CN201962386U - Real-time discharge monitoring system for aluminium electrolytic tank - Google Patents

Real-time discharge monitoring system for aluminium electrolytic tank Download PDF

Info

Publication number
CN201962386U
CN201962386U CN2010206944733U CN201020694473U CN201962386U CN 201962386 U CN201962386 U CN 201962386U CN 2010206944733 U CN2010206944733 U CN 2010206944733U CN 201020694473 U CN201020694473 U CN 201020694473U CN 201962386 U CN201962386 U CN 201962386U
Authority
CN
China
Prior art keywords
real
monitoring system
aluminum oxide
fluorinated alumina
rolling gauge
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
CN2010206944733U
Other languages
Chinese (zh)
Inventor
袁立峰
周淦
刘军
陈伟
张冬梅
彭琳
鞠晓亮
麻劲禹
仲世成
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.)
XIBU MINING SCIENCE AND TECHNOLOGY Co Ltd QINGHAI
Western Mining Co Ltd
Original Assignee
XIBU MINING SCIENCE AND TECHNOLOGY Co Ltd QINGHAI
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 XIBU MINING SCIENCE AND TECHNOLOGY Co Ltd QINGHAI filed Critical XIBU MINING SCIENCE AND TECHNOLOGY Co Ltd QINGHAI
Priority to CN2010206944733U priority Critical patent/CN201962386U/en
Application granted granted Critical
Publication of CN201962386U publication Critical patent/CN201962386U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Electrolytic Production Of Metals (AREA)

Abstract

The utility model relates to a real-time discharge monitoring system for an aluminium electrolytic tank, belonging to the control technology in the aluminium electrolysis industry. A fresh alumina flow rolling measuring instrument of the real-time discharge monitoring system is arranged on an alumina material conveying pipe between a fresh alumina bin and a main chute of a dust collector, and a first fluorinated alumina rolling measuring instrument and a second fluorinated alumina rolling measuring instrument are arranged on the material conveying pipe of a fluorine loading bin between a fluorine loading bin and a flue. The real-time discharge monitoring system for the aluminium electrolytic tank has the advantages that: (1), the construction difficulty is greatly reduced, on the contrary, the signal stability is improved, and the design and construction costs are reduced; (2), the real-time pressure and blowback monitoring is realized, and a host computer system is ensured to monitor the differential pressure and other status data of the dust collector; (3), the discharging amount and all parameters of the whole conveying system can be monitored and adjusted in real time. The real-time discharge monitoring system can be used for the discharge monitoring in the aluminium electrolysis industry.

