WO2013034024A1 - Aluminum electrolytic tank anode carbon block of irregularly-shaped structure with exhaust passage and preparation method thereof - Google Patents

Aluminum electrolytic tank anode carbon block of irregularly-shaped structure with exhaust passage and preparation method thereof Download PDF

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Publication number
WO2013034024A1
WO2013034024A1 PCT/CN2012/078394 CN2012078394W WO2013034024A1 WO 2013034024 A1 WO2013034024 A1 WO 2013034024A1 CN 2012078394 W CN2012078394 W CN 2012078394W WO 2013034024 A1 WO2013034024 A1 WO 2013034024A1
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WO
WIPO (PCT)
Prior art keywords
groove
carbon block
anode carbon
anode
hole
Prior art date
Application number
PCT/CN2012/078394
Other languages
French (fr)
Chinese (zh)
Inventor
冯乃祥
Original Assignee
沈阳北冶冶金科技有限公司
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
Priority claimed from CN201120330635XU external-priority patent/CN202359211U/en
Priority claimed from CN201110260656.3A external-priority patent/CN102345141B/en
Application filed by 沈阳北冶冶金科技有限公司 filed Critical 沈阳北冶冶金科技有限公司
Priority to US14/342,987 priority Critical patent/US20140224651A1/en
Publication of WO2013034024A1 publication Critical patent/WO2013034024A1/en

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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
    • C25C3/12Anodes
    • C25C3/125Anodes based on carbon

Definitions

  • the invention belongs to the technical field of aluminum electrolysis, and particularly relates to an anode carbon block of a profiled structure aluminum electrolysis cell with an exhaust passage and a preparation method thereof.
  • the CE method is the average cell voltage of aluminum electrolysis. It can be seen from this formula that for every 1% increase in the current efficiency of the cell, the DC power consumption can be reduced by about 150 kWh/t aluminum, and the aluminum output can be increased by 1%. By reducing 0.1 volts, the DC power consumption can be reduced by about 300 kWh/t aluminum.
  • the C0 2 gas generated on the surface of the anode bottom of the aluminum electrolytic cell can be quickly escaped from the surface of the anode bottom, and shortening the residence time of C0 2 in the electrolyte can greatly improve the current efficiency of the aluminum electrolytic cell.
  • the purpose is to make the anode gas energy generated under the anode bottom of the electrolytic cell bottom.
  • the ground escapes from the trench to achieve the purpose of reducing the secondary reaction between the anode gas and the aluminum.
  • the depth of the groove on the bottom of the anode of the electrolytic cell is 200 to 250 mm.
  • the groove is too shallow, the groove is completely immersed in the electrolyte melt during most of the anode working time, so that the stroke of the anode gas in the electrolyte melt is not shortened, and the resistance is not It is reduced, so its effect of increasing the current efficiency of the electrolytic cell or reducing the power consumption is not obvious.
  • anode technology including one anode guide rod of Li Wei et al., four steel claws, and four small anode aluminum electrolytic cells.
  • Anode technology patented technology of an anode guide rod, S steel claws and more than 4 small anodes invented by Feng Nai and Peng Jianping; if these patented technologies can be implemented industrially, they can improve the anode gas emission rate and improve The current efficiency of the electrolytic cell is beneficial, but it is actually found during operation that this single small anode technology is liable to cause the anode to fall off on the electrolytic cell.
  • the present invention provides a profiled structure aluminum electrolytic cell anode carbon block with an exhaust passage and a preparation method thereof, through a single anode carbon block carbon bowl in a carbon anode Grooves are disposed between the grooves and the grooves at the bottom of the anode carbon block through the through holes, so that the gas emissions generated by the anodes of the anode carbon block are uniform and uniform, and the effect of gas escape from the electrolyte on the fluctuation of the cathode aluminum liquid is reduced. It can avoid the anode falling off and can quickly discharge the gas from the surface of the anode bottom.
  • the anode side of the anode carbon block of the carbon anode of the profiled aluminum electrolytic cell with the exhaust passage of the invention is provided with chamfering, and one or two rows of carbon bowls are evenly distributed on the top surface, and each row of carbon bowls is along the anode carbon
  • the blocks are arranged vertically, and are composed of 3 to 5 carbon bowls; wherein the carbon bowls are provided with grooves, and the bottom of the anode carbon block is provided with grooves; wherein the bottom of the groove is provided with a through hole communicating with the groove at the bottom of the anode carbon block.
  • each of the grooves is provided with at least one through hole communicating with a groove corresponding to the groove.
  • the axis of the transverse groove is perpendicular to the longitudinal axis of the anode carbon block, and the axis of the transverse groove is located in the center of two adjacent carbon bowls, and both ends of the transverse groove are open to the chamfers on the two long sides of the anode carbon block.
  • the axis of the longitudinal groove is parallel to the axis of the anode carbon block; the longitudinal groove is located in the center of the adjacent two rows of carbon bowls, and both ends of the longitudinal groove are open to the chamfers on the two short sides of the anode carbon block.
  • the top of the trench is 20 ⁇ 50cm from the top of the anode carbon block, and the bottom of the trench is connected to the bottom surface of the anode carbon block, wherein the groove corresponding to the lateral groove is a lateral groove, and the longitudinal groove is The corresponding groove is a longitudinal groove, the length of the transverse groove is equal to the width of the anode carbon block, the length of the longitudinal groove is equal to the length of the anode carbon block, and the width of each groove is 1.0 to 3.5 cm.
  • the groove has a cross section of an inverted isosceles triangle or an inverted isosceles trapezoid, and the groove height is 3 to 10 cm; when the groove has an inverted isosceles triangle, the width of the top surface of the groove is 3 ⁇ 10cm ; when the cross section of the groove is an inverted isosceles trapezoid, the top surface width of the groove is 5 ⁇ 10cm, and the width of the bottom surface is 3 ⁇ 8cm.
  • the above-mentioned through hole is at the bottom of the groove, and its longitudinal axis is perpendicular to the bottom surface of the anode carbon block.
