CN2553253Y - Pulse flat bag dust remover - Google Patents

Pulse flat bag dust remover Download PDF

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Publication number
CN2553253Y
CN2553253Y CN 02274014 CN02274014U CN2553253Y CN 2553253 Y CN2553253 Y CN 2553253Y CN 02274014 CN02274014 CN 02274014 CN 02274014 U CN02274014 U CN 02274014U CN 2553253 Y CN2553253 Y CN 2553253Y
Authority
CN
China
Prior art keywords
flat bag
smoke inlet
casing
dust
deduster
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 - Lifetime
Application number
CN 02274014
Other languages
Chinese (zh)
Inventor
李振中
王阳
白旭东
蔡文海
冯兆兴
庞开宇
张广全
程云驰
朱利民
李辰飞
刘刚
王大虎
曾庆广
马力
苏振东
刘晓东
张悦
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.)
Liaoning Clean Environmental Protection Engineering Co ltd
Liaoning Dongdian Combustion Equipment Co ltd
LIAONING COMBUSTION ENGINEERING TECHNOLOGY CENTER
Original Assignee
Liaoning Clean Environmental Protection Engineering Co ltd
Liaoning Dongdian Combustion Equipment Co ltd
LIAONING COMBUSTION ENGINEERING TECHNOLOGY CENTER
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 Liaoning Clean Environmental Protection Engineering Co ltd, Liaoning Dongdian Combustion Equipment Co ltd, LIAONING COMBUSTION ENGINEERING TECHNOLOGY CENTER filed Critical Liaoning Clean Environmental Protection Engineering Co ltd
Priority to CN 02274014 priority Critical patent/CN2553253Y/en
Application granted granted Critical
Publication of CN2553253Y publication Critical patent/CN2553253Y/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

The utility model relates to a device for removing the dust in the smoke, in particular to a pulse flat bag dust remover, which is connected between the flute outlet and the smoke outlet at the tail of the boiler, comprising a smoke inlet and a housing; wherein, the smoke inlet is a taper body and is arranged on the side wall of the housing, and the enlarging port of the smoke inlet is connected with the housing; a flat bag cluster is arranged in the housing, and the upper part of the flat bag cluster is communicated with a rotary backblowing device, and the lower part of the flat bag cluster is communicated with a dust hopper; a solenoid pulse valve is additionally arranged between the gas bag and the rotary air pipe of the rotary backblowing device. The utility model has the advantages of high dust removal efficiency, reliable operation, and lower operational cost.

