CN105833618A - Bag type dust collector - Google Patents
Bag type dust collector Download PDFInfo
- Publication number
- CN105833618A CN105833618A CN201610310181.7A CN201610310181A CN105833618A CN 105833618 A CN105833618 A CN 105833618A CN 201610310181 A CN201610310181 A CN 201610310181A CN 105833618 A CN105833618 A CN 105833618A
- Authority
- CN
- China
- Prior art keywords
- tower body
- sack cleaner
- filter bag
- air
- air compressor
- 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.)
- Pending
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0039—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with flow guiding by feed or discharge devices
- B01D46/0041—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with flow guiding by feed or discharge devices for feeding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
- B01D46/06—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material with means keeping the working surfaces flat
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/42—Auxiliary equipment or operation thereof
- B01D46/48—Removing dust other than cleaning filters, e.g. by using collecting trays
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
The invention discloses a bag type dust collector which comprises a tower body, an air compressor, an air inlet pipe, an air outlet pipe, a filter bag and a tubular air injection device. A plurality of supporting legs are arranged at the lower end of the tower body. The lower ends of the supporting legs are fixed to the ground. The air compressor is fixedly arranged on the top of the tower body. The upper portion of the air compressor is connected with the air inlet pipe. The upper portion of the side face of the tower body is connected with the air outlet pipe. A discharging outlet is formed in the lower portion of the tower body. A hopper is connected to the lower portion of the discharging outlet. A material picking opening is formed in the hopper. The top face and the bottom face inside the tower body are fixedly connected with the two ends of the filter bag. The inner side of the filter bag is provided with a flow injection chamber in a spaced mode. The top face of the flow injection chamber is provided with a conical flow guiding column. The bottom face of the flow injection chamber is provided with a conical fixing base. The conical flow guiding column and the conical fixing base are each provided with a rotating device. The rotating devices are connected with the two ends of the tubular air injection device through rotating shafts respectively. A plurality of air injection holes are evenly formed in the tubular air injection device. According to the bag type dust collector, smoke is uniformly dispersed on the surface of the filter bag, the dust removal efficiency is high, noise is low, the filtering efficiency is high, the structure is simple, and maintenance is convenient and rapid.
Description
Technical field
The invention belongs to cleaner unit field, be specifically related to a kind of sack cleaner.
Background technology
Filtration dust catcher is to make dust-contained airflow pass through the device that dust separation is trapped by porous filter material, bag-type dusting
Device is the inside formula filter of the surface-type filter using filter cloth, is mainly used in the dedusting of industrial waste gas.
Existing sack cleaner mostly single sided entry also carries out deashing work by vibrating mechanism, can not make flue dust
Uniformly dispersing is on filter bag surface, and the noise caused when deashing is bigger.
Summary of the invention
In order to solve the problem of above-mentioned prior art, the present invention provide a kind of can uniformly dispersing ash-laden gas can
The efficiently sack cleaner of deashing.
The present invention is achieved through the following technical solutions:
A kind of sack cleaner, including tower body, filter bag, blast pipe, discharge pipe and hopper, blast pipe is connected to tower body top, goes out
Airduct is connected to tower body outer upper, and filter bag is fixed in tower body, and hopper is connected to tower body bottom, be provided with tubular type in described tower body
Air jet system.
Further, described tubular type air jet system is cylindrical hollow configuration, is equidistantly provided with and organizes puff prot more outside it,
Dust concentration and speed can be adjusted and pass through multiple puff prot spreading out uniformly by tubular type air jet system.
Further, described tower body inner top surface is provided with conical flow guiding post, and bottom surface is provided with taper and fixes seat, conical flow guiding
Post and taper are fixed and are equipped with tumbler on seat.
Further, described tubular type air jet system one end is fixed seat by tumbler with taper and is connected, and the other end is also
It is connected with conical flow guiding post by another tumbler；Under the drive of tumbler, tubular type air jet system can be according to
Given pace carries out the rotation along self circumference so that ash-laden gas obtains a circumferential speed when puff prot is discharged, and then
Increase the mixed flow speed of ash-laden gas, strengthen the interaction between ash-laden gas dust granule, increase flue dust separation efficiency.
Further, described tower body top is provided with air compressor, and tower body connects blast pipe by air compressor, empty
Air compressor bottom is connected with the conical flow guiding post on tower body top；Ash-laden gas enters air compressor by blast pipe, so
After pressurize, the ash-laden gas after compression is admitted in conical flow guiding post, finally by tumbler send into tubular type jet dress
Put.
Further, it is provided with air inlet outside described air compressor；When clear dirt operation, air compressor pass through into
Cleaned air is forced press-in tubular type air jet system to carry out clear dirt by air port so that the dust covered on filter bag is blown by pressure-air
Falling, certain efficiency of dust collection replied by filter bag, and whole clear dirt process does not results in bigger noise, and efficiency of dust collection is higher.
Further, described filter bag is tubular, and its upper and lower two ends are fixed on inside tower body, and by complete for tubular type air jet system
Surround and form jet flow room；It is isolated with filter bag inner space with tower body mezzanine space outside filter bag so that ash-laden gas can only lead to
Filter bag carries out filtration and is then discharged out.
