CN202246085U - Device for blowing ultra-fine metal silicon powder into bag - Google Patents
Device for blowing ultra-fine metal silicon powder into bag Download PDFInfo
- Publication number
- CN202246085U CN202246085U CN2011203702065U CN201120370206U CN202246085U CN 202246085 U CN202246085 U CN 202246085U CN 2011203702065 U CN2011203702065 U CN 2011203702065U CN 201120370206 U CN201120370206 U CN 201120370206U CN 202246085 U CN202246085 U CN 202246085U
- Authority
- CN
- China
- Prior art keywords
- bag
- silicon
- water
- carbon rod
- injector
- 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
Links
Images
Landscapes
- Silicon Compounds (AREA)
Abstract
The utility model relates to a device for blowing ultra-fine metal silicon powder into a bag. The device comprises a gas storage tank, an oil-water separator, an adjustable sprayer, a conveying pipe, a holder, a carbon rod, a silicon water bag, a storage cabin, a pressure control valve, a gas source control valve and the like, wherein the gas storage stank, the oil-water separator, the adjustable sprayer, the carbon rod and the silicon water bag are connected and communicated through the conveying pipe. Compressed air is taken as conveying power, and ultra-fine metal silicon powder is sprayed into a silicon bag under the action of the adjustable sprayer and is directly sprayed into a high-temperature silicon liquid for undergoing secondary smelting and recycling, so that the product recovery rate is increased, the production cost is lowered, and the problems that the ultra-fine metal silicon powder suspends easily and is difficult to recycle are solved.
Description
One, technical field
The utility model relates to a kind of winding-up anti-package device of superfine metal silica flour, belongs to metallic silicon smelting equipment preparing technical field.
Two, background technology
In metallic silicon power airflow milling production technique, product granularity requires to be 35-180 order (wherein+35 order＜3% ,-180 orders＜5%), yet-180 purpose superfine metal silica flour amounts that produce in the airflow milling actual production process reach 16～18%.Partly powder is less, cheap owing to the market requirement for this, sells difficulty outward, directly returns bag or be used for easy suspension of place mat ingot mould to fly upward, and cause environmental pollution, so burden is bigger, causes production cost to rise, and influences economic benefit.Return bag through winding-up, make the superfine metal silica flour directly fuse into high temperature silicon water and get into product.Improve product recovery rate, reduce production costs, thereby solve the problem that the superfine metal silica flour is easy to suspend and is difficult to recycle.
Known superfine metal silica flour is handled approach: the one, and outer at a low price selling; The 2nd, manual work directly adds silicon water bag or is used for the place mat ingot mould.Outer at a low price selling caused the cost loss.Artificial directly returning wrapped or the place mat ingot mould, and easy suspension is flown upward, not only labour intensity greatly, environmental pollution, have security risk, it is healthy to influence the workman, and recovery utilization rate is low.
Three, summary of the invention
The purpose of the utility model provides a kind of winding-up of superfine metal silica flour and returns bag apparatus; Specifically be to utilize pressurized air, under the effect that can debug injector, the superfine metal silica flour sprayed into the silicon bag as transmitting power; Make the superfine metal silica flour directly spray into high temperature silicon liquid and carry out the secondary smelting recycling; Improve product recovery rate, reduce production costs, thereby solve the problem that the superfine metal silica flour is easy to suspend and is difficult to recycle.
The utility model is implemented by following technical scheme, and it comprises gas-holder 1, water-and-oil separator 2, tensimeter 3, discharge valve 4; Can debug injector 5, adapter bonnet 6, transfer lime 7, supporting apparatus 8, carbon rod 9; Silicon water bag 10, storage bin 11, pressure controlled valve 12, source of the gas valve 13.
Gas-holder 1, water-and-oil separator 2 connects and is communicated with transport pipe 7; Tensimeter 3 is arranged on water-and-oil separator 2 and can debugs on the transport pipe between the injector 5, and discharge valve 4 is arranged on the end opening of storage bin 11, and adapter bonnet 6 is welded on the right side of the outlet that can debug injector 5; The last adapter bonnet 6 that supporting apparatus 8 is welded on silicon water bag 10 is welded on the right side of the outlet that can debug injector 5; Supporting apparatus 8 is welded on the suitable for reading of silicon water bag 10, and pressure controlled valve 12 is arranged between gas-holder 1 and the water-and-oil separator 2, and source of the gas valve 13 is arranged on water-and-oil separator 2 and can debugs between the injector 5; Transport pipe 7 and carbon rod 9 are connected by fabric hose; Carbon rod 9 is fixing by supporting apparatus 8, and carbon rod is hollow barred body, immerses during assembling in the silicon water bag 10; Guarantee under the effect of bottom blowing pressure, not suspend after the superfine metal silica flour sprays into the silicon bag, directly fuse in the high temperature silicon liquid.
During work, storage bin 11 is added the full superfine metal silica flour of storage, opens source of the gas valve 13, pressurized air is purified through water-and-oil separator 2 remove airborne moisture content and greasy dirt, through adjusting control valve 12 with pressure-controlling at 0.2～0.6MPa.Open discharge valve 4 feed; Superfine metal silica flour and pressurized air can change the speed ability through debugging injector 5 in the injector internal pressure, and air and superfine metal silica flour mix the generation energy exchange each other; Form one pressure placed in the middle, speed isostatic gas, solid mixed stream; Mixed stream pressure behind scatterer raises, and forms one high speed mixed stream and gets into transport pipe 7, through carbon rod 9 the superfine metal silica flour is sprayed into silicon bag 10, and carbon rod immerses high temperature silicon liquid 200-500mm; Guarantee under the effect of bottom blowing pressure, not suspend after the superfine metal silica flour sprays into the silicon bag, directly fuse in the high temperature silicon liquid.
Compare the advantage that has with known technology:
The utility model is provided with airtight transport pipe and high-velocity jet device; The superfine metal silica flour is directly sprayed into high temperature silicon liquid with pressurized air carry out the secondary smelting recycling; Improve product recovery rate; Reduce production costs, thereby solve the problem that the superfine metal silica flour is easy to suspend and is difficult to recycle.
Four, description of drawings
Fig. 1 connects synoptic diagram for the utility model technology, among the figure, and the 1st, gas-holder, the 2nd, water-and-oil separator; The 3rd, tensimeter, the 4th, discharge valve, the 5th, can debug injector, the 6th, adapter bonnet, the 7th, transfer lime; The 8th, supporting apparatus, the 9th, carbon rod, the 10th, silicon water bag; The 11st, storage bin, the 12nd, pressure controlled valve, the 13rd, source of the gas valve.
Five, embodiment
As shown in Figure 1, it comprises gas-holder 1, water-and-oil separator 2, and tensimeter 3, discharge valve 4 can be debugged injector 5, adapter bonnet 6, transfer lime 7, supporting apparatus 8, carbon rod 9, silicon water bag 10, storage bin 11, pressure controlled valve 12, source of the gas valve 13.Gas-holder 1, water-and-oil separator 2 connects and is communicated with transport pipe 7; Tensimeter 3 is arranged on water-and-oil separator 2 and can debugs on the transport pipe between the injector 5, and discharge valve 4 is arranged on the end opening of storage bin 11, and adapter bonnet 6 is welded on the right side of the outlet that can debug injector 5; Supporting apparatus 8 is welded on the suitable for reading of silicon water bag 10, and pressure controlled valve 12 is arranged between gas-holder 1 and the water-and-oil separator 2, and source of the gas valve 13 is arranged on water-and-oil separator 2 and can debugs between the injector 5; Transport pipe 7 and carbon rod 9 are connected by fabric hose; Carbon rod 9 is fixing by supporting apparatus 8, and carbon rod is hollow barred body, immerses the high temperature silicon liquid 200-500mm in the silicon water bag 10 during assembling; Guarantee under the effect of bottom blowing pressure, not suspend after the superfine metal silica flour sprays into the silicon bag, directly fuse in the high temperature silicon liquid.
Claims (2)
1. bag apparatus is returned in the winding-up of a superfine metal silica flour, it is characterized in that: it comprises gas-holder (1), water-and-oil separator (2), tensimeter (3); Discharge valve (4) can be debugged injector (5), adapter bonnet (6), transfer lime (7); Supporting apparatus (8), carbon rod (9), silicon water bag (10), storage bin (11); Pressure controlled valve (12), source of the gas valve (13), gas-holder (1), water-and-oil separator (2); Connect and be communicated with transport pipe (7), tensimeter (3) is arranged on water-and-oil separator (2) and can debugs on the transport pipe between the injector (5), and discharge valve (4) is arranged on the end opening of storage bin (11); Adapter bonnet (6) is welded on the right side of the outlet that can debug injector (5), and the last adapter bonnet (6) that supporting apparatus (8) is welded on silicon water bag (10) is welded on the right side of the outlet that can debug injector (5), and supporting apparatus (8) is welded on the suitable for reading of silicon water bag (10); Pressure controlled valve (12) is arranged between gas-holder (1) and the water-and-oil separator (2), and source of the gas valve (13) is arranged on water-and-oil separator (2) and can debugs between the injector (5), and transport pipe (7) is connected by fabric hose with carbon rod (9); Carbon rod (9) is fixing by supporting apparatus (8), and carbon rod is hollow barred body, immerses in the silicon water bag (10) during assembling.
2. bag apparatus is returned in the winding-up of superfine metal silica flour according to claim 1, it is characterized in that: the degree of depth that described carbon rod (9) immerses the high temperature silicon liquid in the silicon water bag (10) is 200-500mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203702065U CN202246085U (en) | 2011-10-08 | 2011-10-08 | Device for blowing ultra-fine metal silicon powder into bag |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203702065U CN202246085U (en) | 2011-10-08 | 2011-10-08 | Device for blowing ultra-fine metal silicon powder into bag |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202246085U true CN202246085U (en) | 2012-05-30 |
Family
ID=46107358
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011203702065U Expired - Fee Related CN202246085U (en) | 2011-10-08 | 2011-10-08 | Device for blowing ultra-fine metal silicon powder into bag |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202246085U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113414123A (en) * | 2021-06-10 | 2021-09-21 | 云南永昌硅业股份有限公司 | Vein quartz color sorting method and device for improving quality of industrial silicon smelting raw materials |
| CN113426707A (en) * | 2021-06-10 | 2021-09-24 | 云南永昌硅业股份有限公司 | Silicon slag color separation method and device for effectively improving silicon metal recovery rate |
-
2011
- 2011-10-08 CN CN2011203702065U patent/CN202246085U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113414123A (en) * | 2021-06-10 | 2021-09-21 | 云南永昌硅业股份有限公司 | Vein quartz color sorting method and device for improving quality of industrial silicon smelting raw materials |
| CN113426707A (en) * | 2021-06-10 | 2021-09-24 | 云南永昌硅业股份有限公司 | Silicon slag color separation method and device for effectively improving silicon metal recovery rate |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201128620Y (en) | Gas-water spray humidifying dust removing apparatus | |
| CN203216310U (en) | Atomization cooling tower | |
| CN203294735U (en) | Single-fluid and dual-fluid combination dust removal device structure | |
| CN202246085U (en) | Device for blowing ultra-fine metal silicon powder into bag | |
| CN204737440U (en) | Powder ration feeder | |
| CN102527660A (en) | Cleaning method using uniformly and stably jet cleaning agent formed by separately using liquid carbon dioxide or mixing liquid carbon dioxide and compressed gas | |
| CN104524901A (en) | Auto-induction atomizing dust collector for crushing station | |
| CN102817612B (en) | Tapered jet foam sol generating device for controlling coal dust at transferring point of conveyor belt | |
| CN203991206U (en) | Spraying aluminum profile feeding cycle device | |
| CN201078239Y (en) | Wind pressure water straining magnetizing dustfall apparatus | |
| CN203525494U (en) | Controllable dry fog dust suppression device for open type receiving point | |
| CN204352698U (en) | A kind of for Crushing Station auto-induction type atomization dust-collecting equipment | |
| CN202427582U (en) | Belt material conveying high pressure water atomization dust suppression device | |
| CN202741225U (en) | Totally-enclosed discharge device for pebble coal of medium-speed coal pulverizer | |
| CN204173619U (en) | A kind of grab bucket discharge system with suppressing dust with dry mist device | |
| CN205997223U (en) | A kind of deodorant cooling conveying device of compounded rubber | |
| CN202337736U (en) | Atomized water spraying device of emulsion explosive conveying belt | |
| CN202277876U (en) | Cold fog humidifier for sulfur grinder | |
| CN208594264U (en) | A kind of efficient process units of washing powder | |
| CN203155154U (en) | Pulse air flow stirring device | |
| CN202511624U (en) | Sintered iron material watering device for belt conveyer | |
| CN202893169U (en) | Device for simultaneously generating ozone, desulfurizing and denitrating by high-pressure electrostatic dust collection electric field of coal-fired unit | |
| CN205628256U (en) | Solid is smashed and conveyer | |
| CN205164388U (en) | Dust recovery device | |
| CN205295663U (en) | With resin glue automatic -mixing jetting device during inorganic fiber insulation material fiber forming |
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: 20120530 Termination date: 20121008 |