CN103471122A - Multi-tube dust remover inside boiler - Google Patents

Multi-tube dust remover inside boiler Download PDF

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Publication number
CN103471122A
CN103471122A CN2013103862710A CN201310386271A CN103471122A CN 103471122 A CN103471122 A CN 103471122A CN 2013103862710 A CN2013103862710 A CN 2013103862710A CN 201310386271 A CN201310386271 A CN 201310386271A CN 103471122 A CN103471122 A CN 103471122A
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CN
China
Prior art keywords
boiler
smoke
box
heating surface
cyclone cylinder
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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.)
Pending
Application number
CN2013103862710A
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Chinese (zh)
Inventor
顾浩东
冯敏芹
田忠权
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.)
Jiangsu Taihu Boiler Co Ltd
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Jiangsu Taihu Boiler Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Jiangsu Taihu Boiler Co Ltd filed Critical Jiangsu Taihu Boiler Co Ltd
Priority to CN2013103862710A priority Critical patent/CN103471122A/en
Publication of CN103471122A publication Critical patent/CN103471122A/en
Pending legal-status Critical Current

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Abstract

The invention provides a multi-tube dust remover inside a boiler. Through the multi-tube dust remover, smoke inside a biomass boiler can be separated quickly and quickly discharged out of the boiler, the tail of the boiler can be unblocked, stopping the boiler to remove the dust is avoided, and normal heating of the biomass boiler is ensured. The multi-tube dust remover comprises a boiler hearth, a boiler high-temperature heated surface, a boiler medium-temperature heated surface, a remover structure, and a boiler low-temperature heated surface. The smoke sequentially passes the boiler hearth, the boiler high-temperature heated surface, the boiler medium-temperature heated surface, the remover structure and the boiler low-temperature heated surface. The multi-tube dust remover is characterized in that the remover structure is disposed on the lower portion of a tail shaft structure of the boiler, and the remover structure comprises a smoke incoming chamber, cyclone separation guide vanes, smoke outgoing tubes, a cyclone cylinder, a dust discharge tube, a dust bucket, and a smoke outgoing chamber. Top smoke outlets of the smoke outgoing tubes are evenly formed and communicated with the bottom of the smoke outgoing chamber.

