CN103132105A - Electrolyte powder preparation, storage and conveying system device - Google Patents
Electrolyte powder preparation, storage and conveying system device Download PDFInfo
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- CN103132105A CN103132105A CN2011103783692A CN201110378369A CN103132105A CN 103132105 A CN103132105 A CN 103132105A CN 2011103783692 A CN2011103783692 A CN 2011103783692A CN 201110378369 A CN201110378369 A CN 201110378369A CN 103132105 A CN103132105 A CN 103132105A
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Abstract
The invention discloses an electrolyte powder preparation, storage and conveying system device. The electrolyte powder preparation, storage and conveying system device is efficient, energy-saving and environmentally friendly and is characterized in that a double-layer electrolyte powder warehouse is arranged between two electrolysis plant workshops; a quantitative feeding screw conveyer (2) and a boiling bed (3) are arranged between an electrolyte warehouse (4) and a fresh alumina warehouse (1) of the double-layer electrolyte powder warehouse; the quantitative feeding screw conveyer (2) and the boiling bed (3) compose a material preparation system; a conveying device (5) is arranged below the electrolyte warehouse (4); and the conveying device (5) is connected to a material addition device (6). Through the double-layer electrolyte powder warehouse and the material preparation system between the upper and lower workshops, efficient production requirements are satisfied; energy is saved; and environmental protection is realized.
Description
Technical field
The present invention relates to a kind of electrolyte powder batching and storing-conveying apparatus, belong to the Aluminium Electrolysis technical field.
Background technology
Electrolyte powder batching and storage are the indispensable technological process of productions of Aluminium Electrolysis enterprise, and the normal operation of Aluminum Electrolysis Production is played vital effect.
At present, usually the method that adopts is: individual layer electrolyte powder warehouse is set between two cell rooms, electrolyte powder is stored without mixing directly to enter in the storehouse with fresh aluminum oxide, by super concentrated phase conveying system, the electrolyte powder in warehouse is delivered to multifunctional electrolytic machine group feeding device in cell room, so, due to simple electrolyte powder illiquidity, easily cause and carry difficulty to increase, the more important thing is that simple electrolyte powder is relatively poor as the heat-insulating property of anode-covered material, cause the anode electrolytic cell heat radiation to strengthen, utilization rate of electrical reduces.
Summary of the invention
The object of the invention is to: provide that a kind of flow process is short, production efficiency is high, energy expenditure is low, electrolyte powder batching and the storage and transportation system device of reliable, convenient operation and management, poor to overcome the heat-insulating property that prior art exists, cause the anode electrolytic cell heat radiation to strengthen, the deficiencies such as utilization rate of electrical reduction.
The present invention adopts following technical scheme: bilayer electrolyte powder warehouse is set between two cell rooms, and bilayer electrolyte powder warehouse is divided into fresh aluminum oxide storehouse and ionogen storehouse by the charging type, its at the middle and upper levels the storehouse be the fresh aluminum oxide storehouse, the lower floor storehouse is the ionogen storehouse; Establish the feed proportioning system that 1 cover is comprised of dosing worm conveyor and ebullated bed between upper and lower layer of storehouse.When ionogen enters ebullated bed by handling equipment, fresh aluminum oxide in the storehouse, upper strata enters ebullated bed by the pressure feeding spiral transfer roller simultaneously, both mix in ebullated bed and send into lower floor's warehousing and store up, the feeding device that mixed electrolyte powder is delivered in cell room by air-driven chute or rubber conveyer adds multi-functional unit hopper, as the anode electrolytic cell mulch.Whole technological process can realize continuously, automatic, closed-loop operation.
Compared with prior art, the present invention is conducive to improve mass transport efficient efficient, is easy to high-efficient purification and gathers dust, and also has advantages of simultaneously the anode-covered material of raising heat-insulating property, reduces the electrolysis production energy consumption.
Description of drawings
Fig. 1 is schematic diagram of the present invention.
Embodiment
Enforcement of the present invention: as shown in Figure 1, bilayer electrolyte powder warehouse is set between two cell rooms, between the fresh aluminum oxide storehouse 1 of bilayer electrolyte powder warehouse, ionogen storehouse 4, dosing worm conveyor 2 and ebullated bed 3 are set, dosing worm conveyor 2 and ebullated bed 3 form feed proportioning system, under ionogen storehouse 4, handling equipment 5 is set, handling equipment 5 is connected with feeding device 6.
In the present invention, bilayer electrolyte powder warehouse is arranged between two cell rooms, its at the middle and upper levels the storehouse be fresh aluminum oxide storehouse 1, fresh aluminum oxide delivers into upper strata warehousing storage by concentrated phase; Establish the feed proportioning system that 1 cover is comprised of dosing worm conveyor 2 and ebullated bed 3 between upper and lower layer of storehouse; The lower floor storehouse is electrolyte powder storehouse 4, and electrolyte powder is sent into ebullated bed 3 by chapelet, and the fresh aluminum oxide in the storehouse, upper strata quantitatively enters ebullated bed 3 by dosing worm conveyor 2 simultaneously, both mixes in ebullated bed and sends into lower floor's warehousing and store up.Mixed electrolyte powder is delivered to multifunctional electrolytic machine group feeding device by air-driven chute or rubber conveyer, adds multi-functional unit hopper, as the anode electrolytic cell mulch.
