CN201952022U - Feeding flow stabilizing airlock for homogenization bunker - Google Patents
Feeding flow stabilizing airlock for homogenization bunker Download PDFInfo
- Publication number
- CN201952022U CN201952022U CN2010206976471U CN201020697647U CN201952022U CN 201952022 U CN201952022 U CN 201952022U CN 2010206976471 U CN2010206976471 U CN 2010206976471U CN 201020697647 U CN201020697647 U CN 201020697647U CN 201952022 U CN201952022 U CN 201952022U
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- Prior art keywords
- storehouse
- bunker
- flow stabilizing
- current stabilization
- slag micropowder
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Abstract
The utility model discloses a feeding flow stabilizing airlock for a homogenization bunker, which comprises a slag micro-powder bunker system, a cement bunker system and a conveyer, wherein the slag micro-powder bunker system comprises a slag micro-powder bunker, a spiral gate, an impeller feeding machine, a flow stabilizing bunker, a feeding reamer and a screw scale; in the slag micro-powder bunker system, an inflated unloading box, a power-driven flow control valve, a starting switch valve and other devices are reduced, and the impeller feeding machine and the flow stabilizing bunker are additionally arranged; and a tapered flow stabilizing bunker with a weighting and metering device and the impeller feeding machine realize automatic control and linkage as well as feeding quantitatively at fixed time. Through a plurality of exhaust dust collector filter bags distributed on the top of the flow stabilizing bunker, residual gases in materials are exhausted, and the flow stabilizing effect is obvious.
Description
Affiliated technical field:
The utility model relates to the powder material blanking from flow control technology.
Background technology:
Open type inflation homogenizer is adopted in the bottom of the reservior in existing cement silo and slag micropowder storehouse, top, storehouse installing duct cyclone.The storehouse is power traction wind against the wind, and discharging control gauging device is followed successively by from top to bottom under the storehouse: the flow control of spiral gate, inflation dump box, electric flow control valve, pneumatic on-off valve, screw feeder, spiral metering scale, two storehouse dischargings, the ratio of material proportion are set, are adjusted and finish by the computing machine master control system.Because material is residual when drawing off from homogenizing storehouse more high pressure gas are arranged, mixing of materials high pressure gas and is entered the discharging gauging device, and under deadweight and high-voltage double action, kinematic velocity is changeable.Spiral metering scale shows numerical value full scale always, and it is inoperative that numerical value is set in control.Enter high-pressure blast in the plenum box of homogenizing storehouse bottom of the reservior and see through when filter cloth makes the material bottom produce strenuous vibration and often cause fluidization of material, materials flow is suddenly big or suddenly small, forms to dash material.When serious, material comes down in torrents as water, following equipment is all flooded push down, and makes to produce to interrupt.
Summary of the invention:
In order to overcome material movement velocity variations impermanence in the discharging of cement homogenizing storehouse, spiral metering scale is malfunctioning, and it is inoperative that numerical value is set in control, often causes the deficiency of fluidization of material, and the utility model provides a kind of homogenizing storehouse blanking current stabilization airlock.Reduce the air content in the material, eliminate the powerful booster action of high pressure gas, utilize impeller to rotate continuously, destroy the continuity of air-flow in the material, top, the storehouse dust exhaustor of passing through on the gas in the material is discharged, play lock wind purpose Flow of Goods and Materials.
The scheme that the utility model solves its technical barrier is by slag micropowder storehouse system, the cement silo system, conveyer constitutes, two storehouse systems are identical, with the slag micropowder storehouse is example, slag micropowder storehouse system is by the slag micropowder storehouse, spiral gate, revolving plow reclaimer, the current stabilization storehouse, the feed reamer, helix balance is formed, the slag micropowder storehouse is circular storehouse, slag warehouse-in mouth is arranged at top, dust-precipitator is installed, bottom, slag micropowder storehouse one side is equipped with roots blower, discharging opening is connected with spiral gate, and spiral gate is connected with revolving plow reclaimer, and the current stabilization storehouse is tapered, periphery is equipped with filter bag, filter bag communicates with the current stabilization storehouse, and revolving plow reclaimer communicates with the current stabilization storehouse, and the outlet of current stabilization storehouse is connected with the import of feed reamer, the outlet of feed reamer is connected with helix balance, and the helix balance outlet communicates with conveyer.
The beneficial effects of the utility model are: slag micropowder storehouse system has reduced devices such as inflation dump box, electric flow control valve, pneumatic on-off valve, revolving plow reclaimer and current stabilization bin device have been increased, the steady feed bin of taper and the revolving plow reclaimer that have Weighing device realize that automatic guidance is chain, at regular time and quantity feeding.By a plurality of exhaust filter bag of dust collector that lay at steady feed bin top, discharge residual gas in the material, steady flow result is obvious.
Description of drawings:
Fig. 1. be the utility model structural front view.
