CN205412539U - Integrated form dust processing system - Google Patents
Integrated form dust processing system Download PDFInfo
- Publication number
- CN205412539U CN205412539U CN201620157332.5U CN201620157332U CN205412539U CN 205412539 U CN205412539 U CN 205412539U CN 201620157332 U CN201620157332 U CN 201620157332U CN 205412539 U CN205412539 U CN 205412539U
- Authority
- CN
- China
- Prior art keywords
- dust
- exhaust
- treatment system
- center
- precipitron
- 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
Landscapes
- Separation Of Particles Using Liquids (AREA)
Abstract
The utility model discloses an integrated form dust processing system, include: dust collector more than two or two, dust return line is with each dust collector's feed opening sealing connection, dust processing center is with dust return line's output sealing connection, the fan for the production gets into dust processing center by dust return line flow direction dust processing center's air current so that fall into dust return line's dust under the drive of air current, the exhaust gas discharging pipe way is with each dust collector's gas vent sealing connection, the exhaust -gas treatment center, with the output sealing connection of exhaust gas discharging pipe way, and including the spray set who is used for spraying the processing to waste gas. The utility model discloses a dust processing system is not only through carry out the centralized processing and improve the treatment effeciency the dust by a wide margin, moreover through carry out the centralized processing and reduce dust emission amount waste gas by a wide margin.
Description
Technical field
This utility model relates to a kind of dust treatment system, especially relates to a kind of for processing the dust treatment system of produced dust in printed circuit board (PCB) production process.
Background technology
In the production process of the products such as such as semiconductor device, printed circuit board (PCB), liquid crystal display, solar film battery, it will usually produce substantial amounts of dust.As a example by the preparation of printed circuit board (PCB), on boring, gong limit, cut, spray in the operations such as stannum, the dust of a large amount of such as copper powder, glass putty etc. can be produced.In order to ensure that operating personnel's is healthy, reduce environmental pollution, and the useful part in dust is recycled, produce the application requirements of dust at these and be collected dust processing.
Chinese invention patent 200710076242.9 discloses the system collecting dust in a kind of production line, it produces in production line and is provided with vacuum cleaner at the operation of dust, this vacuum cleaner is all correspondingly provided with a disposal box, dust enters in the disposal box of correspondence after filtration treatment in sucking vacuum cleaner, each disposal box is in addition to corresponding vacuum cleaner dust outlet airtight connection, also having one can the valve of Automated condtrol, all disposal boxes pass through the Automatic Conveying passage of its valve closing common with respectively and are connected, dust in disposal box can enter transfer passage by valve, it is delivered to be positioned at the dust bucket of transfer passage end through transfer passage.This dust collecting system uses multiple stage vacuum cleaner centralized collection dust, it is achieved dust collection crosses process automation, alleviates dust cleaning work intensity.
China's utility model 201020284009.7 discloses a kind of industry and makes back segment dust blanking air transportation system, comprises: at least one precipitron；Precipitron under single work parts forms a dust mantle group；The precipitron of each set group is parallel to a conveying pipe, and the lower opening of each precipitron connects this conveying pipe；The precipitron of the most each set group connects an aerator, and the dust fallen in this precipitron is blown into this empty defeated pipe by this aerator；One empty defeated pipeline, it connects each conveying pipe, and this empty defeated pipeline front and back end is respectively arranged with an opening, and this front opening connects a filter, for filtering the air plankton sucked；One filters precipitron, and this dust falls in this filtration precipitron；And this filtration precipitron still has a convulsion hole, substantial amounts of air is sucked by this air exhauster, attracts the dust falling into this empty defeated pipeline to fall in this filtration precipitron to the open rearward end of this empty defeated pipeline.
In above prior art; the waste gas discharged by precipitron (or claiming vacuum cleaner) is unprocessed and is directly discharged in air; owing to the filter capacity of precipitron is limited; these waste gas usually contain a large amount of particle diameter and is less than about the fine solid particle granule of 3 to 5 microns; cause dust discharge amount the most too high, be unfavorable for the healthy of operating personnel and environmental conservation.
Summary of the invention
For the deficiencies in the prior art, main purpose of the present utility model provides a kind of dust treatment system having higher dust disposal efficiency and being capable of relatively low dust discharge amount.
In order to realize above-mentioned main purpose, this utility model provides a kind of integrated form dust treatment system, comprising:
Two or more precipitrons；
Dust-recycling duct road, is tightly connected with the feed opening of each precipitron；
Dust disposal center, is tightly connected with the outfan in dust-recycling duct road；
Blower fan, for producing the air-flow being flowed to dust disposal center by dust-recycling duct road, so that the dust falling into dust-recycling duct road enters dust disposal center under the drive of air-flow；And
Exhaust emission pipe, is tightly connected with the air vent of each precipitron；
Exhaust-gas treatment center, is tightly connected with the outfan of exhaust emission pipe, and includes the spray equipment for waste gas carries out spray process.
