CN201862331U - Low-pressure jet pulse bag type dust catcher - Google Patents
Low-pressure jet pulse bag type dust catcher Download PDFInfo
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- CN201862331U CN201862331U CN2010205836036U CN201020583603U CN201862331U CN 201862331 U CN201862331 U CN 201862331U CN 2010205836036 U CN2010205836036 U CN 2010205836036U CN 201020583603 U CN201020583603 U CN 201020583603U CN 201862331 U CN201862331 U CN 201862331U
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Abstract
The utility model relates to a low-pressure jet pulse bag type dust catcher comprising a bracket, a box body, a jet device, filter bags and a control device, wherein the box body is provided with an air inlet and an air outlet; a dust discharge device is arranged below the box body; the control device comprises a pulse control meter electrically connected with the jet device; the jet device is connected with an air compressor through a conduit; and a deflector is arranged between the filter bags. Compared with the prior art, the low-pressure jet pulse bag type dust catcher adopts a differential pressure feedback type pulse electronic controller for automatically regulating pulse intervals of the jet system according to the running resistance of a dust removal plant, and the jet times are minimized. The dust catcher can reduce power loss and prolong the service life of easily-damaged parts, such as membranes, solenoid valves and the like. The dust catcher adopts the jet device with high efficacy and low consumption to realize the jet function with low pressure and short pulse and has the advantages of light weight, small floor space, low manufacturing cost, high dust removal efficiency, stable running and reliable performance and is convenient to maintain.
Description
Technical field
The utility model relates to dust arrester, especially a kind of unit-combination type low pressure winding-up pulse bag type dust collector that adopts high-effect, low consumption blowing device.
Background technology
At present, pulse bag type dust collector generally is made up of several parts such as bottom steel structure stand, ash bucket, casing, inlet and outlet, filter bag, jetting deashing device and control device.The existing common volume of pulse bag type dust collector is big, cost is high, and power consumption is big, efficient is lower.
China utility model patent CN241002Y discloses " pulse bag type dust collector of ultralow pressure winding-up " on December 13rd, 2000.This patent mainly is to replace existing air compressor with Roots blower, and increases gas bag volume, pulse valve escape pipe caliber, winding-up pipe caliber, injection hole aperture, reduces jetting pressure and increases the winding-up air capacity.But it is less that Roots blower is compared air quantity and wind-force that air compressor can provide, and its jetting deashing effect is unsatisfactory.
The utility model content
At the deficiency of above existing pulse bag type dust collector, the purpose of this utility model provides a kind of efficiency of dust collection height, stable, adopts unit-combination type low pressure winding-up pulse bag type dust collector high-effect, the low consumption blowing device.
The purpose of this utility model is achieved by the following technical solution:
Low pressure winding-up pulse bag type dust collector, comprise support, casing, blowing device, filter bag and control device, filter bag is located in the casing, the lower end of casing and upper end are respectively equipped with air inlet and air outlet, be provided with ash-discharging device below the casing, described control device comprises pulse control instrument, and pulse control instrument is connected with described blowing device circuit; Described blowing device be arranged on casing above, blowing device is connected with air compression plant by pipeline.
As optimal technical scheme of the present utility model, described pulse control instrument comprises pressure reduction reaction type pulse control instrument.
As optimal technical scheme of the present utility model, described blowing device comprises winding-up pipe, nozzle and magnetic valve, and magnetic valve is located at the winding-up pipe and upward and with described pulse control instrument circuit is connected.
As optimal technical scheme of the present utility model, described air inlet is connected with ash bucket, and ash bucket is connected with described ash-discharging device.
As optimal technical scheme of the present utility model, described ash bucket outer wall is provided with hopper wall vibrator.
As optimal technical scheme of the present utility model, described ash-discharging device comprises manual dust unloading device and automatic ash-discharging device.
As optimal technical scheme of the present utility model, described manual dust unloading device comprises star-shaped ash unloading valve, and described automatic ash-discharging device comprises conveying worm.
As optimal technical scheme of the present utility model, described filter bag upper end is connected with the filter bag installing rack, and the filter bag lower end is connected with the filter bag locating rack, is provided with deflector between the filter bag.