The specific embodiment:
The utility model is by slag micropowder storehouse 3 systems, cement silo system 12, conveyer 9 constitutes, two storehouse systems are identical, with slag micropowder storehouse 3 is example, slag micropowder storehouse system is by the slag micropowder storehouse, spiral gate 4, revolving plow reclaimer 5, current stabilization storehouse 7, feed reamer 11, helix balance 10 is formed, slag micropowder storehouse 3 is circular storehouse, slag warehouse-in mouth 2 is arranged at top, dust-precipitator 1 is installed, 3 bottoms, slag micropowder storehouse, one side is equipped with roots blower 8, discharging opening is connected with spiral gate 4, and spiral gate 4 is connected with revolving plow reclaimer 5, and current stabilization storehouse 7 is tapered, periphery is equipped with filter bag 6, filter bag 6 communicates with current stabilization storehouse 7, and revolving plow reclaimer 5 communicates with current stabilization storehouse 7, and 7 outlets of current stabilization storehouse are connected with 11 imports of feed reamer, 11 outlets of feed reamer are connected with helix balance 10, and helix balance 10 outlets communicate with conveyer 9.
Claims (1)
1. homogenizing storehouse blanking current stabilization airlock is by slag micropowder storehouse system, the cement silo system, conveyer constitutes, it is characterized in that: slag micropowder storehouse system is by the slag micropowder storehouse, spiral gate, revolving plow reclaimer, the current stabilization storehouse, the feed reamer, helix balance is formed, the slag micropowder storehouse is circular storehouse, slag warehouse-in mouth is arranged at top, dust-precipitator is installed, bottom, slag micropowder storehouse one side is equipped with roots blower, discharging opening is connected with spiral gate, spiral gate is connected with revolving plow reclaimer, the current stabilization storehouse is tapered, periphery is equipped with filter bag, filter bag communicates with the current stabilization storehouse, and revolving plow reclaimer communicates with the current stabilization storehouse, and the outlet of current stabilization storehouse is connected with the import of feed reamer, the outlet of feed reamer is connected with helix balance, and the helix balance outlet communicates with conveyer.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010206976471U CN201952022U (en) | 2010-12-29 | 2010-12-29 | Feeding flow stabilizing airlock for homogenization bunker |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010206976471U CN201952022U (en) | 2010-12-29 | 2010-12-29 | Feeding flow stabilizing airlock for homogenization bunker |
Publications (1)
Publication Number | Publication Date |
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CN201952022U true CN201952022U (en) | 2011-08-31 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN2010206976471U Expired - Fee Related CN201952022U (en) | 2010-12-29 | 2010-12-29 | Feeding flow stabilizing airlock for homogenization bunker |
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CN (1) | CN201952022U (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103057935A (en) * | 2013-01-18 | 2013-04-24 | 戚宗华 | Material balance feeding mechanism of belt conveyor |
CN103287869A (en) * | 2013-05-22 | 2013-09-11 | 南通三鑫重工机械有限公司 | Silo-bottom unloading device |
CN103303612A (en) * | 2013-05-22 | 2013-09-18 | 江苏新业重工股份有限公司 | Warehouse bottom discharging valve system |
CN106766946A (en) * | 2016-08-30 | 2017-05-31 | 彭武星 | The dry coke quenching or sintering deposit cooling stove of even distributing wind uniform discharge lock wind |
CN109539295A (en) * | 2018-12-06 | 2019-03-29 | 广东清远蒙娜丽莎建陶有限公司 | With baking sulphur intelligence feeding system in a kind of furnace |
CN110422638A (en) * | 2019-07-03 | 2019-11-08 | 浙江磊纳微粉材料有限公司 | A kind of large size homogenizing storehouse and its application method |
-
2010
- 2010-12-29 CN CN2010206976471U patent/CN201952022U/en not_active Expired - Fee Related
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103057935A (en) * | 2013-01-18 | 2013-04-24 | 戚宗华 | Material balance feeding mechanism of belt conveyor |
CN103287869A (en) * | 2013-05-22 | 2013-09-11 | 南通三鑫重工机械有限公司 | Silo-bottom unloading device |
CN103303612A (en) * | 2013-05-22 | 2013-09-18 | 江苏新业重工股份有限公司 | Warehouse bottom discharging valve system |
CN106766946A (en) * | 2016-08-30 | 2017-05-31 | 彭武星 | The dry coke quenching or sintering deposit cooling stove of even distributing wind uniform discharge lock wind |
CN109539295A (en) * | 2018-12-06 | 2019-03-29 | 广东清远蒙娜丽莎建陶有限公司 | With baking sulphur intelligence feeding system in a kind of furnace |
CN110422638A (en) * | 2019-07-03 | 2019-11-08 | 浙江磊纳微粉材料有限公司 | A kind of large size homogenizing storehouse and its application method |
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Legal Events
Date | Code | Title | Description |
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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: 20110831 Termination date: 20131229 |