CN2647406Y - High-temperature large cloth bag dust cleaner - Google Patents
High-temperature large cloth bag dust cleaner Download PDFInfo
- Publication number
- CN2647406Y CN2647406Y CN03278847.9U CN03278847U CN2647406Y CN 2647406 Y CN2647406 Y CN 2647406Y CN 03278847 U CN03278847 U CN 03278847U CN 2647406 Y CN2647406 Y CN 2647406Y
- Authority
- CN
- China
- Prior art keywords
- dust
- bag
- temperature
- pipe
- air inlet
- 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
Links
- 239000000428 dust Substances 0.000 title claims abstract description 64
- 239000004744 fabric Substances 0.000 title claims abstract 3
- 238000000926 separation method Methods 0.000 claims abstract description 10
- 238000001514 detection method Methods 0.000 claims abstract 4
- 238000009413 insulation Methods 0.000 claims description 6
- 239000003365 glass fiber Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 6
- 239000002245 particle Substances 0.000 abstract description 6
- 230000005494 condensation Effects 0.000 abstract 1
- 238000009833 condensation Methods 0.000 abstract 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 16
- 239000003546 flue gas Substances 0.000 description 16
- 239000007789 gas Substances 0.000 description 5
- 239000004568 cement Substances 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 230000000505 pernicious effect Effects 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
- Y02A50/2351—Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust
Landscapes
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
本实用新型公开了一种高温大布袋除尘器，含有进风管、反吹风管、出风管、排气室、除尘袋、除尘袋室、壳体、灰斗、卸灰阀，进风管上部设有冷风管，进风管的内下部设有预分离装置，预分离装置由上变向阻流器、下变向阻流器和均流锥构成，进风管设有温度检测装置，出风管设有温度检测装置，壳体和灰斗的外侧面设有保温层。该除尘器能够有效改善粉尘的预分离效果，消除火星颗粒进入除尘袋而引起的烧袋现象；同时当外界温度较低时，不会造成结露和粉尘粘袋。
The utility model discloses a high-temperature large cloth bag dust collector, which comprises an air inlet pipe, an anti-blow pipe, an air outlet pipe, an exhaust chamber, a dust removal bag, a dust removal bag chamber, a shell, an ash hopper, an ash unloading valve, an air inlet pipe The upper part is equipped with a cold air pipe, and the inner and lower part of the air inlet pipe is provided with a pre-separation device. The pre-separation device is composed of an upper directional choke, a lower directional choke and a flow equalizing cone. The air inlet pipe is equipped with a temperature detection device. The air outlet pipe is provided with a temperature detection device, and the outer sides of the casing and the ash hopper are provided with an insulating layer. The dust collector can effectively improve the pre-separation effect of dust and eliminate the phenomenon of bag burning caused by spark particles entering the dust bag; at the same time, when the external temperature is low, it will not cause condensation and dust sticking to the bag.
Description
Technical field
The utility model relates to a kind of smoke dust-removing equipment, the big sack cleaner of especially a kind of high temperature.
Background technology
At present, the machine shaft kiln dust removal problem one in cement plant is to being difficult problem, and this is because the machine shaft kiln has three height, more than two, characteristics that fluctuate, i.e. dust concentration height, and the water capacity height, the gas temperature height, fine dust is many, and pernicious gas is many, and all parameter fluctuations are all bigger.Want to resolve machine shaft kiln dust removal problem, must solve problems such as dewfall, burning bag, the sticking bag of dust.The high-efficiency dust remover that is fit to these class industrial and mining enterprises of China, the effect that the glass fiber bag type deduster uses is relatively good.But the pre-separation weak effect that also has dust; When too high the or Mars particle of flue-gas temperature enters dust settling pocket, cause and burn bag; When ambient temperature is low, cause dewfall, the sticking bag of dust.
The utility model content
For the pre-separation weak effect that overcomes existing glass fiber bag type deduster dust, the deficiency of burning the sticking bag of bag, dewfall and dust.The utility model provides a kind of high temperature big sack cleaner, and this deduster can effectively improve the pre-separation effect of dust, eliminates that the Mars particle enters dust settling pocket and the burning bag phenomenon that causes; When ambient temperature is low, can not cause the sticking bag of dewfall and dust simultaneously.
The technical scheme that its technical problem that solves the utility model adopts is: contain blast pipe, reverse-blow pipe, discharge pipe, exhaust chamber, dust settling pocket, dust settling pocket chamber, housing, ash bucket, unloading valve, blast pipe top is provided with cool air hose, the interior bottom of blast pipe is provided with pre-separate device, pre-separate device is made of last break-in flow plug, following break-in flow plug and equal flow cone, blast pipe is provided with temperature-detecting device, discharge pipe is provided with temperature-detecting device, and the lateral surface of housing and ash bucket is provided with heat-insulation layer.
