CN202700259U - Pulse jetting dust collector - Google Patents

Pulse jetting dust collector Download PDF

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Publication number
CN202700259U
CN202700259U CN 201220306453 CN201220306453U CN202700259U CN 202700259 U CN202700259 U CN 202700259U CN 201220306453 CN201220306453 CN 201220306453 CN 201220306453 U CN201220306453 U CN 201220306453U CN 202700259 U CN202700259 U CN 202700259U
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CN
China
Prior art keywords
dust
air
chamber
ash bucket
pulse
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
CN 201220306453
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Chinese (zh)
Inventor
王水元
华海根
魏海勇
朱广萍
刘洪礼
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.)
SUZHOU OULANSEN ENVIRONMENT EQUIPMENT CO Ltd
Original Assignee
SUZHOU OULANSEN ENVIRONMENT EQUIPMENT 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 SUZHOU OULANSEN ENVIRONMENT EQUIPMENT CO Ltd filed Critical SUZHOU OULANSEN ENVIRONMENT EQUIPMENT CO Ltd
Priority to CN 201220306453 priority Critical patent/CN202700259U/en
Application granted granted Critical
Publication of CN202700259U publication Critical patent/CN202700259U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to a pulse jetting dust collector which comprises a bracket, wherein a dust collecting chamber is arranged on the bracket; an ash bucket is arranged at the bottom of the dust collecting chamber; an air locking valve is arranged at an outlet of the ash bucket; a filtering chamber is arranged at the middle of the dust collecting chamber; a filtering bag is arranged inside the filtering chamber; an air purifying chamber is arranged at the top of the dust collecting chamber; an air purifying outlet is formed in one side of the air purifying chamber and is connected with a main fan; a pulse jetting device is arranged on the bracket and is connected with the filtering bag; a dust-containing gas inlet box is arranged on one side of the dust collecting chamber; and an air inlet chamber baffle is arranged inside the dust-containing gas inlet box. Due to the adoption of the structure, the specifications of the equipment are correspondingly increased and the treatment air quantity reaches 30000m<3>/h to the maximum extent; the air current uniformity of the dust-containing gas entering the inside of the ash bucket is greatly improved, the speed of air current entering the inside of the ash bucket is reduced, the service life of the filtering bag is prolonged, the raising speed of air current in each area is enabled to be lower than the dropping speed of dust and the dust collector can still remove dust when fine dust is treated.

