WO2011079548A1 - Aluminum electrolytic cell having cathode structure with abrasion decelerated bulges on cathode - Google Patents

Aluminum electrolytic cell having cathode structure with abrasion decelerated bulges on cathode Download PDF

Info

Publication number
WO2011079548A1
WO2011079548A1 PCT/CN2010/070947 CN2010070947W WO2011079548A1 WO 2011079548 A1 WO2011079548 A1 WO 2011079548A1 CN 2010070947 W CN2010070947 W CN 2010070947W WO 2011079548 A1 WO2011079548 A1 WO 2011079548A1
Authority
WO
WIPO (PCT)
Prior art keywords
cathode
carbon block
cathode carbon
length
width
Prior art date
Application number
PCT/CN2010/070947
Other languages
French (fr)
Chinese (zh)
Inventor
冯乃祥
Original Assignee
Feng Naixiang
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 Feng Naixiang filed Critical Feng Naixiang
Publication of WO2011079548A1 publication Critical patent/WO2011079548A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C3/00Electrolytic production, recovery or refining of metals by electrolysis of melts
    • C25C3/06Electrolytic production, recovery or refining of metals by electrolysis of melts of aluminium
    • C25C3/08Cell construction, e.g. bottoms, walls, cathodes

Definitions

  • a cathode structure aluminum electrolytic cell capable of alleviating cathode bump abrasion
  • the invention belongs to the technical field of electrolytic aluminum, and particularly relates to a novel cathode structure aluminum electrolytic cell capable of alleviating the erosion of the cathode protrusion.
  • the metal aluminum produced in the industry is produced by molten salt electrolysis.
  • the special equipment is an electrolytic cell lined with carbonaceous material (or silicon nitride combined with silicon carbide brick), carbon lining and steel grooved shell. Between refractory materials and insulation materials.
  • the bottom of the cell is lined with a carbon block with a conductive steel rod mounted on its bottom. This block of carbon is called the cathode carbon block of the cell.
  • the cathode carbon block and the cathode carbon block are connected by a carbon paste, and a plurality of cathode carbon blocks and a crucible between them form a bottom carbon cathode of the electrolytic cell. 5 ⁇
  • the cell voltage of the industrial cell is between 4. 0 ⁇ 4.
  • the pole pitch is between 4. 0 ⁇ 5. 0cm.
  • the reason why the industrial aluminum electrolytic cell can greatly reduce the pole pitch to reduce the voltage of the electrolytic cell is due to the electromagnetic force in the current industrial aluminum electrolytic cell and the anode gas escaping from the anode surface and the electrolyte melt.
  • the liquid level of the cathode aluminum is greatly fluctuated. If the flow rate and amplitude of the fluctuation can be reduced, the pole distance and the cell voltage of the current electrolytic cell can be lowered, thereby achieving the purpose of greatly reducing the power consumption of the aluminum electrolytic production. .
  • CN200710010523. 4 proposes a new type of aluminum electrolytic cell with a cathode structure.
  • the electrolytic cell of the new cathode structure has indeed reduced the power consumption of aluminum electrolysis production after industrial application, but in practice, It has also been found that the height of the convex structure on the cathode surface of the electrolytic cell of the novel cathode structure is gradually reduced, and the consumption rate is about 2 to 4 cm/year. Generally, the consumption is mainly derived from sodium in the aluminum liquid. The erosion and destruction of the crystal lattice surface of the carbon cathode during chemical osmosis, and the subsequent flow of the cathode aluminum liquid on the surface of the carbon cathode cause the surface of the carbon cathode to fall off.
  • the present invention provides an aluminum electrolytic cell capable of slowing down the cathode abrasion, and solves the problem that the life of the cathode surface is low due to physical and chemical abrasion.
  • the aluminum electrolytic cell of the present invention has cathode carbon block protrusions, specifically: a convex structure is formed on the side of the cathode carbon block along the longitudinal direction, which is called a longitudinal direction protrusion; or is processed on the upper part of the cathode carbon block.
  • the protrusion perpendicular to the longitudinal direction of the cathode carbon block is referred to as a width direction protrusion; or the length direction protrusion and the width direction protrusion are simultaneously processed on the upper side of the cathode carbon block.
  • the material of the various cathode carbon block bumps is the same as that of the cathode carbon block, and is an integral structure.
  • the edge of the cathode carbon block immediately adjacent to the aluminum outlet of the electrolytic cell is not machined to the edge of the aluminum outlet.
  • the length of the protrusion in the longitudinal direction is 10 to 18 cm, and the width is 5 to 15 cm, which is located at the side of each cathode carbon block along the length direction, and the horizontal distance between the outer surface of the longitudinally convex portion and the edge of the cathode carbon block is l ⁇ 3cm, when laying the electrolytic cell, the middle slits of two adjacent cathode carbon blocks are sturdy and connected with carbon slag, the height of the tamping paste is equal to the height of the cathode carbon block, and then in two adjacent cathode carbon blocks.
  • the granules of the high-density magnesia bricks have a bulk density of 2. 6 ⁇ 3. 0g/cm
  • These refractory wall panels are placed in a direction parallel to the length direction of the cathode carbon block, and the width thereof is smaller than the width between the longitudinal projections of the adjacent two cathode carbon block edges by 1 to 3 mm.
  • the length is equal to the length of the longitudinal direction of the cathode carbon block, and the upper surface of the refractory wallboard is the same as the height of the convex upper surface of the cathode carbon block and higher than the upper surface of the cathode carbon block. ⁇ 5cm.
  • the refractory wall plate and the adjacent two cathode carbon block edges are longitudinally convex to form an integral length direction protrusion, and the overall length direction convex cross section is rectangular Or trapezoidal, or a composite shape of a rectangle and a trapezoid.
  • the number of protrusions in the overall length direction is 2 to 8.
  • the distance between the protrusions of each of the two overall length directions is 10 to 20 cm.
  • the distance between the protrusions of the two whole length directions except the lower side of the anode is 10 to 20 cm, and the distance between the protrusions of the other overall length direction is 5 to 20 cm. .
  • the width direction projection is located between the above two integral lengthwise projections.
  • the width direction protrusion is integrated with the cathode carbon block, and the distance between the width direction protrusion and the adjacent integral length direction protrusion is 5 to 10 cm on each cathode carbon block.
  • the edge of the cathode carbon block located at the end of the aluminum outlet is not provided with a widthwise projection.
  • the widthwise convex cross section is rectangular, or trapezoidal, or a combination of the two, and the widthwise projection has a width of 15 to 35 cm.
  • Each of the width direction protrusions is inlaid with a refractory wall panel along the width of the cathode carbon block, and the refractory wall panel is a nitrogen silicon carbide refractory board or a high density magnesia brick or a magnesium aluminum spinel board. 0 ⁇ 3. 0g/cm 3 ⁇ The high density of the mass density of 2. 6 ⁇ 3 . 0g / cm 3 .
  • the distance between each of the two widthwise projections is 20 to 40 cm on each cathode carbon block, and the height in the width direction is 10 to 18 cm, and the width is It is 18 ⁇ 30cm, and the length is consistent with the width of the cathode carbon block or less than the width of the cathode carbon block by 2 ⁇ 6cm.
  • Each of the width direction protrusions is inlaid with a refractory wall panel along the width of the cathode carbon block, and the refractory wall board is also a nitrogen silicon carbide refractory board or a high density magnesia brick or a magnesium aluminum spinel board, wherein the bulk density of the high density magnesia brick
  • the width of the refractory wallboard is 2. 5 ⁇ 3. 0g/cm.
  • the width of the refractory wallboard is 5 ⁇ 10cm, and the height is consistent with the height of the convexity in the width direction or higher than that of the width direction by l ⁇ 5cm.
  • the length is consistent, or less than the length of the width direction of the protrusion 4 ⁇ 10cm.
  • the carbon bricks are inlaid on both ends of the refractory wallboard to make the inlaid fireproof
  • the sum of the lengths of the material wall panels and the carbon bricks coincides with the length of the widthwise projections.
  • the cross section in the width direction is a rectangle or a trapezoid, or a composite shape of a rectangle and a trapezoid.
  • the invention has the advantages that the integral protrusion formed by the refractory wall plate and the cathode carbon block protrusion has the effects of slowing the flow rate of the aluminum liquid, reducing the fluctuation of the aluminum liquid, and improving the stability of the aluminum level of the electrolytic cell, and since the refractory wall plate is Made of materials such as anti-abrasion and anti-corrosion aluminum-magnesium spinel or silicon carbonitride, which have no effect on the aluminum electrolysis process and the quality of the aluminum, and the refractory wall-to-wall ratio after the cathode carbon block bumps are abraded.
  • the electrochemical erosion of carbon is small, and refractory wallboard can continue to slow down the flow rate of aluminum.
  • Figure 1 is a plan view of an electrolytic cell having a cathode bulge in the longitudinal direction;
  • FIG. 2 is a plan view of an electrolytic cell having a cathode carbon block having a width direction;
  • FIG. 3 is a plan view of an electrolytic cell in which a cathode carbon block has both a longitudinal direction and a width direction;
  • Figure 4 is a cross-sectional view of the A-A of Figure 1, the refractory wall panel is equal in height to the longitudinal direction;
  • Figure 5 is a schematic cross-sectional view of the A-A of Figure 1, the refractory wall panel is raised higher than the length direction;
  • Figure 6 is a schematic cross-sectional view taken along line B-B of Figure 1;
  • Figure 7 is a schematic cross-sectional view taken along line C-C of Figure 1;
  • Figure 8 is a schematic cross-sectional view of the D-D of Figure 2;
  • Figure 9 is a schematic view showing a longitudinal direction projection or a width direction projection having a trapezoidal cross section
  • Fig. 10 is a schematic view showing a longitudinal direction projection or a width direction projection having a rectangular cross section and a trapezoidal combination shape
  • Fig. 11 is a schematic view showing a longitudinal direction projection or a width direction projection having a rectangular cross section.
  • the novel cathode structure aluminum electrolysis cell of the present invention capable of alleviating the cathode protrusion abrasion is further illustrated by the following examples.
  • the aluminum electrolytic cell which can slow down the cathode abrasion has a side steel shell 9 and a bottom steel shell 13 on the outside, and a groove wall heat insulating material 8 which is in close contact with the side steel shell 9, and the inside of the tank wall heat insulating material 8 is
  • the side carbon block 11 (or silicon carbonitride brick), the cathode carbon block 5 and the side carbon block 11 (or silicon carbonitride brick) are connected by the side slope 1.
  • the whole cathode of the electrolytic cell is composed of a plurality of cathode carbon blocks 5, and two adjacent cathode carbon blocks 5 are connected by a carbon slag paste 4, and the cathode carbon block 5 of the electrolytic cell is connected to an external power source through the cathode steel rod 6 at the cathode carbon
  • the bottom of the block 5 has a bottom insulation material 12, and the bottom of the bottom insulation material 12 is a bottom steel shell 13.
  • the cathode carbon block 5 of the electrolytic cell of the present invention is processed with the longitudinal direction protrusion 2 or the width direction protrusion 7 or the longitudinal direction protrusion 2 and the width direction protrusion 7 at the same time.
  • the upper part of the carbon tamping paste 4 is provided with a refractory wall panel 3 having the same length as the cathode carbon block protrusion, and the cathode carbon block bump and the refractory material
  • the integral bulge formed by the material wall panel 3 has the function of reducing the flow rate of the aluminum liquid and maintaining the stability of the aluminum liquid.
  • the anti-abrasion of the refractory wall board can prolong the life of the cathode carbon block protrusion, and at the same time prevent the aluminum liquid from entering the cathode mid-slit to cause the early stage of the electrolytic cell. damaged.
  • the aluminum electrolytic cell structure of the present invention is as shown in Figs. 1, 5, 6, 7, and 11, and the aluminum electrolytic cell of the present invention has a convex structure processed along the longitudinal direction of each cathode carbon block. , called the longitudinal direction projection.
  • the edge of the cathode carbon block immediately adjacent to the aluminum outlet of the electrolytic cell is not machined to the edge of the aluminum outlet.
  • the length of the protrusion in the longitudinal direction is 14cm
  • the width is 10cm, and it is located at the side of each cathode carbon block along the length direction, and the horizontal distance between the outer surface of the longitudinal direction convex and the edge of the cathode carbon block is 2cm, in the masonry electrolysis
  • the middle slits of two adjacent cathode carbon blocks are sturdy and connected by carbon mash
  • the height of the tamping paste is equal to the height of the cathode carbon block
  • the upper surface of the smear of the two adjacent cathode carbon blocks A refractory wallboard is placed, the material of the refractory wallboard is nitrogen oxycarbide, and the refractory wallboard is placed in a direction parallel to the length of the cathode carbon block, and the width is wider than the adjacent two cathode carbon block edges.
  • the width between the lengthwise projections is 2 mm, and the length is equal to the length of the cathode carbon block side length.
  • the upper surface of the refractory wallboard is the same height as the convex upper surface of the cathode carbon block side.
  • the refractory wall plate and the adjacent two cathode carbon block edges are longitudinally convex to form an integral length direction protrusion, and the overall length direction convex cross section is rectangular .
  • the number of protrusions in the overall length direction is five, except that the distance between the protrusions of the two whole length directions of the lower side of the anode is 15 cm, and the distance between the protrusions of the other overall length direction is 12cm.
  • the aluminum electrolytic cell structure of the present invention is as shown in Figs. 1, 5, 6, 7, and 9.
  • the aluminum electrolytic cell of the present invention has a convex structure processed along the longitudinal direction of each cathode carbon block. , called the longitudinal direction projection.
  • the edge of the cathode carbon block immediately adjacent to the aluminum outlet of the electrolytic cell is not machined to the edge of the aluminum outlet.