Dust settling pocket is made by glass buiky yarn filtrate.
The last break-in flow plug of pre-separate device and following break-in flow plug can be set up one to two respectively.
The beneficial effects of the utility model are, owing to adopt pre-separate device, when high-temperature flue gas installs by this, the conical surface of high-temperature flue gas and upper and lower break-in flow plug and equal wind awl collides, the dust granules of high-temperature flue gas directly falls in the ash bucket after losing kinetic energy, thereby the dust concentration in the high-temperature flue gas reduces greatly, speed in the high-temperature flue gas greatly reduces simultaneously, processes such as Mars bulky grain are above-mentioned repeatedly change direction and collision after, directly fall into ash bucket after losing kinetic energy, avoided the Mars bulky grain directly to contact the phenomenon that causes dust settling pocket to burn out with dust settling pocket.
Because the lateral surface of housing and ash bucket is provided with heat-insulation layer and has guaranteed that the deduster internal temperature is not subjected to the influence of ambient temperature, therefore avoided dewfall, thereby eliminated the generation of the sticking bag of dust phenomenon.
Because blast pipe and discharge pipe is provided with temperature-detecting device, blast pipe top is provided with cool air hose, the serviceability temperature scope that surpasses deduster when the temperature-dawn of blast pipe and discharge pipe, then open cool air hose and enter cold wind, to reduce the temperature in the deduster, guaranteed that the dust settling pocket of deduster can not burnt out.
Description of drawings
The utility model is described in further detail below in conjunction with drawings and Examples.
Fig. 1 is a structural representation of the present utility model.
1. blast pipes among the figure, 2. cool air hose, 3. reverse-blow pipe, 4. discharge pipe, 5. exhaust chamber, 6. dust settling pocket, 7. dust settling pocket chamber, 8. housing, 9. heat-insulation layer is 10. gone up the break-in flow plug, 11. times break-in flow plugs, 12. Air Heaters, 13. ash buckets, 14. unloading valves.
The specific embodiment
Among Fig. 1, housing 8 is a tubular construction, and housing 8 inside are divided into four to eight dust settling pocket chambers 7, are provided with dust settling pocket 6 in the dust settling pocket chamber 7, and 7 tops, dust settling pocket chamber are provided with exhaust chamber 5.The top of housing 8 is provided with discharge pipe 4, reverse-blow pipe 3.Discharge pipe 4 is provided with temperature-detecting device.The below of housing 8 is provided with ash bucket 13, and the lateral surface of housing 8 and ash bucket 13 is provided with heat-insulation layer 9, and ash bucket 13 belows are provided with unloading valve 14.Blast pipe 1 is arranged on the center of top of barrel-type casing 8 and passes housing 8 inside and enters ash bucket 13 inside.The top of blast pipe 1 is provided with cool air hose 2, and blast pipe 1 is provided with temperature-detecting device.The bottom of blast pipe 1 is respectively equipped with break-in flow plug 10, following break-in flow plug 11 and equal wind awl 12.
During operation, the dust-laden high-temperature flue gas of cement in vertical kiln discharging enters through blast pipe 1.At first pass through the last break-in flow plug 10 of this device, after the conical surface of high-temperature flue gas and last break-in flow plug 10 collides, change direction and speed and slow down, after the conical surface of particle in the high-temperature flue gas and last break-in flow plug 10 collides, lose the conical surface whereabouts of kinetic energy along last break-in flow plug 10; After colliding, the high-temperature flue gas of change direction and slow-down and blast pipe 1 inwall change direction once more, enter down break-in flow plug 11, after colliding, the conical surface of particle in the high-temperature flue gas and following break-in flow plug 11 changes direction again, speed slows down again, after the conical surface of particle in the high-temperature flue gas and following break-in flow plug 11 collides, lose the conical surface whereabouts of kinetic energy along following break-in flow plug 11; After another changes the high-temperature flue gas of direction and blast pipe 1 inwall and collides, change direction, collide at last, after the dust granules in the high-temperature flue gas loses kinetic energy, bottom entering along ash bucket 13 inwalls with ash bucket 13 inwalls with equal wind awl 12 back that collides.Processes such as Mars bulky grain are above-mentioned repeatedly change direction and collision after, directly fall into ash bucket after losing kinetic energy, the dust content of high-temperature flue gas is reduced, dust obtains pre-separation.In order to improve the pre-separation effect of dust, the last break-in flow plug 10 and the following break-in flow plug 11 of