CN201598038U - Dust conveyor - Google Patents
Dust conveyor Download PDFInfo
- Publication number
- CN201598038U CN201598038U CN2009202358557U CN200920235855U CN201598038U CN 201598038 U CN201598038 U CN 201598038U CN 2009202358557 U CN2009202358557 U CN 2009202358557U CN 200920235855 U CN200920235855 U CN 200920235855U CN 201598038 U CN201598038 U CN 201598038U
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- Prior art keywords
- pipeline
- dust
- valve
- air inlet
- transfer pot
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Abstract
The utility model discloses a dust conveyor which comprises a conveying tank; a storage hopper is arranged above the conveying tank through an ash unloading pipeline; an ash unloading valve is arranged at the connecting part of the ash unloading pipeline and the storage hopper; an air inlet valve of the tank body is arranged at the connecting part of the ash unloading pipeline and the conveying tank; a pipeline compensator is mounted at the central part of the ash unloading pipeline; a power source is respectively connected with a conveying pipeline and an air inlet pipeline; the conveying tank is connected with the conveying pipeline through a pipeline; a fluidizing device is arranged at the lower end of the conveying tank; a material level meter is mounted on the inner wall of the conveying tank; the air inlet pipeline is connected with the fluidizing device through a pipeline; a manual regulating valve and an automatic regulating valve are arranged on the air inlet pipeline; an air release valve is arranged at the rear end of the air inlet pipeline; and the dust conveyor adopts a fully-closed structure. The dust conveyor solves the problems of secondary dust pollution and energy waste, is mainly applied to the transportation of dust processing systems and material systems of various industries, and can reduce the dust content, so as to optimize the staff working environment, and save the equipment operating cost.
Description
Technical field
The utility model relates to a kind of dust conveyer, but a kind of dust conveyer of pressure regulation particularly.
Background technology
In industry dust disposal systems such as electric power, smelting, cement and potteries, often adopt what send grey mode is scraper plate machine/helical feed, not only poor effect but also noise dust big, that carry has to fly upward and causes secondary pollution; Use transfer pot not have that pressure regulation carries than small part, it is too much pressurized air in use often to occur, and it is very few to enter the dust of tank body, or even does not have dust and enter tank body, carries the phenomenon of still carrying out, and causes very big energy dissipation.
The utility model content
Goal of the invention: the utility model is at secondary pollution that causes in the prior art and energy dissipation phenomenon, but a kind of dust conveyer of fully closed pressure regulation is provided.
Technical scheme: the utility model discloses a kind of dust conveyer, comprise, propulsion source, induction tract, delivery duct, storage bin hopper, pipeline compensator, ash discharging valve, the tank body air inlet valve, manual modulation valve, automatic regulating valve, fluidizer, transfer pot, level-sensing device, ash discharging pipe road and gas atmospheric valve, described storage bin hopper is arranged on the top of transfer pot by the ash discharging pipe road, ash discharging pipe road and storage bin hopper junction are provided with ash discharging valve, ash discharging pipe road and transfer pot junction are provided with the tank body air inlet valve, the tank body air inlet valve is a bivalve plate valve door, described pipeline compensator is installed in middle part, ash discharging pipe road, described propulsion source respectively and delivery duct, induction tract connects, described transfer pot and delivery duct pass through plumbing connection, the transfer pot lower end is provided with fluidizer, described fluidizer is the netted device of stainless steel sift, described level-sensing device is installed in the transfer pot inwall, described induction tract and fluidizer pass through plumbing connection, induction tract is provided with manual modulation valve and automatic regulating valve, be provided with the gas atmospheric valve at the induction tract end, described dust conveyer is a full-closed structure.