Description

Pulse blow filter
Technical field
The utility model relates to a kind of cleaner, especially relates to a kind of pulse blow filter of easy dedusting.
Background technology
DMC type pulse blow filter, it is the practical sack cleaner of a kind of high-efficiency economy, it has that floor space is little, simple in structure, maintenance management convenience, less energy consumption, smooth running, failure rate is low, efficiency of dust collection advantages of higher, though use decades, still be widely used and affirm in each industrial and mining enterprises of China.But the DMC pulse blow filter also has many deficiencies:
(1) series specification is few, and range of application is less, and the DMC pulse blow filter filter bag specification of typing is D130*2000, employing blow valve for DN25 pulse right angle, 8 filter bags of each pulse valve blowing; Have six kinds of specifications, process the air quantity maximum and be no more than 9000m 3/ h;
(2) the DMC pulse dust collector adopts 7 times air inlet structures of ash bucket as shown in Figure 1, the air velocity that enters ash bucket 7 is very fast, washing away of 6 pairs of filter bags 4 of dusty gas is larger, and air-flow is the unevenness of ash bucket 7 large (this also is the less major reason can not doing greatlyr of DMC pulse dust collector specification); Abrasion dust particularly, the wearing and tearing of indivedual filter bags 4 are large especially, often 4 life-spans of filter bag do not reach the requirement of design, in addition, for the ultrafine dust of micron order and submicron order, the dust that unit weight is lighter is because the inhomogeneities of the ash bucket 7 interior rates of climb, so that the rate of climb of ash bucket 7 some regional gas stream has surpassed the dust decrease speed, cause the deashing inefficacy and cause whole duster system failure;
(3) pulse spraying equipment 1 of DMC pulse dust collector is arranged in the casing side, although can reduce the volume of ash bucket 7 and casing, but because pulse spraying equipment 1 is in the side of casing, must increase separately an inspection platform and guardrail 9, and from the casing top to the electromagnetic impulse valve inspection platform an approximately drop of one meter being arranged, the maintenance magnetic valve is not too convenient.
Summary of the invention
Technical problem to be solved in the utility model provides a kind of normally deashing and the wider pulse blow filter of multi-size range of application.
The technical scheme in the invention for solving the technical problem is: a kind of pulse blow filter, comprise support, support is provided with the dedusting cavity, the dedusting cavity bottom is ash bucket, the exit of ash bucket is provided with air valve, the middle part of dedusting cavity is filter chamber, filter chamber inside is provided with filter bag, the top of dedusting cavity is provided with air-purifying chamber, and a side of air-purifying chamber is provided with the pure qi (oxygen) outlet, and the pure qi (oxygen) outlet is connected with main air blower, support is provided with pulse spraying equipment, pulse spraying equipment is connected with filter bag, and a side of described dedusting cavity is provided with the dusty gas inlet tank, is provided with the inlet plenum baffle plate in dusty gas inlet tank inside.
In order to guarantee that each regional air-flow rate of climb has been lower than the dust decrease speed, described inlet plenum baffle plate is skewed.
In order to have made things convenient for the inspection and maintenance of electromagnetic impulse valve, and also reduced an inspection platform and guardrail, described pulse spraying equipment is arranged on the top of air-purifying chamber.
Further concrete, the length of described filter bag is 2450m.
In order to guarantee operating personnel in the safety of repair apparatus, the top of described air-purifying chamber is provided with guardrail.
The beneficial effects of the utility model are: adopted after the said structure, increased accordingly the specification of equipment, processed the air quantity maximum and reach 30000m 3/ h; Greatly improve dusty gas and entered the interior airflow homogeneity of ash bucket, reduced to enter the air velocity of ash bucket, reduced dust-contained airflow washing away filter bag, increased the service life of filter bag, because the rate of climb is even in the ash bucket, guarantee that each regional air-flow rate of climb has been lower than the dust decrease speed, make deduster normal deashing still when processing fine solid particle; Made things convenient for the inspection and maintenance of electromagnetic impulse valve.
Description of drawings
Fig. 1 is the structural representation of prior art;
Fig. 2 is structural representation of the present utility model;
Fig. 3 is the left TV structure schematic diagram of Fig. 2;
Fig. 4 is the plan structure schematic diagram of Fig. 2.
Among the figure: 1, pulse spraying equipment; 2, Purge gas; 3, air-purifying chamber; 4, filter bag; 5, inlet plenum baffle plate; 6, dusty gas; 7, ash bucket; 8, air valve; 9, guardrail; 10, pure qi (oxygen) outlet; 11, main air blower; 12, access door; 13, support; 14, filter chamber; 15, dusty gas inlet tank.
The specific embodiment
Such as Fig. 2, Fig. 3 and a kind of pulse blow filter shown in Figure 4, comprise support 13, support 13 is provided with the dedusting cavity, the dedusting cavity bottom is ash bucket 7, the exit of ash bucket 7 is provided with air valve 8, the middle part of dedusting cavity is filter chamber 14, filter chamber 14 inside are provided with filter bag 4, the top of dedusting cavity is provided with air-purifying chamber 3, and a side of air-purifying chamber 3 is provided with pure qi (oxygen) outlet 10, and pure qi (oxygen) outlet 10 is connected with main air blower 11, support 13 is provided with pulse spraying equipment 1, pulse spraying equipment 1 is connected with filter bag 4, and a side of described dedusting cavity is provided with dusty gas inlet tank 15, is provided with inlet plenum baffle plate 5 in dusty gas inlet tank 15 inside; Described inlet plenum baffle plate 5 is skewed; Described pulse spraying equipment 1 is arranged on the top of air-purifying chamber 3; The length of described filter bag 4 is 2450m; The top of described air-purifying chamber 3 is provided with guardrail 9.
Pulse blow filter of the present utility model has 16 specifications such as DMCIII-80, DMCIII-96, DMCIII-112, DMC III-128, DMCIII-144, DMCIII-160, DMCIII-176, DMCIII-192, DMCIII-208, DMCIII-224, DMCIII-240, DMCIII-256, DMCIII-272, DMCIII-288, DMCIII-304, DMCIII-320, and single filter bag 4 length also make D130*2450m into from D130*2000m; Corresponding filter bag 4 filter areas are 80m 2, 96m 2, 112m 2, 128m 2, 144m 2, 160m 2, 176m 2, 192m 2, 208m 2, 224m 2, 240m 2, 256m 2, 272m 2, 288m 2, 304m 2, 320m 2, process the air quantity maximum and reach 30000m 3/ h.
Pulse blow filter has improved the air intake form, changes former ash bucket 7 air intakes into the bypass air intake, and inlet plenum baffle plate 5 is set in casing, forms the side air intake.After dusty gas 6 enters deduster, by tiltedly every inlet plenum baffle plate 5 stop, force gas downward, larger particles loses the energy of inertia, fall into ash bucket 7 bottoms in the self gravitation effect and be captured, play the effect of elementary dedusting, thereby this deduster permission entrance concentration can be up to 200g/m 3, do not need to increase separately elementary dust arrester, namely reduced floor space, saved again investment cost; Turned to from ash bucket 7 infoldings by the dusty gas 6 of primary treatment, enter filter chamber 14, filtered by filter bag 4, filtered Purge gas 2 is discharged through air-purifying chamber 3, in addition because be provided with the bypass air intake, greatly improve dusty gas 6 and entered airflow homogeneity in the ash bucket 7, reduced to enter the air velocity of ash bucket 7, reduce washing away of 6 pairs of filter bags 4 of dust-contained airflow, increased the service life of filter bag 4, for the ultrafine dust of micron order and submicron order, the dust that unit weight is lighter, since the ash bucket 7 interior rates of climb evenly, guarantee that each regional air-flow rate of climb has been lower than the dust decrease speed, make deduster normal deashing still when processing fine solid particle.
Pulse blow filter is arranged on the dust collector box body top with gas bag and the electromagnetic impulse valve of pulse spraying equipment 1, and the top offers access door 12, has made things convenient for the inspection and maintenance of electromagnetic impulse valve, and has also reduced an inspection platform and guardrail.
It is emphasized that above is better implementation column of the present utility model, and every foundation technical spirit of the present utility model all still belongs in the scope of technical solutions of the utility model any simple modification, equivalent variations and modification that above embodiment does.