  • the length of the protrusion in the longitudinal direction is 18 cm and the width is 15 cm, which is located at the side of each cathode carbon block along the length direction, and the horizontal distance between the outer surface of the lengthwise convex portion and the edge of the cathode carbon block is 3 cm, in the masonry electrolysis In the groove, the middle slits of two adjacent cathode carbon blocks are sturdy and connected by carbon mash, the height of the tamping paste is equal to the height of the cathode carbon block, and then the upper surface of the smear of the two adjacent cathode carbon blocks mounting a refractory wall, the refractory wall material is high-density brick, wherein the bulk density of the high density Magnesia 2.
  • These refractory wall panels are placed in a direction parallel to the length of the cathode carbon block, the width of which is 3 mm smaller than the width between the longitudinal projections of the adjacent two cathode carbon block edges, and the length and the cathode carbon block edge.
  • the lengthwise projections are of equal length, and the upper surface of these refractory wallboards is 3 cm higher than the convex upper surface of the cathode carbon block.
  • the refractory wall plate and the adjacent two cathode carbon block edges are longitudinally convex to form an integral length direction protrusion, and the overall length direction convex cross section is trapezoidal .
  • the whole The number of protrusions in the longitudinal direction is two, and the distance between the protrusions of each of the two overall length directions is 15 cm.
  • the aluminum electrolytic cell structure of the present invention is as shown in FIG. 1, FIG. 5, FIG. 6, FIG. 7, FIG. 10, and a convex structure is formed on each cathode carbon block along the longitudinal direction, which is called a longitudinal direction convex. .
  • the edge of the cathode carbon block immediately adjacent to the aluminum outlet of the electrolytic cell is not machined to the edge of the aluminum outlet.
  • the length of the protrusion in the longitudinal direction is 10 cm, the width is 5 cm, and it is located at the side of each cathode carbon block along the length direction, and the horizontal distance between the outer surface of the lengthwise convex portion and the edge of the cathode carbon block is 1 cm, in the masonry electrolysis In the groove, the middle slits of two adjacent cathode carbon blocks are sturdy and connected by carbon mash, the height of the tamping paste is equal to the height of the cathode carbon block, and then the upper surface of the smear of the two adjacent cathode carbon blocks A refractory wallboard is placed, and the refractory wallboard is made of magnesium aluminate spinel brick.
  • the refractory wall panels are placed in a direction parallel to the length of the cathode carbon block, the width of which is less than the width between the longitudinal projections of the adjacent two cathode carbon block edges, and the length and the cathode carbon block edge
  • the lengthwise projections are of equal length, and the upper surface of these refractory wallboards is 5 cm above the upper surface of the cathode carbon block lengthwise projection.
  • the refractory wall plate and the adjacent two cathode carbon block edges are longitudinally convex to form an integral length direction protrusion, and the overall length direction convex cross section is rectangular And the complex shape of the trapezoid.
  • the number of protrusions in the overall length direction is eight, and the distance between the protrusions of the other overall length directions is 20 cm except for the distance between the protrusions of the two whole length directions on the lower side of the anode. .
  • the aluminum electrolytic cell structure of the present invention is shown in Fig. 2, Fig. 8, and Fig. 11, and a projection which is perpendicular to the longitudinal direction of the cathode carbon block is formed on the cathode carbon block, and is called a width direction convex.
  • the edge of the cathode carbon block immediately adjacent to the aluminum outlet of the electrolytic cell is not machined to the edge of the aluminum outlet.
  • each of the widthwise projections On each cathode carbon block, the distance between each of the two widthwise projections is 30 cm, the width of the widthwise projection is 14 cm, the width is 24 cm, and the length coincides with the width of the cathode carbon block.
  • Each of the width direction protrusions is inlaid with a refractory wall panel along the width of the cathode carbon block.
  • the refractory wall panel is a nitrogen silicon carbide refractory board, and the refractory wall panel is inlaid with a width of 8 cm, and the height and the height of the width direction are convex. Consistently, the length coincides with the length of the bulge in the width direction.
  • the cross section in the width direction is a rectangle.
  • the aluminum electrolytic cell structure of the present invention is shown in Fig. 2, Fig. 8, and Fig. 9, and a projection which is perpendicular to the longitudinal direction of the cathode carbon block is formed on the cathode carbon block, and is called a width direction convex.
  • the edge of the cathode carbon block immediately adjacent to the aluminum outlet of the electrolytic cell is not machined to the edge of the aluminum outlet.
  • the distance between each of the two widthwise projections was 40 cm, the width of the widthwise projections was 18 cm, the width was 30 cm, and the length was less than the width of the cathode carbon block of 4 cm.
  • Each width direction is convex along the middle of the cathode carbon block width
  • the refractory wall panel is inlaid with refractory wallboard, the refractory wallboard is high density magnesia brick, the bulk density of the high density magnesia brick is 2. 8g/cm 3 , the inlaid refractory wallboard has a width of 10cm, and the height is convex than the width direction.
  • the height is 3cm, the length is less than the length of the convexity in the width direction of 7cm, and carbon bricks are further embedded at both ends of the refractory wallboard, so that the sum of the lengths of the inlaid refractory wallboard and the carbon brick is consistent with the length of the widthwise convex.
  • the cross section in the width direction is trapezoidal.
  • the aluminum electrolytic cell structure of the present invention is shown in Fig. 2, Fig. 8, and Fig. 10, and a projection which is perpendicular to the longitudinal direction of the cathode carbon block is formed on the cathode carbon block, and is called a width direction convex.
  • the edge of the cathode carbon block immediately adjacent to the aluminum outlet of the electrolytic cell is not machined to the edge of the aluminum outlet.
  • the distance between each of the two widthwise projections was 20 cm, the height of the projections in the width direction was 10 cm, the width was 18 cm, and the length was less than the width of the cathode carbon block of 6 cm.
  • Refractory wallboard is embedded in the width direction of the cathode carbon block in the middle of each width direction.
  • the refractory wallboard is a magnesium-aluminum spinel board.
  • the width of the refractory wallboard is 5cm, and the height is 5cm higher than the width.
  • the length is less than the length of the convexity in the width direction of 10 cm, and carbon bricks are further embedded at both ends of the refractory wallboard, so that the sum of the lengths of the inlaid refractory wallboard and the carbon bricks coincides with the length of the convexity in the width direction.
  • the cross section in the width direction is a composite shape of a rectangle and a trapezoid.
  • the structure of the aluminum electrolytic cell of the present invention is as shown in Figs. 3 and 11, and the longitudinal direction projection and the width direction projection are simultaneously processed on the upper side portion of the cathode carbon block.
  • the edge of the cathode carbon block immediately adjacent to the aluminum outlet of the electrolytic cell is not machined to the edge of the aluminum outlet.
  • the length of the protrusion in the longitudinal direction is 14cm
  • the width is 10cm, and it is located at the side of each cathode carbon block along the length direction, and the horizontal distance between the outer surface of the longitudinal direction convex and the edge of the cathode carbon block is 2cm, in the masonry electrolysis
  • the middle slits of two adjacent cathode carbon blocks are sturdy and connected by carbon mash
  • the height of the tamping paste is equal to the height of the cathode carbon block
  • the upper surface of the smear of the two adjacent cathode carbon blocks A refractory wallboard is placed, the material of the refractory wallboard is nitrogen oxycarbide, and the refractory wallboard is placed in a direction parallel to the length of the cathode carbon block, and the width is wider than the adjacent two cathode carbon block edges.
  • the width between the lengthwise projections is 2 mm, and the length is equal to the length of the cathode carbon block side length.
  • the upper surface of the refractory wallboard is the same height as the convex upper surface of the cathode carbon block side.
  • the refractory wall plate and the adjacent two cathode carbon block edges are longitudinally convex to form an integral length direction protrusion, and the overall length direction convex cross section is rectangular .
  • the number of protrusions in the overall length direction is five, except that the distance between the protrusions of the two whole length directions of the lower side of the anode is 15 cm, and the distance between the protrusions of the other overall length direction is 12cm.
  • the width direction projection is located between the two integral lengthwise projections described above.
  • the width direction is convex and the cathode carbon block is one Overall, on each cathode carbon block, the distance between the width direction projection and its adjacent integral length direction projection was 8 cm.
  • the edge of the cathode carbon block located at the end of the aluminum outlet is not provided with a widthwise projection.
  • the widthwise convex cross section is rectangular, and the widthwise convex width is 25 cm.
  • Each of the width direction protrusions is inlaid with a refractory wall panel along the width of the cathode carbon block, and the refractory wall panel is a nitrogen silicon carbide refractory board.
  • the structure of the aluminum electrolytic cell of the present invention is as shown in Figs. 3 and 9, and the longitudinal direction projection and the width direction projection are simultaneously processed on the upper side of the cathode carbon block.
  • the edge of the cathode carbon block immediately adjacent to the aluminum outlet of the electrolytic cell is not machined to the edge of the aluminum outlet.
  • the length of the protrusion in the longitudinal direction is 18 cm and the width is 15 cm, which is located at the side of each cathode carbon block along the length direction, and the horizontal distance between the outer surface of the lengthwise convex portion and the edge of the cathode carbon block is 3 cm, in the masonry electrolysis In the groove, the middle slits of two adjacent cathode carbon blocks are sturdy and connected by carbon mash, the height of the tamping paste is equal to the height of the cathode carbon block, and then the upper surface of the smear of the two adjacent cathode carbon blocks.
  • the granules of the high-density magnesia bricks having a bulk density of 2. 8 g / cm 3 .
  • These refractory wall panels are placed in a direction parallel to the length of the cathode carbon block, the width of which is 3 mm smaller than the width between the longitudinal projections of the adjacent two cathode carbon block edges, and the length and the cathode carbon block edge.
  • the longitudinal direction of the bulge is equal, and the upper surface of the refractory wallboard is higher than the upper surface of the cathode carbon block.
  • the refractory wall plate and the adjacent two cathode carbon block edges are longitudinally convex to form an integral length direction protrusion, and the overall length direction convex cross section is trapezoidal .
  • the number of the overall lengthwise projections was two, and the distance between the projections of the two integral lengthwise directions was 15 cm.
  • the width direction projection is located between the two integral lengthwise projections described above.
  • the width direction projection is integral with the cathode carbon block, and on each cathode carbon block, the distance between the width direction projection and its adjacent integral length direction projection is 10 cm.
  • the edge of the cathode carbon block located at the end of the aluminum outlet is not provided with a widthwise projection.
  • the widthwise convex cross section is trapezoidal, and the widthwise convex width is 35 cm.
  • the refractory wallboard is a high-density magnesia brick having a bulk density of 2. 8 g/cm 3 , in the direction of the width of the cathode carbon block.
  • the structure of the aluminum electrolytic cell of the present invention is as shown in Figs. 3 and 10, and the longitudinal direction projections and the widthwise projections are simultaneously processed on the upper side portions of the cathode carbon block.
  • the edge of the cathode carbon block immediately adjacent to the aluminum outlet of the electrolytic cell is not machined to the edge of the aluminum outlet.
  • the length of the protrusion in the longitudinal direction is 10 cm, the width is 5 cm, and it is located at the side of each cathode carbon block along the length direction, and the horizontal distance between the outer surface of the lengthwise convex portion and the edge of the cathode carbon block is 1 cm, in the masonry electrolysis
  • two adjacent yin The middle seam of the carbon block is tamped with a carbon tamping paste, the height of the tamping paste is equal to the height of the cathode carbon block, and then a refractory wall panel is placed on the upper surface of the two adjacent cathode carbon block tamping.
  • the material of the refractory wallboard is magnesium aluminum spinel brick.
  • the refractory wall panels are placed in a direction parallel to the length of the cathode carbon block, the width of which is less than the width between the longitudinal projections of the adjacent two cathode carbon block edges, and the length and the cathode carbon block edge
  • the lengthwise projections are of equal length, and the upper surface of these refractory wallboards is 5 cm above the upper surface of the cathode carbon block lengthwise projection.
  • the refractory wall plate and the adjacent two cathode carbon block edges are longitudinally convex to form an integral length direction protrusion, and the overall length direction convex cross section is rectangular And the complex shape of the trapezoid.
  • the number of protrusions in the overall length direction is eight, and the distance between the protrusions of the other overall length directions is 20 cm except for the distance between the protrusions of the two whole length directions on the lower side of the anode. .
  • the width direction projection is located between the two integral lengthwise projections described above.
  • the width direction projection is integral with the cathode carbon block, and on each cathode carbon block, the distance between the width direction projection and its adjacent integral length direction projection is 5 cm.
  • the edge of the cathode carbon block located at the end of the aluminum outlet is not provided with a widthwise projection.
  • the cross section in the width direction is a composite shape of a rectangle and a trapezoid, and the width of the projection in the width direction is 15 cm.
  • Refractory wall panels are embedded in the width direction of the cathode carbon block in the middle of each width direction convex, and the refractory wall plate is a magnesium aluminum spinel plate.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electrolytic Production Of Metals (AREA)