Described ash discharging pipe road and storage bin hopper junction are provided with ash discharging valve, and ash discharging pipe road and transfer pot junction are provided with the tank body air inlet valve, and middle part, ash discharging pipe road is provided with pipeline compensator.The effect of ash discharging valve is the Dust Capacity that keeps in the storage bin hopper, makes each Dust Capacity of ash down reach some, prevents that dry run from appearring in machine, and perhaps the gas gray scale is excessive; The effect of pipeline compensator is that pipeline junction is carried out buffer protection, increases machine service life; The effect of tank body air inlet valve is to prevent that the gas backwash in the transfer pot from advancing storage bin hopper.
Described induction tract end is provided with the gas atmospheric valve.The effect of gas atmospheric valve is when the pressure in the induction tract is excessive, discharges certain gas, guarantees the invariablenes pressure of liquid of induction tract.
Described dust conveyer is a full-closed structure.The dust conveyer of full-closed structure makes whole workflow all finish in enclosed environment, has eliminated the secondary pollution of dust.
Described level-sensing device is installed in the transfer pot inwall, and described induction tract and fluidizer are by plumbing connection, and induction tract is provided with manual modulation valve and automatic regulating valve.The effect of level-sensing device is the gas gray scale that detects in the transfer pot, when the gas gray scale is excessive, reduces compressed-air actuated suction quantity by manual modulation valve or automatic regulating valve, reduces the gas gray scale; When the gas gray scale is too small, increase compressed-air actuated suction quantity by manual modulation valve or automatic regulating valve, improve the gas gray scale.Actv. has reduced machine idle running rate, has saved the energy, has reduced cost.
When the utility model uses, open ash discharging valve and tank body air inlet valve, dust is entered transfer pot, level-sensing device in the transfer pot can detect the dust gas gray scale in the transfer pot, sends electronic signal according to dust gas gray scale, and automatic regulating valve is regulated the pressurized air that enters transfer pot according to electronic signal, in transfer pot, make dust and air carry out sufficient movement and mixing by fluidizer, reach the fluidized gas ash compound of similar liquid state, then gas ash compound is entered delivery duct, discharge at last.
Beneficial effect: the disclosed dust conveyer of the utility model is a full-closed structure, eliminated the secondary pollution of dust, be in operation, guaranteed to carry under " gas gray scale " comparatively constant state by level-sensing device and automatic regulating valve and carried out, avoid dry run, greatly reduced energy consumption.The disclosed dust conveyer of the utility model has solved the dust secondary pollution of existing dust conveyer and the problem that wastes energy, be mainly used in the dust disposal system of every profession and trade and the conveying of material system, can reduce the environment dust content after adopting the utility model, improve the environmental quality of equipment operator work area, save the over-the-road expense of equipment.
Description of drawings
Accompanying drawing is the utility model structural representation.
The specific embodiment
The utility model is further explained below in conjunction with accompanying drawing.
As shown in drawings, the utility model discloses a kind of dust conveyer, comprise, propulsion source 1, induction tract 2, delivery duct 11, storage bin hopper 14, pipeline compensator 10, ash discharging valve 13, tank body air inlet valve 9, manual modulation valve 3, automatic regulating valve 4, fluidizer 5, transfer pot 8, level-sensing device 7, ash discharging pipe road 12 and gas atmospheric valve 6, described storage bin hopper 14 is arranged on the top of transfer pot 8 by ash discharging pipe road 12, ash discharging pipe road 12 and storage bin hopper 14 junctions are provided with ash discharging valve 13, ash discharging pipe road 12 and transfer pot 8 junctions are provided with tank body air inlet valve 9, described pipeline compensator 10 is installed in 12 middle parts, ash discharging pipe road, described propulsion source 1 respectively with delivery duct 11, induction tract 2 connects, described transfer pot 8 and delivery duct 11 pass through plumbing connection, transfer pot 8 lower ends are provided with fluidizer 5, described level-sensing device 7 is installed in transfer pot 8 inwalls, described induction tract 2 and fluidizer 5 pass through plumbing connection, induction tract 2 is provided with manual modulation valve 3 and automatic regulating valve 4, is provided with gas atmospheric valve 6 at induction tract 2 ends.
