CN204629455U - Boiler smoke flying dust back-burning device - Google Patents

Boiler smoke flying dust back-burning device Download PDF

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Publication number
CN204629455U
CN204629455U CN201520186634.0U CN201520186634U CN204629455U CN 204629455 U CN204629455 U CN 204629455U CN 201520186634 U CN201520186634 U CN 201520186634U CN 204629455 U CN204629455 U CN 204629455U
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CN
China
Prior art keywords
flying dust
fluidisation
air compartment
compressed air
boiler
Prior art date
Legal status (The legal status 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 status listed.)
Expired - Fee Related
Application number
CN201520186634.0U
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Chinese (zh)
Inventor
王希成
于启亮
苗希峰
胡茂荣
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SHANDONG ZIBO FUSHAN ENTERPRISE GROUP Co Ltd
Original Assignee
SHANDONG ZIBO FUSHAN ENTERPRISE GROUP Co Ltd
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Priority to CN201520186634.0U priority Critical patent/CN204629455U/en
Application granted granted Critical
Publication of CN204629455U publication Critical patent/CN204629455U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model belongs to field of boilers, is specifically related to a kind of boiler smoke flying dust back-burning device.Comprise boiler furnace, boiler furnace side is communicated with cyclone inlet by flying dust flue, cyclone separator one side outlet is communicated with smoke processing system by purifying smoke pipeline, cyclone separator outlet at bottom is communicated with fluidisation air compartment by high temperature flying dust pipeline, fluidisation air compartment side is connected with the first air compressor machine by the first compressed air piping, fluidisation air compartment opposite side is connected with boiler furnace by pipeline, be connected with the second air compressor machine by the second compressed air piping bottom fluidisation air compartment, first compressed air piping is provided with the first valve, second compressed air piping is provided with the second valve, fluidisation air compartment bottom interior wall is provided with mushroom blast cap.Collected by burner hearth flying dust, be delivered in stove and burn after fluidisation air compartment purges, to reduce fly ash combustible material, improve boiler thermal output, flying dust sprays evenly, solves flying dust entering the alluvial phenomenon in boiler tube road.

Description

Boiler smoke flying dust back-burning device
Technical field
The utility model belongs to field of boilers, is specifically related to a kind of boiler smoke flying dust back-burning device.
Background technology
The flue gas that existing boiler furnace burning produces needs process just can reach discharge standard, and containing a large amount of flying dusts in flue gas, processes more complicated.The flying dust that furnace outlet gets off through cyclone collection by prior art is delivered in stove through batcher and burns, to reduce fly ash combustible material, improves boiler thermal output.But in actual motion; because flying dust temperature is higher; easily there are bite serious problems in batcher; there are some bulky grains a little or ash quantity is more batcher will be caused to block stop operating; motor decelerating mechanism is caused to damage; burn-down of electric motor, has a strong impact on production, and flying dust is to enter in boiler tube road phenomenon of depositing serious.
Summary of the invention
For the deficiencies in the prior art, the purpose of this utility model is to provide a kind of boiler smoke flying dust back-burning device, and fly ash combustible material is burnt again, improves boiler thermal output.
Boiler smoke flying dust back-burning device described in the utility model, comprise boiler furnace, boiler furnace side is communicated with cyclone inlet by flying dust flue, cyclone separator one side outlet is communicated with smoke processing system by purifying smoke pipeline, cyclone separator outlet at bottom is communicated with fluidisation air compartment by high temperature flying dust pipeline, fluidisation air compartment side is connected with the first air compressor machine by the first compressed air piping, fluidisation air compartment opposite side is connected with boiler furnace by pipeline, be connected with the second air compressor machine by the second compressed air piping bottom fluidisation air compartment, first compressed air piping is provided with the first valve, second compressed air piping is provided with the second valve, fluidisation air compartment bottom interior wall is provided with mushroom blast cap.
Fluidisation air compartment bottom interior wall is provided with 4-6 mushroom blast cap.
During use, the flue gas that boiler furnace produces enters cyclone separator process through flying dust flue, and the purifying smoke after process enters smoke processing system through purifying smoke pipeline and is further processed.The high temperature flying dust obtained after process enters in fluidisation air compartment through high temperature flying dust pipeline under self gravitation effect, the compressed air sent here from the second air compressor machine enters fluidisation air compartment through the second compressed air piping and blows bottom fluidisation air compartment, utilize blast by high temperature flying dust fluidisation, fluidisation air compartment bottom interior wall is provided with mushroom blast cap, mushroom blast cap makes to form a small-sized fluidized bed bottom fluidisation air compartment, makes flying dust more even.The compressed air sent here from the first air compressor machine enters fluidisation air compartment through the first compressed air piping from fluidisation air compartment side and blows, and utilizes blast to be blown in boiler furnace by high temperature flying dust and burns.First compressed air piping is provided with the first valve, and the second compressed air piping is provided with the second valve, achieves and adjusts flying dust amount by controlling air quantity.
In sum, the utility model has the following advantages:
(1) furnace outlet is delivered in stove through the flying dust that cyclone collection gets off and burns by the utility model after fluidisation air compartment purges, and to reduce fly ash combustible material, improves boiler thermal output.
(2) the utility model flying dust sprays evenly, solves flying dust entering the alluvial phenomenon in boiler tube road.
(3) the utility model is rational in infrastructure, can adjust flying dust amount by controlling air quantity.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model embodiment;
In figure: 1-boiler furnace, 2-flying dust flue, 3-cyclone separator, 4-purifying smoke pipeline, 5-smoke processing system, 6-first valve, 7-first air compressor machine, 8-first compressed air piping, 9-second air compressor machine, 10-second valve, 11-second compressed air piping, 12-mushroom blast cap, 13-fluidisation air compartment, 14-high temperature flying dust pipeline.
Detailed description of the invention
Below in conjunction with embodiment, the utility model is described further.
Embodiment
A kind of boiler smoke flying dust back-burning device, as shown in Figure 1, comprise boiler furnace 1, boiler furnace 1 side is by flying dust flue 2 and cyclone separator 3 inlet communication, cyclone separator 3 one side outlet is communicated with smoke processing system 5 by purifying smoke pipeline 4, cyclone separator 3 outlet at bottom is communicated with fluidisation air compartment 13 by high temperature flying dust pipeline 14, fluidisation air compartment 13 side is connected with the first air compressor machine 7 by the first compressed air piping 8, fluidisation air compartment 13 opposite side is connected with boiler furnace 1 by pipeline, be connected with the second air compressor machine 9 by the second compressed air piping 11 bottom fluidisation air compartment 13, first compressed air piping 8 is provided with the first valve 6, second compressed air piping 11 is provided with the second valve 10, fluidisation air compartment 13 bottom interior wall is provided with mushroom blast cap 12.
Fluidisation air compartment 13 bottom interior wall is provided with 4 mushroom blast caps 12.
During use, the flue gas that boiler furnace 1 produces enters cyclone separator 3 through flying dust flue 2 and processes, and the purifying smoke after process enters smoke processing system 5 through purifying smoke pipeline 4 and is further processed.The high temperature flying dust obtained after process enters in fluidisation air compartment 13 through high temperature flying dust pipeline 14 under self gravitation effect, the compressed air sent here from the second air compressor machine 9 enters fluidisation air compartment 13 through the second compressed air piping 11 and blows bottom fluidisation air compartment 13, utilize blast by high temperature flying dust fluidisation, fluidisation air compartment 13 bottom interior wall is provided with mushroom blast cap 12, mushroom blast cap 12 makes to form a small-sized fluidized bed bottom fluidisation air compartment, makes flying dust more even.The compressed air sent here from the first air compressor machine 7 enters fluidisation air compartment 13 through the first compressed air piping 8 from fluidisation air compartment 13 side and blows, and utilizes blast to be blown in boiler furnace 1 by high temperature flying dust and burns.First compressed air piping 8 is provided with the first valve 6, second compressed air piping 11 and is provided with the second valve 10, achieves and adjusts flying dust amount by controlling air quantity.