Abstract

An aluminum electrolytic cell having a cathode structure in which abrasion of the bulges on the cathode can be decelerated is disclosed. Bulges, which are called longitudinal bulges, are machined on each cathode carbon block near its sides along the longitudinal direction; or bulges, which are called transverse bulges, are machined on top of the cathode carbon block along the direction vertical to the longitudinal direction of the cathode carbon block; or both the longitudinal bulges and the transverse bulges are machined on top of the cathode. A refractory wallboard is provided on the carbon tamping paste arranged between two adjacent cathode carbon blocks, and an integral bulge is constructed by the bulge on the cathode carbon block and the refractory wallboard. The integral bulge can lessen the flow speed of molten aluminum and its turbulence, thus it can increase the stability of the molten aluminum on its top surface in the electrolytic cell. As the refractory wallboard can be more resistant to electrochemical abrasion than carbon, when the bulges on the cathode blocks are abraded, it can reduce the flow speed of molten aluminum continuously.

Description

说 明 书 一种能减缓阴极凸起磨蚀的阴极结构铝电解槽 技术领域  Description A cathode structure aluminum electrolytic cell capable of alleviating cathode bump abrasion
本发明属于电解铝技术领域,具体涉及一种能减缓阴极凸起磨蚀的新型阴极结构铝电解 槽。  The invention belongs to the technical field of electrolytic aluminum, and particularly relates to a novel cathode structure aluminum electrolytic cell capable of alleviating the erosion of the cathode protrusion.
背景技术 Background technique
目前工业上生产的金属铝都是用熔盐电解法生产的, 其专用设备为内衬为碳质材料 (或 氮化硅结合碳化硅砖) 的电解槽, 碳质内衬与钢制槽壳之间为耐火材料和保温材料。 电解槽 的底部内衬为其底部安装有导电钢棒的碳块, 此碳块称为电解槽的阴极碳块。 阴极碳块与阴 极碳块之间用碳素糊捣固连接,诸多的阴极碳块和它们之间捣固糊组成电解槽的底部碳阴极。 通常工业电解槽的槽电压在 4. 0〜4. 3伏左右, 而极距在 4. 0〜5. 0cm之间。 目前工业铝电解槽 之所以还能大幅度地降低极距使电解槽槽电压降低的原因在于现行工业铝电解槽内由于电磁 力的作用和阳极气体从阳极表面和电解质熔体中逸出时引起了阴极铝液面产生很大的波动, 如果这种波动的流速和波幅能够得以降低, 那么就可以使目前电解槽的极距和槽电压降低, 从而达到大幅度降低铝电解生产电耗的目的。为此, CN200710010523. 4提出了一种新型阴极 结构的铝电解槽, 这种新型阴极结构的电解槽在工业上应用后确实起到了大幅度地降低铝电 解生产电耗的结果, 但在实践中也发现, 这种新型阴极结构的电解槽其阴极表面上的凸起结 构的高度会逐渐降低, 其消耗速度约在 2〜4cm/年, 一般来说这种消耗主要来源于铝液中钠的 化学渗透作用时碳阴极表面晶格的侵蚀和破坏, 以及而后的阴极铝液的流动对碳阴极表面的 冲刷造成碳阴极表面的脱落而引起的。  At present, the metal aluminum produced in the industry is produced by molten salt electrolysis. The special equipment is an electrolytic cell lined with carbonaceous material (or silicon nitride combined with silicon carbide brick), carbon lining and steel grooved shell. Between refractory materials and insulation materials. The bottom of the cell is lined with a carbon block with a conductive steel rod mounted on its bottom. This block of carbon is called the cathode carbon block of the cell. The cathode carbon block and the cathode carbon block are connected by a carbon paste, and a plurality of cathode carbon blocks and a crucible between them form a bottom carbon cathode of the electrolytic cell. 5厘米之间。 Generally, the cell voltage of the industrial cell is between 4. 0~4. 3 volts, and the pole pitch is between 4. 0~5. 0cm. At present, the reason why the industrial aluminum electrolytic cell can greatly reduce the pole pitch to reduce the voltage of the electrolytic cell is due to the electromagnetic force in the current industrial aluminum electrolytic cell and the anode gas escaping from the anode surface and the electrolyte melt. The liquid level of the cathode aluminum is greatly fluctuated. If the flow rate and amplitude of the fluctuation can be reduced, the pole distance and the cell voltage of the current electrolytic cell can be lowered, thereby achieving the purpose of greatly reducing the power consumption of the aluminum electrolytic production. . To this end, CN200710010523. 4 proposes a new type of aluminum electrolytic cell with a cathode structure. The electrolytic cell of the new cathode structure has indeed reduced the power consumption of aluminum electrolysis production after industrial application, but in practice, It has also been found that the height of the convex structure on the cathode surface of the electrolytic cell of the novel cathode structure is gradually reduced, and the consumption rate is about 2 to 4 cm/year. Generally, the consumption is mainly derived from sodium in the aluminum liquid. The erosion and destruction of the crystal lattice surface of the carbon cathode during chemical osmosis, and the subsequent flow of the cathode aluminum liquid on the surface of the carbon cathode cause the surface of the carbon cathode to fall off.
发明内容 Summary of the invention
针对上述现有技术存在的问题, 本发明提供一种能减缓阴极磨蚀的铝电解槽, 解决阴极 表面凸起因受物理、 化学的磨蚀引起的寿命低的问题。  In view of the above problems in the prior art, the present invention provides an aluminum electrolytic cell capable of slowing down the cathode abrasion, and solves the problem that the life of the cathode surface is low due to physical and chemical abrasion.
本发明的铝电解槽, 具有阴极碳块凸起, 具体为: 在每个阴极碳块上沿长度方向的边部 加工有凸起结构, 称为长度方向凸起; 或在阴极碳块上部加工与阴极碳块的长度方向相垂直 的凸起, 称为宽度方向凸起; 或在阴极碳块上边部同时加工长度方向凸起和宽度方向凸起。  The aluminum electrolytic cell of the present invention has cathode carbon block protrusions, specifically: a convex structure is formed on the side of the cathode carbon block along the longitudinal direction, which is called a longitudinal direction protrusion; or is processed on the upper part of the cathode carbon block. The protrusion perpendicular to the longitudinal direction of the cathode carbon block is referred to as a width direction protrusion; or the length direction protrusion and the width direction protrusion are simultaneously processed on the upper side of the cathode carbon block.
各种阴极碳块凸起的材质与阴极碳块相同, 为一体结构。  The material of the various cathode carbon block bumps is the same as that of the cathode carbon block, and is an integral structure.
紧靠电解槽出铝端的阴极碳块的靠近出铝口的边部不加工凸起。 长度方向凸起的高度为 10〜18cm, 宽度为 5〜15cm, 位于每个阴极碳块沿长度方向的边 部, 且该长度方向凸起的外侧表面与阴极碳块边缘的水平距离为 l〜3cm, 在砌筑电解槽时, 两个相邻阴极碳块的中缝用碳素捣固糊捣固连接, 捣固糊的高度与阴极碳块的高度相等, 然 后在两个相邻阴极碳块捣固糊的上表面安放一条耐火材料墙板, 该耐火材料墙板的材料为氮 碳化硅或高密度镁砖或镁铝尖晶石砖,其中高密度镁砖的体积密度为 2. 6〜3. 0g/cm 这些耐 火材料墙板沿与阴极碳块的长度方向相平行的方向安放, 其宽度比相邻两个阴极碳块边部的 长度方向凸起之间的宽度小 l〜3mm, 长度与阴极碳块边部长度方向凸起长度相等, 这些耐 火材料墙板的上表面与阴极碳块边部长度方向凸起上表面高度一样或高于阴极碳块长度方向 凸起的上表面 l〜5cm。 The edge of the cathode carbon block immediately adjacent to the aluminum outlet of the electrolytic cell is not machined to the edge of the aluminum outlet. The length of the protrusion in the longitudinal direction is 10 to 18 cm, and the width is 5 to 15 cm, which is located at the side of each cathode carbon block along the length direction, and the horizontal distance between the outer surface of the longitudinally convex portion and the edge of the cathode carbon block is l~ 3cm, when laying the electrolytic cell, the middle slits of two adjacent cathode carbon blocks are sturdy and connected with carbon slag, the height of the tamping paste is equal to the height of the cathode carbon block, and then in two adjacent cathode carbon blocks. The granules of the high-density magnesia bricks have a bulk density of 2. 6~ 3. 0g/cm These refractory wall panels are placed in a direction parallel to the length direction of the cathode carbon block, and the width thereof is smaller than the width between the longitudinal projections of the adjacent two cathode carbon block edges by 1 to 3 mm. The length is equal to the length of the longitudinal direction of the cathode carbon block, and the upper surface of the refractory wallboard is the same as the height of the convex upper surface of the cathode carbon block and higher than the upper surface of the cathode carbon block. ~5cm.
在每两个相邻阴极碳块之间, 耐火材料墙板与相邻两个阴极碳块边部的长度方向凸起构 成一个整体长度方向凸起, 该整体长度方向凸起的横截面为矩形或梯形, 或矩形和梯形的复 合形状。每个阴极碳块上, 该整体长度方向凸起的数量为 2〜8个, 当整体长度方向凸起数为 2个时, 每两个整体长度方向凸起之间的距离为 10〜20cm。 当整体长度方向凸起数为 3〜8 个时, 除阳极中缝下边两个整体长度方向凸起之间的距离为 10〜20cm夕卜, 其它整体长度方 向凸起之间的距离为 5〜20cm。  Between each two adjacent cathode carbon blocks, the refractory wall plate and the adjacent two cathode carbon block edges are longitudinally convex to form an integral length direction protrusion, and the overall length direction convex cross section is rectangular Or trapezoidal, or a composite shape of a rectangle and a trapezoid. On each cathode carbon block, the number of protrusions in the overall length direction is 2 to 8. When the number of protrusions in the entire length direction is two, the distance between the protrusions of each of the two overall length directions is 10 to 20 cm. When the number of protrusions in the overall length direction is 3 to 8, the distance between the protrusions of the two whole length directions except the lower side of the anode is 10 to 20 cm, and the distance between the protrusions of the other overall length direction is 5 to 20 cm. .
当长度方向凸起和宽度方向凸起同时存在时, 宽度方向凸起位于上述的两个整体长度方 向凸起之间。 宽度方向凸起与阴极碳块为一个整体, 在每个阴极碳块上, 宽度方向凸起与其 相邻的整体长度方向凸起之间的距离为 5〜10cm。 对于一个整体电解槽而言, 位于出铝口端 的阴极碳块边部不设置宽度方向凸起。 与上述的整体长度方向凸起相似, 宽度方向凸起的横 截面为矩形, 或梯形, 或两者的组合, 宽度方向凸起的宽度为 15〜35cm。 每个宽度方向凸起 中间沿阴极碳块宽度方向镶嵌耐火材料墙板, 耐火材料墙板为氮碳化硅耐火板或高密度镁砖 或镁铝尖晶石板。 其中高密度镁砖的体积密度为 2. 6〜3. 0g/cm3When the longitudinal direction projection and the width direction projection are simultaneously present, the width direction projection is located between the above two integral lengthwise projections. The width direction protrusion is integrated with the cathode carbon block, and the distance between the width direction protrusion and the adjacent integral length direction protrusion is 5 to 10 cm on each cathode carbon block. For an integral electrolytic cell, the edge of the cathode carbon block located at the end of the aluminum outlet is not provided with a widthwise projection. Similar to the above-described overall lengthwise projection, the widthwise convex cross section is rectangular, or trapezoidal, or a combination of the two, and the widthwise projection has a width of 15 to 35 cm. Each of the width direction protrusions is inlaid with a refractory wall panel along the width of the cathode carbon block, and the refractory wall panel is a nitrogen silicon carbide refractory board or a high density magnesia brick or a magnesium aluminum spinel board. 0〜3. 0g/cm 3。 The high density of the mass density of 2. 6~ 3 . 0g / cm 3 .