  • the above-mentioned through holes are divided into small through holes and large through holes, and the small through holes have a circular, elliptical, square or rectangular cross section, and the area is 3 to 18 cm 2 , wherein when the small through holes are square or rectangular in cross section The four corners of the square or rectangle are rounded; the large through hole has a rectangular cross section and an area of 18 to 500 cm 2 .
  • the through hole when the length of the through hole is the same as the length of the anode carbon block, the through hole is connected with the groove, and one anode carbon block is broken in the longitudinal direction to form two identical small anode carbon blocks.
  • the carbon anode of the profiled aluminum electrolytic cell with exhaust passage of the invention is composed of more than 20 monomers having the above-mentioned heterostructure anode carbon block, and the preparation method of the single anode carbon block is:
  • the anode carbon block green body is prepared by vibration molding or compression molding; when the vibration molding method is adopted, the lower surface of the upper weight in the vibration mode has a corresponding protrusion; when the molding method is used, the compression mold The lower surface of the upper core has a corresponding protrusion; a carbon bowl, a groove and a deep hole having a height of 20 to 50 cm are formed on the anode carbon block green body during vibration molding or press molding; After the blank is discharged from the mold and cooled, it is placed in a roasting furnace and fired at 1100 ⁇ 1300 °C to prepare an anode carbon block calcined body with a carbon bowl, a deep hole and a groove at the top; and then physically cut at the bottom of the anode carbon block calcined body.
  • the corresponding protrusion refers to the anode carbon block
  • the anode carbon block of the special-shaped aluminum electrolytic cell with the exhaust passage of the invention is provided with a cover plate on the groove before use, a lateral cover plate is arranged on the lateral groove, and the transverse cover plate is disposed on the lateral groove, the transverse cover plate
  • the length is the same as the width of the anode carbon block
  • the longitudinal cover is provided above the longitudinal groove, the longitudinal cover is on the longitudinal groove, and the length of the longitudinal cover is the same as the length of the anode carbon block;
  • the transverse cover and the longitudinal cover the longitudinal cover and the lateral cover are connected to form an integral structure, the cover is covered with cryolite powder, and then assembled to the anode claw of the aluminum electrolytic cell.
  • the above-mentioned cover plate is made of carbonaceous material or inorganic material or metal material, and the selected inorganic material may be refractory plate or refractory fiberboard, and the selected metal material is made of aluminum plate or iron plate; carbon block or refractory plate or refractory fiber board is selected.
  • the thickness of the cover plate is 5 ⁇ 20cm
  • the aluminum plate or the iron plate is used, the thickness of the aluminum plate or the iron plate is l ⁇ 4mm.
  • the iron plate can be perforated, and the upper surface of the hole is welded with a high mouth.
  • the electrolyte covered with the upper surface of the anode and the iron tube of the thickness of the alumina insulation material make it more advantageous for the anode gas to exit the tank.
  • the working principle of the anode carbon block of the carbon anode of the special-shaped aluminum electrolytic cell with the exhaust passage of the present invention is as follows: When performing aluminum electrolysis, most of the C0 2 gas generated on the bottom surface of the anode carbon block rises into the through hole through the groove. Then, the through hole is collected into the groove on the upper surface of the anode carbon block, enters into the cavity between the cover plate and the groove, and is discharged from the end of the cover plate or the upper iron pipe to the anode carbon through the cavity. Outside the block.
  • the anode carbon block of the special-shaped aluminum electrolytic cell with the exhaust passage of the invention has the characteristics of simple manufacturing process and high working efficiency. After the experiment, the anode carbon block can reduce the tank voltage, and the gas emissions generated by the anode are uniform and uniform, and the gas is The effect of the escape on the fluctuation of the cathode aluminum liquid is obviously reduced, which is beneficial to the improvement of the current efficiency, and avoids the falling off of the small anode carbon block, and has a good application prospect.
  • FIG. 1 is a schematic cross-sectional view showing a carbon anode single anode carbon block of a profiled aluminum electrolytic cell with an exhaust passage according to Embodiment 1 of the present invention
  • Figure 2 is a cross-sectional view taken along line A-A of Figure 1;
  • Figure 3 is a cross-sectional view taken along line B-B of Figure 1;
  • Figure 4 is a cross-sectional view taken along line C-C of Figure 1;
  • Figure 5 is a cross-sectional view taken along line D-D of Figure 1;
  • Figure 6 is a cross-sectional view taken along line E-E of Figure 1;
  • Figure 7 is a schematic cross-sectional view showing the structure of a single anode carbon block of an aluminum-shaped electrolytic cell having a profiled structure with an exhaust passage according to Embodiment 2 of the present invention
  • Figure 8 is a cross-sectional view taken along line A-A of Figure 7;
  • Figure 9 is a cross-sectional view taken along line B-B of Figure 7;
  • Figure 10 is a cross-sectional view taken along line C-C of Figure 7;
  • Figure 11 is a cross-sectional view taken along line D-D of Figure 7;
  • Figure 12 is a cross-sectional view taken along line E-E of Figure 7;
  • Figure 13 is a cross-sectional view showing the structure of an anode carbon block of a profiled aluminum electrolytic cell with an exhaust passage according to Embodiment 3 of the present invention
  • Figure 14 is a cross-sectional view taken along line A-A of Figure 13;
  • Figure 15 is a cross-sectional view taken along line B-B of Figure 13;
  • Figure 16 is a cross-sectional view taken along line C-C of Figure 13;
  • Figure 17 is a cross-sectional view taken along line D-D of Figure 13;
  • Figure 18 is a cross-sectional view taken along line E-E of Figure 13;
  • Figure 19 is a cross-sectional view showing the structure of the anode of the electrolytic cell with the exhaust passage;
  • Figure 20 is a cross-sectional view of the A-A of Figure 19;
