CN2835262Y - Cathode busbar arrangement of 350KA aluminum electrolytic cell - Google Patents

Cathode busbar arrangement of 350KA aluminum electrolytic cell Download PDF

Info

Publication number
CN2835262Y
CN2835262Y CN 200520200554 CN200520200554U CN2835262Y CN 2835262 Y CN2835262 Y CN 2835262Y CN 200520200554 CN200520200554 CN 200520200554 CN 200520200554 U CN200520200554 U CN 200520200554U CN 2835262 Y CN2835262 Y CN 2835262Y
Authority
CN
China
Prior art keywords
bus
bus bars
electrolytic cell
cell
cathode
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
CN 200520200554
Other languages
Chinese (zh)
Inventor
颜非亚
韩笑天
郭海龙
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.)
Guiyang Aluminum Magnesium Design and Research Institute Co Ltd
Original Assignee
Guiyang Aluminum Magnesium Design and Research Institute Co Ltd
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 Guiyang Aluminum Magnesium Design and Research Institute Co Ltd filed Critical Guiyang Aluminum Magnesium Design and Research Institute Co Ltd
Priority to CN 200520200554 priority Critical patent/CN2835262Y/en
Application granted granted Critical
Publication of CN2835262Y publication Critical patent/CN2835262Y/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 discloses a cathode bus bar structure of 350KA aluminum electrolytic cells, which adopts the mode of large-area six-point power input. The power input side is provided with six upright column bus bars, and the bus bars at the power input side and bus bars at the power output side are symmetrically arranged by adopting multilayer bus bars. Cell side bus bars at both ends of an electrolytic cell adopt stepped type arrangement, and compensating bus bars at the bottom of the electrolytic cell are arranged by adopting the mode of penetrating the cell bottom under beams AB of the cell. Cathode bus bars and cathode steel rods are connected by adopting cathode steel rod compression joint devices, and other bus bars are in regular arrangement and connection. The utility model successfully solve the problems of the uniformity and the stability of the magnetic environment of fused masses in an oversize aluminum electrolytic cell, therefore the magnetic field gradient in the cell can be much smaller and the utility model creates conditions for the electrolytic cell to increase production efficiency and operate stably.