当铝电解槽阴极碳块上只有宽度方向凸起时, 每个阴极碳块上, 每两个宽度方向凸起之 间的距离为 20〜40cm, 宽度方向凸起的高度为 10〜18cm, 宽度为 18〜30cm, 长度与阴极碳 块的宽度相一致或小于阴极碳块的宽度 2〜6cm。每个宽度方向凸起中间沿阴极碳块宽度方向 镶嵌耐火材料墙板, 耐火材料墙板同样为氮碳化硅耐火板或高密度镁砖或镁铝尖晶石板, 其 中高密度镁砖的体积密度为 2. 6〜3. 0g/cm 所镶嵌的耐火材料墙板宽度为 5〜10cm, 高度与 宽度方向凸起的高度相一致或高于宽度方向凸起 l〜5cm, 长度与宽度方向凸起的长度相一 致, 或小于宽度方向凸起的长度 4〜10cm, 当镶嵌的耐火材料墙板的长度小于宽度方向凸起 时, 在耐火材料墙板的两端再镶嵌碳砖, 使镶嵌的耐火材料墙板与碳砖的长度之和与宽度方 向凸起的长度一致。 宽度方向凸起的横截面为矩形或梯形, 或矩形和梯形的复合形状。 本发明的优点在于, 耐火材料墙板与阴极碳块凸起构成的整体凸起具有减缓铝液流速、 减少铝液波动、 提高电解槽铝液面稳定性的作用, 且由于耐火墙板是由抗磨蚀、 抗腐蚀的铝 镁尖晶石或碳氮化硅等材料制成的, 不仅对铝电解过程和铝的质量没有影响, 而且在阴极碳 块凸起被磨蚀后由于耐火材料墙板比碳的电化学磨蚀性小, 耐火材料墙板能继续起到减缓铝 液流速的作用。 When only the width direction is convex on the cathode carbon block of the aluminum electrolytic cell, the distance between each of the two widthwise projections is 20 to 40 cm on each cathode carbon block, and the height in the width direction is 10 to 18 cm, and the width is It is 18~30cm, and the length is consistent with the width of the cathode carbon block or less than the width of the cathode carbon block by 2~6cm. Each of the width direction protrusions is inlaid with a refractory wall panel along the width of the cathode carbon block, and the refractory wall board is also a nitrogen silicon carbide refractory board or a high density magnesia brick or a magnesium aluminum spinel board, wherein the bulk density of the high density magnesia brick The width of the refractory wallboard is 2. 5~3. 0g/cm. The width of the refractory wallboard is 5~10cm, and the height is consistent with the height of the convexity in the width direction or higher than that of the width direction by l~5cm. The length is consistent, or less than the length of the width direction of the protrusion 4~10cm. When the length of the inlaid refractory wallboard is less than the width direction, the carbon bricks are inlaid on both ends of the refractory wallboard to make the inlaid fireproof The sum of the lengths of the material wall panels and the carbon bricks coincides with the length of the widthwise projections. The cross section in the width direction is a rectangle or a trapezoid, or a composite shape of a rectangle and a trapezoid. The invention has the advantages that the integral protrusion formed by the refractory wall plate and the cathode carbon block protrusion has the effects of slowing the flow rate of the aluminum liquid, reducing the fluctuation of the aluminum liquid, and improving the stability of the aluminum level of the electrolytic cell, and since the refractory wall plate is Made of materials such as anti-abrasion and anti-corrosion aluminum-magnesium spinel or silicon carbonitride, which have no effect on the aluminum electrolysis process and the quality of the aluminum, and the refractory wall-to-wall ratio after the cathode carbon block bumps are abraded. The electrochemical erosion of carbon is small, and refractory wallboard can continue to slow down the flow rate of aluminum.
附图说明 DRAWINGS
图 1为阴极碳块具有长度方向凸起的电解槽俯视图;  Figure 1 is a plan view of an electrolytic cell having a cathode bulge in the longitudinal direction;
图 2为阴极碳块具有宽度方向凸起的电解槽的俯视图;  2 is a plan view of an electrolytic cell having a cathode carbon block having a width direction;
图 3为阴极碳块兼有长度方向和宽度方向凸起的电解槽的俯视图;  3 is a plan view of an electrolytic cell in which a cathode carbon block has both a longitudinal direction and a width direction;
图 4为图 1中 A-A剖面示意图, 耐火材料墙板与长度方向凸起高度相等;  Figure 4 is a cross-sectional view of the A-A of Figure 1, the refractory wall panel is equal in height to the longitudinal direction;
图 5为图 1中 A-A剖面示意图, 耐火材料墙板比长度方向凸起高;  Figure 5 is a schematic cross-sectional view of the A-A of Figure 1, the refractory wall panel is raised higher than the length direction;
图 6为图 1中 B-B剖面示意图;  Figure 6 is a schematic cross-sectional view taken along line B-B of Figure 1;
图 7为图 1中 C-C剖面示意图;  Figure 7 is a schematic cross-sectional view taken along line C-C of Figure 1;
图 8为图 2中 D-D剖面示意图;  Figure 8 is a schematic cross-sectional view of the D-D of Figure 2;
图 9为横截面为梯形的长度方向凸起或宽度方向凸起的示意图;  Figure 9 is a schematic view showing a longitudinal direction projection or a width direction projection having a trapezoidal cross section;
图 10为横截面为矩形和梯形组合形状的长度方向凸起或宽度方向凸起的示意图; 图 11为横截面为矩形的长度方向凸起或宽度方向凸起的示意图。  Fig. 10 is a schematic view showing a longitudinal direction projection or a width direction projection having a rectangular cross section and a trapezoidal combination shape; Fig. 11 is a schematic view showing a longitudinal direction projection or a width direction projection having a rectangular cross section.
图中: 1侧部斜坡, 2长度方向凸起, 3耐火材料墙板, 4碳素捣固糊, 5阴极碳块, 6阴 极钢棒, 7. 宽度方向凸起, 8槽壁保温材料, 9侧部钢壳, 10浇注耐火材料, 11侧部碳块, 12槽底保温材料, 13底部钢壳。  In the picture: 1 side slope, 2 lengthwise projection, 3 refractory wallboard, 4 carbon tamping paste, 5 cathode carbon block, 6 cathode steel bar, 7. width direction bulging, 8 groove wall insulation material, 9 side steel shell, 10 cast refractory material, 11 side carbon block, 12 groove bottom insulation material, 13 bottom steel shell.
具体实施方式 Detailed ways
以下通过实施例进一步说明本发明的能减缓阴极凸起磨蚀的新型阴极结构铝电解槽。 如附图所示, 能减缓阴极磨蚀的铝电解槽的外部有侧部钢壳 9、 底部钢壳 13, 紧贴侧部 钢壳 9的为槽壁保温材料 8, 槽壁保温材料 8内部为侧部碳块 11 (或碳氮化硅砖), 阴极碳块 5与侧部碳块 11 (或碳氮化硅砖) 通过侧部斜坡 1连接。 电解槽的整体阴极由多块阴极碳块 5组成, 相邻两个阴极碳块 5通过碳素捣固糊 4相连, 电解槽阴极碳块 5通过阴极钢棒 6与 外部电源连接, 在阴极碳块 5底部有槽底保温材料 12, 槽底保温材料 12下部为底部钢壳 13。 与普通铝电解槽不同的是本发明的电解槽的阴极碳块 5上加工有长度方向凸起 2或宽度方向 凸起 7, 或同时加工有长度方向凸起 2和宽度方向凸起 7, 在两个相邻阴极碳块凸起中间, 碳 素捣固糊 4的上部安有与阴极碳块凸起长度相同的耐火材料墙板 3, 阴极碳块凸起与耐火材 料墙板 3构成的整体凸起有降低铝液流速、 保持铝液稳定的作用, 耐火墙板抗磨蚀能够延长 阴极碳块凸起的寿命, 同时防止了铝液进入阴极中缝造成电解槽的早期破损。 The novel cathode structure aluminum electrolysis cell of the present invention capable of alleviating the cathode protrusion abrasion is further illustrated by the following examples. As shown in the drawing, the aluminum electrolytic cell which can slow down the cathode abrasion has a side steel shell 9 and a bottom steel shell 13 on the outside, and a groove wall heat insulating material 8 which is in close contact with the side steel shell 9, and the inside of the tank wall heat insulating material 8 is The side carbon block 11 (or silicon carbonitride brick), the cathode carbon block 5 and the side carbon block 11 (or silicon carbonitride brick) are connected by the side slope 1. The whole cathode of the electrolytic cell is composed of a plurality of cathode carbon blocks 5, and two adjacent cathode carbon blocks 5 are connected by a carbon slag paste 4, and the cathode carbon block 5 of the electrolytic cell is connected to an external power source through the cathode steel rod 6 at the cathode carbon The bottom of the block 5 has a bottom insulation material 12, and the bottom of the bottom insulation material 12 is a bottom steel shell 13. Different from the ordinary aluminum electrolytic cell, the cathode carbon block 5 of the electrolytic cell of the present invention is processed with the longitudinal direction protrusion 2 or the width direction protrusion 7 or the longitudinal direction protrusion 2 and the width direction protrusion 7 at the same time. In the middle of two adjacent cathode carbon block bumps, the upper part of the carbon tamping paste 4 is provided with a refractory wall panel 3 having the same length as the cathode carbon block protrusion, and the cathode carbon block bump and the refractory material The integral bulge formed by the material wall panel 3 has the function of reducing the flow rate of the aluminum liquid and maintaining the stability of the aluminum liquid. The anti-abrasion of the refractory wall board can prolong the life of the cathode carbon block protrusion, and at the same time prevent the aluminum liquid from entering the cathode mid-slit to cause the early stage of the electrolytic cell. damaged.
实施例 1 Example 1
本发明的铝电解槽结构如图 1、 图 5、 图 6、 图 7、 图 11所示, 本发明的铝电解槽, 在每 个阴极碳块上沿长度方向的边部加工有凸起结构, 称为长度方向凸起。  The aluminum electrolytic cell structure of the present invention is as shown in Figs. 1, 5, 6, 7, and 11, and the aluminum electrolytic cell of the present invention has a convex structure processed along the longitudinal direction of each cathode carbon block. , called the longitudinal direction projection.
紧靠电解槽出铝端的阴极碳块的靠近出铝口的边部不加工凸起。  The edge of the cathode carbon block immediately adjacent to the aluminum outlet of the electrolytic cell is not machined to the edge of the aluminum outlet.
长度方向凸起的高度为 14cm, 宽度为 10cm, 位于每个阴极碳块沿长度方向的边部, 且 该长度方向凸起的外侧表面与阴极碳块边缘的水平距离为 2cm, 在砌筑电解槽时, 两个相邻 阴极碳块的中缝用碳素捣固糊捣固连接, 捣固糊的高度与阴极碳块的高度相等, 然后在两个 相邻阴极碳块捣固糊的上表面安放一条耐火材料墙板, 该耐火材料墙板的材料为氮碳化硅, 这些耐火材料墙板沿与阴极碳块的长度方向相平行的方向安放, 其宽度比相邻两个阴极碳块 边部的长度方向凸起之间的宽度小 2mm, 长度与阴极碳块边部长度方向凸起长度相等, 这些 耐火材料墙板的上表面与阴极碳块边部长度方向凸起上表面高度一样。  The length of the protrusion in the longitudinal direction is 14cm, the width is 10cm, and it is located at the side of each cathode carbon block along the length direction, and the horizontal distance between the outer surface of the longitudinal direction convex and the edge of the cathode carbon block is 2cm, in the masonry electrolysis In the groove, the middle slits of two adjacent cathode carbon blocks are sturdy and connected by carbon mash, the height of the tamping paste is equal to the height of the cathode carbon block, and then the upper surface of the smear of the two adjacent cathode carbon blocks A refractory wallboard is placed, the material of the refractory wallboard is nitrogen oxycarbide, and the refractory wallboard is placed in a direction parallel to the length of the cathode carbon block, and the width is wider than the adjacent two cathode carbon block edges. The width between the lengthwise projections is 2 mm, and the length is equal to the length of the cathode carbon block side length. The upper surface of the refractory wallboard is the same height as the convex upper surface of the cathode carbon block side.
在每两个相邻阴极碳块之间, 耐火材料墙板与相邻两个阴极碳块边部的长度方向凸起构 成一个整体长度方向凸起, 该整体长度方向凸起的横截面为矩形。 每个阴极碳块上, 该整体 长度方向凸起的数量为 5个, 除阳极中缝下边两个整体长度方向凸起之间的距离为 15cm夕卜, 其它整体长度方向凸起之间的距离为 12cm。  Between each two adjacent cathode carbon blocks, the refractory wall plate and the adjacent two cathode carbon block edges are longitudinally convex to form an integral length direction protrusion, and the overall length direction convex cross section is rectangular . On each cathode carbon block, the number of protrusions in the overall length direction is five, except that the distance between the protrusions of the two whole length directions of the lower side of the anode is 15 cm, and the distance between the protrusions of the other overall length direction is 12cm.
实施例 2 Example 2
本发明的铝电解槽结构如图 1、 图 5、 图 6、 图 7、 图 9所示, 本发明的铝电解槽, 在每 个阴极碳块上沿长度方向的边部加工有凸起结构, 称为长度方向凸起。  The aluminum electrolytic cell structure of the present invention is as shown in Figs. 1, 5, 6, 7, and 9. The aluminum electrolytic cell of the present invention has a convex structure processed along the longitudinal direction of each cathode carbon block. , called the longitudinal direction projection.
紧靠电解槽出铝端的阴极碳块的靠近出铝口的边部不加工凸起。  The edge of the cathode carbon block immediately adjacent to the aluminum outlet of the electrolytic cell is not machined to the edge of the aluminum outlet.