Further, described tower body bottom is provided with the discharging opening of taper, and discharging opening bottom is connected with hopper.
Further, described hopper side is provided with picks up material mouth, and operator are periodically by picking up the material mouth dust to storage
Process.
Further, described both sides, tower body bottom are equipped with supporting leg, and supporting leg lower end fixes on the ground.
The present invention compared with prior art, has the following advantages and beneficial effect:
(1) this apparatus structure is simple, and filter efficiency is high, and noise is less；
(2) pressurization ash-laden gas can be dispersed in filter bag surface by this device uniformly, increases filter efficiency, reduces filter bag and damages
Consumption；
(3) this device timing can clear up the dust in filter bag surface and flue efficiently, and by pressure-air by ash dust lane
Go out.
Accompanying drawing explanation
Fig. 1 is that the master of the present invention regards sectional view.
Fig. 2 is the top cross-sectional view of the present invention.
Wherein 1 tower body；2 blast pipes；3 discharge pipes；4 filter bags；5 air compressors；6 jet flow rooms；7 cones
Shape fixes seat；8 tubular type air jet systems；9 puff prots；10 tumblers；11 discharging openings；12 hoppers；13 pick up material
Mouthful；14 supporting legs；15 air inlets.
Detailed description of the invention
Below in conjunction with embodiment, the present invention is described in further detail, but embodiments of the present invention are not limited to this.
Embodiment 1:
Being the preferred version of the present invention as depicted in figs. 1 and 2, a kind of sack cleaner, including tower body 1, blast pipe 2, discharge pipe
3, filter bag 4 and tubular type air jet system 8, tower body 1 is cylindrical, and bottom is provided with multiple supporting leg 14, is fixed on the ground by supporting leg 14；
Tower body 1 is internal is provided with cylindrical filter bag 4, and filter bag 4 upper end is fixed on tower body 1 inside top surface, and filter bag 4 lower end is fixed in tower body 2
Bottom surface, portion, forms a jet flow room 6 closed；Described blast pipe 2 one end is connected with tower body 1 top, described tubular type jet dress
Putting 8 and be arranged on inside, jet flow room 6, blast pipe 2 connects with tubular type air jet system 8；Described discharge pipe 3 is arranged on tower body 1 outer wall
Top, and connect with tower body inside.
Embodiment 2:
The present embodiment is to optimize further on the basis of above-described embodiment, the most to better implement the present invention；Described
Tower body jet flow room 6 inner bottom surface be provided with taper and fix seat 7, end face is provided with conical flow guiding post 16, conical flow guiding post 16 and cone
Shape is fixed and is provided with tumbler 10 on seat 7 opposite side, is equipped with rotating shaft, described tubular type air jet system in tumbler
8 one end are fixed seat 7 by the rotating shaft of tumbler 10 with taper and are connected, and the other end is also by the rotating shaft of another tumbler 10
It is connected with conical flow guiding post (16) so that tubular type air jet system 8 can circumferentially rotate around self；Described tubular type air jet system
Equidistantly being provided with eight groups of puff prots 9 on 8, ash-laden gas enters tubular type air jet system 8 by blast pipe 2, then by organizing spray more
QI KOU 9 is evenly distributed in inside whole filter bag 4, and the gas after being filtered by filter bag 4 is left jet flow room 6 and enters discharge pipe.
Embodiment 3:
The present embodiment is to optimize further on the basis of above-described embodiment, the most to better implement the present invention；Described
Tower body 1 outside top be provided with air compressor 5, air compressor 5 top connects with blast pipe 2, the cone in bottom and tower body 1
Shape diversion column 16 connects, and air compressor 5 is provided with air inlet 15；Enter air at ash-laden gas by blast pipe 2 to compress
After machine 5, then it quantitative is passed through tubular type air jet system 8 after compressing by ash-laden gas, sprays finally by puff prot 9；Tool
There is dusty gas strenuous exercise in jet flow room 6 of certain blast so that it is natural that then grit collision aggravation forms bigger grit
Fall, improve smoke filtration efficiency further.
Further；Described air compressor 5 is temporary closure and the connector of blast pipe 2 when clear dirt works, then
By air inlet 15, external world's cleaned air is pressed into tubular type air jet system 8, by the impact of the high pressure cleaned air of certain time
Most of grit inside filter bag 4 is come off, replys certain filter efficiency.
Embodiment 4:
The present embodiment is to optimize further on the basis of above-described embodiment, the most to better implement the present invention；Described
Tower body 1 bottom be provided with discharging opening 11, the lower end, jet flow room 6 within tower body 1 connects with discharging opening 11, discharging opening 11 bottom connect
Having hopper 12, the dust filtered out in jet flow room 6 falls into hopper 12 by discharging opening 11, and then operator periodically pass through hopper
Material mouth 13 of picking up on 12 clears up dust.
The above, be only presently preferred embodiments of the present invention, and the present invention not does any pro forma restriction, every depends on
Any simple modification of being made above example according to the technical spirit of the present invention, equivalent variations, each fall within the protection of the present invention
Scope.
