CN103726073A - Anode carbon block group used for aluminium electrolysis cell - Google Patents
Anode carbon block group used for aluminium electrolysis cell Download PDFInfo
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- CN103726073A CN103726073A CN201210387260.XA CN201210387260A CN103726073A CN 103726073 A CN103726073 A CN 103726073A CN 201210387260 A CN201210387260 A CN 201210387260A CN 103726073 A CN103726073 A CN 103726073A
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- carbon block
- anode carbon
- block group
- rod iron
- iron
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Abstract
The invention relates to a carbon block group, and especially relates to an anode carbon block group used for an aluminium electrolysis cell The anode carbon block group comprises an aluminium guide rod and an anode carbon block; a steel beam is arranged between the aluminium guide rod and the anode carbon block; and conductive steel rods are arranged between the steel beam and the anode carbon block. Advantages of the anode carbon block group are that: the anode carbon block group is not provided with traditional phosphorus iron which is used for connecting a guide rod group with the anode carbon block, so that ion-carbon contact pressure of the anode carbon block group is reduced effectively. Changing of the structure of the anode carbon block group is capable of reducing the ion-carbon contact pressure of the electrolytic cell anode carbon block group, and is beneficial for reduction of voltage of the electrolytic cell, and alternating current consumption of electrolytic cell aluminium production is reduced.
Description
Technical field
The present invention relates to a kind of charcoal piece group, relate in particular to a kind of aluminum electrolyzing cell used anode carbon block group.
Background technology
Modern Aluminium Industry, the anode carbon block group of aluminium cell, as the positive pole of electrolyzer, participates in the normal reaction of electrolyzer.
Conventionally, anode electrolytic cell charcoal piece group is comprised of anode carbon block 5, aluminium guide bar 1, blast welding block 2, steel pawl 6 and the phosphorus pig iron 7, during anode carbon block group assembling, first aluminium guide bar, blast welding block and steel pawl are welded together to composition guide rod group, by guide rod group and anode carbon block group pair, the steel pawl of guide rod group is inserted in the charcoal bowl of anode carbon block again, the phosphorus pig iron of charcoal bowl place casting melting, after cooling, guide rod group and anode carbon block are linked together, composition anode carbon block group.
Conventionally the volts lost of aluminium cell production process Anodic charcoal piece group is about 350mv, comprises the contact drop of anode carbon block pressure drop, the pressure drop of aluminium guide bar group and the phosphorus pig iron, and the contact drop (iron-charcoal contact drop) of the phosphorus pig iron is greater than 100mv conventionally.
Summary of the invention
In order to solve the problems of the technologies described above, the invention provides one
aluminum electrolyzing cell used anode carbon block group, object isthe volts lost producing while reducing anode carbon block group by electric current.
For reaching above-mentioned purpose one of the present invention
aluminum electrolyzing cell used anode carbon block group, comprise aluminium guide bar and anode carbon block, between aluminium guide bar and anode carbon block, be provided with girder steel, between girder steel and anode carbon block, be provided with conduction rod iron.
Aluminium guide bar is connected by blast welding block with girder steel.
One end of conduction rod iron is vertically inserted in the hole of anode carbon block upper surface, the other end and girder steel welding.
Conduction rod iron is perpendicular to anode carbon block.
Conduction rod iron insert one end of anode carbon block with anode carbon block for being threaded or shrink-fit.
At least one of the quantity of conduction rod iron.
Conduction rod iron diameter D and quantity n are definite by the current density η by rod iron, and calculation formula is as follows:
N*D
2=4*I/(η
rod iron current density* π)
Wherein: I is the electric current that anode passes through
η
rod iron current densityspan is at 0.3 ~ 0.45A/mm
2.
Conduction rod iron inserts the depth H of anode carbon block to be determined by iron charcoal contact surface current density, and calculation formula is as follows:
H=I/(n*D* π * η
iron charcoal contact surface current density)
η
iron charcoal contact surface current densityspan is at 0.02 ~ 0.04A/mm
2.
Advantageous effect of the present invention: do not had traditional guide rod group to be connected the phosphorus pig iron of use with anode carbon block, effectively reduced iron-charcoal contact drop of anode carbon block group.Therefore, change the structure of anode carbon block group, reduce anode electrolytic cell charcoal piece group iron-charcoal contact drop, contribute to reduce the voltage of electrolyzer, thereby reduce the ac consumption of electrolyzer production aluminium.
Accompanying drawing explanation
Fig. 1 is existing
the structural representation of anode carbon block group.
fig. 2 is the side-view of Fig. 1.
fig. 3 is structural representation of the present invention.
fig. 4 is the side-view of Fig. 3.
figurein: 1, aluminium guide bar; 2, blast welding block; 3, girder steel; 4, conduction rod iron; 5, anode carbon block; 6, steel pawl; 7, the phosphorus pig iron.
Embodiment
Below in conjunction with accompanying drawing, the invention will be further described, but protection scope of the present invention is not limit by embodiment.
Embodiment 1
One of the present invention as shown in the figure
aluminum electrolyzing cell used anode carbon block group, comprise aluminium guide bar 1 and anode carbon block 5, between aluminium guide bar 1 and anode carbon block 5, be provided with girder steel 3, between girder steel 3 and anode carbon block 5, be provided with conduction rod iron 4, aluminium guide bar 1 is connected by blast welding block 4 with girder steel 3.
One end of conduction rod iron 4 is vertically inserted in the hole of anode carbon block 5 upper surfaces, and the other end and girder steel 3 weld.
One end that conduction rod iron 4 inserts anode carbon block 5 with anode carbon block 5 for being threaded.Take 200kA electrolyzer as example, 28 groups of anode carbon block group, every group of anode carbon block group comprises aluminium guide bar 1, blast welding block 2, girder steel 3, conduction rod iron 4 and anode carbon block 5, anode carbon block 5 is of a size of 1500x660x550mm, conduction rod iron 4 sectional dimensions are diameter 50mm, quantity is 24, boring on anode carbon block 5, be uniformly distributed, quantity is 24, the diameter in hole is identical with conduction rod iron 4 cross sections, after boring, carry out tapping, simultaneously, conduction rod iron 4 inserts anode carbon block 5 parts and is processed as screw rod, then, conduction rod iron 4 is screwed in anode carbon block 5, the other end of conduction rod iron 4 is welded on girder steel 3, welding successively blast welding block 2 and aluminium guide bar 1.
Conduction rod iron diameter D and quantity n are definite by the current density η by rod iron, and calculation formula is as follows:
N*D
2=4*I/(η
rod iron current density* π)
Wherein: I is the electric current that anode passes through
η
rod iron current densityspan is at 0.3 ~ 0.45A/mm
2;
Conduction rod iron inserts the depth H of anode carbon block to be determined by iron charcoal contact surface current density, and calculation formula is as follows:
H=I/(n*D* π * η
iron charcoal contact surface current density)
η
iron charcoal contact surface current densityspan is at 0.02 ~ 0.04A/mm
2.
One end and anode carbon block that conduction rod iron in embodiment 1 inserts anode carbon block are shrink-fit, and the other the same as in Example 1 is identical.
Claims (8)
1. one kind
aluminum electrolyzing cell used anode carbon block group, comprise aluminium guide bar and anode carbon block, it is characterized in that being provided with girder steel between aluminium guide bar and anode carbon block, between girder steel and anode carbon block, be provided with conduction rod iron.
2. one according to claim 1
aluminum electrolyzing cell used anode carbon block group, is characterized in thataluminium guide bar is connected by blast welding block with girder steel.
3. one according to claim 1
aluminum electrolyzing cell used anode carbon block group, is characterized in thatone end of conduction rod iron is vertically inserted in the hole of anode carbon block upper surface, the other end and girder steel welding.
4. one according to claim 3
aluminum electrolyzing cell used anode carbon block group, is characterized in thatconduction rod iron is perpendicular to anode carbon block.
5. one according to claim 4
aluminum electrolyzing cell used anode carbon block group, is characterized in thatconduction rod iron insert one end of anode carbon block with anode carbon block for being threaded or shrink-fit.
6. one according to claim 5
aluminum electrolyzing cell used anode carbon block group, is characterized in thatat least one of the quantity of conduction rod iron.
7. one according to claim 6
aluminum electrolyzing cell used anode carbon block group, is characterized in thatthe sectional dimension D of conduction rod iron and quantity n are definite by the current density of electric current by rod iron, and calculation formula is as follows: n*D
2=4*I/(η
rod iron current density* π), wherein: I is the electric current that anode passes through, η
rod iron current densityspan is at 0.3 ~ 0.45A/mm
2.
8. one according to claim 7
aluminum electrolyzing cell used anode carbon block group, is characterized in thatconduction rod iron inserts the depth H of anode carbon block to be determined by iron charcoal contact surface current density, and calculation formula is as follows: H=I/(n*D* π * η
iron charcoal contact surface current density), η
iron charcoal contact surface current densityspan is at 0.02 ~ 0.04A/mm
2.
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CN201210387260.XA CN103726073A (en) | 2012-10-15 | 2012-10-15 | Anode carbon block group used for aluminium electrolysis cell |
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CN201210387260.XA CN103726073A (en) | 2012-10-15 | 2012-10-15 | Anode carbon block group used for aluminium electrolysis cell |
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Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2816054Y (en) * | 2005-08-09 | 2006-09-13 | 沈阳铝镁设计研究院 | Anode guiding rod group |
CN101748436A (en) * | 2008-11-27 | 2010-06-23 | 沈阳铝镁设计研究院 | Prebaked anode aluminum electrolytic bath |
CN102330113A (en) * | 2011-07-16 | 2012-01-25 | 冯乃祥 | Aluminium electrolysis cell anode carbon block |
CN202226934U (en) * | 2011-08-30 | 2012-05-23 | 湖南创元新材料有限公司 | Positive pole steel claw and positive pole carbon block |
CN102534675A (en) * | 2010-12-21 | 2012-07-04 | 贵阳铝镁设计研究院有限公司 | Anode for electrolytic aluminum |
CN102560547A (en) * | 2010-12-09 | 2012-07-11 | 贵阳铝镁设计研究院有限公司 | Anode carbon block for electrolytic aluminum |
-
2012
- 2012-10-15 CN CN201210387260.XA patent/CN103726073A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2816054Y (en) * | 2005-08-09 | 2006-09-13 | 沈阳铝镁设计研究院 | Anode guiding rod group |
CN101748436A (en) * | 2008-11-27 | 2010-06-23 | 沈阳铝镁设计研究院 | Prebaked anode aluminum electrolytic bath |
CN102560547A (en) * | 2010-12-09 | 2012-07-11 | 贵阳铝镁设计研究院有限公司 | Anode carbon block for electrolytic aluminum |
CN102534675A (en) * | 2010-12-21 | 2012-07-04 | 贵阳铝镁设计研究院有限公司 | Anode for electrolytic aluminum |
CN102330113A (en) * | 2011-07-16 | 2012-01-25 | 冯乃祥 | Aluminium electrolysis cell anode carbon block |
CN202226934U (en) * | 2011-08-30 | 2012-05-23 | 湖南创元新材料有限公司 | Positive pole steel claw and positive pole carbon block |
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Application publication date: 20140416 |
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