CN210653712U - Bag material recovery system explodes - Google Patents
Bag material recovery system explodes Download PDFInfo
- Publication number
- CN210653712U CN210653712U CN201921430573.2U CN201921430573U CN210653712U CN 210653712 U CN210653712 U CN 210653712U CN 201921430573 U CN201921430573 U CN 201921430573U CN 210653712 U CN210653712 U CN 210653712U
- Authority
- CN
- China
- Prior art keywords
- diaphragm pump
- pneumatic diaphragm
- pipeline
- bag
- blanking
- 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.)
- Active
Links
Images
Landscapes
- Air Transport Of Granular Materials (AREA)
Abstract
A bag material recovery system comprises a bag material collecting tank, a material conveying device and a discharging device; the material conveying device comprises a pneumatic diaphragm pump and an auxiliary blowing gas, the auxiliary blowing gas is connected with the gas inlet end of the pneumatic diaphragm pump, the bag-blasting material collecting tank is connected with the material inlet end of the pneumatic diaphragm pump through a material inlet pipe of the pneumatic diaphragm pump, and the material outlet end of the pneumatic diaphragm pump is connected with the blanking device through a material outlet pipe of the pneumatic diaphragm pump; the blanking device comprises a blanking pipeline, a ball socket is arranged at the upper end of the blanking pipeline, and a feeding hole of the ball socket is connected with the tail end of a discharging pipe at the pneumatic diaphragm pump; the lower part of the blanking pipeline is connected with the cyclone separator through an inclined pipeline which inclines upwards; the lower extreme of unloading pipeline and cyclone's lower extreme are connected with the upper end feed inlet one and the feed inlet two of buffer bin respectively, and this system can explode the bag material to aerosil and carry out the closed emergence of retrieving and prevent the aerosil raise dust phenomenon, improves the operational environment between the packing, improves the recovery efficiency who explodes the bag material.
Description
Technical Field
The utility model relates to an explode bag material recovery system belongs to equipment for packing technical field.
Background
The gas phase silicon dioxide packaging process often has the phenomenon of bag explosion, and because the gas phase silicon dioxide particles are extremely fine and belong to micron-sized particles, and the adsorption force is strong, most of bag explosion materials generated in the packaging process are difficult to recover. At present, some of the bag materials that explode that produce in the fumed silica packaging process adopt artifical transport to empty back the product feed bin and retrieve, because artifical transport is retrieved intensity of labour high, inefficiency, and can't realize in the handling that the product seals to retrieve and easily causes the product contaminated, fumed silica's raise dust also can pollute the environment between the packing simultaneously, consequently most bag materials that explode pass through packing fan suction scrubbing tower and handle, cause the waste of product.
Disclosure of Invention
To the problem that above-mentioned prior art exists, the utility model provides an explode bag material recovery system, this system can explode bag material to aerosil and carry out closed recovery, avoids artifical transport to exploding the pollution of bag material, prevents the emergence of aerosil raise dust phenomenon, improves the operational environment between the packing, reduces workman's intensity of labour, improves the recovery efficiency who explodes the bag material.
In order to achieve the purpose, the utility model provides a bag explosion material recovery system, which comprises a bag explosion material collecting tank, a material conveying device and a discharging device;
the material conveying device comprises a pneumatic diaphragm pump and an auxiliary blowing gas, the auxiliary blowing gas is connected with the gas inlet end of the pneumatic diaphragm pump, the bag explosion material collecting tank is connected with the gas inlet end of the pneumatic diaphragm pump through a gas inlet pipe of the pneumatic diaphragm pump, and the discharge end of the pneumatic diaphragm pump is connected with the discharging device through a discharge pipe of the pneumatic diaphragm pump;
the blanking device comprises a blanking pipeline, a ball socket is arranged at the upper end of the blanking pipeline, and a feeding hole of the ball socket is connected with the tail end of a discharging pipe at the pneumatic diaphragm pump; the lower part of the blanking pipeline is connected with the cyclone separator through an inclined pipeline which inclines upwards; the lower end of the blanking pipeline and the lower end of the cyclone separator are respectively connected with a first feeding hole and a second feeding hole at the upper end of the buffer bin.
Furthermore, a first air door and a second air door are respectively arranged in the blanking pipeline and the inclined pipeline.
Furthermore, a downward inclined blanking baffle is arranged on the inner wall of the blanking pipeline at the side opposite to the lowest part of the inclined pipeline.
Furthermore, the inclination angle of the inclined pipeline is 30-45 degrees.
The utility model arranges the ball socket at the upper end of the blanking pipeline, the gas filled in the blanking pipeline can form vortex in the vortex air passage formed by the ball socket, and further buffer the gas, thus preventing the filled gas from directly impacting and entering the stock bin, and further avoiding the generation of gas phase silicon dioxide dust emission phenomenon; cyclone can in time suck the gas that gets into the unloading pipeline to cyclone upper end and discharge through the slope pipeline even more, the material then falls into in the buffer bin through slope pipeline or cyclone's lower extreme discharge gate, this system can explode the bag material to aerosil and carry out closed recovery, the pollution of the bag material of having avoided artifical transport to exploding, the emergence of aerosil raise dust phenomenon has been prevented, the operational environment between the packing has been improved, the labor intensity of workers is reduced, the recovery efficiency of exploding the bag material has been improved.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
In the figure: 1. the device comprises an explosion bag material collecting tank, 2, a material conveying device, 3, a discharging device, 4, a pneumatic diaphragm pump, 5, auxiliary blowing gas, 6, a pneumatic diaphragm pump feeding pipe, 7, a pneumatic diaphragm pump discharging pipe, 8, a discharging pipeline, 9, a ball socket, 10, an inclined pipeline, 11, a cyclone separator, 12, a buffer bin, 13, a feeding hole I, 14, a feeding hole II, 15, an air door I, 16, an air door II, 17 and a discharging baffle.
Detailed Description
The present invention will be further explained with reference to the accompanying drawings.
As shown in fig. 1, the recovery system for the bag bursting material comprises a bag bursting material collecting tank 1, a material conveying device 2 and a discharging device 3;
the material conveying device 2 comprises a pneumatic diaphragm pump 4 and an auxiliary blowing gas 5, the auxiliary blowing gas 5 is connected with the gas inlet end of the pneumatic diaphragm pump 4, the bag explosion material collecting tank 1 is connected with the gas inlet end of the pneumatic diaphragm pump 4 through a pneumatic diaphragm pump feeding pipe 6, and the gas outlet end of the pneumatic diaphragm pump 4 is connected with the blanking device 3 through a pneumatic diaphragm pump discharging pipe 7;
the blanking device 3 comprises a blanking pipeline 8, a ball socket 9 is arranged at the upper end of the blanking pipeline 8, and a feeding hole of the ball socket 9 is connected with the tail end of a discharging pipe 7 of the pneumatic diaphragm pump; the lower part of the blanking pipeline 8 is connected with a cyclone separator 11 through an inclined pipeline 10 which inclines upwards; the lower end of the blanking pipeline 8 and the lower end of the cyclone separator 11 are respectively connected with a first feeding hole 13 and a second feeding hole 14 at the upper end of the buffer bin 12.
In order to adjust the air volume more in line with the actual requirement, a first air door 15 and a second air door 16 are respectively arranged in the blanking pipeline 8 and the inclined pipeline 10.
In order to prevent the air flow from directly impacting the buffer bin, the inner wall of the blanking pipeline 8 at the side opposite to the lowest part of the inclined pipeline 10 is provided with a blanking baffle 17 which inclines downwards.
In order to ensure that the inclined pipeline 10 is in the best working state, the inclined angle is set to be 30-45 degrees.
The material of the bag explosion is collected in the collecting tank of the material explosion belt, the pneumatic diaphragm pump 4 conveys the material of the bag explosion into the blanking pipeline through the inlet pipe of the pneumatic diaphragm pump and the outlet pipe of the pneumatic diaphragm pump under the pushing action of the auxiliary blowing gas, the material passes through the ball socket arranged at the upper end of the blanking pipeline at first, the gas filled into the blanking pipeline can form vortex in the vortex air passage formed by the ball socket, and then cushion the gas, prevent the gas filled from directly impacting and entering the stock bin, meanwhile, the cyclone separator sucks the gas entering the blanking pipeline to the upper end of the cyclone separator through the inclined pipeline and discharges the gas, one part of the material in the inclined pipeline falls to the buffer stock bin, and the other part falls to the buffer stock bin through the cyclone separator; the system can carry out closed recovery on the fumed silica blasting bag material, avoids pollution caused by manual carrying of the blasting bag material, prevents the fumed silica dust raising phenomenon, improves the working environment between packages, reduces the labor intensity of workers, and improves the recovery efficiency of the blasting bag material.
Claims (4)
1. The system for recovering the bag-bursting materials comprises a bag-bursting material collecting tank, and is characterized by further comprising a material conveying device and a discharging device;
the material conveying device comprises a pneumatic diaphragm pump and an auxiliary blowing gas, the auxiliary blowing gas is connected with the gas inlet end of the pneumatic diaphragm pump, the bag explosion material collecting tank is connected with the gas inlet end of the pneumatic diaphragm pump through a gas inlet pipe of the pneumatic diaphragm pump, and the discharge end of the pneumatic diaphragm pump is connected with the discharging device through a discharge pipe of the pneumatic diaphragm pump;
the blanking device comprises a blanking pipeline, a ball socket is arranged at the upper end of the blanking pipeline, and a feeding hole of the ball socket is connected with the tail end of a discharging pipe at the pneumatic diaphragm pump; the lower part of the blanking pipeline is connected with the cyclone separator through an inclined pipeline which inclines upwards; the lower end of the blanking pipeline and the lower end of the cyclone separator are respectively connected with a first feeding hole and a second feeding hole at the upper end of the buffer bin.
2. The bag bursting material recycling system according to claim 1, wherein a first air door and a second air door are respectively arranged in the blanking pipeline and the inclined pipeline.
3. The bag bursting material recycling system according to claim 1 or 2, wherein a downward inclined blanking baffle is arranged on the inner wall of the blanking pipeline at the side opposite to the lowest part of the inclined pipeline.
4. The bag bursting material recycling system according to claim 3, wherein the inclined angle of the inclined pipeline is 30-45 degrees.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921430573.2U CN210653712U (en) | 2019-08-30 | 2019-08-30 | Bag material recovery system explodes |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921430573.2U CN210653712U (en) | 2019-08-30 | 2019-08-30 | Bag material recovery system explodes |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210653712U true CN210653712U (en) | 2020-06-02 |
Family
ID=70837252
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921430573.2U Active CN210653712U (en) | 2019-08-30 | 2019-08-30 | Bag material recovery system explodes |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210653712U (en) |
-
2019
- 2019-08-30 CN CN201921430573.2U patent/CN210653712U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN210875757U (en) | Dustless environmental protection analysis system sand powder process device of slay | |
| CN103691215A (en) | Heat preservation powder negative pressure recycling system in production of refractory material by using fusion casting method | |
| CN201042715Y (en) | Negative pressure dust removing device | |
| CN108543435A (en) | A kind of warehouse hybrid system and method | |
| CN210653712U (en) | Bag material recovery system explodes | |
| CN201553614U (en) | Automatic feeing system for producing spherical graphite | |
| CN106429449A (en) | Material conveying device for waste tire pyrolysis carbon black | |
| CN106076850A (en) | A kind of vibrosieve and the garbage sorting device of wind-force | |
| CN2894867Y (en) | Ultrasonic pressurized classifier | |
| CN202344408U (en) | Sand and dust separating and absorbing environment friendly device for blasting sand at inner wall of pipeline | |
| CN201950028U (en) | Impurity-removing and warehouse-entering system for raw material | |
| CN208761681U (en) | A kind of environment-friendly dustless miberal powder spike selection by winnowing conveying device | |
| CN104624402B (en) | A kind of cyclone separator | |
| CN206980349U (en) | A kind of grey storehouse ash-discharging device | |
| CN212768673U (en) | Environment-friendly powder storage system | |
| CN205818390U (en) | Vacuum charging device | |
| CN214861937U (en) | Light powder is not easily subsided with off-line jetting dust remover | |
| CN111776599B (en) | Stone paper production is with dustless dosing unit | |
| CN210456711U (en) | Bucket type ash discharging device for preventing dust from escaping | |
| CN209835033U (en) | Pneumatic conveying device | |
| CN205953045U (en) | Integral type powdery material material loading conveying system | |
| CN209814810U (en) | Dustless environmental protection feed bin | |
| CN206087494U (en) | Packing balance system that possesses dust removal function | |
| CN219816597U (en) | Dust collection hopper of crushing equipment | |
| CN213132297U (en) | Dust removal equipment for flour mill |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |