CN203345764U - Lead powder pneumatic delivery system - Google Patents
Lead powder pneumatic delivery system Download PDFInfo
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- CN203345764U CN203345764U CN 201320389229 CN201320389229U CN203345764U CN 203345764 U CN203345764 U CN 203345764U CN 201320389229 CN201320389229 CN 201320389229 CN 201320389229 U CN201320389229 U CN 201320389229U CN 203345764 U CN203345764 U CN 203345764U
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- lead powder
- delivery system
- sending cans
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Abstract
The utility model discloses a lead powder pneumatic delivery system. The lead powder pneumatic delivery system comprises a compressed air processing system, a lead powder delivery system and a gas-solid separating and filtering system, wherein the compressed air processing system is connected with the lead powder delivery system through a compressed air filter, and the lead powder delivery system is connected with the gas-solid separating and filtering system through a dedusting pipeline. When the lead powder pneumatic delivery system is used for delivering lead powder, leakage of the lead powder is avoided due to the fact that the lead powder is delivered in a full-sealing mode, and the environment is prevented from being polluted; due to the fact that the lead powder is delivered in the sealed environment, moisture in the air is prevented from being absorbed by the lead powder, then reaction between the moisture and the lead powder is prevented, and paste preparing performance at the later state is not affected; long-distance delivery of the lead powder is available, and the lead powder can be delivered both in the horizontal direction and in the vertical direction; the technique is simple and breakdowns can not occur easily.
Description
Technical field
The utility model relates to delivery system, is specially a kind of lead powder gas delivery system.
Background technology
Lead powder is to fill the active pole plate of lead-acid storage battery, form the primary raw material of reactivity material, the mode of production of lead powder is divided into ball-milling method and vapour phase oxidation process, and the lead powder of producing is transported to the mode of subsequent processing, generally adopts conveyor screw, scraper plate plate conveyer and bucket elevator to carry out.
Because conveyor screw, slat conveyer and bucket elevator can't be accomplished to seal fully, so, in the process of carrying at lead powder, easily cause lead powder to reveal, contaminated environment, affect workers ' health; Simultaneously lead powder is again the material of moisture absorption reaction very easily, if in course of conveying, the bad meeting of sealing causes lead powder to absorb airborne moisture reacting, affect the quality of lead powder.
Due to the design reasons of conveyor screw and slat conveyer self, can't carry out remote lead powder conveying, and stifled powder, card powder easily occur, thereby cause the faults such as conveyer off-axis, distortion, motor overload.。
Summary of the invention
The technical matters that the utility model solves is to provide a kind of lead powder gas delivery system, to solve the problem proposed in the above-mentioned background technology.
The technical matters that the utility model solves realizes by the following technical solutions: a kind of lead powder gas delivery system, comprise: compressed air processing system, lead powder delivery system, gas solid separation filtering system, described compressed air processing system is connected in the lead powder delivery system through compressed-air cleaner, and the lead powder delivery system is connected by cleaning shaft with the gas solid separation filtering system.
Described compressed air processing system comprises: air compressor, freeze drier, compressed air piping, storage tank, compressed-air cleaner, pressure regulating valve, described air compressor is connected with freeze drier, freeze drier is connected in storage tank by compressed air piping, compressed-air cleaner is connected on storage tank, and compressed-air cleaner is provided with pressure regulating valve.
Described lead powder delivery system comprises: making-up air device air inlet valve, sending cans air inlet valve, lead powder storehouse, lead powder warehouse discharging valve, sending cans inlet valve, sending cans blow off valve, sending cans, sending cans bleeder valve, making-up air device, lead powder delivery duct, buffer bin, buffer bin bleeder valve, described sending cans are provided with sending cans inlet valve, sending cans blow off valve, sending cans bleeder valve, making-up air device, making-up air device air inlet valve, sending cans air inlet valve, the lead powder storehouse is arranged at the sending cans upper end, and lower end, lead powder storehouse is provided with lead powder warehouse discharging valve; Sending cans are connected in buffer bin by the lead powder delivery duct, and the buffer bin lower end is provided with the buffer bin bleeder valve.
Described gas solid separation filtering system comprises: cleaning shaft, dust exhaustor and centrifugal blower, and described dust exhaustor is connected in sending cans, buffer bin by cleaning shaft, and dust exhaustor is provided with centrifugal blower.
Compared with prior art, the beneficial effects of the utility model are:
1. adopt the lead powder gas delivery system to carry lead powder, because be hermetically sealed conveying, lead powder can not revealed, and does not pollute the environment.
2. adopt with the lead powder gas delivery system and carry lead powder, lead powder is carried under sealed environment, can not absorb airborne moisture and react, and affects later stage and cream performance.
3. adopt with the lead powder gas delivery system and carry lead powder, fed distance is far away, can carry in the horizontal and vertical direction, and apparatus and process is simple, is difficult for et out of order.
The accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
The specific embodiment
In order to make of the present utility modelly to realize technological means, creation characteristic, reach purpose and effect is easy to understand, below in conjunction with concrete diagram, further set forth the utility model.