Claims (5)

1. pulse blow filter, comprise support (13), support (13) is provided with the dedusting cavity, the dedusting cavity bottom is ash bucket (7), the exit of ash bucket (7) is provided with air valve (8), the middle part of dedusting cavity is filter chamber (14), filter chamber (14) inside is provided with filter bag (4), the top of dedusting cavity is provided with air-purifying chamber (3), one side of air-purifying chamber (3) is provided with pure qi (oxygen) outlet (10), pure qi (oxygen) outlet (10) is connected with main air blower (11), support (13) is provided with pulse spraying equipment (1), pulse spraying equipment (1) is connected with filter bag (4), it is characterized in that: a side of described dedusting cavity is provided with dusty gas inlet tank (15), is provided with inlet plenum baffle plate (5) in dusty gas inlet tank (15) inside.
2. pulse blow filter according to claim 1, it is characterized in that: described inlet plenum baffle plate (5) is skewed.
3. pulse blow filter according to claim 1, it is characterized in that: described pulse spraying equipment (1) is arranged on the top of air-purifying chamber (3).
4. pulse blow filter according to claim 1, it is characterized in that: the length of described filter bag (4) is 2450m.
5. pulse blow filter according to claim 1, it is characterized in that: the top of described air-purifying chamber (3) is provided with guardrail (9).
CN 201220306453 2012-06-28 2012-06-28 Pulse jetting dust collector Expired - Fee Related CN202700259U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220306453 CN202700259U (en) 2012-06-28 2012-06-28 Pulse jetting dust collector

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220306453 CN202700259U (en) 2012-06-28 2012-06-28 Pulse jetting dust collector

Publications (1)

Publication Number Publication Date
CN202700259U true CN202700259U (en) 2013-01-30

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CN 201220306453 Expired - Fee Related CN202700259U (en) 2012-06-28 2012-06-28 Pulse jetting dust collector

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103230718A (en) * 2013-04-25 2013-08-07 科林环保装备股份有限公司 Pulse dust collector with super-long filter bags having a length no less than 10m
CN104353298A (en) * 2014-11-19 2015-02-18 张家港市艾尔环保设备有限公司 Bag dust collector
CN104548800A (en) * 2014-12-23 2015-04-29 浙江洁宇环保装备科技有限公司 Industrial dust collector
CN104548776A (en) * 2014-12-23 2015-04-29 浙江洁宇环保装备科技有限公司 Industrial dust collector with improved structure
CN105498934A (en) * 2016-02-03 2016-04-20 江苏新业重工股份有限公司 Vertical slag milling system
CN108854393A (en) * 2018-07-23 2018-11-23 中国华电科工集团有限公司 A kind of electric-bag complex dust collector and on-bne repair method of no poppet

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103230718A (en) * 2013-04-25 2013-08-07 科林环保装备股份有限公司 Pulse dust collector with super-long filter bags having a length no less than 10m
CN104353298A (en) * 2014-11-19 2015-02-18 张家港市艾尔环保设备有限公司 Bag dust collector
CN104548800A (en) * 2014-12-23 2015-04-29 浙江洁宇环保装备科技有限公司 Industrial dust collector
CN104548776A (en) * 2014-12-23 2015-04-29 浙江洁宇环保装备科技有限公司 Industrial dust collector with improved structure
CN106237749A (en) * 2014-12-23 2016-12-21 浙江洁宇环保装备科技有限公司 A kind of industrial dust collector of improvement
CN104548776B (en) * 2014-12-23 2017-01-25 浙江洁宇环保装备科技有限公司 Industrial dust collector with improved structure
CN106422586A (en) * 2014-12-23 2017-02-22 浙江洁宇环保装备科技有限公司 Industrial dust remover with gas inlet pipe
CN106422586B (en) * 2014-12-23 2018-10-30 浙江洁宇环保装备科技有限公司 A kind of industrial dust collector with air inlet pipe
CN105498934A (en) * 2016-02-03 2016-04-20 江苏新业重工股份有限公司 Vertical slag milling system
CN108854393A (en) * 2018-07-23 2018-11-23 中国华电科工集团有限公司 A kind of electric-bag complex dust collector and on-bne repair method of no poppet

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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: 20130130

Termination date: 20150628

EXPY Termination of patent right or utility model