Description

A kind of aluminum cell supplying real-time monitoring system
Technical field
The utility model relates to a kind of electrolysis of aluminum industry control techniques, specifically relates to a kind of aluminum cell supplying real-time monitoring system.
Background technology
The thing level detecting apparatus that the alumina blanking of electrolysis of aluminum industry adopts aluminium cell hopper top to install is a level switch, be blocking rotary type level switch or tuning-fork type level switch, these two kinds of switches can only simply be judged the ceiling value of material level, can't be according to the accurate controlled oxidation aluminium of material amount addition in the hopper.In the actual production, as long as the high charge level blackout of electrolytic bath feed box, no matter how many interior material actual consumption amounts of hopper is, feeder system is just pressed a certain amount of be charging of the cell and batching, it is reinforced discontented or add the inaccurate of overflow and batching hopper often to occur, cause the waste of aluminum oxide and aluminum fluoride, the molecular ratio in the electrolyzer can not in time be adjusted, and the qualification rate of molecular ratio is very low.Have a strong impact on the maintenance of the ordinary production and the technical qualification of electrolyzer, increased production cost again.The enterprise that also has uses bucket to claim to occupy very big solid space, and is in high empty position and is unfavorable for safeguarding.Of paramount importance is that it can't stablize materials flow, can not throw in fresh aluminum oxide and fluorinated alumina uniformly, all unfavorable to defluorination and electrolysis.
Summary of the invention
The purpose of this utility model is the deficiency that exists at prior art, and a kind of aluminum cell supplying real-time monitoring system is provided.
A kind of aluminum cell supplying real-time monitoring system of the utility model is achieved by following technical proposals: a kind of aluminum cell supplying real-time monitoring system of the utility model comprises fresh aluminum oxide flow rolling gauge, the first fluorinated alumina rolling gauge, the second fluorinated alumina rolling gauge, carry the fluorine storehouse, the fresh aluminum oxide storehouse, the aluminum oxide carrier pipe, the fluorinated alumina carrier pipe, carry fluorine storehouse carrier pipe, fly-ash separator master chute, flue, described fresh aluminum oxide flow rolling gauge is arranged on the aluminum oxide carrier pipe between fresh aluminum oxide storehouse and the fly-ash separator master chute, and the described first fluorinated alumina rolling gauge and the second fluorinated alumina rolling gauge are arranged on carries carrying on the carrier pipe of fluorine storehouse between fluorine storehouse and the flue.
A kind of aluminum cell supplying real-time monitoring system of the utility model has following beneficial effect compared with prior art: because the utility model has adopted the rolling gauge that aluminum oxide and fluorinated alumina blanking are carried out real time measure, make the materials flow of blanking amount stable, the Measuring Precision height, and rolling gauge volume is little, convenient for installation and maintenance, control flexibly, as long as after setting flow on computers, rolling gauge basis is adjusted after comparing when having the blanking amount now and presetting blanking automatically, whole process need not artificial participation, and the flow control error is in 5 ‰; The material setting range can be from 0 ton/hour~30 tons/hour.The advantage of a kind of aluminum cell supplying real-time monitoring system of the utility model: 1) greatly reduce difficulty of construction, on the contrary, improved signal stability, reduced design and construction cost; 2) realize that pressure and blowback detect in real time, guarantee that master system can monitor status datas such as fly-ash separator pressure reduction; 3) can monitor and adjust blanking amount and whole delivery system parameters in real time.The utility model can be applicable to the blanking prosecution of electrolysis of aluminum industry.
Description of drawings
Fig. 1 is a kind of aluminum cell supplying real-time monitoring system of the utility model structural representation.
Wherein: 1, fresh aluminum oxide flow rolling gauge; 2, the first fluorinated alumina rolling gauge; 3, the second fluorinated alumina rolling gauge; 4, carry the fluorine storehouse; 5, fresh aluminum oxide storehouse; 6, aluminum oxide carrier pipe; 7, fluorinated alumina carrier pipe; 8, carry fluorine storehouse carrier pipe; 9, fly-ash separator master chute; 10, flue.
Embodiment
Below in conjunction with drawings and Examples a kind of aluminum cell supplying real-time monitoring system of the utility model technical scheme is further described.
As shown in Figure 1, a kind of aluminum cell supplying real-time monitoring system of the utility model comprises fresh aluminum oxide flow rolling gauge 1, the first fluorinated alumina rolling gauge 2, the second fluorinated alumina rolling gauge 3, carry fluorine storehouse 4, fresh aluminum oxide storehouse 5, aluminum oxide carrier pipe 6, fluorinated alumina carrier pipe 7, carry fluorine storehouse carrier pipe 8, fly-ash separator master chute 9, flue 10, described fresh aluminum oxide flow rolling gauge 1 is arranged on the aluminum oxide carrier pipe 6 between fresh aluminum oxide storehouse 5 and the fly-ash separator master chute 9, and the described first fluorinated alumina rolling gauge 2 and the second fluorinated alumina rolling gauge 3 are arranged on carries carrying on the fluorine storehouse carrier pipe 8 between fluorine storehouse 4 and the flue 10.
Described fresh aluminum oxide flow rolling gauge 1, the first fluorinated alumina rolling gauge 3 are connected with the slot control machine upper computer by lead with the second fluorinated alumina rolling gauge 3.
Embodiment 1.
As shown in Figure 1, a kind of aluminum cell supplying real-time monitoring system of the utility model comprises fresh aluminum oxide flow rolling gauge 1, the first fluorinated alumina rolling gauge 2, the second fluorinated alumina rolling gauge 3, carry fluorine storehouse 4, fresh aluminum oxide storehouse 5, aluminum oxide carrier pipe 6, fluorinated alumina carrier pipe 7, carry fluorine storehouse carrier pipe 8, fly-ash separator master chute 9, flue 10, described fresh aluminum oxide flow rolling gauge 1 is arranged on the aluminum oxide carrier pipe 6 between fresh aluminum oxide storehouse 5 and the fly-ash separator master chute 9, and the described first fluorinated alumina rolling gauge 2 and the second fluorinated alumina rolling gauge 3 are arranged on carries carrying on the fluorine storehouse carrier pipe 8 between fluorine storehouse 4 and the flue 10.
Described fresh aluminum oxide flow rolling gauge 1, the first fluorinated alumina rolling gauge 3 are connected with the slot control machine upper computer by lead with the second fluorinated alumina rolling gauge 3.
Among the figure 1,2,3 is the rolling gauge, and 1 is control fresh aluminum oxide flow, and 2,3 is to control the fluorinated alumina flow, uses as secondary circulation.Wherein be connected with fresh storehouse blanking material pipe 6 on 1, be connected with fly-ash separator master chute 9 down, 2,3 as control fluorinated alumina flow usefulness, go up with a year fluorine storehouse carrier pipe 8 to be connected, under be connected with flue 10.

