CN205717289U - Coal dust amount automatic adjustable pulverized coal carried by hot air boiler - Google Patents
Coal dust amount automatic adjustable pulverized coal carried by hot air boiler Download PDFInfo
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- CN205717289U CN205717289U CN201620457185.3U CN201620457185U CN205717289U CN 205717289 U CN205717289 U CN 205717289U CN 201620457185 U CN201620457185 U CN 201620457185U CN 205717289 U CN205717289 U CN 205717289U
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- coal
- boiler
- pulverized
- pulverized coal
- pipeline
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Abstract
The utility model discloses a kind of coal dust amount automatic adjustable pulverized coal carried by hot air boiler, including coal feedstock transportation mechanism, coal dust separating mechanism, mill exhauster, boiler, Pulverized Coal Bin and first, second and third airduct, also include mateiral pump, flow control valve and boiler combustion detector, described mateiral pump and described flow control valve are installed on described feed pipe, described boiler combustion detector is arranged on described boiler, described boiler combustion detector communicates to connect with described flow control valve, and described flow control valve is messaging in described mateiral pump；Also include sack cleaner and spiral powder conveying machine, described third time airduct is connected with described sack cleaner, being installed with lock gate hatch and regulation door between described third time airduct and described sack cleaner, described spiral powder conveying machine is connected between described sack cleaner and described Pulverized Coal Bin；This coal dust amount automatic adjustable pulverized coal carried by hot air boiler can improve efficiency of combustion, reduces discharge, automatically adjusts the coal dust amount of feeding.
Description
Technical field
This utility model relates to pulverized coal carried by hot air field of boilers, particularly relates to a kind of coal dust amount automatic adjustable pulverized coal carried by hot air pot
Stove.
Background technology
Joining the boiler of pulverized coal carried by hot air the ball type pulverizer system, due to the existence of a large amount of tertiary airs, the burning to boiler exists
Extremely disadvantageous impact, causes boiler economics to reduce, discharged nitrous oxides is too high, exclusion secondary wind causes cannot effective group
Knit burning etc. in stove.
The most domestic Coal-pulverizing Systems with Ball Mill also having larger proportion.The existence smoke evacuation in various degree of these boilers
The situation of temperature drift, and the situation that furnace outlet discharged nitrous oxides exceeds standard the most generally exists, major part is fired through too low nitrogen
The unit of burner transformation is the most less desirable for the effect of fall nitrogen.So transforming targetedly, either from economic benefit,
It is all that necessary carrying out is studied and practice for environmental benefit or market prospect.
Existing pulverized coal carried by hot air boiler cannot adjust the amount of feeding of coal dust in combustion at any time, and the coal dust amount of feeding is too high
Can cause burning completely, waste raw material very much, too increase cost, the too low meeting of the coal dust amount of feeding causes efficiency of combustion low,
Do not reach combustion standard.
Because above-mentioned defect, the design people, the most in addition research and innovation, it is automatically adjusted to founding a kind of coal dust amount
Formula pulverized coal carried by hot air boiler so that it is have more the value in industry.
Utility model content
For solving above-mentioned technical problem, the purpose of this utility model is to provide one can improve efficiency of combustion, reduces row
Put, automatically adjust the coal dust amount automatic adjustable pulverized coal carried by hot air boiler of the coal dust amount of feeding.
