CN202148043U - Pneumatic slurry residue conveyor - Google Patents
Pneumatic slurry residue conveyor Download PDFInfo
- Publication number
- CN202148043U CN202148043U CN201120179818U CN201120179818U CN202148043U CN 202148043 U CN202148043 U CN 202148043U CN 201120179818 U CN201120179818 U CN 201120179818U CN 201120179818 U CN201120179818 U CN 201120179818U CN 202148043 U CN202148043 U CN 202148043U
- Authority
- CN
- China
- Prior art keywords
- pneumatic valve
- operated pneumatic
- pressure container
- vacuum generator
- exhaust tube
- 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
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Abstract
A pneumatic slurry residue conveyor comprises a suction pipe, an air inlet pneumatic valve, a compressed air inlet, a vacuum generator pneumatic valve, a vacuum generator, a discharge pipe, a discharge pipe pneumatic valve, a transit pressure container and a suction pipe pneumatic valve. The transit pressure container is a main part of the pneumatic slurry residue conveyor and in a structure of a tank body, the air inlet pneumatic valve is arranged in the middle of the upper end of the transit pressure container, and the upper end of the air inlet pneumatic valve is connected with the compressed air inlet. The suction pipe pneumatic valve is arranged on one side at the upper end of the transit pressure container, and the suction pipe is arranged at the upper end of the suction pipe pneumatic valve in connection mode. The vacuum generator pneumatic valve is arranged on the other side at the upper end of the transit pressure container, and the outer end of the vacuum generator pneumatic valve is connected with the vacuum generator. The lower end of the transit pressure container is connected with the discharge pipe pneumatic valve, and the outer end of the discharge pipe pneumatic valve is connected with the discharge pipe. The pneumatic slurry residue conveyor is simple in structure, convenient to operate and use, good in stability and high in reliability.
Description
Technical field
The utility model belongs to the cleaning suction and carries the machine of slag slurry and loose dry material, relates in particular to pneumatic slag slurry conveyer.
Background technology
The cleaning suction and the conveying of existing slag slurry and loose dry material generally are with hand digging and conveying, the suction of slag stock pump and conveying or belt feeder conveying.Adopt the form of hand digging and conveying undoubtedly; Labour intensity height and production efficiency are low; Even adopt some non-professional equipment also can handle the conveying of slag slurry, because defective and the amateur character of equipment in design causes working environment undesirable; Production efficiency is low, can not satisfy normal production needs.
The utility model content
The purpose of the utility model is, overcomes the weak point of prior art, and a kind of pneumatic slag slurry conveyer is provided, and can improve the production efficiency that slag slurry or loose dry material are carried preferably, realizes carrying out production strictly in line with rules and regulations, and guarantees good production work environment.
The described pneumatic slag slurry conveyer of the utility model includes induction pipe, admission port operated pneumatic valve, compressed air inlet port, vacuum generator operated pneumatic valve, vacuum generator, exhaust tube, exhaust tube operated pneumatic valve, transfer pressure container and induction pipe operated pneumatic valve and forms.The transfer pressure container is the main component of the utility model, and integral body is tank structure, and the upper end of transfer pressure container is provided with the admission port operated pneumatic valve between two parties, is connected with compressed air inlet port in the upper end of admission port operated pneumatic valve.One side in the upper end of transfer pressure container is provided with the induction pipe operated pneumatic valve, and the upper end at the induction pipe operated pneumatic valve is connected with induction pipe.The opposite side in the upper end of transfer pressure container is provided with the vacuum generator operated pneumatic valve, and the outer end at the vacuum generator operated pneumatic valve is connected with vacuum generator.In the lower end of transfer pressure container, be connected with the exhaust tube operated pneumatic valve, the outer end of exhaust tube operated pneumatic valve is connected with exhaust tube.The described pneumatic slag slurry conveyer of the utility model is the induction pipe that is separately installed with the band operated pneumatic valve in the upper end of one or one group transfer pressure container, the vacuum generator of band operated pneumatic valve and the compressed air inlet port of band operated pneumatic valve; The exhaust tube of band operated pneumatic valve is installed in the lower end of transfer pressure container; The outlet of vacuum generator and exhaust tube UNICOM.The operated pneumatic valve of each pipeline all links to each other with pneumatic control system.The working process of the utility model is: at first the vacuum generator operated pneumatic valve is opened, and the transfer pressure container is vacuumized, and after the induction pipe operated pneumatic valve was opened, slag slurry or loose dry material can be under the pressure differential effects, in induction pipe enters into the transfer pressure container.The induction pipe operated pneumatic valve of the vacuum generator operated pneumatic valve of vacuum generator and induction pipe is closed then, and exhaust tube operated pneumatic valve and admission port operated pneumatic valve are opened, and pressurized air gets into the transfer pressure container, and slag slurry or loose dry material are discharged through exhaust tube.After the waste gas that vacuum generator is discharged gets into exhaust tube, slurry of the slag in the exhaust tube or loose dry material are discharged complementaryly.Above process is by pneumatic control system, drives each operated pneumatic valve automatically and moves in order and realize.