  • Figure 21 is a cross-sectional view taken along line B-B of Figure 19;
  • Figure 22 is a cross-sectional view taken along line C-C of Figure 19;
  • Figure 23 is a cross-sectional view taken along line D-D of Figure 19;
  • Figure 24 is a cross-sectional view taken along line E-E of Figure 19;
  • Figure 25 is a diagram showing a profiled structure of an anode having an exhaust passage according to Embodiment 5 of the present invention
  • Figure 26 is a cross-sectional view taken along line AA of Figure 25;
  • Figure 27 is a cross-sectional view taken along line B-B of Figure 25;
  • Figure 28 is a cross-sectional view taken along line C-C of Figure 25;
  • Figure 29 is a cross-sectional view taken along line D-D of Figure 25;
  • Figure 30 is a cross-sectional view taken along line E-E of Figure 25;
  • Figure 31 is a cross-sectional view showing the structure of an anode carbon block of a profiled aluminum electrolytic cell with an exhaust passage according to Embodiment 6 of the present invention
  • Figure 32 is a cross-sectional view taken along line A-A of Figure 31;
  • Figure 33 is a cross-sectional view taken along line B-B of Figure 31;
  • Figure 34 is a cross-sectional view taken along line C-C of Figure 31;
  • Figure 35 is a cross-sectional view taken along line D-D of Figure 31;
  • Figure 36 is a cross-sectional view taken along line E-E of Figure 31;
  • Figure 37 is a cross-sectional view showing the structure of an anode carbon block of a profiled aluminum electrolytic cell with an exhaust passage according to Embodiment 7 of the present invention
  • Figure 38 is a cross-sectional view taken along line A-A of Figure 37;
  • Figure 39 is a cross-sectional view taken along line B-B of Figure 37;
  • Figure 40 is a cross-sectional view taken along line C-C of Figure 37;
  • Figure 41 is a cross-sectional view taken along line D-D of Figure 37;
  • Figure 42 is a cross-sectional view taken along line E-E of Figure 37;
  • Figure 43 is a cross-sectional view showing the structure of an anode carbon block of a profiled aluminum electrolytic cell with an exhaust passage according to Embodiment 8 of the present invention; and Figure 44 is a cross-sectional view taken along line A-A of Figure 43;
  • Figure 45 is a cross-sectional view taken along line B-B of Figure 43;
  • Figure 46 is a cross-sectional view taken along line C-C of Figure 43;
  • Figure 47 is a cross-sectional view taken along line D-D of Figure 43;
  • Figure 48 is a sectional view taken along line E-E of Figure 43;
  • Figure 49 is a cross-sectional view showing the structure of an anode carbon block of a profiled structure aluminum electrolytic cell with an exhaust passage according to Embodiment 9 of the present invention; and Figure 50 is a cross-sectional view taken along line A-A of Figure 49;
  • Figure 51 is a cross-sectional view taken along line B-B of Figure 49;
  • Figure 52 is a cross-sectional view taken along line C-C of Figure 49;
  • Figure 53 is a cross-sectional view taken along line D-D of Figure 49;
  • Figure 54 is a sectional view taken along line E-E of Figure 49;
  • Figure 55 is a cross-sectional view showing the structure of an anode carbon block of a profiled aluminum electrolytic cell with an exhaust passage according to Embodiment 10 of the present invention.
  • Figure 56 is a cross-sectional view taken along line A-A of Figure 55;
  • Figure 57 is a cross-sectional view taken along line C-C of Figure 55;
  • FIG. 1 anode carbon block, 2, charcoal bowl, 3, groove, 4, through hole, 5, groove, 6, cover.
  • the carbon bowl in the embodiment of the present invention has an inner diameter of 100 to 250 mm and a depth of 100 to 200 mm.
  • the cross-sectional structure of the anode carbon block of the special-shaped aluminum electrolysis cell with exhaust passage is shown in Fig. 1.
  • the structure of AA surface is shown in Fig. 2
  • the structure of BB surface is shown in Fig. 3
  • the structure of CC surface is shown in Fig. 4.
  • the surface structure is shown in Fig. 5.
  • the EE surface structure is shown in Fig. 6.
  • the top surface of the anode carbon block 1 is chamfered, and two rows of carbon bowls are uniformly distributed on the top surface, and each row of carbon bowls is along the anode carbon block.
  • the longitudinal arrangement is composed of 4 carbon bowls 2; the carbon bowl is provided with a groove 3, the bottom of the groove is provided with a through hole 4 communicating with the groove 5 at the bottom of the anode carbon block; a cover plate 6 is arranged above the groove;
  • Each groove is provided with a groove at a position corresponding to the bottom surface of the anode carbon block; and three through holes are provided at the bottom of each groove to communicate with the groove corresponding to the groove.
  • the axis of the transverse groove is perpendicular to the longitudinal axis of the anode carbon block, the axis of the transverse groove is located in the middle of two adjacent carbon bowls, and both ends of the transverse groove are open to the chamfers on the two long sides of the anode carbon block;
  • the axis of the groove is parallel to the axis of the anode carbon block;
  • the longitudinal groove is located in the middle of the adjacent two rows of carbon bowls, and both ends of the longitudinal groove are open to the chamfers on the two short sides of the anode carbon block;
  • each groove is 20 ⁇ 50cm from the top of the anode carbon block, and the bottom part is connected to the bottom surface of the anode carbon block, wherein the groove corresponding to the lateral groove is a lateral groove, and the groove corresponding to the longitudinal groove
  • the length of the transverse groove is equal to the width of the anode carbon block
  • the length of the longitudinal groove is equal to the length of the anode carbon block
  • the width of each groove is 2.5 to 3.5 cm
  • the cross section of each groove is an inverted triangle , the height is 3 ⁇ 10cm, and the width of the top surface is 3 ⁇ 10cm;
  • the longitudinal axis of the through hole is perpendicular to the bottom surface of the anode carbon block
  • the through hole is a small through hole, and the cross section is a rectangle with four corners rounded, and the area is 10 cm 2 ;
  • the preparation method is:
  • the anode carbon block green body is prepared by vibration molding, and the lower surface of the weight of the upper part of the carbon paste in the vibration mode has corresponding protrusions, and the corresponding protrusions are corresponding to the positions of the carbon bowl, the groove and the deep hole on the anode carbon block.