A kind of coal dust amount automatic adjustable pulverized coal carried by hot air boiler that the utility model proposes, it is characterised in that: include that coal is former
Material conveyer structure, coal dust separating mechanism, mill exhauster, boiler, Pulverized Coal Bin and first, second and third airduct, described coal dust separating mechanism
Being connected to by pipeline is the top of described conveying coal feedstock transportation mechanism, and described Pulverized Coal Bin is connected to described coal dust by pipeline
The lower section of separating mechanism, a fixed feed pipe in described Pulverized Coal Bin, described feed pipe is connected on described first time airduct, described
Mill exhauster is connected to the side of described coal dust separating mechanism by pipeline, and described mill exhauster is connected with described third time airduct, institute
State first and second airduct to be all connected with described boiler；
Also include that mateiral pump, flow control valve and boiler combustion detector, described mateiral pump and described flow control valve are equal
Being arranged on described feed pipe, described boiler combustion detector is arranged on described boiler, described boiler combustion detector and institute
Stating flow control valve communication connection, described flow control valve is messaging in described mateiral pump；
Also including sack cleaner and spiral powder conveying machine, described third time airduct is connected with described sack cleaner, described
Being installed with lock gate hatch and regulation door for the third time between airduct and described sack cleaner, described spiral powder conveying machine is connected to described cloth
Between bag dust collector and described Pulverized Coal Bin；
Also including boiler dust remover, air-introduced machine and chimney, described boiler is connected with described boiler dust remover by pipeline, institute
Stating sack cleaner and be provided with a blast pipe road, described blast pipe road is connected on described boiler dust remover, and described air-introduced machine is even
It is connected between described boiler dust remover and described chimney.
As further improvement of the utility model, described coal feedstock transportation mechanism includes coal bunker, feeder and coal pulverizer,
Described feeder is connected with described coal bunker by pipeline, and described coal pulverizer is connected with described feeder by pipeline, described coal supply
Machine is positioned at the lower section of described coal bunker, and described coal pulverizer is positioned at the lower section of described feeder.
As further improvement of the utility model, described coal dust separating mechanism includes that mill separator separates with fine powder
Device, described mill separator is connected with described coal pulverizer by pipeline, and described pulverized-coal collector is divided with described coarse powder by pipeline
Connecting from device, described mill separator is positioned at the top of described coal pulverizer, and described pulverized-coal collector is put down with described mill separator
Row is arranged.
As further improvement of the utility model, described mill exhauster is connected to the upper of described pulverized-coal collector by pipeline
Side, described Pulverized Coal Bin is connected to the lower section of described pulverized-coal collector by pipeline.
As further improvement of the utility model, described feed pipe is fixedly connected on the bottom of described Pulverized Coal Bin, described
Primary air piping is positioned at the lower section of described Pulverized Coal Bin.
As further improvement of the utility model, also include that secondary air box, described secondary air box are connected to described second
On secondary airduct.
By such scheme, this utility model at least has the advantage that this coal dust amount automatic adjustable pulverized coal carried by hot air pot
Tertiary air can be discharged and not enter and participate in burning in boiler by stove, does not change original system by the transformation of pulverized coal preparation system,
Switching mutually can be realized with original system.The coal dust separated by sack cleaner is transported to coal dust through spiral powder conveying machine
Storehouse, thus improve the utilization rate of coal dust, it is effectively increased efficiency of combustion, through purifying the weary gas of about 70 DEG C, passes through boiler dusting
Device, air-introduced machine, chimney enter air, thus reduce discharge, and economic indicator and discharge index for boiler have bigger meaning
Justice.
Check the combustion case of boiler by boiler combustion detector and pass to flow control valve during by inspection fructufy,
Adjust the amount of feeding of coal dust by the moment that coordinates of flow control valve and mateiral pump, enable coal dust to burn the most completely, it is to avoid
The waste of raw material, ensures the efficiency of combustion of boiler simultaneously, makes boiler can reach combustion standard all the time.
Described above is only the general introduction of technical solutions of the utility model, in order to better understand skill of the present utility model
Art means, and can being practiced according to the content of description, below with preferred embodiment of the present utility model and coordinate accompanying drawing detailed
Describe in detail bright as after.
Accompanying drawing explanation
Fig. 1 is the structural representation of this utility model coal dust amount automatic adjustable pulverized coal carried by hot air boiler.
Detailed description of the invention
Below in conjunction with the accompanying drawings and embodiment, detailed description of the invention of the present utility model is described in further detail.Below
Embodiment is used for illustrating this utility model, but is not limited to scope of the present utility model.