Description

A kind of boiler internal multi-pipe dust removing device
Technical field
The present invention relates to the ash disposal technical field of structures of boiler, be specially a kind of boiler internal multi-pipe dust removing device.
Background technology
If the boiler main Industrial Boiler that living beings are fuel, boiler capacity is generally in the 10t/h left and right.Industrial Boiler is the important thermal powerplant of China, use widely, demand is large, in recent years, the boiler of biomass fuel is gradually to large scale development, be accompanied by large scale development, the dedusting structure of existing biomass fuel boiler inside, do not reach quick ash disposal, make the dirt in flue gas to enter into together afterbody along with flue gas, finally cause afterbody blocked, the blowing out deashing of having to, it makes the heat production work of biomass boiler be affected.
Summary of the invention
For the problems referred to above, the invention provides a kind of boiler internal multi-pipe dust removing device, it makes the ash in the flue gas of biomass boiler inside to be separated fast, discharge fast boiler, the afterbody of guaranteeing boiler is unimpeded, without the blowing out deashing, guarantees normally carrying out of biomass boiler heat production work.
A kind of boiler internal multi-pipe dust removing device, its technical scheme is such: it comprises boiler furnace, the boiler high temperature heating surface, warm heating surface in boiler, the deduster structure, the boiler low-temperature heating surface forms, and described flue gas passes through described boiler furnace in turn, the boiler high temperature heating surface, warm heating surface in boiler, the deduster structure, the boiler low-temperature heating surface is characterized in that: described deduster structural configuration is in the bottom of the tail vertical well structure of boiler, and described deduster structure comprises into smoke-box, the cyclonic separation guide vane, pipe, cyclone cylinder, ash tube, ash bucket, go out smoke-box, the described below that goes out smoke-box is communicated with respectively the top outlet flue of uniform described pipe, the deeply inside of corresponding described cyclone cylinder of mouth is entered in the bottom of described pipe, the external diameter of described pipe is less than the internal diameter of described cyclone cylinder, the upper end internal cavity of each described cyclone cylinder is equipped with described cyclonic separation guide vane, describedly goes out smoke-box and is positioned at the described inside of advancing smoke-box, and advance the smoke-box isolation with described, describedly enter the top that smoke-box is arranged in described deduster structure, in described boiler, the outlet of warm heating surface is communicated with described import of advancing smoke-box, describedly enter the smoke-box below and be communicated with respectively end entrance on described cyclone cylinder, the lower end outlet of described cyclone cylinder is provided with ash tube, every described ash tube passes into respectively described ash bucket, and a described side that goes out smoke-box has the import that outlet is communicated with described boiler low-temperature heating surface.
It is further characterized in that: described cyclonic separation guide vane is specially and utilizes the whirlwind tangential velocity to carry out the blade of vortex, and it is positioned at the inner chamber of the cyclone cylinder of corresponding diameter;
The lateral surface of described cyclonic separation guide vane is specially the circular arc type structure;
Described ash tube is the circular cone structure closed up downwards.
After adopting the present invention, flue gas enter into after smoke-box by the cyclonic separation guide vane respectively water conservancy diversion enter in corresponding cyclone cylinder, in cyclone cylinder, flue gas completes and separates under the centrifugal power effect with dust, dust after separation enters ash tube downwards along the inwall of cyclone cylinder, finally from ash bucket, discharge, flue gas after simultaneously purifying is from bottom to top drawn from pipe, enter out smoke-box, the final import that enters into the boiler low-temperature heating surface from a side outlet, the flue gas after purifying enters into boiler tail, can not produce fouling phenomenon; To sum up, it makes the ash in the flue gas of biomass boiler inside to be separated fast, discharges fast boiler, guarantees that the afterbody of boiler is unimpeded, without the blowing out deashing, guarantees normally carrying out of biomass boiler heat production work.
The accompanying drawing explanation
Fig. 1 is structural representation of the present invention;
Fig. 2 is the structure for amplifying schematic diagram of cyclonic separation guide vane of the present invention.
Fig. 3 is that the present invention is installed on the structural representation in boiler.
The specific embodiment
See Fig. 1~3, it comprises boiler furnace 1, boiler high temperature heating surface 2, warm heating surface 3 in boiler, deduster structure 4, boiler low-temperature heating surface 5 forms, and flue gas passes through boiler furnace 1 in turn, boiler high temperature heating surface 2, warm heating surface 3 in boiler, deduster structure 4, boiler low-temperature heating surface 5, deduster structure 4 is arranged in the bottom of the tail vertical well structure 13 of boiler, and the deduster structure comprises into smoke-box 6, cyclonic separation guide vane 7, pipe 8, cyclone cylinder 9, ash tube 10, ash bucket 11, go out smoke-box 12, the below that goes out smoke-box 12 is communicated with respectively the top outlet flue of uniform pipe 8, the inside that mouth gos deep into corresponding cyclone cylinder 9 is entered in the bottom of pipe 8, the external diameter of pipe 8 is less than the internal diameter of cyclone cylinder 9, the upper end internal cavity of each cyclone cylinder 9 is equipped with cyclonic separation guide vane 7, goes out smoke-box 12 and is positioned at into the inside of smoke-box 6, and with advance smoke-box 6 isolation, enter the top that smoke-box 6 is arranged in deduster structure 4, in boiler, the outlet of warm heating surface 3 is communicated with into the import of smoke-box 6, enter smoke-box 6 belows and be communicated with respectively end entrance on cyclone cylinder 9, the lower end outlet of cyclone cylinder 9 is provided with ash tube 10, every ash tube 10 passes into respectively ash bucket 11, and a side that goes out smoke-box 12 has the import that outlet is communicated with boiler low-temperature heating surface 5.Cyclonic separation guide vane 7 is specially and utilizes the whirlwind tangential velocity to carry out the blade of vortex, and it is positioned at the inner chamber of the cyclone cylinder of corresponding diameter; The lateral surface of cyclonic separation guide vane 7 is specially the circular arc type structure; Ash tube 10 is the circular cone structure closed up downwards.
The flow direction that in figure, arrow is flue gas.

Claims (4)