As optimal technical scheme of the present utility model, be provided with air intake passage between described air inlet and the air outlet, air intake passage is provided with volume damper.
As optimal technical scheme of the present utility model, also be provided with the air intake passage switching mechanism on the described casing.
The beneficial effects of the utility model are: with respect to prior art, the utility model adopts pressure reduction reaction type pulsed electron controller, regulates pulse spacing of injection system voluntarily according to the cleaner running resistance, makes the winding-up number of times reduce to minimum.Can reduce the service life of consumable accessorys such as kinetic equation loss, prolongation diaphragm, magnetic valve.The utility model adopts high-effect, low consumption blowing device, realizes the winding-up function of low-pressure, short pulse, and it is in light weight, take up an area of less, cost is low, and efficiency of dust collection height, stable, dependable performance, easy to maintenance.
Description of drawings
Fig. 1 is a main TV structure schematic diagram of the present utility model;
Fig. 2 is a plan structure schematic diagram of the present utility model;
Fig. 3 is a left TV structure schematic diagram of the present utility model.
The specific embodiment
The utility model is described in further detail below in conjunction with accompanying drawing and specific embodiment:
As Fig. 1, Fig. 2 and shown in Figure 3, low pressure winding-up pulse bag type dust collector, comprise support 1, casing 2, blowing device 3, filter bag 7 and control device, filter bag 7 is located in the casing 2, the lower end of casing 2 and upper end are respectively equipped with air inlet 10 and air outlet 9, be provided with ash-discharging device 4 below the casing 2, described control device comprises pulse control instrument, and pulse control instrument is connected with described blowing device 3 circuit; Described blowing device 3 be arranged on casing 2 above, blowing device 3 is connected with air compression plant by pipeline.
In the present embodiment, described pulse control instrument is a pressure reduction reaction type pulse control instrument; Described blowing device comprises winding-up pipe, nozzle and magnetic valve, and magnetic valve is located at the winding-up pipe and upward and with described pulse control instrument circuit is connected.Described air inlet 10 is connected with ash bucket, and ash bucket is connected with described ash-discharging device 4.According to different dedusting requirements, the outer wall of ash bucket described in the embodiment can also be provided with hopper wall vibrator, to strengthen the effect of deashing.
Ash-discharging device 4 of the present utility model comprises manual dust unloading device and automatic ash-discharging device, and according to different instructions for uses, described manual dust unloading device comprises star-shaped ash unloading valve, and described automatic ash-discharging device comprises conveying worm 13.Described filter bag 7 upper ends are connected with filter bag installing rack 14, and filter bag 7 lower ends are connected with filter bag locating rack 11, are provided with deflector 8 between the filter bag 7.Be provided with air intake passage between described air inlet 10 and the air outlet 9, air intake passage is provided with volume damper 12.Also be provided with staircase platform 5 above the described casing, staircase platform 5 is provided with air intake passage switching mechanism 6.
The utility model is made as unit-combination type, and there are 24 row's filter bags each unit, and every row has 14 filter bags, and there are 336 filter bags promptly every unit.Filter bag described in the above embodiment 7 adopts the film composite filtering materials, and it not only can improve filtration velocity, and the cleaner resistance reduce, stable, make cleaner be specially adapted to the dedusting of high temperature, high humidity dusty gas, for example industry such as cement, electric power.
In the utility model work time-histories, dusty gas is entered by air inlet 10, and the deflector 8 in ash flue bucket makes that the part big dust particle is separated by the inertia force effect in the gas, directly falls into ash bucket.Dusty gas is by the laggard filter bag filtering area of going into casing 2 of ash bucket, and gas passes filter bag 7, and dust is delayed at the outer surface of filter bag 7, and purified gas is discharged by air outlet 9 after filter pocket mouths enters casing 2 again.Along with the prolongation of filtration time, the dust layer on the filter bag 7 is constantly thickeied, and the resistance of dedusting constantly rises, and when equipment resistance rose to setting value, ash-discharging device 4 was started working.During the equipment deashing, compressed air passes through each pulse valve in order with the extremely very brief time, nozzle on the winding-up pipe sprays to filter bag, filter bag is expanded rapidly produce vibration, and under the effect of inverted draft, be stripped from and fall into ash bucket attached to the dust on the filter bag outer surface, concentrate by ash-discharging device 4 by ash bucket again and discharge.