In technique scheme, on the one hand, larger particles dust (usually more than 3 to 5 microns) collected by precipitron enters dust-recycling duct road through feed opening, and under the drive of the produced air-flow of blower fan, enter dust disposal center and processed by dust disposal central collection, and the waste gas that precipitron is discharged is transported to exhaust-gas treatment center and is made spray process by spray equipment, to collect fine solid particle granule (usually less than 3 to 5 microns) entrained in waste gas, thus realize relatively low even close to zero dust discharge amount；On the other hand, multiple precipitrons are connected respectively to same dust disposal center and exhaust-gas treatment center, it is achieved that dust disposal integrated, thus reach higher dust disposal efficiency.
As a kind of preferred implementation, above-mentioned exhaust-gas treatment center farther includes the dehydrating unit being arranged on above spray equipment, with moisture contained in gas obtained by reducing or eliminating after spray processes.
As another preferred implementation, the position that connects between exhaust-gas treatment center and exhaust emission pipe is arranged on the lower section of spray equipment, to improve efficiency and the effect that waste gas spray processes.
According to a kind of detailed description of the invention of the present utility model, the bottom at above-mentioned exhaust-gas treatment center is provided with tank, and this tank includes the first sump area, the second sump area and is arranged on the defecator between the first sump area and the second sump area；First sump area is used for accommodating process waste water, and the second sump area processes water source to spray equipment supply under water pump drives.Such being advantageous in that, the process waste water in the first sump area can enter the second sump area after defecator filters so that processes waste water and is reused, thus decrease the consumption processing water source, reduces processing cost.
According to another detailed description of the invention of the present utility model, each precipitron all includes small end dust storage cone down, and feed opening is arranged on the bottom of dust storage cone.In this embodiment, dust storage cone can effectively be collected whereabouts dust and is directed to feed opening, in order to the recovery of dust.
In this utility model, as required, dust-recycling duct road directly can be tightly connected with feed opening, it is also possible to by being indirectly tightly connected between middle conveyance conduit and dust-recycling duct road.
Preferably, being provided with the control valve for controlling feed opening opening and closing at each feed opening, this control valve can use self-timing to open and/or manually opened control mode.
In this utility model, the air vent of precipitron directly can be tightly connected with exhaust emission pipe, it is also possible to is indirectly tightly connected with exhaust emission pipe by medial exhaust pipeline, and is preferably provided with control valve on this medial exhaust pipeline.
As a kind of embodiment, above-mentioned blower fan could be arranged to be connected with dust disposal center, with formation negative pressure intracardiac in dust disposal.
It addition, dust treatment system of the present utility model may further include standby fan；The air inlet of this standby fan is connected with one or more precipitron via intake stack, and exhaust outlet is tightly connected with exhaust emission pipe via exhaust duct, to produce the air-flow being flowed to exhaust emission pipe by these one or more precipitrons.Standby fan plays the effect substituting dust blower when the dust blower of corresponding precipitron damages, or coordinates it to use when the dust blower of corresponding precipitron normally works.
In order to more clearly illustrate the purpose of this utility model, technical scheme and advantage, with detailed description of the invention, this utility model is described in further detail below in conjunction with the accompanying drawings.
Accompanying drawing explanation
Fig. 1 is the Part I structural representation of this utility model dust treatment system embodiment；
Fig. 2 is the Part II structural representation of this utility model dust treatment system embodiment.
Detailed description of the invention
Figures 1 and 2 show that the integrated form dust treatment system as this utility model preferred embodiment, for simplicity, Fig. 1 illustrate only the exhaust-gas treatment part (relatively fine solid particle particle disposal part) of this processing system, Fig. 2 illustrate only the relatively coarse powder dirt particle disposal part of this processing system.In this utility model, relatively fine solid particle refers to the dust that precipitron used cannot be collected by filtration, and its particle diameter is generally at about less than 3 to 5 microns；Relatively coarse powder dirt refers to the dust collected by precipitron used, and its particle diameter is generally at about more than 3 to 5 microns.
Seeing Fig. 1, the integrated form dust treatment system of the present embodiment includes multiple precipitron 10, exhaust-gas treatment center 20, exhaust emission pipe 30 and standby fan 40, wherein:
Multiple precipitrons 10 collect dust produced by different station respectively, and it includes body part 11, dust storage cone 12, dust blower 13 and for connecting body part 11 and the pipeline 14 of dust blower 13 air inlet.Dust storage cone 12 is arranged on the lower section of body part 11, and is provided with feed opening 121 bottom it, is provided with the control valve (not shown) controlling its opening and closing at each feed opening 121.Dust falls to dust storage cone 12 after entering body part 11 under the drive of the produced air-flow of dust blower 13.