Description

350KA aluminium electrolytic cell cathode bus structure
Technical field:
The utility model relates to a kind of negative busbar configuration structure that is used for super-huge prebaked cell.
Technical background:
Along with improving constantly of aluminium cell designing technique and process operation level, the working current of modern large-scale aluminum electrolytic cell increases just day by day, and the magnetic field that its current carrying bus and melt electric current produce more shows outstanding to the production of electrolyzer and the influence of steady running.Because the electromagnetic force that magnetic field and melt Interaction Law of Electric Current produce makes in the groove melt circulation quicken, and causes liquid aluminum generation protuberance, deflection and fluctuation, in addition may influence electrolyzer can not ordinary production.Therefore, when dynamical large scale electrolytic cell of design, must consider to weaken and the control flume internal magnetic field, its magnetic-field component value is dropped in the numerical range of qualification by rational busbar arrangement.Thereby obtain stable, production effect efficiently.
The utility model content:
The purpose of this utility model is: the novel bus configuration structure that a kind of 350KA of being applicable to electrolyzer is provided, make it under the big strength of current of 350KA, the magnetic field of melt is distributed rationally, is stablized in the electrolyzer, the electric current distributed uniform, guaranteeing stable, the ordinary production of electrolyzer, and for improving current efficiency, reducing power consumption and create conditions.
The utility model is to constitute like this: it comprises riser bus bar (1), adopt 6 in big face to advance the mode of electricity, electricity input side has 6 root post buses (1), electricity input side bus (2) adopts the balanced configuration of multilayer bus with electricity output side bus (5), the groove side bus (3) at electrolyzer two ends adopts the staged configuration, compensation bus (4) at the bottom of the electrolytic bath adopts and is lower than groove AB beam and wears the mode of bottom land and dispose, adopt cathode steel bar connector presser (7) to connect between negative busbar (6) and the cathode steel bar (8), other be routine layout be connected.
In above-described formation, the current ratio distribution means of 6 root post buses (1) of electricity input side for equating, electricity output side bus (5) adopts the frame mode around negative busbar.
The configuration structure characteristics of this bus are: advance a side bus (2) and adopt balanced configuration with electricity output side bus (5), guaranteed the homogeneity of groove internal magnetic field, and in electricity output side bus (5), the electricity output side cathodic current is divided into 6 groups, all adopt mode, with the distribution of current of balance AB side around negative busbar.At the influence of big galvanic series adjacent row slot, groove side bus (3) is taked the staged configuration, offsets the reverse influence of electrolyzer AB side vertical magnetic field simultaneously.Bottom land compensation bus (4) adopts and is lower than the collocation form of wearing bottom land of electrolyzer AB beam, thereby greatly reduces electrolyzer vertical magnetic field gradient in the horizontal direction.Riser bus bar (1) adopts 6 geometric ratios of big face to advance the frame mode of electricity.Consider the welding difficulty of electrolytic cell overhaul, adopt cathode steel bar connector presser (7) to connect between cathode soft bus (6) and the cathode steel bar (8).
During work, galvanic current enters the 6 root post buses (1) of this groove from the upstream electrolyzer, electric current enters on the anode large bus bar of groove superstructure by riser bus bar, be redistributed to and respectively organize anode, flow through melt dielectric substrate, aluminium liquid layer in the groove, and behind the cathode carbon pieces, cathode steel bar, by being connected in the cathode steel bar connector presser (7) between cathode steel bar (8) and the cathode soft bus (6), the cathode soft bus of A side imports electricity input side bus (2) with electric current, the B side then import to electricity output side bus (5).The electric current of electricity input side bus (2) enters on the 6 root post buses of downstream slot by groove side bus (3) and 6 bottom land compensation buses (4) at electrolyzer both ends respectively, and the electric current of electricity output side bus (5) then directly imports the riser bus bar of downstream slot.Wherein the electric current of electricity input side about 60% enters downstream slot by the groove side bus (3) at two ends, and about 40% electric current enters downstream slot by the compensation bus (4) of bottom land.
The beneficial effects of the utility model are: it has successfully solved the homogeneity of melt magnetic environment in the super-huge aluminium electrolysis cell, the problem of stationarity, thereby make that groove internal magnetic field gradient is littler, for electrolyzer is enhanced productivity, steady running is laid a good foundation.
Description of drawings:
Fig. 1 is a structural representation of the present utility model;
Fig. 2 be among Fig. 1 A to B to view combination.
Embodiment:
Embodiment of the present utility model: the electricity input side at electrolyzer adopts 6 in big face to advance the mode of electricity, electricity input side is provided with 6 root post buses (1), its 6 root post bus (1) is equal current ratio distribution means, electricity input side bus (2) adopts the balanced configuration of multilayer bus with electricity output side bus (5), and electricity output side bus (5) adopts the frame mode around negative busbar; As shown in Figure 1, the left end of electrolyzer is a flue end, and right-hand member is an aluminium inlet, is equipped with groove side bus (3) at its two ends, and groove side bus (3) adopts the staged configuration; Compensation bus (4) at the bottom of the electrolytic bath has 6 groups, all adopts to be lower than groove AB beam and to wear the mode of bottom land and dispose; Adopt cathode steel bar connector presser (7) to connect between negative busbar (6) and the cathode steel bar (8), other be routine layout be connected.

Claims (3)

1.350KA aluminium electrolytic cell cathode bus structure, it comprises riser bus bar (1), it is characterized in that: adopt 6 in big face to advance the mode of electricity, electricity input side has 6 root post buses (1), electricity input side bus (2) adopts the balanced configuration of multilayer bus with electricity output side bus (5), the groove side bus (3) at electrolyzer two ends adopts the staged configuration, compensation bus (4) at the bottom of the electrolytic bath adopts and is lower than groove AB beam and wears the mode of bottom land and dispose, adopt cathode steel bar connector presser (7) to connect between negative busbar (6) and the cathode steel bar (8), other be routine layout be connected.
2. 350KA aluminium electrolytic cell cathode bus structure according to claim 1 is characterized in that: the current ratio distribution means of 6 root post buses (1) of electricity input side for equating.
3. 350KA aluminium electrolytic cell cathode bus structure according to claim 1 is characterized in that: electricity output side bus (5) adopts the frame mode around negative busbar.
CN 200520200554 2005-08-04 2005-08-04 Cathode busbar arrangement of 350KA aluminum electrolytic cell Expired - Fee Related CN2835262Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200520200554 CN2835262Y (en) 2005-08-04 2005-08-04 Cathode busbar arrangement of 350KA aluminum electrolytic cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200520200554 CN2835262Y (en) 2005-08-04 2005-08-04 Cathode busbar arrangement of 350KA aluminum electrolytic cell

