverized coal supply system is positioned at almost the center of the burner 10 and provided with a separator 20 for distributing a mixture of a primary air and pulverized coal to a rich portion and a lean portion as described later for the purpose of improving an ignition performance. The separator 20 has a cyclone structure that is based on centrifugal separation. A primary air pipe 22 for supplying a mixed gas from a tangent line direction is connected to a side wall of an external cylinder 21. A high-particle-concentration gas pipe 23 is connected to a small diameter portion 21a obtained by tapering the external cylinder 21 into a cone shape, and a rich portion nozzle 24 that is open to the furnace 1 is provided at its tip end.
Further, a low-particle-concentration gas pipe 25 is concentrically inserted into the external cylinder 21. The low-particle-concentration gas pipe 25 extends from the external cylinder 21 to the opposite side to the high-particle-concentration gas pipe 23 and makes a U-turn. A lean nozzle 26 is provided adjacent to the rich portion nozzle 24 at substantially the same level, at a tip end of the low-particle-concentration gas pipe 25. Incidentally, an opening 25a of the low-particle-concentration gas pipe 25 is positioned on the downstream side (rich portion nozzle 24 side) of a joint of the primary air pipe 22 in a flow 5 direction of the mixed gas.
As for a positional relationship between the rich portion nozzle 24 and the lean portion nozzle 26, the lean portion nozzle 26 for burning a low-particle-concentration gas is provided on the side of a furnace wall 2 that forms the
10 furnace 1.
A variable control part for changing a flow path sectional area is provided in at least one of a gas flow path communicating with the rich portion nozzle 24 and a gas flow path communication with the lean portion nozzle 26 on the downstream side of the separator 20.
In the illustrated structure, a core 27 that is, for example, triangular in section is provided as a movable resistor that can reciprocate in a gas flow direction, in the small diameter portion 21a connected to the high-particle-concentration gas pipe 23 for supplying a high-particle-concentration gas from the separator 20 to the rich portion nozzle 24. Along with movement of the core 27 in the small diameter portion 21a in an axial direction as indicated by an arrow 28, a sectional area of a flow path extending from the separator 20 to the high-particle-concentration gas pipe 23 is
A variable control part for changing a flow path sectional area is provided in at least one of a gas flow path communicating with the rich portion nozzle 24 and a gas flow path communication with the lean portion nozzle 26 on the downstream side of the separator 20.
In the illustrated structure, a core 27 that is, for example, triangular in section is provided as a movable resistor that can reciprocate in a gas flow direction, in the small diameter portion 21a connected to the high-particle-concentration gas pipe 23 for supplying a high-particle-concentration gas from the separator 20 to the rich portion nozzle 24. Along with movement of the core 27 in the small diameter portion 21a in an axial direction as indicated by an arrow 28, a sectional area of a flow path extending from the separator 20 to the high-particle-concentration gas pipe 23 is
11 changed. In other words, a sectional area of a flow path of the high-particle-concentration gas pipe 23 is substantially changed.
Incidentally, the movable resistor is not limited to the illustrated core 27. For example, a butterfly valve or other such members capable of changing a sectional area of a flow path of the high-particle-concentration gas pipe 23 can be used.
In a gas flow path for supplying a low-particle-concentration gas from the separator 20 to the lean portion nozzle 26, that is, in an appropriate position in the low-particle-concentration gas pipe 25, a flow adjusting/blocking valve 29 such as a butterfly valve is provided as the variable control part. The flow adjusting/blocking valve 29 changes a valve member position from a totally-closed position to a full-open position to thereby adjust a sectional area of a flow path extending from the separator 20 to the low-particle-concentration gas pipe 25. Further, the flow adjusting/blocking valve 29 can totally close the low-particle-concentration gas pipe 25 (flow path sectional area=0) if necessary.
A secondary air supply path (secondary air pipe) 30 that communicates with the furnace 1 is provided around the rich portion nozzle 24 and the lean portion nozzle 26 so as to surround the two nozzles. Here, the secondary air supply path
Incidentally, the movable resistor is not limited to the illustrated core 27. For example, a butterfly valve or other such members capable of changing a sectional area of a flow path of the high-particle-concentration gas pipe 23 can be used.