Embodiment: a kind of coal dust amount automatic adjustable pulverized coal carried by hot air boiler, separates including coal feedstock transportation mechanism 1, coal dust
Mechanism 2, mill exhauster 3, boiler 4, Pulverized Coal Bin 5 and first, second and third airduct 6,7,8, described coal dust separating mechanism is by pipeline even
Being connected on is the top of described conveying coal feedstock transportation mechanism, and described Pulverized Coal Bin is connected to described coal dust separating mechanism by pipeline
Lower section, a fixed feed pipe 9 in described Pulverized Coal Bin, described feed pipe is connected on described first time airduct, and described mill exhauster leads to
Piping is connected to the side of described coal dust separating mechanism, and described mill exhauster is connected with described third time airduct, and described first and second
Secondary airduct is all connected with described boiler；
Also include mateiral pump 41, flow control valve 42 and boiler combustion detector 43, described mateiral pump and described flow control
Valve processed is installed on described feed pipe, and described boiler combustion detector is arranged on described boiler, and described boiler combustion detects
Device communicates to connect with described flow control valve, and described flow control valve is messaging in described mateiral pump；
Also include that sack cleaner 10 and spiral powder conveying machine 11, described third time airduct are connected with described sack cleaner,
Being installed with lock gate hatch 12 and regulation door 13 between described third time airduct and described sack cleaner, described spiral powder conveying machine connects
Between described sack cleaner and described Pulverized Coal Bin；
Also including boiler dust remover 14, air-introduced machine 15 and chimney 16, described boiler is by pipeline and described boiler dust remover
Connection, described sack cleaner is provided with a blast pipe road 17, and described blast pipe road is connected on described boiler dust remover, described
Air-introduced machine is connected between described boiler dust remover and described chimney.
Described coal feedstock transportation mechanism includes coal bunker 21, feeder 22 and coal pulverizer 23, described feeder by pipeline with
Described coal bunker connects, and described coal pulverizer is connected with described feeder by pipeline, and described feeder is positioned at the lower section of described coal bunker,
Described coal pulverizer is positioned at the lower section of described feeder.
Described coal dust separating mechanism includes mill separator 31 and pulverized-coal collector 32, and described mill separator passes through pipeline
Connecting with described coal pulverizer, described pulverized-coal collector is connected with described mill separator by pipeline, described mill separator position
In the top of described coal pulverizer, described pulverized-coal collector be arranged in parallel with described mill separator.
Described mill exhauster is connected to the top of described pulverized-coal collector by pipeline, and described Pulverized Coal Bin is connected to by pipeline
The lower section of described pulverized-coal collector.
Described feed pipe is fixedly connected on the bottom of described Pulverized Coal Bin, and described primary air piping is positioned under described Pulverized Coal Bin
Side.
Also include that secondary air box 18, described secondary air box are connected on described second time airduct.
Tertiary air can be discharged and not enter and participate in burning in boiler by this coal dust amount automatic adjustable pulverized coal carried by hot air boiler,
Do not change original system by the transformation of pulverized coal preparation system, switching mutually can be realized with original system.Divided by sack cleaner
The coal dust separated out is transported to Pulverized Coal Bin through spiral powder conveying machine, thus improves the utilization rate of coal dust, is effectively increased efficiency of combustion,
Through purifying the weary gas of about 70 DEG C, enter air, thus reduce discharge by boiler dust remover, air-introduced machine, chimney, for boiler
Economic indicator and discharge index have bigger meaning.
Check the combustion case of boiler by boiler combustion detector and pass to flow control valve during by inspection fructufy,
Adjust the amount of feeding of coal dust by the moment that coordinates of flow control valve and mateiral pump, enable coal dust to burn the most completely, it is to avoid
The waste of raw material, ensures the efficiency of combustion of boiler simultaneously, makes boiler can reach combustion standard all the time.
The above is only preferred implementation of the present utility model, is not limited to this utility model, it is noted that
For those skilled in the art, on the premise of without departing from this utility model know-why, it is also possible to do
Going out some improvement and modification, these improve and modification also should be regarded as protection domain of the present utility model.