Claims (2)

1. a boiler smoke flying dust back-burning device, it is characterized in that: comprise boiler furnace (1), boiler furnace (1) side is by flying dust flue (2) and cyclone separator (3) inlet communication, cyclone separator (3) one side outlet is communicated with smoke processing system (5) by purifying smoke pipeline (4), cyclone separator (3) outlet at bottom is communicated with fluidisation air compartment (13) by high temperature flying dust pipeline (14), fluidisation air compartment (13) side is connected with the first air compressor machine (7) by the first compressed air piping (8), fluidisation air compartment (13) opposite side is connected with boiler furnace (1) by pipeline, fluidisation air compartment (13) bottom is connected with the second air compressor machine (9) by the second compressed air piping (11), first compressed air piping (8) is provided with the first valve (6), second compressed air piping (11) is provided with the second valve (10), fluidisation air compartment (13) bottom interior wall is provided with mushroom blast cap (12).
2. boiler smoke flying dust back-burning device according to claim 1, is characterized in that: fluidisation air compartment (13) bottom interior wall is provided with 4-6 mushroom blast cap (12).
CN201520186634.0U 2015-03-31 2015-03-31 Boiler smoke flying dust back-burning device Expired - Fee Related CN204629455U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520186634.0U CN204629455U (en) 2015-03-31 2015-03-31 Boiler smoke flying dust back-burning device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520186634.0U CN204629455U (en) 2015-03-31 2015-03-31 Boiler smoke flying dust back-burning device

Publications (1)

Publication Number Publication Date
CN204629455U true CN204629455U (en) 2015-09-09

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201520186634.0U Expired - Fee Related CN204629455U (en) 2015-03-31 2015-03-31 Boiler smoke flying dust back-burning device

Country Status (1)

Country Link
CN (1) CN204629455U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111486448A (en) * 2020-04-01 2020-08-04 南京航空航天大学 Axial-flow cyclone separation fluidized bed boiler fly ash recycling device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111486448A (en) * 2020-04-01 2020-08-04 南京航空航天大学 Axial-flow cyclone separation fluidized bed boiler fly ash recycling device

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CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20150909

CF01 Termination of patent right due to non-payment of annual fee