In a gas flow path for supplying a low-particle-concentration gas from the separator 20 to the lean portion nozzle 26, that is, in an appropriate position in the low-particle-concentration gas pipe 25, a flow adjusting/blocking valve 29 such as a butterfly valve is provided as the variable control part. The flow adjusting/blocking valve 29 changes a valve member position from a totally-closed position to a full-open position to thereby adjust a sectional area of a flow path extending from the separator 20 to the low-particle-concentration gas pipe 25. Further, the flow adjusting/blocking valve 29 can totally close the low-particle-concentration gas pipe 25 (flow path sectional area=0) if necessary.
A secondary air supply path (secondary air pipe) 30 that communicates with the furnace 1 is provided around the rich portion nozzle 24 and the lean portion nozzle 26 so as to surround the two nozzles. Here, the secondary air supply path
12 30 serves as a secondary air system provided for supplying an air at relatively high temperatures to the both of the nozzles 24 and 26.
In the above separator 20, a mixed gas supplied from the primary air pipe 22 flows while whirling around the low-particle-concentration gas pipe 25 in the external cylinder 21 to thereby centrifuge the mixture to a peripheral rich portion and a central lean portion. As a result, a high-particle-concentration gas containing pulverized coal in a high particle concentration flows in a gas flow direction while whirling around the low-particle-concentration gas pipe 25, and is guided to the rich portion nozzle 24 through the small diameter portion 21a and the high-particle-concentration gas pipe 23. On the other hand, a low-particle-concentration gas containing pulverized coal in a low particle concentration flows in a gas flow direction while whirling around the low-particle-concentration gas pipe 25 and then makes a U-turn to the opening 25a of the low-particle-concentration gas pipe 25, and is guided to the lean portion nozzle 26 through the low-particle-concentration gas pipe 25.
With regard to a distribution rate of fuel particles suitable in the case of using pulverized coal obtained by pulverizing anthracite as a fuel, that is, a distribution rate of fuel particles suitable to keep high ignition performance and combustion stability, about 93% of pulverized coal and
In the above separator 20, a mixed gas supplied from the primary air pipe 22 flows while whirling around the low-particle-concentration gas pipe 25 in the external cylinder 21 to thereby centrifuge the mixture to a peripheral rich portion and a central lean portion. As a result, a high-particle-concentration gas containing pulverized coal in a high particle concentration flows in a gas flow direction while whirling around the low-particle-concentration gas pipe 25, and is guided to the rich portion nozzle 24 through the small diameter portion 21a and the high-particle-concentration gas pipe 23. On the other hand, a low-particle-concentration gas containing pulverized coal in a low particle concentration flows in a gas flow direction while whirling around the low-particle-concentration gas pipe 25 and then makes a U-turn to the opening 25a of the low-particle-concentration gas pipe 25, and is guided to the lean portion nozzle 26 through the low-particle-concentration gas pipe 25.
With regard to a distribution rate of fuel particles suitable in the case of using pulverized coal obtained by pulverizing anthracite as a fuel, that is, a distribution rate of fuel particles suitable to keep high ignition performance and combustion stability, about 93% of pulverized coal and
13 about 50% of air in the total amount of mixed gas are distributed to the rich portion nozzle 24, and about 7% of pulverized coal and 50% of air in the total amount of mixed gas are distributed to the lean portion nozzle 26.
In the thus-structured nozzle 10, if a mixed gas supply is changed along with changes in boiler load or the like, the distribution rate of fuel particles is changed, so a predetermined distribution rate of fuel particles is kept by adjusting the core 27 position.