The described pneumatic slag slurry conveyer of the utility model, integral structure is simple, and is easy for operation, good stability, reliability is high.The utility model is applicable to is not having electric power supply, in the less environment in space, and cleaning suction and carry slag slurry and loose dry material.Can solve the labor cleaning, carry capacity rating to be lower than the heavy problem of manual labor; Prior art slag stock pump can be solved and slag slurry or the loose dry material higher can not be aspirated with transportation concentration, and the big susceptible to plugging problem of wearing and tearing; Can also solve the prior art belt feeder only can higher slag slurry or the loose dry material of transportation concentration, the problem of not clearing up pumping function.
Description of drawings
Accompanying drawing 1 is the structural representation of the said pneumatic slag slurry conveyer of the utility model.1-induction pipe, 2-admission port operated pneumatic valve, 3-compressed air inlet port, 4-vacuum generator operated pneumatic valve, 5-vacuum generator, 6-exhaust tube, 7-exhaust tube operated pneumatic valve, 8-transfer pressure container, 9-induction pipe operated pneumatic valve.
The specific embodiment
Existing with reference to accompanying drawing 1; Explain as follows in conjunction with embodiment: the described pneumatic slag slurry conveyer of the utility model includes induction pipe 1, admission port operated pneumatic valve 2, compressed air inlet port 3, vacuum generator operated pneumatic valve 4, vacuum generator 5, exhaust tube 6, exhaust tube operated pneumatic valve 7, transfer pressure container 8 and induction pipe operated pneumatic valve 9 and forms.Transfer pressure container 8 is main components of the utility model, and integral body is tank structure, and the upper end of transfer pressure container 8 is provided with admission port operated pneumatic valve 2 between two parties, is connected with compressed air inlet port 3 in the upper end of admission port operated pneumatic valve 2.The side in the upper end of transfer pressure container 8 is provided with induction pipe operated pneumatic valve 9, in the upper end of induction pipe operated pneumatic valve 9, is connected with induction pipe 1.The opposite side in the upper end of transfer pressure container 8 is provided with vacuum generator operated pneumatic valve 4, in the outer end of vacuum generator operated pneumatic valve 4, is connected with vacuum generator 5.In the lower end of transfer pressure container 8, be connected with exhaust tube operated pneumatic valve 7, the outer end of exhaust tube operated pneumatic valve 7 is connected with exhaust tube 6.The described pneumatic slag slurry conveyer of the utility model is the induction pipe 1 that is separately installed with the band operated pneumatic valve in the upper end of one or one group transfer pressure container 8, the vacuum generator 5 of band operated pneumatic valve and the compressed air inlet port 3 of band operated pneumatic valve; The exhaust tube 6 of band operated pneumatic valve is installed in the lower end of transfer pressure container 8; The outlet of vacuum generator 5 and exhaust tube 6 UNICOMs.The operated pneumatic valve of each pipeline all links to each other with pneumatic control system.The working process of the utility model is: at first vacuum generator operated pneumatic valve 4 is opened; Transfer pressure container 8 is vacuumized; After induction pipe operated pneumatic valve 9 was opened, slag slurry or loose dry material can be under the pressure differential effects, in induction pipe 1 enters into transfer pressure container 8.The induction pipe operated pneumatic valve 9 of the vacuum generator operated pneumatic valve 4 of vacuum generator 5 and induction pipe 1 is closed then; Exhaust tube operated pneumatic valve 7 is opened with admission port operated pneumatic valve 2; Pressurized air gets into transfer pressure container 8, and slag slurry or loose dry material are discharged through exhaust tube 6.After the waste gas that vacuum generator 5 is discharged gets into exhaust tube 6, slurry of the slag in the exhaust tube 6 or loose dry material are discharged complementaryly.Above process is by pneumatic control system, drives each operated pneumatic valve automatically and moves in order and realize.The described pneumatic slag slurry conveyer of the utility model, integral structure is simple, and is easy for operation, good stability, reliability is high.The utility model is applicable to is not having electric power supply, in the less environment in space, and cleaning suction and carry slag slurry and loose dry material.Can solve the labor cleaning, carry capacity rating to be lower than the heavy problem of manual labor; Prior art slag stock pump can be solved and slag slurry or the loose dry material higher can not be aspirated with transportation concentration, and the big susceptible to plugging problem of wearing and tearing; Can also solve the prior art belt feeder only can higher slag slurry or the loose dry material of transportation concentration, the problem of not clearing up pumping function.
Claims (1)
1. pneumatic slag slurry conveyer is characterized in that the upper end of transfer pressure container (8) is provided with admission port operated pneumatic valve (2) between two parties, is connected with compressed air inlet port (3) in the upper end of admission port operated pneumatic valve (2); The side in the upper end of transfer pressure container (8); Be provided with induction pipe operated pneumatic valve (9), the upper end in induction pipe operated pneumatic valve (9) is connected with induction pipe (1); Upper end opposite side at transfer pressure container (8); Be provided with vacuum generator operated pneumatic valve (4), the outer end in vacuum generator operated pneumatic valve (4) is connected with vacuum generator (5); Lower end in transfer pressure container (8) is connected with exhaust tube operated pneumatic valve (7), and the outer end of exhaust tube operated pneumatic valve (7) is connected with exhaust tube (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120179818U CN202148043U (en) | 2011-05-31 | 2011-05-31 | Pneumatic slurry residue conveyor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120179818U CN202148043U (en) | 2011-05-31 | 2011-05-31 | Pneumatic slurry residue conveyor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202148043U true CN202148043U (en) | 2012-02-22 |
Family
ID=45589111
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201120179818U Expired - Fee Related CN202148043U (en) | 2011-05-31 | 2011-05-31 | Pneumatic slurry residue conveyor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202148043U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103407799A (en) * | 2013-08-28 | 2013-11-27 | 北京环卫集团环境研究发展有限公司 | Material vacuum conveying system and usage method thereof |
| CN103411135A (en) * | 2013-08-13 | 2013-11-27 | 甘肃兰凯淀粉水处理设备制造有限公司 | Positive-negative double-acting bubble removing and rapid conveying device for starch slurry |
-
2011
- 2011-05-31 CN CN201120179818U patent/CN202148043U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103411135A (en) * | 2013-08-13 | 2013-11-27 | 甘肃兰凯淀粉水处理设备制造有限公司 | Positive-negative double-acting bubble removing and rapid conveying device for starch slurry |
| CN103407799A (en) * | 2013-08-28 | 2013-11-27 | 北京环卫集团环境研究发展有限公司 | Material vacuum conveying system and usage method thereof |
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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: 20120222 Termination date: 20120531 |