  • the convex structure is formed into a carbon bowl groove and a deep hole having a height of 20 to 50 cm on the anode carbon block green body during vibration molding, and then the demolded anode carbon block green body is sent to the baking furnace.
  • anode carbon block calcined body having a charcoal bowl, a groove and a deep hole; Then, a groove is physically cut at the bottom of the anode carbon block calcining body, and the groove is connected with the deep hole to form a through hole, and the anode carbon block of the special-shaped aluminum electrolytic cell with the exhaust passage is formed;
  • a cover plate is arranged on the groove; the cover plate is placed on the groove, so that the cover plate is integrated with the carbon block, and a tunnel having a triangular cross section is formed between the cover plate and the groove.
  • the anode carbon block can reduce the tank voltage, the gas emissions generated by the anode are unimpeded, and the gas escape has a significant effect on the fluctuation of the cathode aluminum liquid, and the anode carbon block does not fall off.
  • the cross-sectional structure of the anode carbon block of the profiled aluminum electrolytic cell with exhaust passage is shown in Fig. 7.
  • the structure of the AA surface is shown in Fig. 8
  • the structure of the BB surface is shown in Fig. 9, and the structure of the CC surface is shown in Fig. 10.
  • the surface structure is shown in Fig. 11, and the EE surface structure is shown in Fig.
  • the top surface of the anode carbon block 1 is chamfered, and a row of carbon bowls evenly distributed on the top surface is arranged along the longitudinal direction of the anode carbon block, and a row of carbon
  • the bowl is composed of 4 carbon bowls 2; the carbon bowl is provided with a groove 3, the bottom of the groove is provided with a through hole 4 communicating with the groove 5 at the bottom of the anode carbon block; a cover plate 6 is arranged above the groove;
  • a lateral groove is disposed between two adjacent carbon bowls; each groove is provided with a groove at a corresponding position on the bottom surface of the anode carbon block; and 7 through holes are provided at the bottom of each groove corresponding to the groove Groove connection;
  • the axis of the transverse groove is perpendicular to the longitudinal axis of the anode carbon block, the axis of the transverse groove is located in the middle of two adjacent carbon bowls, and both ends of the transverse groove open to the chamfers on the two long sides of the anode carbon block;
  • the top surface of the trench is 20 ⁇ 50cm from the top of the anode carbon block, and the bottom surface is connected with the bottom surface of the anode carbon block.
  • the length of the groove is equal to the width of the anode carbon block, and the width of each groove is 2.5 ⁇ 3.5cm;
  • the cross section of the groove is an inverted triangle with a height of 3 ⁇ 10cm; the width of the top surface is 3 ⁇ 10cm ;
  • the longitudinal axis of the through hole is perpendicular to the bottom surface of the anode carbon block
  • the through hole is a small through hole, and the cross section is a rectangle with four corners rounded, and the area is 12 cm 2 ;
  • the preparation method is:
  • the carbon block is formed by compression molding, and the lower surface of the upper core in the stamper has corresponding protrusions, and the carbon bowl, the groove and the height are formed on the anode carbon block green body at the time of molding, and the height is 20-50 cm.
  • the deep hole, the rest is the same as in Example 1;
  • the anode carbon block was used to reduce the cell voltage, and the gas emissions generated by the anode were unsteadily uniform, and the gas escaping significantly reduced the fluctuation of the cathode aluminum liquid, and the anode carbon block did not fall off.
  • the cross-sectional structure of the anode carbon block of the shaped aluminum electrolysis cell with exhaust passage is shown in Fig. 13, the AA surface structure is shown in Fig. 14, the BB surface structure is shown in Fig. 15, and the CC surface structure is shown in Fig. 16, DD
  • the surface structure is shown in Figure 17, EE surface
  • the structure is as shown in FIG. 18; the structure is the same as that in Embodiment 1, except that: the transverse groove is provided with two through holes communicating with the corresponding grooves, and the longitudinal groove is provided with a through hole and a corresponding groove. Connected
  • the top surface of the trench is 20 ⁇ 50cm from the top of the anode carbon block, and the width of the trench is 2.5 ⁇ 3.5cm;
  • the cross section of the groove is an inverted triangle, the height is 3 ⁇ 10cm, and the width of the top surface is 3 ⁇ 10cm;
  • the through hole is a large through hole, the cross section is rectangular, the cross-sectional area of the two through holes in the transverse groove is 50 cm 2 , and the area of the through hole in the longitudinal groove is 390 cm 2 ;
  • the preparation method is the same as that in the embodiment 1;
  • the anode carbon block was used to reduce the cell voltage, and the gas emissions generated by the anode were unsteadily uniform, and the gas escaping significantly reduced the fluctuation of the cathode aluminum liquid, and the anode carbon block did not fall off.
  • the cross-sectional structure of the anode carbon block of the shaped aluminum electrolysis cell with exhaust passage is shown in Fig. 19, the structure of the AA surface is shown in Fig. 20, the structure of the BB surface is shown in Fig. 21, and the structure of the CC surface is shown in Fig. 22, DD
  • the surface structure is shown in FIG. 23, and the EE surface structure is as shown in FIG. 24; the structure is the same as that in Embodiment 1, except that: one through hole is provided at the bottom of each groove to communicate with the groove corresponding to the groove;
  • the top surface of the trench is 20 ⁇ 50cm from the top of the anode carbon block, and the width of each trench is 2.5 ⁇ 3.5cm;
  • the cross section of the groove is an inverted triangle, the height of the groove is 3 ⁇ 10cm, and the width of the top surface is 3 ⁇ 10cm ;
  • the through hole is a large through hole, the cross section is rectangular, the through hole area in the lateral groove is 100 cm 2 , and the through hole area in the longitudinal groove is 390 cm 2 ; each through hole is connected to each other;
  • the preparation method is the same as in the embodiment 2;
  • the anode carbon block was used to reduce the cell voltage, and the gas emissions generated by the anode were unsteadily uniform, and the gas escaping significantly reduced the fluctuation of the cathode aluminum liquid, and the anode carbon block did not fall off.