To be specific, the opening 25a of the low-particle-concentration gas pipe 25 is designed to obtain a desired distribution rate of fuel particles with an amount of mixed gas supplied under predetermined operation conditions such as rated operations. Thus, if a supply of the mixed gas is decreased, an amount of pulverized coal distributed to the high-particle-concentration gas side tends to decrease due to reduction in centrifugal force. To that end, the core 27 is moved in the arrow 28 direction in accordance with the decrease in mixed gas supply to thereby increase a sectional area of a flow path communicating with the high-particle-concentration gas pipe 23 from the separator 20. As a result, a resistance of the flow path extending to the rich portion nozzle 24 is lowered, and an amount of pulverized coal distributed to the rich portion nozzle 24 side is increased.
Hence, a distribution rate of pulverized coal is adjusted to a
In the thus-structured nozzle 10, if a mixed gas supply is changed along with changes in boiler load or the like, the distribution rate of fuel particles is changed, so a predetermined distribution rate of fuel particles is kept by adjusting the core 27 position.
To be specific, the opening 25a of the low-particle-concentration gas pipe 25 is designed to obtain a desired distribution rate of fuel particles with an amount of mixed gas supplied under predetermined operation conditions such as rated operations. Thus, if a supply of the mixed gas is decreased, an amount of pulverized coal distributed to the high-particle-concentration gas side tends to decrease due to reduction in centrifugal force. To that end, the core 27 is moved in the arrow 28 direction in accordance with the decrease in mixed gas supply to thereby increase a sectional area of a flow path communicating with the high-particle-concentration gas pipe 23 from the separator 20. As a result, a resistance of the flow path extending to the rich portion nozzle 24 is lowered, and an amount of pulverized coal distributed to the rich portion nozzle 24 side is increased.
Hence, a distribution rate of pulverized coal is adjusted to a
14 predetermined value.
On the other hand, if a supply of mixed gas is increased, an amount of pulverized coal distributed to the high-particle-concentration gas side tends to increase due to an increase in centrifugal force. To that end, the core 27 is moved in the arrow 28 direction in accordance with an increase in mixed gas supply to thereby decrease a sectional area of a flow path communicating with the high-particle-concentration gas pipe 23 from the separator 20. As a result, a resistance of a flow path extending to the rich portion nozzle 24 is increased and an amount of pulverized coal distributed to the rich portion nozzle 24 side is decreased. In this case as well, a distribution rate of pulverized coal is adjusted to a predetermined value.
Further, the distribution rate can be adjusted by controlling the flow adjusting/blocking valve 29 provided in the low-particle-concentration gas pipe 25.
To be specific, if the mixed gas supply is decreased, the flow adjusting/blocking valve 29 is closed in accordance with the decrease in mixed gas supply to thereby reduce a sectional area of a flow path of the low-particle-concentration gas pipe 25. As a result, a resistance of a flow path extending to the lean portion nozzle 26 is increased, while a resistance of a flow path extending to the rich portion nozzle 24 is relatively decreased, so an amount of pulverized coal distributed to the rich portion nozzle 24 side is increased, and a distribution rate of pulverized coal is adjusted to a predetermined value.
On the other hand, if the mixed gas supply is increased, 5 the flow adjusting/blocking valve 29 is opened in accordance with the increase in mixed gas supply to thereby increase a sectional area of a flow path of the low-particle-concentration gas pipe 25. As a result, a resistance of a flow path extending to the lean portion nozzle 26 is 10 decreased, while a resistance of a flow path extending to the rich portion nozzle 24 is relatively increased, so an amount of pulverized coal distributed to the rich portion nozzle 24 side is decreased, and a distribution rate of pulverized coal is adjusted to a predetermined value.
On the other hand, if a supply of mixed gas is increased, an amount of pulverized coal distributed to the high-particle-concentration gas side tends to increase due to an increase in centrifugal force. To that end, the core 27 is moved in the arrow 28 direction in accordance with an increase in mixed gas supply to thereby decrease a sectional area of a flow path communicating with the high-particle-concentration gas pipe 23 from the separator 20. As a result, a resistance of a flow path extending to the rich portion nozzle 24 is increased and an amount of pulverized coal distributed to the rich portion nozzle 24 side is decreased. In this case as well, a distribution rate of pulverized coal is adjusted to a predetermined value.