Description

A kind of pulse flat bag deduster
Technical field
The utility model belongs to the device of getting rid of dust in flue gas, is specially a kind of pulse flat bag deduster.
Background technology
Deduster is the important component part of station boiler dust pelletizing system, directly affects the economy and the security of station boiler unit in its performance, cost and service life.In addition, functional, cheap deduster is to improve one of the economic benefit in power station and essential condition of social benefit.The thermal power generation unit of homemade thermal power generation unit of China and early stage import mainly uses dust arresters such as gravity settling chamber, cyclone dust collectors, wet scrubber, electric cleaner, all in various degree exist the problem that some are difficult to overcome.As: the gravity settling chamber volume is big, efficient is low, can only be as the pre-dedusting device of high-efficiency dust remover; Lower, the easy obstruction of the efficient of cyclone dust collectors is had relatively high expectations to the flowability of grit in the flue gas; The wet scrubber water consumption is big, is unwell to the water-deficient area and uses; The operational reliability of electric cleaner is low, efficient is unstable.The problems referred to above cause shortcomings such as boiler dusting system dust removing efficient is low, operational reliability is poor, equipment cost height, be difficult to improve the economy and the safety inspection of boiler unit operation, and above deduster all can not adapt to more and more strict emission control standards.
The utility model content
The purpose of this utility model is for overcoming above-mentioned shortcoming, and a kind of efficiency of dust collection height, reliable, pulse flat bag deduster that operating cost is lower are provided, and it can be used in the dust pelletizing system of coal-fired power station boiler.
The technical solution of the utility model is: a kind of pulse flat bag deduster, be connected between boiler back end ductwork outlet and the exhanst gas outlet, constitute by smoke inlet, casing, rotary counter-blowing mechanism, ash bucket etc., wherein smoke inlet places wall box, is bullet, and its enlarging one side is connected with casing, establish flat bag bunch in the casing, its top and rotary counter-blowing mechanism connection, its underpart is communicated with ash bucket, adds impulse electromagnetic valve between the gas bag of rotary counter-blowing mechanism and revolution airduct.
Add orifice plate shape air-flow buffering current equalizer in the smoke inlet, vertical with the flue gas airintake direction, air-flow buffering current equalizer is 2~4 layers; The smoke inlet cross section is circular or square; Flat bag bunch is that flat bag is arranged into column with concentric circles, and flat bag cross section is oval.
The utility model beneficial effect is as follows:
1. efficiency of dust collection height.The utility model is taked the arrangement form of side air inlet, be that dusty gas enters from deduster sidewall open to the outside world formula, casing top communicates with rotary counter-blowing mechanism, pure qi (oxygen) body after the filtration is from the arrangement of deduster top emptying, adopt this arrangement SR less, and dust can fall to entering ash bucket rapidly behind the deashing, and dust second adsorption rate is little, can realize online ash removal; In addition, the flat bag bunch flat cloth bag non-rectilinear arranged in concentric circles mode of employing makes limited space reach maximum filter area, thereby improves efficiency of dust collection in the utility model casing.
2. simple in structure, reliable, operating cost is lower.The utility model adopts heavy caliber action of low-voltage pulse rotary counter-blowing, combine the advantage of rotary counter-blowing and pulse dust cleaning deduster, need not resemble the pulse dust cleaning deduster and arrange the more pulse valve of number, reduce maintenance rate, avoided the air consumption of rotary counter-blowing purge mode big, can not increase back blowing machine, make the deduster structure simpler.
3. the utility model is provided with air-flow buffering current equalizer in smoke inlet, makes the part coarse granule dust sedimentation after clashing in the ash-laden gas slip into ash bucket, avoids dust granule directly to clash into filter bag filter bag is caused damage, and the effect of protection filter bag is arranged.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Fig. 2 is the vertical view of Fig. 1.
Fig. 3 is a smoke inlet structure enlarged drawing among Fig. 1.
Fig. 4 is the vertical view of Fig. 3.
Fig. 5 is that the A of Fig. 3 is to view.
Fig. 6 is Fig. 1 mesolow pulse rotary counter-blowing mechanism enlarged drawing.
The specific embodiment
Embodiment
Shown in Fig. 1~6, the utility model is connected between boiler back end ductwork outlet 9 and the exhanst gas outlet 3, by smoke inlet 1, casing 6, rotary counter-blowing mechanism 2, ash bucket 7 constitutes, smoke inlet 1 places casing 6 sidewalls, be bullet, its enlarging one side is connected with casing 6, establish flat bag bunch 61 in the casing 6, its top is communicated with rotary counter-blowing mechanism 2, its underpart is communicated with ash bucket 7, the gas bag 21 of rotary counter-blowing mechanism 2 and 24 of airducts of revolution add impulse electromagnetic valve 22, flat bag bunch 61 is that flat bag is arranged into column with concentric circles, flat bag cross section is oval, thereby reaches maximum filter area in limited space, adds two-layer orifice plate shape air-flow buffering current equalizer 11 in the smoke inlet 1,12, vertical with the flue gas airintake direction, ash discharging hole 8 is established in ash bucket 7 bottoms, and exhanst gas outlet 3 outsides are provided with wind blocking door 4, and casing 6 one sides are provided with cat ladder and inspection platform 5.
Smoke inlet 1 of the present utility model (shown in Fig. 3~5) is that two-layer air-flow buffering current equalizer 11 is equipped with in an inside; 12 bullet; portion's flow resistance is quite little within it for flue gas; ash-laden gas enters smoke inlet 1 by boiler back end ductwork outlet 9; enter smoke inlet 1 by bullet reducing one side; through being installed on the two-layer air-flow buffering current equalizer 11 of its inside; 12 enter casing 6 by bullet enlarging one side; because the sudden enlargement of passage section; make flue gas flow rate die-off part coarse granule dust in the ash-laden gas in smoke inlet 1 directly sedimentation or with air-flow buffering current equalizer 11; 12 bump back sedimentations slip into ash bucket, air-flow buffering current equalizer 11; 12 have current-sharing; the effect of protection cloth bag.
Rotary counter-blowing mechanism 2 (as shown in Figure 6) in the utility model is an action of low-voltage pulse rotary counter-blowing mechanism, form by gas bag 21, electromagnetic impulse valve 22, turning motor 23, revolution airduct 24, revoliving arm 25, nozzle 26, impulse electromagnetic valve 22 air inlets link to each other with gas bag 21, its gas outlet connects the revolution airduct 24 that is driven by turning motor 23, revoliving arm 25 and revolution airduct 24 vertical connections, its bottom is provided with downward nozzle 26.The utility model selects for use 22 pairs of filter bags of single heavy caliber (Φ is more than 200) electromagnetic impulse valve to carry out reverse gas cleaning, the big shortcoming of fault rate height, maintenance capacity when having avoided using a plurality of pulse valves to use simultaneously, heavy caliber electromagnetic impulse valve 22 is made up of magnetic valve and diaphragm type pulse valve, has long service life, characteristics that flow area is big.
The flat bag that the utility model is flat bag bunch 61 adopts high-quality filtering material, as polyphenylene sulfide, aromatic polyamide, glass fibre etc.
The course of work of the present utility model is as follows:
Ash-laden gas is through boiler back end ductwork outlet 9; reducing one side by smoke inlet 1 enters; through being installed on the two-layer air-flow buffering current equalizer 11 of its inside; 12 enlarging one sides by smoke inlet 1 enter casing 6; because the sudden enlargement of passage section; make flue gas flow rate die-off part coarse granule dust in the ash-laden gas in smoke inlet 1 directly sedimentation or with air-flow buffering current equalizer 11; 12 bump back sedimentations slip into ash bucket 7; remaining ash-laden gas becomes clean flue gas by the filter bag outside after filter bag filters; grit is stayed the filter bag outside; carry out reverse gas cleaning through 2 pairs of filter bags of rotary counter-blowing mechanism; fall in the ash bucket 7; discharge by the ash discharging hole 8 of being located at ash bucket 7 bottoms; clean flue gas enters exhanst gas outlet 3 and enters atmosphere; its efficiency of dust collection is greater than 99.6%, dust content<100mg/m 3