Claims (2)

1. aluminum cell supplying real-time monitoring system, comprise fresh aluminum oxide flow rolling gauge (1), the first fluorinated alumina rolling gauge (2), the second fluorinated alumina rolling gauge (3), carry fluorine storehouse (4), fresh aluminum oxide storehouse (5), aluminum oxide carrier pipe (6), fluorinated alumina carrier pipe (7), carry fluorine storehouse carrier pipe (8), fly-ash separator master chute (9), flue (10), it is characterized in that: described fresh aluminum oxide flow rolling gauge (1) is arranged on the aluminum oxide carrier pipe (6) between fresh aluminum oxide storehouse (5) and the fly-ash separator master chute (9), and the described first fluorinated alumina rolling gauge (2) and the second fluorinated alumina rolling gauge (3) are arranged on year fluorine storehouse carrier pipe (8) that carries between fluorine storehouse (4) and the flue (10).
2. aluminum cell supplying real-time monitoring system as claimed in claim 1 is characterized in that: described fresh aluminum oxide flow rolling gauge (1), the first fluorinated alumina rolling gauge (3) and the second fluorinated alumina rolling gauge (3) are connected with the slot control machine upper computer by lead.
CN2010206944733U 2010-12-31 2010-12-31 Real-time discharge monitoring system for aluminium electrolytic tank Expired - Fee Related CN201962386U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010206944733U CN201962386U (en) 2010-12-31 2010-12-31 Real-time discharge monitoring system for aluminium electrolytic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010206944733U CN201962386U (en) 2010-12-31 2010-12-31 Real-time discharge monitoring system for aluminium electrolytic tank

Publications (1)

Publication Number Publication Date
CN201962386U true CN201962386U (en) 2011-09-07

Family

ID=44524923

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010206944733U Expired - Fee Related CN201962386U (en) 2010-12-31 2010-12-31 Real-time discharge monitoring system for aluminium electrolytic tank

Country Status (1)

Country Link
CN (1) CN201962386U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104195597A (en) * 2014-09-16 2014-12-10 湖南创元铝业有限公司 Feeding control method for aluminum oxide
CN106011941A (en) * 2016-08-02 2016-10-12 重庆大学 Control method for aluminum electrolysis crown block stock bin material level online monitoring and fault alarm system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104195597A (en) * 2014-09-16 2014-12-10 湖南创元铝业有限公司 Feeding control method for aluminum oxide
CN104195597B (en) * 2014-09-16 2016-08-17 湖南创元铝业有限公司 Aluminum oxide feeds intake control method
CN106011941A (en) * 2016-08-02 2016-10-12 重庆大学 Control method for aluminum electrolysis crown block stock bin material level online monitoring and fault alarm system

Similar Documents

Publication Publication Date Title
CN104907158B (en) Intelligent separation of coarse slime machine
CN201955663U (en) Intelligent control system for raw material conveying equipment
CN108034967B (en) Rare earth electrolytic cell discharging device and rare earth electrolytic cell
CN201962386U (en) Real-time discharge monitoring system for aluminium electrolytic tank
CN105752692A (en) Pneumatic conveying and feeding system of reaction kettle
CN105775782A (en) Feeding device for rotary chute of stock bin
CN103752378A (en) Full-automatic ball feeding system
CN202670499U (en) Powdery material buffer flow-stabilizing shaping device
CN103009494A (en) Method and device for feeding airspace packet material of mixing system in rubber industry
CN213067864U (en) Multi-component metering bin for pneumatic transmission of lithium battery
CN205087209U (en) Automatic proportioning device of (dirt) mud soil solidifying agent is used for becoming silted up
CN212334988U (en) Continuous accurate feeding system of TFT liquid crystal glazing kiln
CN207209417U (en) One kind lock wind device for discharging
CN203783634U (en) Mineral powder recycling structure for underground mine
CN113158410B (en) Dynamic setting method for electric dust removal ash conveying cycle period
CN203544994U (en) Biomass block-shaped fuel conveying system
RU2407826C1 (en) System of automatic supply of raw material to aluminium electrolyser
CN211365740U (en) Mechanical material level measuring device for granules and powder
CN203695244U (en) Novel coal ash sorting device
CN204489668U (en) A kind of coal blending is weighed hopper
CN209082011U (en) A kind of broken material Lifting Convey charging device
CN203497466U (en) Dead material position cleaner for bunker
CN103121594A (en) Spiral cushion material blanking device
CN221439713U (en) Quantitative adding device for powder additive of powder bin system
CN211593856U (en) Discharging chute

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20110907

Termination date: 20151231

EXPY Termination of patent right or utility model