Exhaust-gas treatment center 20 is configured to water and drenches the form of tower, including being arranged at its internal spray equipment 21, being positioned at the dehydrating unit 22 above spray equipment 21 and be positioned at the tank 23 of bottom.Tank 23 includes the 231, second sump area 232, the first sump area and is arranged on the drainage screen 233 between the first sump area 231 and the second sump area 232.First sump area 231 is used for accommodating spray equipment 21 and waste gas carries out spray process produced process waste water；Second sump area 232 is connected with spray equipment 21 via water pipeline 25, water circulating pump 24 it is provided with on water pipeline 25, when water circulating pump 24 works, process waste water in first sump area 231 enters the second sump area 232 after drainage screen 233 filters, and be pumped to spray equipment 21 further, thus realize recycling of process water.
Exhaust emission pipe 30 realizes being tightly connected via between the air vent (i.e. the air outlet of dust blower 13) of medial exhaust pipeline 31 and each precipitron 10, and is provided with the control valve 311 controlling pipeline break-make on each medial exhaust pipeline 31.The outfan of exhaust emission pipe 30 is tightly connected with exhaust-gas treatment center 20, and the position 32 that connects therebetween is arranged on the lower section of spray equipment 21 and is positioned on tank 23.Under the effect of dust blower 13, the waste gas carrying relatively fine solid particle granule discharged by air vent enters exhaust-gas treatment center 20 through medial exhaust pipeline 31 and exhaust emission pipe 30, relatively fine solid particle granule in waste gas is precipitated in the first sump area 21 under the spray process effect of spray equipment 21 and is collected, and the gas after spray processes is discharged in air after dehydrating unit 22 is except water, thus substantially stop the discharge of relatively fine solid particle granule.
With continued reference to Fig. 1, the air inlet of standby fan 40 is connected with the pipeline 14 of two precipitrons 10 being positioned in figure left side (being i.e. positioned at more away from position, exhaust-gas treatment center 20) via intake stack 41, exhaust outlet is tightly connected with exhaust emission pipe 30 via exhaust duct, to produce the air-flow being flowed to exhaust emission pipe 30 by coupled precipitron 10.Wherein, between two coupled precipitrons 10 and between standby fan 40 and the precipitron 10 adjacent with standby fan 40, it is each provided with one on intake stack 41 control to be again provided with on valve 411, and the exhaust duct of connection standby fan 40 and exhaust gas discharge conduit 30 controlling valve.
Seeing Fig. 2, the dust treatment system of the present embodiment farther includes dust disposal center 50, blower fan 51, useless powder storage case 53 and dust-recycling duct road 60.Wherein, dust-recycling duct road 60 is tightly connected with the feed opening 121 of each precipitron 10, and dust disposal center 50 is tightly connected with the outfan in dust-recycling duct road 60.Blower fan 51 is connected with dust disposal center 50 via pipeline 52, to form negative pressure in dust disposal center 50, thus produces the air-flow being flowed to dust disposal center 50 by dust-recycling duct road 60.Useless powder storage case 53 is removably tightly connected with dust disposal center 50, to accommodate by the relatively crude particle dust collected by dust disposal center 50.
When being arranged on the control valve opening at feed opening 121, relatively crude particle dust in dust storage cone 12 falls into dust-recycling duct road 60, and under the drive of the produced air-flow of blower fan 51, enter dust disposal center 50, it is stored in useless powder storage case 53 after the unified collection in dust disposal center 50 processes.In the present embodiment, the composite class of dust disposal center 50, blower fan 51 and pipeline 52 is similar to precipitron 10, and simply its specifications and models are different.
Although depicting this utility model above by preferred implementation, but it is to be understood that, those of ordinary skill in the art, without departing from invention scope of the present utility model, are improved on an equal basis according to what this utility model made, should be invention scope of the present utility model and contained.
Claims (10)
1. an integrated form dust treatment system, including:
Two or more precipitrons；
Dust-recycling duct road, is tightly connected with the feed opening of each described precipitron；
Dust disposal center, is tightly connected with the outfan in described dust-recycling duct road；
Blower fan, for producing the air-flow being flowed to described dust disposal center by described dust-recycling duct road, so that the dust falling into described dust-recycling duct road enters described dust disposal center under the drive of described air-flow；
It is characterized in that:
Exhaust emission pipe, is tightly connected with the air vent of each described precipitron；
Exhaust-gas treatment center, is tightly connected with the outfan of described exhaust emission pipe, and includes the spray equipment for waste gas carries out spray process.