长度方向凸起的高度为 18cm, 宽度为 15cm, 位于每个阴极碳块沿长度方向的边部, 且 该长度方向凸起的外侧表面与阴极碳块边缘的水平距离为 3cm, 在砌筑电解槽时, 两个相邻 阴极碳块的中缝用碳素捣固糊捣固连接, 捣固糊的高度与阴极碳块的高度相等, 然后在两个 相邻阴极碳块捣固糊的上表面安放一条耐火材料墙板,该耐火材料墙板的材料为高密度镁砖, 其中高密度镁砖的体积密度为 2. 8g/cm3。 这些耐火材料墙板沿与阴极碳块的长度方向相平行 的方向安放, 其宽度比相邻两个阴极碳块边部的长度方向凸起之间的宽度小 3mm, 长度与阴 极碳块边部长度方向凸起长度相等, 这些耐火材料墙板的上表面高于阴极碳块长度方向凸起 的上表面 3cm。 The length of the protrusion in the longitudinal direction is 18 cm and the width is 15 cm, which is located at the side of each cathode carbon block along the length direction, and the horizontal distance between the outer surface of the lengthwise convex portion and the edge of the cathode carbon block is 3 cm, in the masonry electrolysis In the groove, the middle slits of two adjacent cathode carbon blocks are sturdy and connected by carbon mash, the height of the tamping paste is equal to the height of the cathode carbon block, and then the upper surface of the smear of the two adjacent cathode carbon blocks mounting a refractory wall, the refractory wall material is high-density brick, wherein the bulk density of the high density Magnesia 2. 8g / cm 3. These refractory wall panels are placed in a direction parallel to the length of the cathode carbon block, the width of which is 3 mm smaller than the width between the longitudinal projections of the adjacent two cathode carbon block edges, and the length and the cathode carbon block edge. The lengthwise projections are of equal length, and the upper surface of these refractory wallboards is 3 cm higher than the convex upper surface of the cathode carbon block.
在每两个相邻阴极碳块之间, 耐火材料墙板与相邻两个阴极碳块边部的长度方向凸起构 成一个整体长度方向凸起, 该整体长度方向凸起的横截面为梯形。 每个阴极碳块上, 该整体 长度方向凸起的数量为 2个, 每两个整体长度方向凸起之间的距离为 15cm。 Between each two adjacent cathode carbon blocks, the refractory wall plate and the adjacent two cathode carbon block edges are longitudinally convex to form an integral length direction protrusion, and the overall length direction convex cross section is trapezoidal . On each cathode carbon block, the whole The number of protrusions in the longitudinal direction is two, and the distance between the protrusions of each of the two overall length directions is 15 cm.
实施例 3 Example 3
本发明的铝电解槽结构如图 1、 图 5、 图 6、 图 7、 图 10所示, 在每个阴极碳块上沿长度 方向的边部加工有凸起结构, 称为长度方向凸起。  The aluminum electrolytic cell structure of the present invention is as shown in FIG. 1, FIG. 5, FIG. 6, FIG. 7, FIG. 10, and a convex structure is formed on each cathode carbon block along the longitudinal direction, which is called a longitudinal direction convex. .
紧靠电解槽出铝端的阴极碳块的靠近出铝口的边部不加工凸起。  The edge of the cathode carbon block immediately adjacent to the aluminum outlet of the electrolytic cell is not machined to the edge of the aluminum outlet.
长度方向凸起的高度为 10cm, 宽度为 5cm, 位于每个阴极碳块沿长度方向的边部, 且该 长度方向凸起的外侧表面与阴极碳块边缘的水平距离为 lcm, 在砌筑电解槽时, 两个相邻阴 极碳块的中缝用碳素捣固糊捣固连接, 捣固糊的高度与阴极碳块的高度相等, 然后在两个相 邻阴极碳块捣固糊的上表面安放一条耐火材料墙板,该耐火材料墙板的材料为镁铝尖晶石砖。 这些耐火材料墙板沿与阴极碳块的长度方向相平行的方向安放, 其宽度比相邻两个阴极碳块 边部的长度方向凸起之间的宽度小 lmm, 长度与阴极碳块边部长度方向凸起长度相等, 这些 耐火材料墙板的上表面高于阴极碳块长度方向凸起的上表面 5cm。  The length of the protrusion in the longitudinal direction is 10 cm, the width is 5 cm, and it is located at the side of each cathode carbon block along the length direction, and the horizontal distance between the outer surface of the lengthwise convex portion and the edge of the cathode carbon block is 1 cm, in the masonry electrolysis In the groove, the middle slits of two adjacent cathode carbon blocks are sturdy and connected by carbon mash, the height of the tamping paste is equal to the height of the cathode carbon block, and then the upper surface of the smear of the two adjacent cathode carbon blocks A refractory wallboard is placed, and the refractory wallboard is made of magnesium aluminate spinel brick. The refractory wall panels are placed in a direction parallel to the length of the cathode carbon block, the width of which is less than the width between the longitudinal projections of the adjacent two cathode carbon block edges, and the length and the cathode carbon block edge The lengthwise projections are of equal length, and the upper surface of these refractory wallboards is 5 cm above the upper surface of the cathode carbon block lengthwise projection.
在每两个相邻阴极碳块之间, 耐火材料墙板与相邻两个阴极碳块边部的长度方向凸起构 成一个整体长度方向凸起, 该整体长度方向凸起的横截面为矩形和梯形的复合形状。 每个阴 极碳块上, 该整体长度方向凸起的数量为 8个, 除阳极中缝下边两个整体长度方向凸起之间 的距离为 20cm外, 其它整体长度方向凸起之间的距离为 18cm。  Between each two adjacent cathode carbon blocks, the refractory wall plate and the adjacent two cathode carbon block edges are longitudinally convex to form an integral length direction protrusion, and the overall length direction convex cross section is rectangular And the complex shape of the trapezoid. On each cathode carbon block, the number of protrusions in the overall length direction is eight, and the distance between the protrusions of the other overall length directions is 20 cm except for the distance between the protrusions of the two whole length directions on the lower side of the anode. .
实施例 4 Example 4
本发明的铝电解槽结构如图 2、 图 8、 图 11所示, 在阴极碳块上加工与阴极碳块的长度 方向相垂直的凸起, 称为宽度方向凸起。  The aluminum electrolytic cell structure of the present invention is shown in Fig. 2, Fig. 8, and Fig. 11, and a projection which is perpendicular to the longitudinal direction of the cathode carbon block is formed on the cathode carbon block, and is called a width direction convex.
紧靠电解槽出铝端的阴极碳块的靠近出铝口的边部不加工凸起。  The edge of the cathode carbon block immediately adjacent to the aluminum outlet of the electrolytic cell is not machined to the edge of the aluminum outlet.
每个阴极碳块上, 每两个宽度方向凸起之间的距离为 30cm, 宽度方向凸起的高度为 14cm, 宽度为 24cm, 长度与阴极碳块的宽度相一致。 每个宽度方向凸起中间沿阴极碳块宽 度方向镶嵌耐火材料墙板, 耐火材料墙板为氮碳化硅耐火板, 所镶嵌的耐火材料墙板宽度为 8cm, 高度与宽度方向凸起的高度相一致, 长度与宽度方向凸起的长度相一致。  On each cathode carbon block, the distance between each of the two widthwise projections is 30 cm, the width of the widthwise projection is 14 cm, the width is 24 cm, and the length coincides with the width of the cathode carbon block. Each of the width direction protrusions is inlaid with a refractory wall panel along the width of the cathode carbon block. The refractory wall panel is a nitrogen silicon carbide refractory board, and the refractory wall panel is inlaid with a width of 8 cm, and the height and the height of the width direction are convex. Consistently, the length coincides with the length of the bulge in the width direction.
宽度方向凸起的横截面为矩形。  The cross section in the width direction is a rectangle.
实施例 5 Example 5
本发明的铝电解槽结构如图 2、 图 8、 图 9所示, 在阴极碳块上加工与阴极碳块的长度方 向相垂直的凸起, 称为宽度方向凸起。  The aluminum electrolytic cell structure of the present invention is shown in Fig. 2, Fig. 8, and Fig. 9, and a projection which is perpendicular to the longitudinal direction of the cathode carbon block is formed on the cathode carbon block, and is called a width direction convex.
紧靠电解槽出铝端的阴极碳块的靠近出铝口的边部不加工凸起。  The edge of the cathode carbon block immediately adjacent to the aluminum outlet of the electrolytic cell is not machined to the edge of the aluminum outlet.
每个阴极碳块上, 每两个宽度方向凸起之间的距离为 40cm, 宽度方向凸起的高度为 18cm, 宽度为 30cm, 长度小于阴极碳块的宽度 4cm。 每个宽度方向凸起中间沿阴极碳块宽 度方向镶嵌耐火材料墙板,耐火材料墙板为高密度镁砖, 高密度镁砖的体积密度为 2. 8g/cm3, 所镶嵌的耐火材料墙板宽度为 10cm, 高度比宽度方向凸起高 3cm, 长度小于宽度方向凸起的 长度 7cm, 在耐火材料墙板的两端再镶嵌碳砖, 使镶嵌的耐火材料墙板与碳砖的长度之和与 宽度方向凸起的长度一致。 On each cathode carbon block, the distance between each of the two widthwise projections was 40 cm, the width of the widthwise projections was 18 cm, the width was 30 cm, and the length was less than the width of the cathode carbon block of 4 cm. Each width direction is convex along the middle of the cathode carbon block width The refractory wall panel is inlaid with refractory wallboard, the refractory wallboard is high density magnesia brick, the bulk density of the high density magnesia brick is 2. 8g/cm 3 , the inlaid refractory wallboard has a width of 10cm, and the height is convex than the width direction. The height is 3cm, the length is less than the length of the convexity in the width direction of 7cm, and carbon bricks are further embedded at both ends of the refractory wallboard, so that the sum of the lengths of the inlaid refractory wallboard and the carbon brick is consistent with the length of the widthwise convex.
宽度方向凸起的横截面是梯形。  The cross section in the width direction is trapezoidal.
实施例 6 Example 6
本发明的铝电解槽结构如图 2、 图 8、 图 10所示, 在阴极碳块上加工与阴极碳块的长度 方向相垂直的凸起, 称为宽度方向凸起。  The aluminum electrolytic cell structure of the present invention is shown in Fig. 2, Fig. 8, and Fig. 10, and a projection which is perpendicular to the longitudinal direction of the cathode carbon block is formed on the cathode carbon block, and is called a width direction convex.
紧靠电解槽出铝端的阴极碳块的靠近出铝口的边部不加工凸起。  The edge of the cathode carbon block immediately adjacent to the aluminum outlet of the electrolytic cell is not machined to the edge of the aluminum outlet.
每个阴极碳块上, 每两个宽度方向凸起之间的距离为 20cm, 宽度方向凸起的高度为 10cm, 宽度为 18cm, 长度小于阴极碳块的宽度 6cm。 每个宽度方向凸起中间沿阴极碳块宽 度方向镶嵌耐火材料墙板, 耐火材料墙板为镁铝尖晶石板, 所镶嵌的耐火材料墙板宽度为 5cm, 高度比宽度方向凸起高度 5cm, 长度小于宽度方向凸起的长度 10cm, 在耐火材料墙板 的两端再镶嵌碳砖, 使镶嵌的耐火材料墙板与碳砖的长度之和与宽度方向凸起的长度一致。  On each cathode carbon block, the distance between each of the two widthwise projections was 20 cm, the height of the projections in the width direction was 10 cm, the width was 18 cm, and the length was less than the width of the cathode carbon block of 6 cm. Refractory wallboard is embedded in the width direction of the cathode carbon block in the middle of each width direction. The refractory wallboard is a magnesium-aluminum spinel board. The width of the refractory wallboard is 5cm, and the height is 5cm higher than the width. The length is less than the length of the convexity in the width direction of 10 cm, and carbon bricks are further embedded at both ends of the refractory wallboard, so that the sum of the lengths of the inlaid refractory wallboard and the carbon bricks coincides with the length of the convexity in the width direction.
宽度方向凸起的横截面是矩形和梯形的复合形状。  The cross section in the width direction is a composite shape of a rectangle and a trapezoid.
实施例 7 Example 7
本发明的铝电解槽的结构如图 3、 图 11所示, 在阴极碳块上边部同时加工长度方向凸起 和宽度方向凸起。  The structure of the aluminum electrolytic cell of the present invention is as shown in Figs. 3 and 11, and the longitudinal direction projection and the width direction projection are simultaneously processed on the upper side portion of the cathode carbon block.
紧靠电解槽出铝端的阴极碳块的靠近出铝口的边部不加工凸起。  The edge of the cathode carbon block immediately adjacent to the aluminum outlet of the electrolytic cell is not machined to the edge of the aluminum outlet.