Claims (5)

1. pulse flat bag deduster, be connected between boiler back end ductwork outlet and the exhanst gas outlet, have smoke inlet, casing, it is characterized in that smoke inlet (1) places casing (6) sidewall, be bullet, its enlarging one side is connected with casing (6), establish flat bag bunch (61) in the casing (6), its top is communicated with rotary counter-blowing mechanism (2), and its underpart is communicated with ash bucket (7), adds impulse electromagnetic valve (22) between the gas bag (21) of rotary counter-blowing mechanism (2) and revolution airduct (24).
2. according to the described pulse flat bag deduster of claim 1, it is characterized in that adding in the smoke inlet (1) orifice plate shape air-flow buffering current equalizer, vertical with airintake direction.
3. according to the described pulse flat bag deduster of claim 2, it is characterized in that air-flow buffering current equalizer is 2~4 layers.
4. according to claim 1 or 2 described pulse flat bag dedusters, it is characterized in that smoke inlet (1) cross section is for circular or square.
5. according to the described pulse flat bag deduster of claim 1, it is characterized in that flat bag bunch (61) is arranged into column for flat bag with concentric circles, flat bag cross section is oval.
CN 02274014 2002-07-05 2002-07-05 Pulse flat bag dust remover Expired - Lifetime CN2553253Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 02274014 CN2553253Y (en) 2002-07-05 2002-07-05 Pulse flat bag dust remover

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 02274014 CN2553253Y (en) 2002-07-05 2002-07-05 Pulse flat bag dust remover

Publications (1)

Publication Number Publication Date
CN2553253Y true CN2553253Y (en) 2003-05-28

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ID=33738353

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 02274014 Expired - Lifetime CN2553253Y (en) 2002-07-05 2002-07-05 Pulse flat bag dust remover

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CN (1) CN2553253Y (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1948833B (en) * 2006-11-06 2011-09-21 贵阳铝镁设计研究院有限公司 Smoke inlet device of incinerator
CN103277147A (en) * 2013-05-24 2013-09-04 成都昊特新能源技术股份有限公司 Dual-power ORC power generation system and power generation method of same
CN103291392A (en) * 2013-05-24 2013-09-11 成都昊特新能源技术股份有限公司 ORC (organic Rankine cycle) power generation system and method
CN105521668A (en) * 2014-09-30 2016-04-27 江苏鑫伟环保设备制造有限公司 Low-noise vibration dust-cleaning dust remover
CN107137991A (en) * 2017-06-02 2017-09-08 常州大学 A kind of aluminium powder collects explosion-proof explosion unit

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1948833B (en) * 2006-11-06 2011-09-21 贵阳铝镁设计研究院有限公司 Smoke inlet device of incinerator
CN103277147A (en) * 2013-05-24 2013-09-04 成都昊特新能源技术股份有限公司 Dual-power ORC power generation system and power generation method of same
CN103291392A (en) * 2013-05-24 2013-09-11 成都昊特新能源技术股份有限公司 ORC (organic Rankine cycle) power generation system and method
CN105521668A (en) * 2014-09-30 2016-04-27 江苏鑫伟环保设备制造有限公司 Low-noise vibration dust-cleaning dust remover
CN107137991A (en) * 2017-06-02 2017-09-08 常州大学 A kind of aluminium powder collects explosion-proof explosion unit

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Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CX01 Expiry of patent term

Expiration termination date: 20120705

Granted publication date: 20030528