Publications (1)

Publication Number Publication Date
CN2835262Y true CN2835262Y (en) 2006-11-08

Family

ID=37299920

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200520200554 Expired - Fee Related CN2835262Y (en) 2005-08-04 2005-08-04 Cathode busbar arrangement of 350KA aluminum electrolytic cell

Country Status (1)

Country Link
CN (1) CN2835262Y (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104674303A (en) * 2013-12-02 2015-06-03 贵阳铝镁设计研究院有限公司 Testing potroom busbar configuration structure

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104674303A (en) * 2013-12-02 2015-06-03 贵阳铝镁设计研究院有限公司 Testing potroom busbar configuration structure

Similar Documents

Publication Publication Date Title
CN101248218A (en) Module busbar arrangement for powerful aluminum electrolytic cells
CN100424230C (en) Bus allocation method of 350 KA aluminium electrolytic tank
CN2835262Y (en) Cathode busbar arrangement of 350KA aluminum electrolytic cell
CN102534682B (en) Bus configuration method for aluminum electrolysis cell with equidistant current paths
CN200996054Y (en) Cathodic bus arrangement structure for superlarge aluminum electrolyzer
CN101857960A (en) Method for configuring bus bar of aluminum electrolytic bath
CN101838826A (en) Configuration method and configuration system of busbars on periphery of aluminum electrolysis cell with vertical electricity outlet
CN101760760A (en) Bottom-discharging aluminum cell
CN101629306B (en) Non-symmetrical six-point electric input busbar configuration structure for large-scale aluminum electrolytic cell
CN101423959A (en) Bus-bar collocation structure of aluminum cell
CN101748443B (en) Method and structure for collocating aluminum electrolysis cell cathode bus bar in charging mode at two points on terminals
CN1793432B (en) Process for distributing cathode mother wire of aluminium electrolytic tank
CN201367473Y (en) Aluminum electrolysis bath cathode structure
CN201545919U (en) Aluminum electrolytic tank cathode structure
CN2856068Y (en) Cathode bus configuration structure of longitudinal arranged electrolyzer
CN201729892U (en) Configuration system of peripheral buses of vertical electricity-generating aluminum electrolytic cell
CN202643861U (en) Five-point power-on busbar configuration structure of aluminum electrolytic cell
CN100564605C (en) Encircling type busbar arrangement method for vertical row cell
CN214572277U (en) Aluminum electrolysis cell bus structure with bottom power output
CN2804128Y (en) Structure of preventing magnetic field interfrence between vertical disposition tanks of aluminum electrolyzer
CN201834987U (en) Cathode power outlet device of aluminium electrolysis cell
CN209082009U (en) A kind of cathode construction quickly isolating aluminium cell range of instability
CN203270052U (en) Horizontal power inlet aluminium cell electrode
CN221588716U (en) Busbar configuration structure for asymmetric electricity output of electricity inlet and outlet sides of aluminum electrolysis cell
CN202181357U (en) Electrolytic tank capable of greatly reducing horizontal current

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C56 Change in the name or address of the patentee

Owner name: GUIYANG ALUMINUM AND MAGNESIUM DESIGN INSTITUTE CO

Free format text: FORMER NAME: GUIYANG ALUMINIUM AND MAGNESIUM DESIGN INST.

CP03 Change of name, title or address

Address after: 550081 Guiyang Province, Jinyang New District, Zhu Zhu Road, No. 2

Patentee after: Guiyang Aluminum & Magnesium Design Institute Co., Ltd.

Address before: 550004 No. 208, Beijing Road, Guiyang, Guizhou

Patentee before: Guiyang Aluminium and Magnesium Design Inst.

CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20061108

Termination date: 20140804

EXPY Termination of patent right or utility model