  • the cross-sectional structure of the anode carbon block of the profiled aluminum electrolytic cell with exhaust passage is shown in Fig. 25.
  • the structure of the AA surface is shown in Fig. 26, the structure of the BB surface is shown in Fig. 27, and the structure of the CC surface is shown in Fig. 28.
  • the surface structure is shown in Fig. 29, and the EE surface structure is shown in Fig. 30; the structure is the same as that in the first embodiment, and the difference is that: each of the lateral grooves is provided with one through hole communicating with the corresponding groove, the longitudinal groove 4 through holes are communicated with corresponding grooves;
  • the top surface of the trench is 20 ⁇ 50cm from the top of the anode carbon block, and the width of each trench is 2.5 ⁇ 3.5cm;
  • the cross section of the groove is an inverted triangle with a height of 3 ⁇ 10cm and a top surface width of 3 ⁇ 10cm ;
  • the through hole is a large through hole, the cross section is rectangular, the cross hole area of the through hole in the horizontal groove is 100 cm 2 , and the area of the through hole in the longitudinal groove is 300 cm 2 ;
  • the preparation method is the same as that in the embodiment 1;
  • the anode carbon block was used to reduce the cell voltage, and the gas emissions generated by the anode were unsteadily uniform, and the gas escaping significantly reduced the fluctuation of the cathode aluminum liquid, and the anode carbon block did not fall off.
  • the cross-sectional structure of the anode carbon block of the profiled aluminum electrolytic cell with the exhaust passage is shown in Fig. 31, the AA surface structure is shown in Fig. 32, the BB surface structure is shown in Fig. 33, and the CC surface structure is shown in Fig. 34, DD.
  • the surface structure is shown in FIG. 35, and the EE surface structure is as shown in FIG. 36; the structure is the same as that in Embodiment 1, except that: two through holes are provided at the bottom of each lateral groove to communicate with the groove corresponding to the groove; Each of the longitudinal grooves is provided with four through holes communicating with corresponding grooves;
  • the top surface of the trench is 20 ⁇ 50cm from the top of the anode carbon block, and the width is 2.5 ⁇ 3.5cm;
  • the cross section of the groove is an inverted triangle with a height of 3 ⁇ 10cm and a top surface width of 3 ⁇ 10cm ;
  • the through hole is a large through hole, and the cross section is rectangular, and the area is 50 cm 2 ;
  • the preparation method is the same as in the embodiment 2;
  • the anode carbon block was used to reduce the cell voltage, and the gas emissions generated by the anode were unsteadily uniform, and the gas escaping significantly reduced the fluctuation of the cathode aluminum liquid, and the anode carbon block did not fall off.
  • the profile structure of the anode carbon block of the profiled aluminum reduction cell with exhaust passage is shown in Fig. 37, the AA surface structure is shown in Fig. 38, the BB surface structure is shown in Fig. 39, and the CC surface structure is shown in Fig. 40, DD
  • the surface structure is shown in Fig. 41, and the EE surface structure is as shown in Fig. 42; the structure is the same as that in the embodiment 6, and the difference is that: three lateral grooves are respectively provided with a small pass at the three intersections of the longitudinal grooves.
  • the hole and the small through hole have a circular cross section with an area of 11 cm 2 ;
  • the preparation method is the same as that in the embodiment 1;
  • the anode carbon block was used to reduce the cell voltage, and the gas emissions generated by the anode were unsteadily uniform, and the gas escaping significantly reduced the fluctuation of the cathode aluminum liquid, and the anode carbon block did not fall off.
  • the cross-sectional structure of the anode carbon block of the profiled aluminum electrolytic cell with the exhaust passage is shown in Fig. 43, the AA surface structure is shown in Fig. 44, the BB surface structure is shown in Fig. 45, and the CC surface structure is shown in Fig. 46, DD
  • the surface structure is shown in Figure 47, EE surface
  • the structure is as shown in Fig. 48, the top side of the anode carbon block 1 is chamfered, and two rows of carbon bowls are uniformly distributed on the top surface, and each row of carbon bowls is arranged along the longitudinal direction of the anode carbon block, and is composed of four carbon bowls 2.
  • a groove 3 is provided between the carbon bowls, and a through hole 4 is formed in the bottom of the groove to communicate with the groove 5 at the bottom of the anode carbon block, and a cover plate 6 is disposed above the groove;
  • the groove is a longitudinal groove between the two rows of carbon bowls; the groove is provided with a groove at a position corresponding to the bottom surface of the anode carbon block; and a through hole is provided at the bottom of the groove to communicate with the groove;
  • the axis of the longitudinal groove is parallel to the axis of the anode carbon block; the longitudinal groove is located in the middle of the adjacent two rows of carbon bowls, and the two ends of the longitudinal groove are open to the chamfered position on the two short sides of the anode carbon block;
  • the top surface of the trench is 20 ⁇ 50cm from the top of the anode carbon block, and the bottom surface is connected with the bottom surface of the anode carbon block, and the width of the groove is 2.5 ⁇ 3.5cm ;
  • the cross section of the groove is an inverted triangle, the height is 3 ⁇ 10cm, and the width of the top surface is 3 ⁇ 10cm;
  • the longitudinal axis of the through hole is perpendicular to the bottom surface of the anode carbon block
  • the through hole is a large through hole, and the cross section is rectangular, and the area is 390 cm 2 ;
  • the preparation method is the same as in the embodiment 2;
  • a longitudinal cover is provided on the groove in the same manner as in the first embodiment.
  • the anode carbon block was used to reduce the cell voltage, and the gas emissions generated by the anode were unsteadily uniform, and the gas escaping significantly reduced the fluctuation of the cathode aluminum liquid, and the anode carbon block did not fall off.