As shown in Figure 1, a kind of lead powder gas delivery system, comprise: compressed air processing system, lead powder delivery system, gas solid separation filtering system, described compressed air processing system is connected in the lead powder delivery system through compressed-air cleaner 5, and the lead powder delivery system is connected by cleaning shaft 18 with the gas solid separation filtering system.
Described compressed air processing system comprises: air compressor 1, freeze drier 2, compressed air piping 3, storage tank 4, compressed-air cleaner 5, pressure regulating valve 6, described air compressor 1 is connected with freeze drier 2, freeze drier 2 is connected in storage tank 4 by compressed air piping 3, compressed-air cleaner 5 is connected on storage tank 4, and compressed-air cleaner 5 is provided with pressure regulating valve 6.
Described lead powder delivery system comprises: making-up air device air inlet valve 7, sending cans air inlet valve 8, lead powder storehouse 9, lead powder warehouse discharging valve 10, sending cans inlet valve 11, sending cans blow off valve 12, sending cans 13, sending cans bleeder valve 14, making-up air device 15, lead powder delivery duct 16, buffer bin 17, buffer bin bleeder valve 21, described sending cans 13 are provided with sending cans inlet valve 11, sending cans blow off valve 12, sending cans bleeder valve 14, making-up air device 15, making-up air device air inlet valve 7, sending cans air inlet valve 8, lead powder storehouse 9 is arranged at sending cans 13 upper ends, 9 lower ends, lead powder storehouse are provided with lead powder warehouse discharging valve 10, sending cans 13 are connected in buffer bin 17 by lead powder delivery duct 16, and buffer bin 17 lower ends are provided with buffer bin bleeder valve 21.
Described gas solid separation filtering system comprises: cleaning shaft 18, dust exhaustor 19 and centrifugal blower 20, and described dust exhaustor 19 is connected in sending cans 13, buffer bin 17 by cleaning shaft 18, and dust exhaustor 19 is provided with centrifugal blower 20.
While carrying lead powder, lead powder warehouse discharging valve 10 and sending cans inlet valve 11 are opened, in sending cans 13 below lead powder joins under Action of Gravity Field, the air displaced enters in dust exhaustor 19 by sending cans blow off valve 12 and cleaning shaft 18, filter out lead powder by being entered in atmosphere by centrifugal blower 20 exhausr ports, when sending cans 13 are filled, lead powder warehouse discharging valve 10, sending cans inlet valve 11 and sending cans blow off valve 12 are closed sealing simultaneously, pressurized air is via air compressor 1 simultaneously, freeze drier 2, compressed air piping 3, storage tank 4, compressed-air cleaner 5, pressure regulating valve 6 and sending cans air inlet valve 8 enter sending cans and lead powder carries out the solid mixture of gas-solid mixing formation dense phase gas, when reaching setting value, just automatically opens the pressure in sending cans 13 the sending cans bleeder valve 14 of bottom, the solid mixture of the dense phase gas that lead powder and pressurized air form via making-up air device 15 and making-up air device air inlet valve 7 secondary pressurizeds after, exert pressure and carried to whole lead powder delivery duct 16, until lead powder all is delivered in buffer bin 17 through lead powder delivery duct 16, finally in buffer bin 17, carry out gas solid separation, gas enters in dust exhaustor 19 by exhausr port and the cleaning shaft 18 at buffer bin 17 tops, filter out lead powder by being entered in atmosphere by centrifugal blower 20 exhausr ports, repeat said process, until buffer bin 17 advances full lead powder, just can open buffer bin bleeder valve 21 lead powder is delivered to subsequent processing.
Above demonstration and described groundwork of the present utility model and principal character and advantage of the present utility model.The technical personnel of the industry should be understood; the utility model is not restricted to the described embodiments; that in above-described embodiment and specification sheets, describes just illustrates principle of the present utility model; under the prerequisite that does not break away from the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall in claimed the utility model scope.Claimed scope of the present utility model is defined by appending claims and equivalent thereof.
Claims (4)
1. a lead powder gas delivery system, comprise: compressed air processing system, lead powder delivery system, gas solid separation filtering system, it is characterized in that: described compressed air processing system is connected in the lead powder delivery system through compressed-air cleaner, and the lead powder delivery system is connected by cleaning shaft with the gas solid separation filtering system.
2. a kind of lead powder gas delivery system according to claim 1, it is characterized in that: described compressed air processing system comprises: air compressor, freeze drier, compressed air piping, storage tank, compressed-air cleaner, pressure regulating valve, described air compressor is connected with freeze drier, freeze drier is connected in storage tank by compressed air piping, compressed-air cleaner is connected on storage tank, and compressed-air cleaner is provided with pressure regulating valve.