Further, the distribution rate can be adjusted by controlling the flow adjusting/blocking valve 29 provided in the low-particle-concentration gas pipe 25.
To be specific, if the mixed gas supply is decreased, the flow adjusting/blocking valve 29 is closed in accordance with the decrease in mixed gas supply to thereby reduce a sectional area of a flow path of the low-particle-concentration gas pipe 25. As a result, a resistance of a flow path extending to the lean portion nozzle 26 is increased, while a resistance of a flow path extending to the rich portion nozzle 24 is relatively decreased, so an amount of pulverized coal distributed to the rich portion nozzle 24 side is increased, and a distribution rate of pulverized coal is adjusted to a predetermined value.
On the other hand, if the mixed gas supply is increased, 5 the flow adjusting/blocking valve 29 is opened in accordance with the increase in mixed gas supply to thereby increase a sectional area of a flow path of the low-particle-concentration gas pipe 25. As a result, a resistance of a flow path extending to the lean portion nozzle 26 is 10 decreased, while a resistance of a flow path extending to the rich portion nozzle 24 is relatively increased, so an amount of pulverized coal distributed to the rich portion nozzle 24 side is decreased, and a distribution rate of pulverized coal is adjusted to a predetermined value.
15 In this way, the distribution rate of pulverized coal can be adjusted by moving the core 27 or opening/closing the flow adjusting/blocking valve 29, so at least one of the core 27 and the flow adjusting/blocking valve 29 has only to be provided. However, both of the core 27 and the flow adjusting/blocking valve 29 may be moved at the same time to adjust the rate.
Further, if the flow adjusting/blocking valve 29 is totally closed, the low-particle-concentration gas pipe 25 can be blocked. Hence, it is possible to prevent backflow from C
the lean portion nozzle 26 to the separator 20 side, for
Further, if the flow adjusting/blocking valve 29 is totally closed, the low-particle-concentration gas pipe 25 can be blocked. Hence, it is possible to prevent backflow from C
the lean portion nozzle 26 to the separator 20 side, for
16 example, if the burner 10 is not used.
Incidentally, the external cylinder 21 of the separator 20 has an area against which pulverized particles flowing therein from the primary air pipe 22 at high speeds collide.
To that end, on an inner wall of the area, a wear-resistant wall 21b that is optionally given a hardwearing finish is formed as shown in Fig. 2.
To elaborate, conceivable examples of the hardwearing finish include bonding with a ceramic material or wear-resistant hardfacing (25Cr cast iron, CHR-3, etc.). A wear resistance is improved by forming the wear-resistant wall 21b, so even if pulverized coal particles collide against the cylinder, the cylinder does not thin out at an early stage, and a durability of the separator 20 can be improved.
Further, as for the positional relationship between the rich portion nozzle 24 and the lean portion nozzle 26, the lean portion nozzle 26 is provided close to the furnace wall 2 side. In addition, the lean portion nozzle 26 is preferably attached with an offset relative to the furnace wall 2 side in a horizontal direction. That is, as shown in the plane view of Fig. 1, a blowoff angle of the lean portion nozzle 26 is offset from that of the rich portion nozzle 24 that ejects a gas in a direction parallel to the furnace wall 2 as viewed in the horizontal direction of Fig. 1, and an ejection direction of the lean portion nozzle 26 is directed toward the furnace
Incidentally, the external cylinder 21 of the separator 20 has an area against which pulverized particles flowing therein from the primary air pipe 22 at high speeds collide.
To that end, on an inner wall of the area, a wear-resistant wall 21b that is optionally given a hardwearing finish is formed as shown in Fig. 2.
To elaborate, conceivable examples of the hardwearing finish include bonding with a ceramic material or wear-resistant hardfacing (25Cr cast iron, CHR-3, etc.). A wear resistance is improved by forming the wear-resistant wall 21b, so even if pulverized coal particles collide against the cylinder, the cylinder does not thin out at an early stage, and a durability of the separator 20 can be improved.
Further, as for the positional relationship between the rich portion nozzle 24 and the lean portion nozzle 26, the lean portion nozzle 26 is provided close to the furnace wall 2 side. In addition, the lean portion nozzle 26 is preferably attached with an offset relative to the furnace wall 2 side in a horizontal direction. That is, as shown in the plane view of Fig. 1, a blowoff angle of the lean portion nozzle 26 is offset from that of the rich portion nozzle 24 that ejects a gas in a direction parallel to the furnace wall 2 as viewed in the horizontal direction of Fig. 1, and an ejection direction of the lean portion nozzle 26 is directed toward the furnace
17 wall 2 side. In this case, a preferred blowoff angle Oh is about 10 degrees; the blowoff angle 9h is an angle offset from the rich portion nozzle 24 toward the furnace wall 2 side with respect to the horizontal direction.
As described above, if the blowoff angle of the lean portion nozzle 26 is offset to the furnace wall 2 side in the horizontal direction, it is possible to prevent interference of flames of the adjacent rich portion nozzle 24 and lean portion nozzle 26, and a fuel can be continuously burned under satisfactory conditions with a small loss. In addition, an ignition performance can be improved. Moreover, the ejection direction of the lean portion nozzle 26 is directed to the furnace wall 2 side due to the offset, so slagging as adherence of foreign materials such as coal ash to the furnace 1 wall can be suppressed.
Further, as for the positional relationship between the rich portion nozzle 24 and the lean portion nozzle 26, the lean portion nozzle 26 is provided close to the furnace wall 2 side. In addition, as shown in Fig. 3, the lean portion nozzle 26 is preferably attached with an offset between the blowoff angle of the rich portion nozzle 24 and the blowoff angle of the lean portion nozzle 26 in the vertical direction.
More specifically, it is preferred to set the ejection direction of the lean portion nozzle 26 to a horizontal O
direction, and to tilt the rich portion nozzle 24 downwardly
As described above, if the blowoff angle of the lean portion nozzle 26 is offset to the furnace wall 2 side in the horizontal direction, it is possible to prevent interference of flames of the adjacent rich portion nozzle 24 and lean portion nozzle 26, and a fuel can be continuously burned under satisfactory conditions with a small loss. In addition, an ignition performance can be improved. Moreover, the ejection direction of the lean portion nozzle 26 is directed to the furnace wall 2 side due to the offset, so slagging as adherence of foreign materials such as coal ash to the furnace 1 wall can be suppressed.
Further, as for the positional relationship between the rich portion nozzle 24 and the lean portion nozzle 26, the lean portion nozzle 26 is provided close to the furnace wall 2 side. In addition, as shown in Fig. 3, the lean portion nozzle 26 is preferably attached with an offset between the blowoff angle of the rich portion nozzle 24 and the blowoff angle of the lean portion nozzle 26 in the vertical direction.
More specifically, it is preferred to set the ejection direction of the lean portion nozzle 26 to a horizontal O
direction, and to tilt the rich portion nozzle 24 downwardly
18 by a predetermined blowoff angle Av. In this case, a preferred inclination angle 9v of the rich portion nozzle 24 is approximately -10 degrees to 30 degrees, most preferably, 30 degrees on the provision that an angle increases (+) as a distance from the horizontal position as a reference position increases. This is because if the inclination angle Av is larger than 30 degrees, interference of flames of adjacent upper and lower nozzles 24 occurs this time.
An offset is set between the blowoff angles of the rich portion nozzle 24 and the lean portion nozzle 26 in the vertical direction as described above, making it possible to prevent interference of flames of the adjacent rich portion nozzle 24 and lean portion nozzle 26. Hence, a fuel can be continuously burned under satisfactory conditions with a small loss, and an ignition performance can be improved.
Incidentally, if the blowoff angles of the rich portion nozzle 24 and the lean portion nozzle 26 have offsets in vertical and horizontal directions, interference of flames can be prevented more easily.