  • the cross-sectional structure of the anode carbon block of the profiled aluminum electrolytic cell with the exhaust passage is shown in Fig. 49, the structure of the AA surface is shown in Fig. 50, the structure of the BB surface is shown in Fig. 51, and the structure of the CC surface is shown in Fig. 52, DD
  • the surface structure is shown in Fig. 53, and the EE surface structure is as shown in Fig. 54; the structure is the same as that in the second embodiment, and the difference is:
  • a through hole is provided at the bottom of each groove to communicate with a groove corresponding to the groove;
  • the top surface of the trench is 20 ⁇ 50cm from the top of the anode carbon block, and the width of the trench is 2.5 ⁇ 3.5cm;
  • the cross section of the groove is an inverted triangle with a height of 3 ⁇ 10cm and a top surface width of 3 ⁇ 10cm ;
  • the through hole is a large through hole, and the cross section is rectangular, and the area is 100 cm 2 ;
  • the preparation method is the same as that in the embodiment 1;
  • a lateral cover is disposed on the groove, the method is the same as in Embodiment 1;
  • the anode carbon block was used to reduce the cell voltage, and the gas emissions generated by the anode were unsteadily uniform, and the gas escaping significantly reduced the fluctuation of the cathode aluminum liquid, and the anode carbon block did not fall off.
  • the profile structure of the anode carbon block of the shaped aluminum electrolysis cell with the exhaust passage is shown in Fig. 55, and the AA surface structure is shown in Fig. 56.
  • the CC surface structure is shown in Fig. 57; the top surface of the anode carbon block is chamfered, and one or two rows of carbon bowls 2 are evenly distributed on the top surface, and each row of carbon bowls 2 are arranged longitudinally along the anode carbon block 1.
  • groove 3 is arranged between the carbon bowl 2, the bottom of the anode carbon block 1 is provided with a groove 5; the bottom of the groove 3 is provided with a through hole 4 communicating with the groove 5, the through hole 4
  • the length is the same as the length of the anode carbon block 1, the through hole 4 is connected with the groove 5, and the anode carbon block is broken in the longitudinal direction to form two identical small anode carbon blocks;
  • the groove is a longitudinal groove located between the two rows of charcoal bowls;
  • the top surface of the trench is 40 cm from the top of the anode carbon block, and the width of the trench is 3 cm;
  • the cross section of the groove is an inverted triangle with a height of 6 cm and a top surface having a width of 6 m .
  • the channel width is the same as the groove, the length is 150cm, and the cross-sectional area is 450cm 2 ;
  • the preparation method comprises the following steps: preparing the anode carbon block green body by vibration molding; the lower surface of the upper weight in the vibration mode has corresponding protrusions, and forming a carbon bowl and a groove on the anode carbon block green body during vibration molding. And a deep hole having a height of 40 cm and the same length as the anode carbon block; the anode carbon block green body is discharged from the mold and cooled, and then placed in a roasting furnace and fired to 1100 to 1300 ° C to form a carbon block, a deep hole and a groove.
  • the anode carbon block is fired; then the groove is physically cut at the bottom of the anode carbon block calcined body, and the groove is connected with the deep hole, and an anode carbon block is divided into two small anode carbon blocks to be made with exhaust gas.
  • the anode carbon block was used to reduce the cell voltage, and the gas emissions generated by the anode were unsteadily uniform, and the gas escaping significantly reduced the fluctuation of the cathode aluminum liquid, and the anode carbon block did not fall off.

Abstract

An aluminum electrolytic tank anode carbon block of an irregularly-shaped structure with an exhaust passage and a preparation method thereof. The edge part of a top surface is provided with a chamfer. A row or two rows of carbon bowls are uniformly distributed on the top surface. Each row of the carbon bowls are longitudinally arranged along the anode carbon block and consist of 3 to 5 carbon bowls. A groove is formed between the carbon bowls, the bottom of the anode carbon block is provided with a trench, and the bottom of the groove is provided with a through hole which is communicated with the trench at the bottom of the anode carbon block. The preparation method comprises: preparing the carbon block by using a vibration mould or pressing mould with corresponding bumps by a vibration molding method or a compression molding method; and roasting and then cutting out the trench. The aluminum electrolytic tank anode carbon block of the irregularly-shaped structure with the exhaust passage of the present invention has the characteristics of a simple and convenient preparation process, high working efficiency and the like. Besides, it is obtained through testing that the tank voltage can be reduced by using the anode carbon block, the gas produced by an anode is smoothly and uniformly discharged, and the influence of gas escape on fluctuation of cathode aluminum liquid is obviously reduced.

Description

带有排气通道的异形结构铝电解槽阳极炭块及其制备方法 技术领域  Shaped structure aluminum electrolytic cell anode carbon block with exhaust passage and preparation method thereof
本发明属于铝电解技术领域,特别涉及一种带有排气通道的异形结构铝电解槽阳极炭块 及其制备方法。  The invention belongs to the technical field of aluminum electrolysis, and particularly relates to an anode carbon block of a profiled structure aluminum electrolysis cell with an exhaust passage and a preparation method thereof.
背景技术 Background technique
对工业铝电解槽来说, 有两个重要的技术经济指标, 一个是电流效率, 一个是直流电耗, 两个指标虽然概念不同, 但关系密切, 铝电解的电流效率 CE ( % )与直流电耗 W (kWh/t-Al) 之间的关系可用如下公式来表示: tV = 2980 ^ ( 1 )  For industrial aluminum electrolysis cells, there are two important technical and economic indicators, one is current efficiency, and the other is DC power consumption. Although the two indicators are different in concept, they are closely related. The current efficiency of aluminum electrolysis (CE) and DC power consumption The relationship between W (kWh/t-Al) can be expressed by the following formula: tV = 2980 ^ ( 1 )
CE 式中^为铝电解的平均槽电压, 由此公式可以看出, 电解槽电流效率每提高 1%, 可使 直流电耗降低 150kWh/t铝左右, 同时使铝产量增加 1% ; 而槽电压降低 0.1伏, 能使直流电 耗降低 300kWh/t铝左右。  The CE method is the average cell voltage of aluminum electrolysis. It can be seen from this formula that for every 1% increase in the current efficiency of the cell, the DC power consumption can be reduced by about 150 kWh/t aluminum, and the aluminum output can be increased by 1%. By reducing 0.1 volts, the DC power consumption can be reduced by about 300 kWh/t aluminum.