Claims (10)
1. low pressure winding-up pulse bag type dust collector, comprise support, casing, blowing device, filter bag and control device, filter bag is located in the casing, the lower end of casing and upper end are respectively equipped with air inlet and air outlet, be provided with ash-discharging device below the casing, it is characterized in that: described control device comprises pulse control instrument, and pulse control instrument is connected with described blowing device circuit; Described blowing device be arranged on casing above, blowing device is connected with air compression plant by pipeline.
2. low pressure winding-up pulse bag type dust collector according to claim 1, it is characterized in that: described pulse control instrument comprises pressure reduction reaction type pulse control instrument.
3. low pressure winding-up pulse bag type dust collector according to claim 1, it is characterized in that: described blowing device comprises winding-up pipe, nozzle and magnetic valve, magnetic valve is located at the winding-up pipe and upward and with described pulse control instrument circuit is connected.
4. low pressure winding-up pulse bag type dust collector according to claim 1, it is characterized in that: described air inlet is connected with ash bucket, and ash bucket is connected with described ash-discharging device.
5. low pressure winding-up pulse bag type dust collector according to claim 4, it is characterized in that: described ash bucket outer wall is provided with hopper wall vibrator.
6. according to claim 1 or 4 described low pressure winding-up pulse bag type dust collectors, it is characterized in that: described ash-discharging device comprises manual dust unloading device and automatic ash-discharging device.
7. low pressure winding-up pulse bag type dust collector according to claim 6, it is characterized in that: described manual dust unloading device comprises star-shaped ash unloading valve, and described automatic ash-discharging device comprises conveying worm.
8. according to claim 1 or 4 described low pressure winding-up pulse bag type dust collectors, it is characterized in that: described filter bag upper end is connected with the filter bag installing rack, and the filter bag lower end is connected with the filter bag locating rack, is provided with deflector between the filter bag.
9. low pressure winding-up pulse bag type dust collector according to claim 1 is characterized in that: also be provided with the air intake passage switching mechanism on the described casing.
10. according to claim 1 or 9 described low pressure winding-up pulse bag type dust collectors, it is characterized in that: be provided with air intake passage between described air inlet and the air outlet, air intake passage is provided with volume damper.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205836036U CN201862331U (en) | 2010-10-29 | 2010-10-29 | Low-pressure jet pulse bag type dust catcher |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205836036U CN201862331U (en) | 2010-10-29 | 2010-10-29 | Low-pressure jet pulse bag type dust catcher |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201862331U true CN201862331U (en) | 2011-06-15 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205836036U Expired - Fee Related CN201862331U (en) | 2010-10-29 | 2010-10-29 | Low-pressure jet pulse bag type dust catcher |
Country Status (1)
| Country | Link |
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| CN (1) | CN201862331U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103239950A (en) * | 2013-05-23 | 2013-08-14 | 南通中正机械有限公司 | Low-pressure blowing pulse bag-type dust collector |
| CN104606974A (en) * | 2015-01-28 | 2015-05-13 | 张汉桥 | Low-frequency pulse dust remover |
| CN110022962A (en) * | 2018-11-30 | 2019-07-16 | 安徽天顺环保设备股份有限公司 | A kind of high-efficient automatic treating flour dust device |
-
2010
- 2010-10-29 CN CN2010205836036U patent/CN201862331U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103239950A (en) * | 2013-05-23 | 2013-08-14 | 南通中正机械有限公司 | Low-pressure blowing pulse bag-type dust collector |
| CN104606974A (en) * | 2015-01-28 | 2015-05-13 | 张汉桥 | Low-frequency pulse dust remover |
| CN110022962A (en) * | 2018-11-30 | 2019-07-16 | 安徽天顺环保设备股份有限公司 | A kind of high-efficient automatic treating flour dust device |
| WO2020107408A1 (en) * | 2018-11-30 | 2020-06-04 | 安徽天顺环保设备股份有限公司 | Highly-effective automatic dust treatment apparatus |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110615 Termination date: 20131029 |