pre-separate device can be set up one to two respectively.High-temperature flue gas speed after colliding with ash bucket 13 slows down greatly, concentration reduces greatly, evenly enter the dust settling pocket 6 in the dust settling pocket chamber 7, dust is trapped in dust settling pocket 6 inner surfaces, and dusty gas then filters through dust settling pocket 6 and is purified, and purified gas enters discharge pipe 4 through exhaust chamber 5 and discharges.Can at high temperature normally movingly go in order to ensure dust settling pocket 6, dust settling pocket 6 is made by glass buiky yarn filtrate.Deduster is after operation a period of time, the dust layer that dust settling pocket 6 inner surfaces capture thickens, the running resistance of deduster increases, after being increased to certain value, just need carry out deashing to the dust settling pocket 6 in certain dust settling pocket chamber 7, the opposite gas of airflow direction when reverse-blow pipe 3 is blown into air-out enters in the dust settling pocket chamber 7, and the dust settling pocket 6 that expands is originally shriveled distortion, dispose the dust that dust settling pocket 6 inner surfaces adhere to, the dust under falls in the ash bucket 13 clearly.The lateral surface of housing 8 and ash bucket 13 is provided with heat-insulation layer 9 and has guaranteed that the deduster internal temperature is not subjected to the influence of ambient temperature, has therefore avoided dewfall, thereby has eliminated the generation of the sticking bag of dust phenomenon.Blast pipe 1 and discharge pipe 4 are provided with temperature-detecting device, blast pipe 1 top is provided with cool air hose 2, in a single day the safe handling temperature range that surpasses deduster when the temperature of blast pipe 1 and discharge pipe 4, then open cool air hose 2 and enter cold wind, to reduce the temperature in the deduster, guaranteed that the dust settling pocket 6 of deduster can not burnt out.Guarantee the normal operation of deduster.
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN03278847.9U CN2647406Y (en) | 2003-09-28 | 2003-09-28 | High-temperature large cloth bag dust cleaner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN03278847.9U CN2647406Y (en) | 2003-09-28 | 2003-09-28 | High-temperature large cloth bag dust cleaner |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2647406Y true CN2647406Y (en) | 2004-10-13 |
Family
ID=34332182
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN03278847.9U Expired - Fee Related CN2647406Y (en) | 2003-09-28 | 2003-09-28 | High-temperature large cloth bag dust cleaner |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2647406Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2009143699A1 (en) * | 2008-05-27 | 2009-12-03 | 综合能源有限公司 | An application of a bag-type dust removing method in processing crude synthetic gas produced by fluidized-bed equipment of coal gasification and bag-type dust removing equipment thereof |
| CN102294154A (en) * | 2011-08-12 | 2011-12-28 | 洪泽建材机械有限公司 | Bag-free cage type pulsed stand-alone dust collector |
| CN102527161A (en) * | 2011-12-13 | 2012-07-04 | 浙江海洋学院 | Dust collecting device |
| CN103446834A (en) * | 2013-08-28 | 2013-12-18 | 南通海鹰机电集团有限公司 | Vacuum filter |
| CN105032058A (en) * | 2015-09-01 | 2015-11-11 | 启东精马液压有限公司 | Nonhazardous environment-friendly dust-removing device |
-
2003
- 2003-09-28 CN CN03278847.9U patent/CN2647406Y/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2009143699A1 (en) * | 2008-05-27 | 2009-12-03 | 综合能源有限公司 | An application of a bag-type dust removing method in processing crude synthetic gas produced by fluidized-bed equipment of coal gasification and bag-type dust removing equipment thereof |
| CN102046262A (en) * | 2008-05-27 | 2011-05-04 | 综合能源有限公司 | An application of a bag-type dust removing method in processing crude synthetic gas produced by fluidized-bed equipment of coal gasification and bag-type dust removing equipment thereof |
| CN102046262B (en) * | 2008-05-27 | 2014-09-17 | 综合能源有限公司 | An application of a bag-type dust removing method in processing crude synthetic gas produced by fluidized-bed equipment of coal gasification and bag-type dust removing equipment thereof |
| AU2009253633B2 (en) * | 2008-05-27 | 2014-10-09 | Synthesis Energy Systems, Inc. | An application of a bag-type dust removing method in processing crude synthetic gas produced by fluidized-bed equipment of coal gasification and bag-type dust removing equipment thereof |
| CN102294154A (en) * | 2011-08-12 | 2011-12-28 | 洪泽建材机械有限公司 | Bag-free cage type pulsed stand-alone dust collector |
| CN102527161A (en) * | 2011-12-13 | 2012-07-04 | 浙江海洋学院 | Dust collecting device |
| CN103446834A (en) * | 2013-08-28 | 2013-12-18 | 南通海鹰机电集团有限公司 | Vacuum filter |
| CN103446834B (en) * | 2013-08-28 | 2015-11-25 | 南通海鹰机电集团有限公司 | A kind of vacuum filter |
| CN105032058A (en) * | 2015-09-01 | 2015-11-11 | 启东精马液压有限公司 | Nonhazardous environment-friendly dust-removing device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |