CN205471646U - Powder pneumatic conveyor system - Google Patents

Powder pneumatic conveyor system Download PDF

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Publication number
CN205471646U
CN205471646U CN201620304168.6U CN201620304168U CN205471646U CN 205471646 U CN205471646 U CN 205471646U CN 201620304168 U CN201620304168 U CN 201620304168U CN 205471646 U CN205471646 U CN 205471646U
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CN
China
Prior art keywords
cyclone dust
dust extractor
powder
cla
discharge
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
Application number
CN201620304168.6U
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Chinese (zh)
Inventor
王治航
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Zhengzhou Chenhang Electrical And Mechanical Technology Co Ltd
Original Assignee
Zhengzhou Chenhang Electrical And Mechanical Technology Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Zhengzhou Chenhang Electrical And Mechanical Technology Co Ltd filed Critical Zhengzhou Chenhang Electrical And Mechanical Technology Co Ltd
Priority to CN201620304168.6U priority Critical patent/CN205471646U/en
Application granted granted Critical
Publication of CN205471646U publication Critical patent/CN205471646U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model belongs to powder transportation field especially relates to powder pneumatic conveyor system. The system includes former feed bin, discharging material silo and drying device, and former feed bin bottom is equipped with the discharge gate with feed - pipe connection, and discharge gate department is equipped with and pushes away the material auger, and the conveying pipe passes through cyclone to be connected with discharging material silo, and cyclone passes through the backwind tube and is connected with the air exhauster, drying device includes air -blower and connected main tuber pipe, and main tuber pipe lies in and is equipped with heating device on the outside body of former feed bin, and main tuber pipe lies in and is equipped with several tuber pipes on the inside body of former feed bin, be equipped with gaseous cleaning device on the backwind tube between cyclone and the air exhauster, the discharging material silo bottom is equipped with electronics weighing device, and electronics weighing device is connected with external display device electricity. The utility model discloses simple structure can effectively solve the problem that the powder that gets damp blockked up pipe and valve.

Description

Powder wind-force induction system
Technical field
This utility model belongs to powder transport field, particularly relates to powder wind-force induction system.
Background technology
Powder delivery system of the prior art, mostly is belt conveyor, buries scraper plate or conveying worm adds bucket elevator, and due to the many poor sealing of its transmission failure, during the conveying of a distance high position, equipment is huge.In prior art, also having employing gases at high pressure conveyer device conveying powder, but discharging efficiency is low, powder is hygroscopic in addition gets damp, and causes pipe and valve blockage, and is ultimately discharged in the gases at high pressure in the external world containing powder, causes environmental pollution.
Utility model content
The purpose of this utility model is to provide a kind of powder wind-force induction system, this utility model simple in construction, it is possible to effectively solve get damp powder blocking pipe and the problem of valve.
For solving above-mentioned technical problem, the technical solution adopted in the utility model is as follows:
Powder wind-force induction system, described system includes raw material cabin, discharge bin and drying device, is provided with the discharging opening being connected with feed pipe bottom raw material cabin, and discharge outlet is provided with pusher auger, feed pipe is connected with discharge bin by cyclone dust extractor, and cyclone dust extractor is connected with air exhauster by backwind tube;Drying device includes aerator and connected air main, and air main is positioned at the body outside raw material cabin and is provided with heater, and air main is positioned at the body within raw material cabin and is provided with several discharge pipe;Backwind tube between cyclone dust extractor and air exhauster is provided with air cleaning device;Being provided with electronic weighing device bottom discharge bin, electronic weighing device electrically connects with extraneous display device.
Preferably, described air cleaning device includes dirt pocket and the hothouse that top connects, and is provided with the spray head for water spray, is provided with desiccant packed layer in hothouse in dirt pocket.
Preferably, described cyclone dust extractor is CLA cyclone dust extractor.
Preferably, the charging aperture of described CLA cyclone dust extractor is connected with feed pipe, and the exhaust outlet of CLA cyclone dust extractor is connected with backwind tube, and CLA cyclone dust extractor discharge gate is connected with discharge bin.
Preferably, described CLA cyclone dust extractor discharge gate is provided with star-shaped dust-discharging valve with the junction of discharge bin.
The air main and the discharge pipe that are positioned at raw material cabin are all buried by powder.
During work, air exhauster and aerator start simultaneously, aerator passes through air main and discharge pipe to blasting the gas after heating devices heat in raw material cabin, powder in raw material cabin is dried, the most also compressing powder is discharged from discharging opening, powder is by entering feed pipe after the promotion of pusher auger and gas, and realizes gas, material separation in the charging aperture entrance CLA cyclone dust extractor of CLA cyclone dust extractor, and powder enters discharge bin eventually through star-shaped dust-discharging valve;Gas enters backwind tube by the exhaust outlet of CLA cyclone dust extractor, gas is in the dirt pocket of air cleaning device, the water sprayed by spray head is carried out, the dust being mingled with is removed, subsequently into hothouse and be dried indoor desiccant packed layer suck steam, be finally discharged outside under the swabbing action of air exhauster;After the powder in discharge bin reaches certain mass, corresponding data is shown by electronic weighing device by display device, facilitates staff to close relevant device.
This utility model compared with prior art, has the advantage that
1) by air main and discharge pipe, the powder in raw material cabin is carried out hot air drying, prevent get damp powder blocking pipe and valve;
2) it is cleaned processing to gas by dirt pocket and hothouse, prevents dust be discharged to the external world and pollute environment.
Accompanying drawing explanation
Fig. 1 is the structural representation of powder wind-force induction system in detailed description of the invention;
Figure is labeled as: raw material cabin 1, discharge bin 2, aerator 3, air exhauster 4, heater 5, air main 6, discharge pipe 7, pusher auger 8, feed pipe 9, backwind tube 10, electronic weighing device 11, dirt pocket 12, hothouse 13, spray head 14, desiccant packed layer 15, CLA cyclone dust extractor 16.
Detailed description of the invention
In order to make the purpose of this utility model, technical scheme and advantage clearer, below in conjunction with drawings and Examples, this utility model is further elaborated.Should be appreciated that specific embodiment described herein, only in order to explain this utility model, is not used to limit this utility model.
As shown in Figure 1, powder wind-force induction system, described system includes raw material cabin 1, discharge bin 2 and drying device, the discharging opening being connected with feed pipe 9 it is provided with bottom raw material cabin 1, discharge outlet is provided with pusher auger 8, feed pipe 9 is connected with the charging aperture of CLA cyclone dust extractor 16, and the exhaust outlet of CLA cyclone dust extractor 16 is connected with air exhauster 4 by backwind tube 10, and the discharge gate of CLA cyclone dust extractor 16 is connected with discharge bin 2 by star-shaped dust-discharging valve;Drying device includes aerator 3 and connected air main 6, and air main 6 is positioned at the body outside raw material cabin 1 and is provided with heater 5, and air main 6 is positioned at the body within raw material cabin 1 and is provided with several discharge pipe 7;Backwind tube 10 between CLA cyclone dust extractor 16 and air exhauster 4 is provided with air cleaning device, air cleaning device includes dirt pocket 12 and the hothouse 13 that top connects, it is provided with the spray head 14 for water spray in dirt pocket 12, in hothouse 13, is provided with desiccant packed layer 15;Being provided with electronic weighing device 11 bottom discharge bin 2, electronic weighing device 11 electrically connects with extraneous display device.
The air main 6 and the discharge pipe 7 that are positioned at raw material cabin are all buried by powder.
During work, air exhauster 4 and aerator 3 start simultaneously, aerator 3 passes through air main 6 and discharge pipe 7 to the gas blasted in raw material cabin 1 after heater 5 heats, powder in raw material cabin is dried, the most also compressing powder is discharged from discharging opening, powder is by entering feed pipe 9 after the promotion of pusher auger 8 and gas, and realizes gas, material separation in the charging aperture entrance CLA cyclone dust extractor of CLA cyclone dust extractor 16, and powder enters discharge bin 2 eventually through star-shaped dust-discharging valve;Gas enters backwind tube 10 by the exhaust outlet of CLA cyclone dust extractor 16, gas is in the dirt pocket 12 of air cleaning device, the water sprayed by spray head 14 is carried out, the dust being mingled with is removed, subsequently into hothouse 13 and be dried indoor desiccant packed layer 15 suck steam, be finally discharged outside under the swabbing action of air exhauster 4;After the powder in discharge bin 2 reaches certain mass, corresponding data is shown by electronic weighing device 11 by display device, facilitates staff to close relevant device.

Claims (5)

1. powder wind-force induction system, it is characterized in that, described system includes raw material cabin, discharge bin and drying device, the discharging opening being connected with feed pipe it is provided with bottom raw material cabin, discharge outlet is provided with pusher auger, feed pipe is connected with discharge bin by cyclone dust extractor, and cyclone dust extractor is connected with air exhauster by backwind tube;Drying device includes aerator and connected air main, and air main is positioned at the body outside raw material cabin and is provided with heater, and air main is positioned at the body within raw material cabin and is provided with several discharge pipe;Backwind tube between cyclone dust extractor and air exhauster is provided with air cleaning device;Being provided with electronic weighing device bottom discharge bin, electronic weighing device electrically connects with extraneous display device.
2. powder wind-force induction system as claimed in claim 1, it is characterised in that described air cleaning device includes dirt pocket and the hothouse that top connect, is provided with the spray head for spraying water, is provided with desiccant packed layer in hothouse in dirt pocket.
3. powder wind-force induction system as claimed in claim 1, it is characterised in that described cyclone dust extractor is CLA cyclone dust extractor.
4. powder wind-force induction system as claimed in claim 3, it is characterised in that the charging aperture of described CLA cyclone dust extractor is connected with feed pipe, and the exhaust outlet of CLA cyclone dust extractor is connected with backwind tube, and CLA cyclone dust extractor discharge gate is connected with discharge bin.
5. powder wind-force induction system as claimed in claim 4, it is characterised in that described CLA cyclone dust extractor discharge gate is provided with star-shaped dust-discharging valve with the junction of discharge bin.
CN201620304168.6U 2016-04-13 2016-04-13 Powder pneumatic conveyor system Expired - Fee Related CN205471646U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620304168.6U CN205471646U (en) 2016-04-13 2016-04-13 Powder pneumatic conveyor system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620304168.6U CN205471646U (en) 2016-04-13 2016-04-13 Powder pneumatic conveyor system

Publications (1)

Publication Number Publication Date
CN205471646U true CN205471646U (en) 2016-08-17

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620304168.6U Expired - Fee Related CN205471646U (en) 2016-04-13 2016-04-13 Powder pneumatic conveyor system

Country Status (1)

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CN (1) CN205471646U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108622666A (en) * 2018-07-02 2018-10-09 芜湖万向新元环保科技有限公司 A kind of rod shaped materials pneumatic transport equipment

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108622666A (en) * 2018-07-02 2018-10-09 芜湖万向新元环保科技有限公司 A kind of rod shaped materials pneumatic transport equipment
CN108622666B (en) * 2018-07-02 2020-04-28 芜湖万向新元环保科技有限公司 Bar-shaped material pneumatic conveying equipment

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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: 20160817

Termination date: 20200413