长度方向凸起的高度为 14cm, 宽度为 10cm, 位于每个阴极碳块沿长度方向的边部, 且 该长度方向凸起的外侧表面与阴极碳块边缘的水平距离为 2cm, 在砌筑电解槽时, 两个相邻 阴极碳块的中缝用碳素捣固糊捣固连接, 捣固糊的高度与阴极碳块的高度相等, 然后在两个 相邻阴极碳块捣固糊的上表面安放一条耐火材料墙板, 该耐火材料墙板的材料为氮碳化硅, 这些耐火材料墙板沿与阴极碳块的长度方向相平行的方向安放, 其宽度比相邻两个阴极碳块 边部的长度方向凸起之间的宽度小 2mm, 长度与阴极碳块边部长度方向凸起长度相等, 这些 耐火材料墙板的上表面与阴极碳块边部长度方向凸起上表面高度一样。  The length of the protrusion in the longitudinal direction is 14cm, the width is 10cm, and it is located at the side of each cathode carbon block along the length direction, and the horizontal distance between the outer surface of the longitudinal direction convex and the edge of the cathode carbon block is 2cm, in the masonry electrolysis In the groove, the middle slits of two adjacent cathode carbon blocks are sturdy and connected by carbon mash, the height of the tamping paste is equal to the height of the cathode carbon block, and then the upper surface of the smear of the two adjacent cathode carbon blocks A refractory wallboard is placed, the material of the refractory wallboard is nitrogen oxycarbide, and the refractory wallboard is placed in a direction parallel to the length of the cathode carbon block, and the width is wider than the adjacent two cathode carbon block edges. The width between the lengthwise projections is 2 mm, and the length is equal to the length of the cathode carbon block side length. The upper surface of the refractory wallboard is the same height as the convex upper surface of the cathode carbon block side.
在每两个相邻阴极碳块之间, 耐火材料墙板与相邻两个阴极碳块边部的长度方向凸起构 成一个整体长度方向凸起, 该整体长度方向凸起的横截面为矩形。 每个阴极碳块上, 该整体 长度方向凸起的数量为 5个, 除阳极中缝下边两个整体长度方向凸起之间的距离为 15cm夕卜, 其它整体长度方向凸起之间的距离为 12cm。  Between each two adjacent cathode carbon blocks, the refractory wall plate and the adjacent two cathode carbon block edges are longitudinally convex to form an integral length direction protrusion, and the overall length direction convex cross section is rectangular . On each cathode carbon block, the number of protrusions in the overall length direction is five, except that the distance between the protrusions of the two whole length directions of the lower side of the anode is 15 cm, and the distance between the protrusions of the other overall length direction is 12cm.
宽度方向凸起位于上述的两个整体长度方向凸起之间。 宽度方向凸起与阴极碳块为一个 整体, 在每个阴极碳块上, 宽度方向凸起与其相邻的整体长度方向凸起之间的距离为 8cm。 对于一个整体电解槽而言, 位于出铝口端的阴极碳块边部不设置宽度方向凸起。 与上述的整 体长度方向凸起相似, 宽度方向凸起的横截面为矩形, 宽度方向凸起的宽度为 25cm。 每个宽 度方向凸起中间沿阴极碳块宽度方向镶嵌耐火材料墙板, 耐火材料墙板为氮碳化硅耐火板。 实施例 8 The width direction projection is located between the two integral lengthwise projections described above. The width direction is convex and the cathode carbon block is one Overall, on each cathode carbon block, the distance between the width direction projection and its adjacent integral length direction projection was 8 cm. For an integral electrolytic cell, the edge of the cathode carbon block located at the end of the aluminum outlet is not provided with a widthwise projection. Similar to the above-described overall lengthwise projection, the widthwise convex cross section is rectangular, and the widthwise convex width is 25 cm. Each of the width direction protrusions is inlaid with a refractory wall panel along the width of the cathode carbon block, and the refractory wall panel is a nitrogen silicon carbide refractory board. Example 8
本发明的铝电解槽的结构如图 3、 图 9所示, 在阴极碳块上边部同时加工长度方向凸起 和宽度方向凸起。  The structure of the aluminum electrolytic cell of the present invention is as shown in Figs. 3 and 9, and the longitudinal direction projection and the width direction projection are simultaneously processed on the upper side of the cathode carbon block.
紧靠电解槽出铝端的阴极碳块的靠近出铝口的边部不加工凸起。  The edge of the cathode carbon block immediately adjacent to the aluminum outlet of the electrolytic cell is not machined to the edge of the aluminum outlet.
长度方向凸起的高度为 18cm, 宽度为 15cm, 位于每个阴极碳块沿长度方向的边部, 且 该长度方向凸起的外侧表面与阴极碳块边缘的水平距离为 3cm, 在砌筑电解槽时, 两个相邻 阴极碳块的中缝用碳素捣固糊捣固连接, 捣固糊的高度与阴极碳块的高度相等, 然后在两个 相邻阴极碳块捣固糊的上表面安放一条耐火材料墙板,该耐火材料墙板的材料为高密度镁砖, 高密度镁砖的体积密度为 2. 8g/cm3。 这些耐火材料墙板沿与阴极碳块的长度方向相平行的方 向安放, 其宽度比相邻两个阴极碳块边部的长度方向凸起之间的宽度小 3mm, 长度与阴极碳 块边部长度方向凸起长度相等, 这些耐火材料墙板的上表面高于阴极碳块长度方向凸起的上 表面 3cm The length of the protrusion in the longitudinal direction is 18 cm and the width is 15 cm, which is located at the side of each cathode carbon block along the length direction, and the horizontal distance between the outer surface of the lengthwise convex portion and the edge of the cathode carbon block is 3 cm, in the masonry electrolysis In the groove, the middle slits of two adjacent cathode carbon blocks are sturdy and connected by carbon mash, the height of the tamping paste is equal to the height of the cathode carbon block, and then the upper surface of the smear of the two adjacent cathode carbon blocks The granules of the high-density magnesia bricks having a bulk density of 2. 8 g / cm 3 . These refractory wall panels are placed in a direction parallel to the length of the cathode carbon block, the width of which is 3 mm smaller than the width between the longitudinal projections of the adjacent two cathode carbon block edges, and the length and the cathode carbon block edge. The longitudinal direction of the bulge is equal, and the upper surface of the refractory wallboard is higher than the upper surface of the cathode carbon block.
在每两个相邻阴极碳块之间, 耐火材料墙板与相邻两个阴极碳块边部的长度方向凸起构 成一个整体长度方向凸起, 该整体长度方向凸起的横截面为梯形。 每个阴极碳块上, 该整体 长度方向凸起的数量为 2个, 每两个整体长度方向凸起之间的距离为 15cm。  Between each two adjacent cathode carbon blocks, the refractory wall plate and the adjacent two cathode carbon block edges are longitudinally convex to form an integral length direction protrusion, and the overall length direction convex cross section is trapezoidal . On each of the cathode carbon blocks, the number of the overall lengthwise projections was two, and the distance between the projections of the two integral lengthwise directions was 15 cm.
宽度方向凸起位于上述的两个整体长度方向凸起之间。 宽度方向凸起与阴极碳块为一个 整体, 在每个阴极碳块上, 宽度方向凸起与其相邻的整体长度方向凸起之间的距离为 10cm。 对于一个整体电解槽而言, 位于出铝口端的阴极碳块边部不设置宽度方向凸起。 与上述的整 体长度方向凸起相似, 宽度方向凸起的横截面为梯形, 宽度方向凸起的宽度为 35cm。 每个宽 度方向凸起中间沿阴极碳块宽度方向镶嵌耐火材料墙板, 耐火材料墙板为体积密度为 2. 8g/cm3的高密度镁砖。 The width direction projection is located between the two integral lengthwise projections described above. The width direction projection is integral with the cathode carbon block, and on each cathode carbon block, the distance between the width direction projection and its adjacent integral length direction projection is 10 cm. For an integral electrolytic cell, the edge of the cathode carbon block located at the end of the aluminum outlet is not provided with a widthwise projection. Similar to the above-described overall lengthwise projection, the widthwise convex cross section is trapezoidal, and the widthwise convex width is 35 cm. The refractory wallboard is a high-density magnesia brick having a bulk density of 2. 8 g/cm 3 , in the direction of the width of the cathode carbon block.
实施例 9 Example 9
本发明的铝电解槽的结构如图 3、 图 10所示, 在阴极碳块上边部同时加工长度方向凸起 和宽度方向凸起。  The structure of the aluminum electrolytic cell of the present invention is as shown in Figs. 3 and 10, and the longitudinal direction projections and the widthwise projections are simultaneously processed on the upper side portions of the cathode carbon block.
紧靠电解槽出铝端的阴极碳块的靠近出铝口的边部不加工凸起。  The edge of the cathode carbon block immediately adjacent to the aluminum outlet of the electrolytic cell is not machined to the edge of the aluminum outlet.
长度方向凸起的高度为 10cm, 宽度为 5cm, 位于每个阴极碳块沿长度方向的边部, 且该 长度方向凸起的外侧表面与阴极碳块边缘的水平距离为 lcm, 在砌筑电解槽时, 两个相邻阴 极碳块的中缝用碳素捣固糊捣固连接, 捣固糊的高度与阴极碳块的高度相等, 然后在两个相 邻阴极碳块捣固糊的上表面安放一条耐火材料墙板,该耐火材料墙板的材料为镁铝尖晶石砖。 这些耐火材料墙板沿与阴极碳块的长度方向相平行的方向安放, 其宽度比相邻两个阴极碳块 边部的长度方向凸起之间的宽度小 lmm, 长度与阴极碳块边部长度方向凸起长度相等, 这些 耐火材料墙板的上表面高于阴极碳块长度方向凸起的上表面 5cm。 The length of the protrusion in the longitudinal direction is 10 cm, the width is 5 cm, and it is located at the side of each cathode carbon block along the length direction, and the horizontal distance between the outer surface of the lengthwise convex portion and the edge of the cathode carbon block is 1 cm, in the masonry electrolysis When slotting, two adjacent yin The middle seam of the carbon block is tamped with a carbon tamping paste, the height of the tamping paste is equal to the height of the cathode carbon block, and then a refractory wall panel is placed on the upper surface of the two adjacent cathode carbon block tamping. The material of the refractory wallboard is magnesium aluminum spinel brick. The refractory wall panels are placed in a direction parallel to the length of the cathode carbon block, the width of which is less than the width between the longitudinal projections of the adjacent two cathode carbon block edges, and the length and the cathode carbon block edge The lengthwise projections are of equal length, and the upper surface of these refractory wallboards is 5 cm above the upper surface of the cathode carbon block lengthwise projection.
在每两个相邻阴极碳块之间, 耐火材料墙板与相邻两个阴极碳块边部的长度方向凸起构 成一个整体长度方向凸起, 该整体长度方向凸起的横截面为矩形和梯形的复合形状。 每个阴 极碳块上, 该整体长度方向凸起的数量为 8个, 除阳极中缝下边两个整体长度方向凸起之间 的距离为 20cm外, 其它整体长度方向凸起之间的距离为 18cm。  Between each two adjacent cathode carbon blocks, the refractory wall plate and the adjacent two cathode carbon block edges are longitudinally convex to form an integral length direction protrusion, and the overall length direction convex cross section is rectangular And the complex shape of the trapezoid. On each cathode carbon block, the number of protrusions in the overall length direction is eight, and the distance between the protrusions of the other overall length directions is 20 cm except for the distance between the protrusions of the two whole length directions on the lower side of the anode. .
宽度方向凸起位于上述的两个整体长度方向凸起之间。 宽度方向凸起与阴极碳块为一个 整体, 在每个阴极碳块上, 宽度方向凸起与其相邻的整体长度方向凸起之间的距离为 5cm。 对于一个整体电解槽而言, 位于出铝口端的阴极碳块边部不设置宽度方向凸起。 与上述的整 体长度方向凸起相似, 宽度方向凸起的横截面为矩形和梯形的复合形状, 宽度方向凸起的宽 度为 15cm。每个宽度方向凸起中间沿阴极碳块宽度方向镶嵌耐火材料墙板, 耐火材料墙板为 镁铝尖晶石板。  The width direction projection is located between the two integral lengthwise projections described above. The width direction projection is integral with the cathode carbon block, and on each cathode carbon block, the distance between the width direction projection and its adjacent integral length direction projection is 5 cm. For an integral electrolytic cell, the edge of the cathode carbon block located at the end of the aluminum outlet is not provided with a widthwise projection. Similar to the above-described overall lengthwise projection, the cross section in the width direction is a composite shape of a rectangle and a trapezoid, and the width of the projection in the width direction is 15 cm. Refractory wall panels are embedded in the width direction of the cathode carbon block in the middle of each width direction convex, and the refractory wall plate is a magnesium aluminum spinel plate.