1. a boiler internal multi-pipe dust removing device, it comprises boiler furnace, the boiler high temperature heating surface, warm heating surface in boiler, the deduster structure, the boiler low-temperature heating surface forms, and described flue gas passes through described boiler furnace in turn, the boiler high temperature heating surface, warm heating surface in boiler, the deduster structure, the boiler low-temperature heating surface is characterized in that: described deduster structural configuration is in the bottom of the tail vertical well structure of boiler, and described deduster structure comprises into smoke-box, the cyclonic separation guide vane, pipe, cyclone cylinder, ash tube, ash bucket, go out smoke-box, the described below that goes out smoke-box is communicated with respectively the top outlet flue of uniform described pipe, the deeply inside of corresponding described cyclone cylinder of mouth is entered in the bottom of described pipe, the external diameter of described pipe is less than the internal diameter of described cyclone cylinder, the upper end internal cavity of each described cyclone cylinder is equipped with described cyclonic separation guide vane, describedly goes out smoke-box and is positioned at the described inside of advancing smoke-box, and advance the smoke-box isolation with described, describedly enter the top that smoke-box is arranged in described deduster structure, in described boiler, the outlet of warm heating surface is communicated with described import of advancing smoke-box, describedly enter the smoke-box below and be communicated with respectively end entrance on described cyclone cylinder, the lower end outlet of described cyclone cylinder is provided with ash tube, every described ash tube passes into respectively described ash bucket, and a described side that goes out smoke-box has the import that outlet is communicated with described boiler low-temperature heating surface.
2. a kind of boiler internal multi-pipe dust removing device according to claim 1, it is characterized in that: described cyclonic separation guide vane is specially and utilizes the whirlwind tangential velocity to carry out the blade of vortex, and it is positioned at the inner chamber of the cyclone cylinder of corresponding diameter.
3. a kind of boiler internal multi-pipe dust removing device according to claim 1 and 2, it is characterized in that: the lateral surface of described cyclonic separation guide vane is specially the circular arc type structure.
4. a kind of boiler internal multi-pipe dust removing device according to claim 1, is characterized in that: the circular cone structure of described ash tube for closing up downwards.
CN2013103862710A 2013-08-30 2013-08-30 Multi-tube dust remover inside boiler Pending CN103471122A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2013103862710A CN103471122A (en) 2013-08-30 2013-08-30 Multi-tube dust remover inside boiler

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Application Number Priority Date Filing Date Title
CN2013103862710A CN103471122A (en) 2013-08-30 2013-08-30 Multi-tube dust remover inside boiler

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CN103471122A true CN103471122A (en) 2013-12-25

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107957182A (en) * 2017-11-20 2018-04-24 李茵茵 Efficient air flow dryer is used in a kind of charcoal production

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2248562A (en) * 1990-10-01 1992-04-15 F E Beaumont Ltd A chimney installation
CN2250201Y (en) * 1996-01-05 1997-03-26 王敏学 Multiple tube centrifugal dust remover
US6022390A (en) * 1997-11-17 2000-02-08 Neste Oy Assembly for separating solids from a gaseous phase
CN2743711Y (en) * 2004-10-28 2005-11-30 蔡改贫 Flow guiding type biexhaust pipe low resistance cyclone dust collector
CN2767848Y (en) * 2004-12-24 2006-03-29 苏永亮 Multifunctional low-resistance cooling cartridge
CN101269289A (en) * 2008-04-23 2008-09-24 清华大学 Resistance reduction type centrifugal separation device
CN202018030U (en) * 2011-04-06 2011-10-26 安丰宝 Dust removal economizer
CN102734779A (en) * 2012-06-12 2012-10-17 江苏太湖锅炉股份有限公司 Fixed grate type biomass boiler
CN202647698U (en) * 2012-06-12 2013-01-02 江苏太湖锅炉股份有限公司 Fixed grate biomass boiler
CN203464307U (en) * 2013-08-30 2014-03-05 江苏太湖锅炉股份有限公司 Internal multi-tube dust removal device of boiler

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2248562A (en) * 1990-10-01 1992-04-15 F E Beaumont Ltd A chimney installation
CN2250201Y (en) * 1996-01-05 1997-03-26 王敏学 Multiple tube centrifugal dust remover
US6022390A (en) * 1997-11-17 2000-02-08 Neste Oy Assembly for separating solids from a gaseous phase
CN2743711Y (en) * 2004-10-28 2005-11-30 蔡改贫 Flow guiding type biexhaust pipe low resistance cyclone dust collector
CN2767848Y (en) * 2004-12-24 2006-03-29 苏永亮 Multifunctional low-resistance cooling cartridge
CN101269289A (en) * 2008-04-23 2008-09-24 清华大学 Resistance reduction type centrifugal separation device
CN202018030U (en) * 2011-04-06 2011-10-26 安丰宝 Dust removal economizer
CN102734779A (en) * 2012-06-12 2012-10-17 江苏太湖锅炉股份有限公司 Fixed grate type biomass boiler
CN202647698U (en) * 2012-06-12 2013-01-02 江苏太湖锅炉股份有限公司 Fixed grate biomass boiler
CN203464307U (en) * 2013-08-30 2014-03-05 江苏太湖锅炉股份有限公司 Internal multi-tube dust removal device of boiler

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
庞学群: "《工业卫生工程》", 31 May 1991 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107957182A (en) * 2017-11-20 2018-04-24 李茵茵 Efficient air flow dryer is used in a kind of charcoal production

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Application publication date: 20131225