众所周知, 铝电解槽内电流效率的降低是由于溶解在电解质熔体内的金属铝与阳极产生 并排放出的 C02发生的所谓铝的二次反应引起的, 这就意味着电解槽的阳极越大, 阳极气体 从阳极底掌下放出, 然后逸出于电解质表面所引起的路程越长, 与电解质熔体中金属铝发生 的铝的二次反应就越多, 造成电流效率损失也就越大。 因此, 让铝电解槽中阳极底掌表面生 成的 C02气体能够快速地从阳极底掌表面逸出, 缩短 C02在电解质中的停留时间则可以大大 提高铝电解槽的电流效率。 It is well known that the reduction in current efficiency in an aluminum electrolytic cell is caused by a secondary reaction of so-called aluminum in which metal aluminum dissolved in the electrolyte melt and C0 2 generated by the anode are discharged, which means that the anode of the electrolytic cell is larger. The longer the anode gas is discharged from the bottom of the anode bottom, and the longer the distance caused by the escape of the electrolyte surface, the more secondary reaction with aluminum in the electrolyte melt, and the greater the current efficiency loss. Therefore, the C0 2 gas generated on the surface of the anode bottom of the aluminum electrolytic cell can be quickly escaped from the surface of the anode bottom, and shortening the residence time of C0 2 in the electrolyte can greatly improve the current efficiency of the aluminum electrolytic cell.
基于上述理论, 美国人发明了一种在电解槽的纵向方向从阳极底掌表面向上开 2个沟槽 的电解槽阳极技术, 其目的是为了让电解槽阳极底掌下生成的阳极气体能部分地从沟槽中逸 出来, 以达到减少阳极气体与铝的二次反应的目的, 这种电解槽阳极底掌上的沟槽的深度为 200〜250mm。然而由于这种沟槽太浅, 在大部分的阳极工作时间内, 其沟槽全部浸没在电解 质熔体中, 致使阳极气体在电解质熔体中的行程并没有缩短, 其所受的阻力也没有减小, 因 此, 其提高电解槽电流效率或降低电耗的效果并不明显。  Based on the above theory, the Americans invented an electrolytic cell anode technology that opens two grooves upward from the surface of the anode bottom in the longitudinal direction of the electrolytic cell. The purpose is to make the anode gas energy generated under the anode bottom of the electrolytic cell bottom. The ground escapes from the trench to achieve the purpose of reducing the secondary reaction between the anode gas and the aluminum. The depth of the groove on the bottom of the anode of the electrolytic cell is 200 to 250 mm. However, since the groove is too shallow, the groove is completely immersed in the electrolyte melt during most of the anode working time, so that the stroke of the anode gas in the electrolyte melt is not shortened, and the resistance is not It is reduced, so its effect of increasing the current efficiency of the electrolytic cell or reducing the power consumption is not obvious.
其后, 为了改进这种情况, 人们又发明了其它结构型式的铝电解槽阳极技术, 这其中包 括李劼等人的 1个阳极导杆、 4个钢爪、 4个小阳极的铝电解槽阳极技术, 冯乃样和彭建平发 明的 1个阳极导杆、 S个钢爪、 4个以上小阳极的专利技术; 这些专利技术在工业上能够实施 的话, 固然对提高阳极气体的排放速度, 提高电解槽的电流效率有好处, 但是实际在运行过 程中发现, 这种单个小阳极技术, 在电解槽上容易造成阳极的脱落, 这种脱落是由于没有来 自于阳极钢爪之上的横梁在电解槽上表的高温情况下所产生的膨胀力对阳极炭碗横向作用力 的支撑所致, 因此开发一种有利于阳极快速排气的技术是目前急需解决的问题。 Thereafter, in order to improve this situation, other structural types of aluminum electrolytic cell anode technology have been invented, including one anode guide rod of Li Wei et al., four steel claws, and four small anode aluminum electrolytic cells. Anode technology, patented technology of an anode guide rod, S steel claws and more than 4 small anodes invented by Feng Nai and Peng Jianping; if these patented technologies can be implemented industrially, they can improve the anode gas emission rate and improve The current efficiency of the electrolytic cell is beneficial, but it is actually found during operation that this single small anode technology is liable to cause the anode to fall off on the electrolytic cell. Since the expansion force generated by the beam above the anode steel claw in the high temperature condition of the electrolytic cell is supported by the lateral force of the anode carbon bowl, it is urgent to develop a technology which is advantageous for the rapid exhaust of the anode. solved problem.
发明内容 Summary of the invention
针对现有铝电解槽阳极在排气上存在的上述问题, 本发明提供一种带有排气通道的异形 结构铝电解槽阳极炭块及其制备方法, 通过在炭阳极单个阳极炭块炭碗之间设置凹槽, 凹槽 通过通孔与阳极炭块底部的沟槽连通, 使阳极炭块在工作时阳极产生的气体排放畅通均匀, 减少气体从电解质中逸出对阴极铝液波动影响, 既能避免阳极脱落, 又能使气体从阳极底掌 表面快速排出。  In view of the above problems existing in the existing aluminum electrolytic cell anode on the exhaust gas, the present invention provides a profiled structure aluminum electrolytic cell anode carbon block with an exhaust passage and a preparation method thereof, through a single anode carbon block carbon bowl in a carbon anode Grooves are disposed between the grooves and the grooves at the bottom of the anode carbon block through the through holes, so that the gas emissions generated by the anodes of the anode carbon block are uniform and uniform, and the effect of gas escape from the electrolyte on the fluctuation of the cathode aluminum liquid is reduced. It can avoid the anode falling off and can quickly discharge the gas from the surface of the anode bottom.