When the utility model uses, open ash discharging valve 13 and tank body air inlet valve 9, dust is entered transfer pot 8, level-sensing device 7 in the transfer pot 8 can detect the dust gas gray scale in the transfer pot 8, send electronic signal according to dust gas gray scale, automatic regulating valve 4 is regulated the pressurized air that enters transfer pot 8 according to electronic signal, in transfer pot 8, make dust and air carry out sufficient movement and mixing by fluidizer 5, reach the fluidized gas ash compound of similar liquid state, then gas ash compound is entered delivery duct 11, discharge at last.
But thinking and method that the utility model provides a kind of dust of environmental protection and energy saving pressure regulation to carry unit; the method and the approach of this technical scheme of specific implementation are a lot; the above only is a preferred implementation of the present utility model; should be understood that; for those skilled in the art; under the prerequisite that does not break away from the utility model principle; can also make some improvements and modifications; these improvements and modifications also should be considered as protection domain of the present utility model, and all available prior art of each component part not clear and definite in the present embodiment is realized.
Claims (5)
1. dust conveyer, it is characterized in that, described dust conveyer comprises, propulsion source (1), induction tract (2), delivery duct (11), storage bin hopper (14), tank body air inlet valve (9), automatic regulating valve (4), fluidizer (5), transfer pot (8), level-sensing device (7) and ash discharging pipe road (12), described storage bin hopper (14) is arranged on the top of transfer pot (8) by ash discharging pipe road (12), described propulsion source (1) respectively and delivery duct (11), induction tract (2) connects, described transfer pot (8) and delivery duct (11) pass through plumbing connection, transfer pot (8) lower end is provided with fluidizer (5), described level-sensing device (7) is installed in transfer pot (8) inwall, described induction tract (2) and fluidizer (5) are by plumbing connection, and induction tract (2) is provided with manual modulation valve (3) and automatic regulating valve (4).
2. dust conveyer according to claim 1, it is characterized in that, described ash discharging pipe road (12) and storage bin hopper (14) junction are provided with ash discharging valve (13), ash discharging pipe road (12) and transfer pot (8) junction are provided with tank body air inlet valve (9), and ash discharging pipe road (12) middle part is provided with pipeline compensator (10).
3. dust conveyer according to claim 1 is characterized in that, described fluidizer (5) is the netted device of stainless steel sift.
4. dust conveyer according to claim 1 is characterized in that, described induction tract (2) end is provided with gas atmospheric valve (6).
5. dust conveyer according to claim 1 is characterized in that, described dust conveyer is a full-closed structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202358557U CN201598038U (en) | 2009-10-09 | 2009-10-09 | Dust conveyor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202358557U CN201598038U (en) | 2009-10-09 | 2009-10-09 | Dust conveyor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201598038U true CN201598038U (en) | 2010-10-06 |
Family
ID=42809090
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009202358557U Expired - Fee Related CN201598038U (en) | 2009-10-09 | 2009-10-09 | Dust conveyor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201598038U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104418090A (en) * | 2013-08-21 | 2015-03-18 | 确成硅化学股份有限公司 | Pneumatic pipeline transmission device |
| CN108928651A (en) * | 2018-05-30 | 2018-12-04 | 武汉钢铁有限公司 | A kind of closed collection processing/transfer system of metallurgy dedusting ash and technique |
-
2009
- 2009-10-09 CN CN2009202358557U patent/CN201598038U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104418090A (en) * | 2013-08-21 | 2015-03-18 | 确成硅化学股份有限公司 | Pneumatic pipeline transmission device |
| CN104418090B (en) * | 2013-08-21 | 2017-03-08 | 确成硅化学股份有限公司 | Pneumatic pipe conveyer device |
| CN108928651A (en) * | 2018-05-30 | 2018-12-04 | 武汉钢铁有限公司 | A kind of closed collection processing/transfer system of metallurgy dedusting ash and technique |
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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: 20101006 Termination date: 20131009 |