Claims (10)
1. a sack cleaner, including tower body (1), filter bag (4), blast pipe (2), discharge pipe (3) and hopper (12), blast pipe
(2) being connected to tower body (1) top, discharge pipe (3) is connected to tower body (1) outer upper, and filter bag (4) is fixed in tower body (1), material
Bucket (12) is arranged on tower body (1) bottom, it is characterised in that: it is provided with tubular type air jet system (8) in described tower body (1).
A kind of sack cleaner the most according to claim 1, it is characterised in that: described tubular type air jet system (8) is circle
Cylindrical hollow structure, and outside is equidistantly provided with and organizes puff prot (9) more.
A kind of sack cleaner the most according to claim 1, it is characterised in that: described tower body (1) inner top surface is provided with
Conical flow guiding post (16), bottom surface is provided with taper and fixes seat (7), and conical flow guiding post (16) and taper are fixed and be equipped with on seat (7)
Tumbler (10).
A kind of sack cleaner the most according to claim 3, it is characterised in that: described tubular type air jet system (8) one end
Fixing seat (7) by tumbler (10) with taper to be connected, the other end is also by another tumbler (10) and conical flow guiding
Post (16) is connected.
A kind of sack cleaner the most according to claim 4, it is characterised in that: described tower body (1) top is provided with air
Compressor (5), tower body (1) is connected on blast pipe (2), air compressor (5) bottom and tower body (1) by air compressor (5)
The conical flow guiding post (16) in portion is connected.
A kind of sack cleaner the most according to claim 5, it is characterised in that: described air compressor (5) is outside to be set
There is air inlet (15).
7. according to the sack cleaner described in any one of claim 1-6, it is characterised in that: described filter bag (4) is tubular, and on
Lower two ends are fixed on tower body (1) inner side, and tubular type air jet system (8) surrounds formation jet flow room completely.
8. according to the sack cleaner described in any one of claim 1-6, it is characterised in that: described tower body (1) bottom is provided with
The discharging opening (11) of taper, discharging opening (11) bottom is connected with hopper (12).
A kind of sack cleaner the most according to claim 8, it is characterised in that: described hopper (12) side is provided with picks up material
Mouth (13).
10. according to the sack cleaner described in any one of claim 1-6, it is characterised in that: described tower body (1) bottom is provided with
Organizing supporting leg (14), supporting leg (14) lower end fixes on the ground more.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610310181.7A CN105833618A (en) | 2016-05-12 | 2016-05-12 | Bag type dust collector |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610310181.7A CN105833618A (en) | 2016-05-12 | 2016-05-12 | Bag type dust collector |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105833618A true CN105833618A (en) | 2016-08-10 |
Family
ID=56591480
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610310181.7A Pending CN105833618A (en) | 2016-05-12 | 2016-05-12 | Bag type dust collector |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105833618A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108654238A (en) * | 2018-06-29 | 2018-10-16 | 海宁鼎合工程技术开发有限公司 | A kind of sack cleaner with filter bag protection device |
| CN108786307A (en) * | 2018-08-10 | 2018-11-13 | 柳州鑫磊冷却设备有限公司 | Dedusting filtering bag dust remover |
| CN111888878A (en) * | 2020-09-02 | 2020-11-06 | 江西千翔环保工程有限公司 | Waste gas treatment device for waste incineration |
| CN112295317A (en) * | 2019-07-30 | 2021-02-02 | 理光高科技(深圳)有限公司 | Dry type cleaning device |
| CN114797257A (en) * | 2022-04-30 | 2022-07-29 | 绍兴砩特环保科技有限公司 | High-precision microporous filter |
| CN115634529A (en) * | 2022-12-22 | 2023-01-24 | 佛山市禅城燃气有限公司 | Filter for gas dust removal |
-
2016
- 2016-05-12 CN CN201610310181.7A patent/CN105833618A/en active Pending
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108654238A (en) * | 2018-06-29 | 2018-10-16 | 海宁鼎合工程技术开发有限公司 | A kind of sack cleaner with filter bag protection device |
| CN108786307A (en) * | 2018-08-10 | 2018-11-13 | 柳州鑫磊冷却设备有限公司 | Dedusting filtering bag dust remover |
| CN108786307B (en) * | 2018-08-10 | 2024-04-19 | 柳州鑫磊冷却设备有限公司 | Dust removing filter bag ash cleaner |
| CN112295317A (en) * | 2019-07-30 | 2021-02-02 | 理光高科技(深圳)有限公司 | Dry type cleaning device |
| CN111888878A (en) * | 2020-09-02 | 2020-11-06 | 江西千翔环保工程有限公司 | Waste gas treatment device for waste incineration |
| CN114797257A (en) * | 2022-04-30 | 2022-07-29 | 绍兴砩特环保科技有限公司 | High-precision microporous filter |
| CN115634529A (en) * | 2022-12-22 | 2023-01-24 | 佛山市禅城燃气有限公司 | Filter for gas dust removal |
| CN115634529B (en) * | 2022-12-22 | 2023-04-07 | 佛山市禅城燃气有限公司 | Filter for gas dust removal |
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