Claims

权 利 要 求 书 Claim
1、一种能减缓阴极凸起磨蚀的新型阴极结构铝电解槽, 其特征在于在每个阴极碳块上沿 长度方向的边部加工有凸起结构, 称为长度方向凸起; 或在阴极碳块上部加工与阴极碳块的 长度方向相垂直的凸起, 称为宽度方向凸起; 或在阴极碳块上边部同时加工长度方向凸起和 宽度方向凸起; 三种结构形式如下: 1. A novel cathode structure aluminum electrolytic cell capable of mitigating cathode protrusion abrasion, characterized in that a convex structure is formed on a side of a length direction of each cathode carbon block, which is called a longitudinal direction protrusion; or a cathode The upper part of the carbon block is perpendicular to the longitudinal direction of the cathode carbon block, and is called a width direction protrusion; or the longitudinal direction protrusion and the width direction protrusion are simultaneously processed on the upper side of the cathode carbon block; the three structural forms are as follows:
( 1 ) 在每个阴极碳块上沿长度方向的边部加工有长度方向凸起  (1) A longitudinal projection is processed on the side of each of the cathode carbon blocks along the length direction
长度方向凸起的高度为 10〜18cm, 宽度为 5〜15cm, 位于每个阴极碳块沿长度方向的边 部, 且该长度方向凸起的外侧表面与阴极碳块边缘的水平距离为 l〜3cm, 两个相邻阴极碳块 的中缝用碳素捣固糊捣固连接, 捣固糊的高度与阴极碳块的高度相等, 在两个相邻阴极碳块 捣固糊的上表面安放一条耐火材料墙板, 在每两个相邻阴极碳块之间, 耐火材料墙板与相邻 两个阴极碳块边部的长度方向凸起构成一个整体长度方向凸起;  The length of the protrusion in the longitudinal direction is 10 to 18 cm, and the width is 5 to 15 cm, which is located at the side of each cathode carbon block along the length direction, and the horizontal distance between the outer surface of the longitudinally convex portion and the edge of the cathode carbon block is l~ 3cm, the middle slits of two adjacent cathode carbon blocks are sturdy and connected with carbon slag, the height of the tamping paste is equal to the height of the cathode carbon block, and one of the upper surfaces of two adjacent cathode carbon block tamping pastes is placed. Refractory wallboard, between each two adjacent cathode carbon blocks, the refractory wall panel and the longitudinal direction of the adjacent two cathode carbon block edges form an overall lengthwise protrusion;
(2) 在阴极碳块上部同时加工长度方向凸起和宽度方向凸起  (2) Machining the longitudinal direction projection and the width direction projection simultaneously on the upper portion of the cathode carbon block
宽度方向凸起位于上述的两个整体长度方向凸起之间, 宽度方向凸起与阴极碳块为一个 整体, 在每个阴极碳块上, 宽度方向凸起与其相邻的整体长度方向凸起之间的距离为 5〜 10cm;  The width direction protrusion is located between the two integral length direction protrusions described above, and the width direction protrusion is integral with the cathode carbon block. On each cathode carbon block, the width direction protrusion and its adjacent overall length direction protrusion The distance between them is 5~10cm;
( 3 ) 在阴极碳块上部加工宽度方向凸起  (3) processing the width direction convex on the upper part of the cathode carbon block
每个阴极碳块上, 每两个宽度方向凸起之间的距离为 20〜40cm, 宽度方向凸起的高度为 10〜18cm, 宽度为 18〜30cm,长度与阴极碳块的宽度相一致或小于阴极碳块的宽度 2〜6cm。  On each cathode carbon block, the distance between each of the two widthwise projections is 20 to 40 cm, the width of the widthwise projection is 10 to 18 cm, the width is 18 to 30 cm, and the length is consistent with the width of the cathode carbon block or It is smaller than the width of the cathode carbon block by 2 to 6 cm.
2、 按照权利要求 1所述的能减缓阴极凸起磨蚀的新型阴极结构铝电解槽, 其特征在于结 构形式(1 ) 中, 耐火材料墙板的材料为氮碳化硅或高密度镁砖或镁铝尖晶石砖, 其中高密度 镁砖的体积密度为 2. 6〜3. 0g/cm3, 耐火材料墙板沿与阴极碳块的长度方向相平行的方向安 放, 其宽度比相邻两个阴极碳块边部的长度方向凸起之间的宽度小 l〜3mm, 长度与阴极碳 块边部长度方向凸起长度相等, 耐火材料墙板的上表面与阴极碳块边部长度方向凸起上表面 高度一样或高于阴极碳块长度方向凸起的上表面 l〜5cm。 2. A novel cathode structure aluminum electrolytic cell capable of mitigating cathode protrusion abrasion according to claim 1, wherein in the structural form (1), the material of the refractory wallboard is nitrogen silicon carbide or high density magnesium brick or magnesium. The aluminum stellite brick, wherein the bulk density of the high-density magnesia brick is 2. 6~ 3 . 0g/cm 3 , the refractory wall panel is placed in a direction parallel to the length direction of the cathode carbon block, and the width is adjacent to the adjacent two The width between the protrusions in the longitudinal direction of the side of the cathode carbon block is small by 1 to 3 mm, and the length is equal to the length of the protrusion of the side of the cathode carbon block. The upper surface of the refractory wallboard and the length of the side of the cathode carbon block are convex. The upper surface has the same height or higher than the upper surface of the cathode carbon block in the longitudinal direction of l~5 cm.
3、 按照权利要求 1所述的能减缓阴极凸起磨蚀的新型阴极结构铝电解槽, 其特征在于结 构形式(1 ) 中, 整体长度方向凸起的横截面为矩形或梯形或矩形和梯形的复合形状, 每个阴 极碳块上, 该整体长度方向凸起的数量为 2〜8个, 当整体长度方向凸起数为 2个时, 每两个 整体长度方向凸起之间的距离为 10〜20cm, 当整体长度方向凸起数为 3〜8个时, 除阳极中 缝下边两个整体长度方向凸起之间的距离为 10〜20cm夕卜, 其它整体长度方向凸起之间的距 离为 5〜20cm。 3. A novel cathode structure aluminum electrolytic cell capable of mitigating cathode protrusion abrasion according to claim 1, characterized in that in the structural form (1), the overall lengthwise convex cross section is rectangular or trapezoidal or rectangular and trapezoidal. Composite shape, the number of protrusions in the overall length direction is 2 to 8 on each cathode carbon block, and when the number of protrusions in the whole length direction is 2, the distance between the protrusions of each of the two entire length directions is 10 ~20cm, when the number of protrusions in the overall length direction is 3~8, the distance between the protrusions of the two whole length directions except the lower side of the anode is 10~20cm, and the distance between the protrusions of other overall length directions The distance is 5~20cm.
4、 按照权利要求 1所述的能减缓阴极凸起磨蚀的新型阴极结构铝电解槽, 其特征在于结 构形式(2) 中, 宽度方向凸起的横截面为矩形或梯形或两者的组合, 宽度方向凸起的宽度为 15〜35cm, 每个宽度方向凸起中间沿阴极碳块宽度方向镶嵌耐火材料墙板, 耐火材料墙板为 氮碳化硅耐火板或高密度镁砖或镁铝尖晶石板, 其中高密度镁砖的体积密度为 2. 6〜 3. 0g/cm  4. A novel cathode structure aluminum electrolytic cell capable of mitigating cathode protrusion abrasion according to claim 1, wherein in the structural form (2), the widthwise convex cross section is rectangular or trapezoidal or a combination of the two. The width of the protrusion in the width direction is 15 to 35 cm, and the refractory wall panel is inlaid along the width of the cathode carbon block in the middle of each width direction convex, and the refractory wall board is a nitrogen silicon carbide refractory board or a high density magnesia brick or a magnesium aluminum spinel. 5〜 3. 0g/厘米。 The slab, wherein the bulk density of the high-density magnesia is 2. 6~ 3. 0g / cm
5、按照权利要求 1所述的能减缓阴极凸起磨蚀的新型阴极结构铝电解槽, 其特征在于结 构形式(3 ) 中, 每个宽度方向凸起中间沿阴极碳块宽度方向镶嵌耐火材料墙板, 耐火材料墙 板为氮碳化硅耐火板或高密度镁砖或镁铝尖晶石板,所镶嵌的耐火材料墙板宽度为 5〜10cm, 高度与宽度方向凸起的高度相一致或高于宽度方向凸起 l〜5cm,长度与宽度方向凸起的长度 相一致, 或小于宽度方向凸起的长度 4〜10cm。  5. A novel cathode structure aluminum electrolytic cell capable of mitigating cathode protrusion abrasion according to claim 1, wherein in the structural form (3), a refractory wall is embedded in the width direction of the cathode carbon block in the middle of each width direction. The refractory wallboard is a nitrogen silicon carbide refractory board or a high-density magnesia brick or a magnesia-alumina spinel board. The refractory wall panel is inlaid with a width of 5 to 10 cm, and the height is consistent with or higher than the height of the width direction. The width direction is convex by 1 to 5 cm, and the length coincides with the length of the protrusion in the width direction, or is smaller than the length of the protrusion in the width direction of 4 to 10 cm.
6、按照权利要求 5所述的能减缓阴极凸起磨蚀的新型阴极结构铝电解槽, 其特征在于当 镶嵌的耐火材料墙板的长度小于宽度方向凸起时, 在耐火材料墙板的两端再镶嵌碳砖, 使镶 嵌的耐火材料墙板与碳砖的长度之和与宽度方向凸起的长度一致。  6. A novel cathode structure aluminum electrolytic cell capable of mitigating cathode protrusion abrasion according to claim 5, wherein when the length of the inlaid refractory wallboard is less than the width direction, at both ends of the refractory wallboard The carbon brick is re-inlaid so that the sum of the lengths of the inlaid refractory wallboard and the carbon brick coincides with the length of the widthwise projection.
PCT/CN2010/070947 2009-12-30 2010-03-10 Aluminum electrolytic cell having cathode structure with abrasion decelerated bulges on cathode WO2011079548A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN2009102488841A CN101724863B (en) 2009-12-30 2009-12-30 Aluminum electrolytic tank with novel cathode structure capable of reducing protruding abrasion of cathode
CN200910248884.1 2009-12-30

Publications (1)

Publication Number Publication Date
WO2011079548A1 true WO2011079548A1 (en) 2011-07-07

Family

ID=42446397

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2010/070947 WO2011079548A1 (en) 2009-12-30 2010-03-10 Aluminum electrolytic cell having cathode structure with abrasion decelerated bulges on cathode

Country Status (2)

Country Link
CN (1) CN101724863B (en)
WO (1) WO2011079548A1 (en)

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9312522B2 (en) 2012-10-18 2016-04-12 Ambri Inc. Electrochemical energy storage devices
US9502737B2 (en) 2013-05-23 2016-11-22 Ambri Inc. Voltage-enhanced energy storage devices
US9520618B2 (en) 2013-02-12 2016-12-13 Ambri Inc. Electrochemical energy storage devices
US9735450B2 (en) 2012-10-18 2017-08-15 Ambri Inc. Electrochemical energy storage devices
US9893385B1 (en) 2015-04-23 2018-02-13 Ambri Inc. Battery management systems for energy storage devices
US10181800B1 (en) 2015-03-02 2019-01-15 Ambri Inc. Power conversion systems for energy storage devices
US10270139B1 (en) 2013-03-14 2019-04-23 Ambri Inc. Systems and methods for recycling electrochemical energy storage devices
US10541451B2 (en) 2012-10-18 2020-01-21 Ambri Inc. Electrochemical energy storage devices
US10608212B2 (en) 2012-10-16 2020-03-31 Ambri Inc. Electrochemical energy storage devices and housings
US10637015B2 (en) 2015-03-05 2020-04-28 Ambri Inc. Ceramic materials and seals for high temperature reactive material devices
US11211641B2 (en) 2012-10-18 2021-12-28 Ambri Inc. Electrochemical energy storage devices
US11387497B2 (en) 2012-10-18 2022-07-12 Ambri Inc. Electrochemical energy storage devices
US11411254B2 (en) 2017-04-07 2022-08-09 Ambri Inc. Molten salt battery with solid metal cathode
US11721841B2 (en) 2012-10-18 2023-08-08 Ambri Inc. Electrochemical energy storage devices
US11909004B2 (en) 2013-10-16 2024-02-20 Ambri Inc. Electrochemical energy storage devices
US11929466B2 (en) 2016-09-07 2024-03-12 Ambri Inc. Electrochemical energy storage devices

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101880895A (en) * 2010-06-13 2010-11-10 冯乃祥 Aluminum cell with two rows of mutually staggered bulges arranged on same cathode block
DE102011001834A1 (en) * 2010-09-30 2012-04-05 Guangxi Qiangqiang Carbon Co. Ltd Zuoyixiang Novel combined graphitized heterotyped cathode for the recovery of aluminum and its graphitized cathode barrier block
CN102719850A (en) * 2012-06-29 2012-10-10 东北大学 Method for nesting cylindrical bump on upper surface of cathode carbon block and base body

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4631121A (en) * 1986-02-06 1986-12-23 Reynolds Metals Company Alumina reduction cell
US4919782A (en) * 1989-02-21 1990-04-24 Reynolds Metals Company Alumina reduction cell
US20030010628A1 (en) * 1999-10-26 2003-01-16 Vittorio De Nora Low temperature operating cell for the electrowinning of aluminium
CN101413136A (en) * 2008-10-10 2009-04-22 冯乃祥 Novel cathode structured aluminum cell with longitudinal and transversal wave damping functions
CN201305634Y (en) * 2008-10-10 2009-09-09 冯乃祥 Novel cathode-structure aluminum electrolytic cell with functions of longitudinal wave reduction and horizontal wave reduction

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4631121A (en) * 1986-02-06 1986-12-23 Reynolds Metals Company Alumina reduction cell
US4919782A (en) * 1989-02-21 1990-04-24 Reynolds Metals Company Alumina reduction cell
US20030010628A1 (en) * 1999-10-26 2003-01-16 Vittorio De Nora Low temperature operating cell for the electrowinning of aluminium
CN101413136A (en) * 2008-10-10 2009-04-22 冯乃祥 Novel cathode structured aluminum cell with longitudinal and transversal wave damping functions
CN201305634Y (en) * 2008-10-10 2009-09-09 冯乃祥 Novel cathode-structure aluminum electrolytic cell with functions of longitudinal wave reduction and horizontal wave reduction

Cited By (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10608212B2 (en) 2012-10-16 2020-03-31 Ambri Inc. Electrochemical energy storage devices and housings
US11387497B2 (en) 2012-10-18 2022-07-12 Ambri Inc. Electrochemical energy storage devices
US11721841B2 (en) 2012-10-18 2023-08-08 Ambri Inc. Electrochemical energy storage devices
US9312522B2 (en) 2012-10-18 2016-04-12 Ambri Inc. Electrochemical energy storage devices
US11211641B2 (en) 2012-10-18 2021-12-28 Ambri Inc. Electrochemical energy storage devices
US9735450B2 (en) 2012-10-18 2017-08-15 Ambri Inc. Electrochemical energy storage devices
US9825265B2 (en) 2012-10-18 2017-11-21 Ambri Inc. Electrochemical energy storage devices
US10541451B2 (en) 2012-10-18 2020-01-21 Ambri Inc. Electrochemical energy storage devices
US11611112B2 (en) 2012-10-18 2023-03-21 Ambri Inc. Electrochemical energy storage devices
US11196091B2 (en) 2012-10-18 2021-12-07 Ambri Inc. Electrochemical energy storage devices
US9728814B2 (en) 2013-02-12 2017-08-08 Ambri Inc. Electrochemical energy storage devices
US9520618B2 (en) 2013-02-12 2016-12-13 Ambri Inc. Electrochemical energy storage devices
US10270139B1 (en) 2013-03-14 2019-04-23 Ambri Inc. Systems and methods for recycling electrochemical energy storage devices
US10297870B2 (en) 2013-05-23 2019-05-21 Ambri Inc. Voltage-enhanced energy storage devices
US9502737B2 (en) 2013-05-23 2016-11-22 Ambri Inc. Voltage-enhanced energy storage devices
US9559386B2 (en) 2013-05-23 2017-01-31 Ambri Inc. Voltage-enhanced energy storage devices
US11909004B2 (en) 2013-10-16 2024-02-20 Ambri Inc. Electrochemical energy storage devices
US10566662B1 (en) 2015-03-02 2020-02-18 Ambri Inc. Power conversion systems for energy storage devices
US10181800B1 (en) 2015-03-02 2019-01-15 Ambri Inc. Power conversion systems for energy storage devices
US11289759B2 (en) 2015-03-05 2022-03-29 Ambri, Inc. Ceramic materials and seals for high temperature reactive material devices
US10637015B2 (en) 2015-03-05 2020-04-28 Ambri Inc. Ceramic materials and seals for high temperature reactive material devices
US11840487B2 (en) 2015-03-05 2023-12-12 Ambri, Inc. Ceramic materials and seals for high temperature reactive material devices
US9893385B1 (en) 2015-04-23 2018-02-13 Ambri Inc. Battery management systems for energy storage devices
US11929466B2 (en) 2016-09-07 2024-03-12 Ambri Inc. Electrochemical energy storage devices
US11411254B2 (en) 2017-04-07 2022-08-09 Ambri Inc. Molten salt battery with solid metal cathode

Also Published As

Publication number Publication date
CN101724863A (en) 2010-06-09
CN101724863B (en) 2012-07-04

Similar Documents

Publication Publication Date Title
WO2011079548A1 (en) Aluminum electrolytic cell having cathode structure with abrasion decelerated bulges on cathode
CN101432466B (en) Cathodes for aluminium electrolysis cell with non-planar slot design
CA2680087C (en) Aluminum electrolytic cells having profiled cathode carbon blocks
EP1146146B1 (en) Horizontal drained cathode surface with recessed grooves for aluminium electrowinning
CN101748436B (en) Prebaked anode aluminum electrolytic bath
WO2011082659A1 (en) Cathode with protrusion structure for aluminum electrolytic cell
WO2010040270A1 (en) Aluminum electrolytic cell with new type of cathode structure for shortening vertical fluctuations and horizontal fluctuations
CN103060848B (en) Aluminum electrolytic tank with artificial hearth
CN201049966Y (en) Abnormal structure cathode carbon block of aluminum electrolysis bath
CN101503809A (en) Novel energy-saving aluminum cell with chamfering grooving cathode
CN101892497A (en) Anode used for aluminum electrolysis
CN201313942Y (en) Pre-baked anode aluminum reduction cell above 400kA
WO2014098642A1 (en) Aluminium electrolysis cell cathode shunt design
CN201358306Y (en) Novel energy-saving aluminum electrolysis bath with chamfered and grooved cathode
CN201305634Y (en) Novel cathode-structure aluminum electrolytic cell with functions of longitudinal wave reduction and horizontal wave reduction
CA3148080C (en) Aluminium reduction cell with a heat insulated side lining
CN101949035B (en) Novel composite graphitized deformed cathode for aluminium electrolysis
JP2013536321A (en) Cathode, equipment for aluminum production and use of cathode in aluminum production
CN103403227A (en) Cathode assembly comprising a surface-profiled cathode block having variable groove depth
WO2013078746A1 (en) Aluminum reduction cell cathode structure that reduces voltage and improves current distribution
CN201793763U (en) Novel assembled graphitized special cathode for aluminium electrolysis
CN210657165U (en) Lining heat-insulating structure of acid-process alumina electrolytic cell and acid-process alumina electrolytic cell
CN101949037A (en) Building method of aluminum electrolysis cell
CA2354120C (en) Aluminium electrowinning cell with improved carbon cathode blocks
CA2811553A1 (en) Electrolytic cell for extracting aluminium

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 10840338

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 10840338

Country of ref document: EP

Kind code of ref document: A1