2. dust treatment system as claimed in claim 1, it is characterised in that: described exhaust-gas treatment center farther includes to be arranged on the dehydrating unit above described spray equipment.
3. dust treatment system as claimed in claim 1, it is characterised in that: the position that connects between described exhaust-gas treatment center and described exhaust emission pipe is arranged on the lower section of described spray equipment.
4. dust treatment system as claimed in claim 1, it is characterized in that: the bottom at described exhaust-gas treatment center is provided with tank, described tank includes the first sump area, the second sump area and is arranged on the defecator between described first sump area and described second sump area；Described first sump area is used for accommodating process waste water, and described second sump area processes water source to described spray equipment supply under water pump drives.
5. dust treatment system as claimed in claim 1, it is characterised in that: each described precipitron all includes small end dust storage cone down, and described feed opening is arranged on the bottom of described dust storage cone.
6. dust treatment system as claimed in claim 1, it is characterised in that: described dust-recycling duct road is directly tightly connected with described feed opening.
7. dust treatment system as claimed in claim 1, it is characterised in that: it is provided with the control valve for controlling described feed opening opening and closing at each described feed opening.
8. dust treatment system as claimed in claim 1, it is characterised in that: described air vent is tightly connected with described exhaust emission pipe indirectly by medial exhaust pipeline, and is provided with control valve on described medial exhaust pipeline.
9. dust treatment system as claimed in claim 1, it is characterised in that: described blower fan is connected with described dust disposal center, with formation negative pressure intracardiac in described dust disposal.
10. dust treatment system as claimed in claim 1, it is characterised in that: described dust treatment system farther includes standby fan；The air inlet of described standby fan is connected with one or more precipitron via intake stack, and exhaust outlet is tightly connected with described exhaust emission pipe via exhaust duct, to produce the air-flow being flowed to described exhaust emission pipe by the one or more precipitron.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620157332.5U CN205412539U (en) | 2016-03-01 | 2016-03-01 | Integrated form dust processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620157332.5U CN205412539U (en) | 2016-03-01 | 2016-03-01 | Integrated form dust processing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205412539U true CN205412539U (en) | 2016-08-03 |
Family
ID=56544555
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620157332.5U Expired - Fee Related CN205412539U (en) | 2016-03-01 | 2016-03-01 | Integrated form dust processing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205412539U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109876584A (en) * | 2019-04-17 | 2019-06-14 | 浙江欧思睦环保科技有限公司 | A kind of device for recovering powder and method |
-
2016
- 2016-03-01 CN CN201620157332.5U patent/CN205412539U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109876584A (en) * | 2019-04-17 | 2019-06-14 | 浙江欧思睦环保科技有限公司 | A kind of device for recovering powder and method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105944483A (en) | Efficient environment-friendly dust removal device | |
| CN105727640A (en) | Modularized paint-mist filtering device | |
| CN206110054U (en) | Electronic floor sweeper with raise dust processing apparatus | |
| CN205412539U (en) | Integrated form dust processing system | |
| CN208032158U (en) | A kind of water-saving device for reducing dust in construction site | |
| CN107716186A (en) | A kind of vertical jetting house system | |
| CN215890555U (en) | Wet-type dust removal fan with filtering capability | |
| CN207936156U (en) | A kind of novel oil smoke processing unit for catering industry | |
| CN201422831Y (en) | Exhaust-gas recirculation vacuum type multifunctional dust collector | |
| CN208680038U (en) | A kind of graphite dust recyclable device | |
| CN211463897U (en) | Air separation sundry removing device in construction waste | |
| CN219292346U (en) | Dust device and dust pelletizing system in advance | |
| CN211488443U (en) | Water pollutant collector | |
| CN106120624A (en) | A kind of electric ground sweeper with airborne dust processing means | |
| CN218221723U (en) | Mining dust remover of high-efficient water spray | |
| CN108079727A (en) | A kind of industrial refuse cracking incineration tail gas dust removing treatment system | |
| CN105586848A (en) | Dust-unloading vacuum dust control device of sweeper truck | |
| CN220901353U (en) | Negative pressure suction and delivery integrated energy-saving cleaning equipment | |
| CN212262661U (en) | Pulse bag type dust removal system for purifying dust-containing waste gas | |
| CN219785938U (en) | Concentrated-discharge scattered dust removal system | |
| CN204219957U (en) | A kind of clarifier particulate collection treatment system | |
| CN209204941U (en) | Waste gas pre-treating device based on pulverized limestone circulation absorption | |
| CN212494456U (en) | Dust storage and suction device of dust remover | |
| CN208642038U (en) | A kind of gravitational dust collecting device of solder flux production | |
| CN209289517U (en) | Dust-extraction unit is used in a kind of production of external wall insulation |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160803 Termination date: 20200301 |