Claims (3)
1. an electrolyte powder is prepared burden and the storage and transportation system device, it is characterized in that: bilayer electrolyte powder warehouse is set between two cell rooms, between the fresh aluminum oxide storehouse (1) of bilayer electrolyte powder warehouse, ionogen storehouse (4), dosing worm conveyor (2) and ebullated bed (3) are set, dosing worm conveyor (2) and ebullated bed (3) form feed proportioning system, handling equipment (5) is set under ionogen storehouse (4), and handling equipment (5) is connected with feeding device (6).
2. electrolyte powder according to claim 1 is prepared burden and the storage and transportation system device, and it is characterized in that: handling equipment (5) is air-driven chute or rubber conveyer.
3. electrolyte powder according to claim 1 is prepared burden and the storage and transportation system device, and it is characterized in that: feeding device (6) is device of overhead traveling crane material feeding.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110378369.2A CN103132105B (en) | 2011-11-24 | 2011-11-24 | Electrolyte powder batching and storage and transportation system device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110378369.2A CN103132105B (en) | 2011-11-24 | 2011-11-24 | Electrolyte powder batching and storage and transportation system device |
Publications (2)
| Publication Number | Publication Date |
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| CN103132105A true CN103132105A (en) | 2013-06-05 |
| CN103132105B CN103132105B (en) | 2016-05-11 |
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| CN201110378369.2A Active CN103132105B (en) | 2011-11-24 | 2011-11-24 | Electrolyte powder batching and storage and transportation system device |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105401171A (en) * | 2015-12-30 | 2016-03-16 | 贵阳铝镁设计研究院有限公司 | Continuous aluminum oxide blanking method and device |
| CN106809549A (en) * | 2017-03-23 | 2017-06-09 | 中国有色（沈阳）冶金机械有限公司 | A kind of fluoride salt charging vehicle |
| CN106882108A (en) * | 2017-03-23 | 2017-06-23 | 中国有色（沈阳）冶金机械有限公司 | A kind of fluoride salt charging vehicle with Digiplex operation |
| CN106894050A (en) * | 2015-12-18 | 2017-06-27 | 沈阳铝镁设计研究院有限公司 | Heat preservation ventilating type cell room structure |
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| US3681229A (en) * | 1970-07-17 | 1972-08-01 | Aluminum Co Of America | Alumina feeder |
| GB1478924A (en) * | 1974-04-04 | 1977-07-06 | Mikropul Mahl & Staubtech Gmbh | Appararatus for the controlled rate discharge of a granular mixture from a hopper or bin |
| US4299683A (en) * | 1980-07-17 | 1981-11-10 | Aluminum Company Of America | Apparatus and method for efficient transfer of powdered ore |
| US4930691A (en) * | 1987-10-09 | 1990-06-05 | Norsk Hydro A.S. | Pneumatic dosimeter |
| WO2003006717A1 (en) * | 2001-07-11 | 2003-01-23 | Moltech Invent S.A. | Electrolytic cell with improved powder feed device |
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| CN201661094U (en) * | 2010-05-04 | 2010-12-01 | 贵阳铝镁设计研究院 | Storage warehouse convenient for alumina storage and material supplying and dispensing |
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| CN202401143U (en) * | 2011-11-24 | 2012-08-29 | 贵阳铝镁设计研究院有限公司 | Electrolyte powder preparing, storing and conveying system device |
-
2011
- 2011-11-24 CN CN201110378369.2A patent/CN103132105B/en active Active
Patent Citations (10)
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| US3681229A (en) * | 1970-07-17 | 1972-08-01 | Aluminum Co Of America | Alumina feeder |
| GB1478924A (en) * | 1974-04-04 | 1977-07-06 | Mikropul Mahl & Staubtech Gmbh | Appararatus for the controlled rate discharge of a granular mixture from a hopper or bin |
| US4299683A (en) * | 1980-07-17 | 1981-11-10 | Aluminum Company Of America | Apparatus and method for efficient transfer of powdered ore |
| US4930691A (en) * | 1987-10-09 | 1990-06-05 | Norsk Hydro A.S. | Pneumatic dosimeter |
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| US20040247400A1 (en) * | 2001-10-26 | 2004-12-09 | Christian Cloue | System for distribution of pulverulent material with controlled gravimetric flow rates |
| CN101054694A (en) * | 2007-02-17 | 2007-10-17 | 贵阳铝镁设计研究院 | Charging method and device for purifying two stages by electrolyzing flue gas using aluminum |
| CN201661094U (en) * | 2010-05-04 | 2010-12-01 | 贵阳铝镁设计研究院 | Storage warehouse convenient for alumina storage and material supplying and dispensing |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106894050A (en) * | 2015-12-18 | 2017-06-27 | 沈阳铝镁设计研究院有限公司 | Heat preservation ventilating type cell room structure |
| CN105401171A (en) * | 2015-12-30 | 2016-03-16 | 贵阳铝镁设计研究院有限公司 | Continuous aluminum oxide blanking method and device |
| CN106809549A (en) * | 2017-03-23 | 2017-06-09 | 中国有色（沈阳）冶金机械有限公司 | A kind of fluoride salt charging vehicle |
| CN106882108A (en) * | 2017-03-23 | 2017-06-23 | 中国有色（沈阳）冶金机械有限公司 | A kind of fluoride salt charging vehicle with Digiplex operation |
| CN106882108B (en) * | 2017-03-23 | 2020-01-07 | 中国有色（沈阳）冶金机械有限公司 | Fluoride salt charging vehicle with wireless remote controller operation |
| CN106809549B (en) * | 2017-03-23 | 2020-01-07 | 中国有色（沈阳）冶金机械有限公司 | Fluoride salt charging vehicle |
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| CN103132105B (en) | 2016-05-11 |
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