According to the present invention, in the burner 10 structured to distribute fuel particles of a low combustibility fuel with the separator 20, the core 27 or the flow adjusting/blocking valve 29 is moved to prevent changes in distribution rate in accordance with operation conditions and gas backflow, so high ignition performance and combustion
An offset is set between the blowoff angles of the rich portion nozzle 24 and the lean portion nozzle 26 in the vertical direction as described above, making it possible to prevent interference of flames of the adjacent rich portion nozzle 24 and lean portion nozzle 26. Hence, a fuel can be continuously burned under satisfactory conditions with a small loss, and an ignition performance can be improved.
Incidentally, if the blowoff angles of the rich portion nozzle 24 and the lean portion nozzle 26 have offsets in vertical and horizontal directions, interference of flames can be prevented more easily.
According to the present invention, in the burner 10 structured to distribute fuel particles of a low combustibility fuel with the separator 20, the core 27 or the flow adjusting/blocking valve 29 is moved to prevent changes in distribution rate in accordance with operation conditions and gas backflow, so high ignition performance and combustion
19 stability can be ensured. Further, an offset is set between ejection directions of the rich portion nozzle 24 and the lean portion nozzle 26 to prevent interference of flames of adjacent nozzles to thereby ensure high ignition performance and combustion stability.
The present invention is not limited to the above-described embodiment and might be modified as appropriate without departing from the scope of the present invention.
O
The present invention is not limited to the above-described embodiment and might be modified as appropriate without departing from the scope of the present invention.
O
Claims (5)
EXCLUSIVE PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS
FOLLOWS:
1. A low combustibility fuel firing burner for burning a pulverized low combustibility fuel comprising:
(a) a separator for separating said pulverized low combustibility fuel into a high-particle concentration gas and a low-particle concentration gas;
(b) a supply means for supplying said pulverized low combustibility fuel together with an air to said separator;
(c) a high-particle concentration gas pipe for distributing the high-particle concentration gas to a rich portion nozzle provided in a furnace, said high-particle concentration gas pipe defining a rich gas flow path extending from a downstream side of the separator and communicating with the rich portion nozzle;
(d) a low-particle concentration gas pipe for distributing the low-particle concentration gas to a lean portion nozzle provided in the furnace, said low-particle concentration gas pipe defining a lean gas flow path extending from the downstream side of the separator and communicating with the lean portion nozzle;
(e) a first variable control means for changing the flow path sectional area of the lean gas flow path; and (f) a second variable control means for changing the flow path sectional area of the rich gas flow path, wherein the first variable control means and the second variable control means are adapted to control the flow rate of the high-particle-concentration gas and the low-particle-concentration gas, and the ratio between the high-particle concentration gas and the low-particle concentration gas.
(a) a separator for separating said pulverized low combustibility fuel into a high-particle concentration gas and a low-particle concentration gas;
(b) a supply means for supplying said pulverized low combustibility fuel together with an air to said separator;
(c) a high-particle concentration gas pipe for distributing the high-particle concentration gas to a rich portion nozzle provided in a furnace, said high-particle concentration gas pipe defining a rich gas flow path extending from a downstream side of the separator and communicating with the rich portion nozzle;
(d) a low-particle concentration gas pipe for distributing the low-particle concentration gas to a lean portion nozzle provided in the furnace, said low-particle concentration gas pipe defining a lean gas flow path extending from the downstream side of the separator and communicating with the lean portion nozzle;
(e) a first variable control means for changing the flow path sectional area of the lean gas flow path; and (f) a second variable control means for changing the flow path sectional area of the rich gas flow path, wherein the first variable control means and the second variable control means are adapted to control the flow rate of the high-particle-concentration gas and the low-particle-concentration gas, and the ratio between the high-particle concentration gas and the low-particle concentration gas.
2. The low combustibility fuel firing burner according to claim 1, wherein the first variable control means is a flow adjusting/blocking valve provided in said lean gas flow path.
3. The low combustibility fuel firing burner according to claim 1 or claim 2, wherein a wall against which the low combustibility fuel supplied into the separator collides is given a hardwearing finish.