Claims (6)
1. a coal dust amount automatic adjustable pulverized coal carried by hot air boiler, it is characterised in that: include that coal feedstock transportation mechanism, coal dust separate
Mechanism, mill exhauster, boiler, Pulverized Coal Bin and first, second and third airduct, described coal dust separating mechanism is connected to be institute by pipeline
Stating the top of conveying coal feedstock transportation mechanism, described Pulverized Coal Bin is connected to the lower section of described coal dust separating mechanism, institute by pipeline
Stating a fixed feed pipe in Pulverized Coal Bin, described feed pipe is connected on described first time airduct, and described mill exhauster is by pipeline even
Being connected on the side of described coal dust separating mechanism, described mill exhauster is connected with described third time airduct, and described first and second airduct is equal
It is connected with described boiler；
Also include that mateiral pump, flow control valve and boiler combustion detector, described mateiral pump and described flow control valve are respectively mounted
On described feed pipe, described boiler combustion detector is arranged on described boiler, described boiler combustion detector and described stream
Control valve communicates to connect, and described flow control valve is messaging in described mateiral pump；
Also include that sack cleaner and spiral powder conveying machine, described third time airduct are connected with described sack cleaner, the described 3rd
Being installed with lock gate hatch and regulation door between secondary airduct and described sack cleaner, described spiral powder conveying machine is connected to described cloth bag and removes
Between dirt device and described Pulverized Coal Bin；
Also including boiler dust remover, air-introduced machine and chimney, described boiler is connected with described boiler dust remover by pipeline, described cloth
Bag dust collector is provided with a blast pipe road, and described blast pipe road is connected on described boiler dust remover, and described air-introduced machine is connected to
Between described boiler dust remover and described chimney.
Coal dust amount automatic adjustable pulverized coal carried by hot air boiler the most according to claim 1, it is characterised in that: described coal raw material is defeated
Sending mechanism to include coal bunker, feeder and coal pulverizer, described feeder is connected with described coal bunker by pipeline, and described coal pulverizer passes through
Pipeline connects with described feeder, and described feeder is positioned at the lower section of described coal bunker, and described coal pulverizer is positioned at described feeder
Lower section.
Coal dust amount automatic adjustable pulverized coal carried by hot air boiler the most according to claim 2, it is characterised in that: described coal dust separates
Mechanism includes mill separator and pulverized-coal collector, and described mill separator is connected with described coal pulverizer by pipeline, described carefully
Powder separator is connected with described mill separator by pipeline, and described mill separator is positioned at the top of described coal pulverizer, described
Pulverized-coal collector be arranged in parallel with described mill separator.
Coal dust amount automatic adjustable pulverized coal carried by hot air boiler the most according to claim 3, it is characterised in that: described mill exhauster leads to
Piping is connected to the top of described pulverized-coal collector, and described Pulverized Coal Bin is connected under described pulverized-coal collector by pipeline
Side.
Coal dust amount automatic adjustable pulverized coal carried by hot air boiler the most according to claim 4, it is characterised in that: described feed pipe
Being fixedly connected on the bottom of described Pulverized Coal Bin, described primary air piping is positioned at the lower section of described Pulverized Coal Bin.
Coal dust amount automatic adjustable pulverized coal carried by hot air boiler the most according to claim 5, it is characterised in that: also include secondary wind
Case, described secondary air box is connected on described second time airduct.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620457185.3U CN205717289U (en) | 2016-05-18 | 2016-05-18 | Coal dust amount automatic adjustable pulverized coal carried by hot air boiler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620457185.3U CN205717289U (en) | 2016-05-18 | 2016-05-18 | Coal dust amount automatic adjustable pulverized coal carried by hot air boiler |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205717289U true CN205717289U (en) | 2016-11-23 |
Family
ID=57299350
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620457185.3U Expired - Fee Related CN205717289U (en) | 2016-05-18 | 2016-05-18 | Coal dust amount automatic adjustable pulverized coal carried by hot air boiler |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205717289U (en) |
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2016
- 2016-05-18 CN CN201620457185.3U patent/CN205717289U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161123 Termination date: 20170518 |
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| CF01 | Termination of patent right due to non-payment of annual fee |