3. a kind of lead powder gas delivery system according to claim 1, it is characterized in that: described lead powder delivery system comprises: the making-up air device air inlet valve, the sending cans air inlet valve, the lead powder storehouse, lead powder warehouse discharging valve, the sending cans inlet valve, the sending cans blow off valve, sending cans, the sending cans bleeder valve, making-up air device, the lead powder delivery duct, buffer bin, the buffer bin bleeder valve, described sending cans are provided with the sending cans inlet valve, the sending cans blow off valve, the sending cans bleeder valve, making-up air device, the making-up air device air inlet valve, the sending cans air inlet valve, the lead powder storehouse is arranged at the sending cans upper end, lower end, lead powder storehouse is provided with lead powder warehouse discharging valve, sending cans are connected in buffer bin by the lead powder delivery duct, and the buffer bin lower end is provided with the buffer bin bleeder valve.
4. a kind of lead powder gas delivery system according to claim 1, it is characterized in that: described gas solid separation filtering system comprises: cleaning shaft, dust exhaustor and centrifugal blower, described dust exhaustor is connected in sending cans, buffer bin by cleaning shaft, and dust exhaustor is provided with centrifugal blower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320389229 CN203345764U (en) | 2013-07-02 | 2013-07-02 | Lead powder pneumatic delivery system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320389229 CN203345764U (en) | 2013-07-02 | 2013-07-02 | Lead powder pneumatic delivery system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203345764U true CN203345764U (en) | 2013-12-18 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320389229 Expired - Lifetime CN203345764U (en) | 2013-07-02 | 2013-07-02 | Lead powder pneumatic delivery system |
Country Status (1)
| Country | Link |
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| CN (1) | CN203345764U (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104210848A (en) * | 2014-08-11 | 2014-12-17 | 江苏博傲机电科技有限公司 | Environmental-friendly lead powder pneumatic conveying system |
| CN104401736A (en) * | 2014-10-20 | 2015-03-11 | 无锡红旗除尘设备有限公司 | Lead powder and nitrogen gas closed-cycle static-pressure dense-phase sectional boosting pneumatic conveying system |
| CN104444377A (en) * | 2014-10-20 | 2015-03-25 | 无锡红旗除尘设备有限公司 | Nitrogen closed-cycle static pressure dense-phase segmented boosting pneumatic conveying method for lead powder |
| CN105366367A (en) * | 2015-12-04 | 2016-03-02 | 湖南三一路面机械有限公司 | Powder conveying system and mixing station |
| CN105383935A (en) * | 2015-10-29 | 2016-03-09 | 长安大学 | Thick paste conveying device |
| CN105731077A (en) * | 2016-04-11 | 2016-07-06 | 江阴市高达输送机械科技有限公司 | Pulverized coal pneumatic conveying nitrogen cyclic utilization system |
| CN106195642A (en) * | 2016-08-30 | 2016-12-07 | 天津海辰华环保科技股份有限公司 | Ventilation type pipeline mud pressurizer |
| CN107890617A (en) * | 2017-11-09 | 2018-04-10 | 山东金力特管业有限公司 | A kind of fireproof device of flue |
| CN110436223A (en) * | 2019-08-13 | 2019-11-12 | 安徽知华粉体装备科技有限公司 | A kind of bulk cement Pneumatic transport shipment system |
-
2013
- 2013-07-02 CN CN 201320389229 patent/CN203345764U/en not_active Expired - Lifetime
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104210848A (en) * | 2014-08-11 | 2014-12-17 | 江苏博傲机电科技有限公司 | Environmental-friendly lead powder pneumatic conveying system |
| CN104401736A (en) * | 2014-10-20 | 2015-03-11 | 无锡红旗除尘设备有限公司 | Lead powder and nitrogen gas closed-cycle static-pressure dense-phase sectional boosting pneumatic conveying system |
| CN104444377A (en) * | 2014-10-20 | 2015-03-25 | 无锡红旗除尘设备有限公司 | Nitrogen closed-cycle static pressure dense-phase segmented boosting pneumatic conveying method for lead powder |
| CN105383935A (en) * | 2015-10-29 | 2016-03-09 | 长安大学 | Thick paste conveying device |
| CN105366367A (en) * | 2015-12-04 | 2016-03-02 | 湖南三一路面机械有限公司 | Powder conveying system and mixing station |
| CN105731077A (en) * | 2016-04-11 | 2016-07-06 | 江阴市高达输送机械科技有限公司 | Pulverized coal pneumatic conveying nitrogen cyclic utilization system |
| CN106195642A (en) * | 2016-08-30 | 2016-12-07 | 天津海辰华环保科技股份有限公司 | Ventilation type pipeline mud pressurizer |
| CN107890617A (en) * | 2017-11-09 | 2018-04-10 | 山东金力特管业有限公司 | A kind of fireproof device of flue |
| CN107890617B (en) * | 2017-11-09 | 2020-03-10 | 山东金力特管业有限公司 | Flue fire protection device |
| CN110436223A (en) * | 2019-08-13 | 2019-11-12 | 安徽知华粉体装备科技有限公司 | A kind of bulk cement Pneumatic transport shipment system |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20131218 |
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| CX01 | Expiry of patent term |