4. The low combustibility fuel firing burner according to any one of claims 1 to 3, wherein a blowoff angle of the rich portion nozzle and a blowoff angle of the lean portion nozzle are offset in a vertical direction.
5. The low combustibility fuel firing burner according to any one of claims 1 to 3, wherein a blowoff angle of the lean portion nozzle is offset to a furnace wall side in a horizontal direction.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2006-286692 | 2006-10-20 | ||
| JP2006286692A JP5021999B2 (en) | 2006-10-20 | 2006-10-20 | Flame retardant fuel burner |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2608051A1 CA2608051A1 (en) | 2008-04-20 |
| CA2608051C true CA2608051C (en) | 2013-01-08 |
Family
ID=38804931
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA2608051A Expired - Fee Related CA2608051C (en) | 2006-10-20 | 2007-10-17 | A burner with tiltable nozzles |
Country Status (9)
| Country | Link |
|---|---|
| US (1) | US20080092789A1 (en) |
| EP (1) | EP1916476A3 (en) |
| JP (1) | JP5021999B2 (en) |
| KR (1) | KR100951214B1 (en) |
| CN (1) | CN101165400A (en) |
| CA (1) | CA2608051C (en) |
| CL (1) | CL2007002944A1 (en) |
| MX (1) | MX2007012952A (en) |
| TW (1) | TWI429853B (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101881441B (en) * | 2010-06-18 | 2013-03-27 | 王兴道 | Gasification combustion hydrolyzing auxiliary combustion device and method of pulverized coal |
| US8882400B2 (en) * | 2010-10-29 | 2014-11-11 | General Electric Company | Solids feeder discharge port |
| GB201502891D0 (en) * | 2015-02-20 | 2015-04-08 | Doosan Babcock Ltd | Downshot burner |
| CN107152678B (en) * | 2016-03-02 | 2019-08-30 | 山西三合盛节能环保技术股份有限公司 | A kind of enhancing shunts the pulverized coal decoupling combustor and combustion method of enrichment |
| CN110043898B (en) * | 2019-04-10 | 2020-02-21 | 清华大学 | Multi-stage backflow reverse-spraying type cyclone pulverized coal burner |
| IT201900020510A1 (en) | 2019-11-06 | 2021-05-06 | Ac Boilers S P A | BURNER GROUP, METHOD FOR OPERATING SAID BURNER GROUP AND SYSTEM INCLUDING SAID BURNER GROUP |
Family Cites Families (24)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4252069A (en) * | 1979-04-13 | 1981-02-24 | Combustion Engineering, Inc. | Low load coal bucket |
| US4448135A (en) | 1981-11-16 | 1984-05-15 | The Babcock & Wilcox Company | Inline air-coal separator |
| US4412496A (en) * | 1982-04-27 | 1983-11-01 | Foster Wheeler Energy Corp. | Combustion system and method for a coal-fired furnace utilizing a low load coal burner |
| CA1190093A (en) * | 1982-08-06 | 1985-07-09 | Ralph D. Winship | Method of reducing no.sub.x and so.sub.x emission |
| US4570549A (en) * | 1984-05-17 | 1986-02-18 | Trozzi Norman K | Splitter for use with a coal-fired furnace utilizing a low load burner |
| US4627366A (en) * | 1985-09-16 | 1986-12-09 | The Babcock & Wilcox Company | Primary air exchange for a pulverized coal burner |
| US4655148A (en) * | 1985-10-29 | 1987-04-07 | Combustion Engineering, Inc. | Method of introducing dry sulfur oxide absorbent material into a furnace |
| JPH05649Y2 (en) | 1986-02-21 | 1993-01-11 | ||
| JPH0512578Y2 (en) * | 1987-04-24 | 1993-03-31 | ||
| JP2641738B2 (en) * | 1987-10-07 | 1997-08-20 | バブコツク日立株式会社 | Pulverized coal combustion equipment |
| FI87246C (en) * | 1989-04-10 | 1992-12-10 | Ahlstroem Oy | PROCEDURE FOR MEASUREMENT OF INSPECTION OF FUERBRAENNINGSLUFT I EN ELDSTAD |
| JPH0348643A (en) * | 1989-07-18 | 1991-03-01 | Mitsui Toatsu Chem Inc | Production of non-cyclic ethyleneamines |
| US5363812A (en) * | 1994-02-18 | 1994-11-15 | The Babcock & Wilcox Company | Method and apparatus for controlling the bed temperature in a circulating fluidized bed reactor |
| FI96541C (en) * | 1994-10-03 | 1996-07-10 | Ahlstroem Oy | Device on a wall and method for coating the wall |
| JPH08178210A (en) * | 1994-12-26 | 1996-07-12 | Mitsubishi Heavy Ind Ltd | Burner of furnace for gyratory combustion |
| US5678499A (en) * | 1995-07-03 | 1997-10-21 | Foster Wheeler Energy Corporation | System for preheating fuel |
| US5611682A (en) * | 1995-09-05 | 1997-03-18 | Air Products And Chemicals, Inc. | Low-NOx staged combustion device for controlled radiative heating in high temperature furnaces |
| JP2995013B2 (en) * | 1997-03-31 | 1999-12-27 | 三菱重工業株式会社 | Pulverized fuel combustion burner |
| US5937772A (en) * | 1997-07-30 | 1999-08-17 | Institute Of Gas Technology | Reburn process |
| US6475267B2 (en) * | 2000-12-13 | 2002-11-05 | Foster Wheeler Energy Corporation | System and method for removing gas from a stream of a mixture of gas and particulate solids |
| JP3679998B2 (en) * | 2001-01-31 | 2005-08-03 | 三菱重工業株式会社 | Pulverized coal burner |
| CA2410725C (en) * | 2001-11-16 | 2008-07-22 | Hitachi, Ltd. | Solid fuel burner, burning method using the same, combustion apparatus and method of operating the combustion apparatus |
| US6986311B2 (en) * | 2003-01-22 | 2006-01-17 | Joel Vatsky | Burner system and method for mixing a plurality of solid fuels |
| US6923203B2 (en) * | 2003-05-29 | 2005-08-02 | Rickey E. Wark | Variable orifice valve for airstream containing particulate coal |
-
2006
- 2006-10-20 JP JP2006286692A patent/JP5021999B2/en not_active Expired - Fee Related
-
2007
- 2007-10-04 TW TW096137289A patent/TWI429853B/en not_active IP Right Cessation
- 2007-10-11 EP EP07118299A patent/EP1916476A3/en not_active Withdrawn
- 2007-10-12 CL CL200702944A patent/CL2007002944A1/en unknown
- 2007-10-16 US US11/907,652 patent/US20080092789A1/en not_active Abandoned
- 2007-10-16 KR KR1020070103787A patent/KR100951214B1/en active IP Right Grant
- 2007-10-17 CN CNA2007101823307A patent/CN101165400A/en active Pending
- 2007-10-17 CA CA2608051A patent/CA2608051C/en not_active Expired - Fee Related
- 2007-10-17 MX MX2007012952A patent/MX2007012952A/en active IP Right Grant
Also Published As
| Publication number | Publication date |
|---|---|
| KR100951214B1 (en) | 2010-04-06 |
| JP5021999B2 (en) | 2012-09-12 |
| EP1916476A2 (en) | 2008-04-30 |
| KR20080035966A (en) | 2008-04-24 |
| TW200829833A (en) | 2008-07-16 |
| CN101165400A (en) | 2008-04-23 |
| JP2008101883A (en) | 2008-05-01 |
| CA2608051A1 (en) | 2008-04-20 |
| EP1916476A3 (en) | 2013-02-27 |
| CL2007002944A1 (en) | 2008-05-30 |
| US20080092789A1 (en) | 2008-04-24 |
| TWI429853B (en) | 2014-03-11 |
| MX2007012952A (en) | 2009-02-13 |
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| EEER | Examination request | ||
| MKLA | Lapsed |
Effective date: 20211018 |