本发明的带有排气通道的异形结构铝电解槽炭阳极的阳极炭块的顶面边部设有倒角, 顶 面上均匀分布有一排或两排炭碗, 每排炭碗沿阳极炭块纵向排列, 由 3~5个炭碗组成; 其中 炭碗之间设有凹槽, 阳极炭块底部设有沟槽; 其中凹槽底部设有通孔与阳极炭块底部的沟槽 连通。  The anode side of the anode carbon block of the carbon anode of the profiled aluminum electrolytic cell with the exhaust passage of the invention is provided with chamfering, and one or two rows of carbon bowls are evenly distributed on the top surface, and each row of carbon bowls is along the anode carbon The blocks are arranged vertically, and are composed of 3 to 5 carbon bowls; wherein the carbon bowls are provided with grooves, and the bottom of the anode carbon block is provided with grooves; wherein the bottom of the groove is provided with a through hole communicating with the groove at the bottom of the anode carbon block.
上述的阳极炭块中, 当阳极炭块顶面上设有一排炭碗时, 相邻两个炭碗之间设有横向凹 槽; 当阳极炭块顶面上设有两排炭碗时, 在两排炭碗之间设有纵向凹槽, 或者同一排的相邻 两个炭碗之间设有横向凹槽并且在两排炭碗之间设有纵向凹槽, 当同时设有横向凹槽和纵向 凹槽时, 横向凹槽与纵向凹槽连通。  In the above anode carbon block, when a row of carbon bowls is arranged on the top surface of the anode carbon block, lateral grooves are arranged between two adjacent carbon bowls; when two rows of carbon bowls are arranged on the top surface of the anode carbon block, There are longitudinal grooves between the two rows of charcoal bowls, or lateral grooves between two adjacent carbon bowls in the same row and longitudinal grooves between the two rows of charcoal bowls. In the case of the groove and the longitudinal groove, the transverse groove communicates with the longitudinal groove.
上述的沟槽位于与每个凹槽在阳极炭块底面相对应的位置; 每个凹槽底部设有至少一个 通孔与该凹槽相对应的沟槽连通。  The above-mentioned grooves are located at positions corresponding to the bottom surface of each of the anode carbon blocks; each of the grooves is provided with at least one through hole communicating with a groove corresponding to the groove.
上述的横向凹槽的轴线与阳极炭块的纵向轴线垂直, 横向凹槽的轴线位于相邻两个炭碗 正中, 横向凹槽的两端通到阳极炭块两个长边上的倒角上; 上述的纵向凹槽的轴线与阳极炭 块的轴线平行; 纵向凹槽位于相邻两排炭碗正中, 纵向凹槽的两端通到阳极炭块两个短边上 的倒角上。  The axis of the transverse groove is perpendicular to the longitudinal axis of the anode carbon block, and the axis of the transverse groove is located in the center of two adjacent carbon bowls, and both ends of the transverse groove are open to the chamfers on the two long sides of the anode carbon block. The axis of the longitudinal groove is parallel to the axis of the anode carbon block; the longitudinal groove is located in the center of the adjacent two rows of carbon bowls, and both ends of the longitudinal groove are open to the chamfers on the two short sides of the anode carbon block.
上述的沟槽的顶部距阳极炭块顶部高度为 20~50cm,沟槽的底部通到阳极炭块的底表面, 其中与横向凹槽相对应的沟槽为横向沟槽, 与纵向凹槽相对应的沟槽为纵向沟槽, 横向沟槽 的长度与阳极炭块宽度相等, 纵向沟槽的长度与阳极炭块长度相等, 各沟槽的宽度为 1.0~3.5cm。  The top of the trench is 20~50cm from the top of the anode carbon block, and the bottom of the trench is connected to the bottom surface of the anode carbon block, wherein the groove corresponding to the lateral groove is a lateral groove, and the longitudinal groove is The corresponding groove is a longitudinal groove, the length of the transverse groove is equal to the width of the anode carbon block, the length of the longitudinal groove is equal to the length of the anode carbon block, and the width of each groove is 1.0 to 3.5 cm.
上述的凹槽的横截面为倒置的等腰三角形或倒置的等腰梯形, 凹槽高度为 3~10cm; 当 凹槽的横截面为倒置的等腰三角形时, 该凹槽顶面的宽度为 3~10cm; 当凹槽的横截面为倒置 的等腰梯形时, 该凹槽的顶面宽度为 5~10cm, 底面的宽度为 3~8cm。 The groove has a cross section of an inverted isosceles triangle or an inverted isosceles trapezoid, and the groove height is 3 to 10 cm; when the groove has an inverted isosceles triangle, the width of the top surface of the groove is 3~10cm ; when the cross section of the groove is an inverted isosceles trapezoid, the top surface width of the groove is 5~10cm, and the width of the bottom surface is 3~8cm.
上述的通孔在凹槽底部, 且其纵向轴线与阳极炭块底面垂直。 上述的通孔分为小通孔和大通孔, 小通孔的横截面为圆形、 椭圆形、 正方形或长方形, 面积为 3~18cm2, 其中当小通孔的横截面为方形或长方形时, 该方形或长方形的四个角为圆 角; 大通孔的横截面为长方形, 面积为 18~500cm2The above-mentioned through hole is at the bottom of the groove, and its longitudinal axis is perpendicular to the bottom surface of the anode carbon block. The above-mentioned through holes are divided into small through holes and large through holes, and the small through holes have a circular, elliptical, square or rectangular cross section, and the area is 3 to 18 cm 2 , wherein when the small through holes are square or rectangular in cross section The four corners of the square or rectangle are rounded; the large through hole has a rectangular cross section and an area of 18 to 500 cm 2 .
上述的阳极炭块中, 当通孔的长度与阳极炭块的长度相同时, 通孔与沟槽连接在一起, 将一个阳极炭块在纵向断开形成两个相同的小阳极炭块  In the above anode carbon block, when the length of the through hole is the same as the length of the anode carbon block, the through hole is connected with the groove, and one anode carbon block is broken in the longitudinal direction to form two identical small anode carbon blocks.
本发明的带有排气通道的异形结构铝电解槽炭阳极是由 20个以上的单体的具有上述异 型结构阳极炭块组成的, 单个阳极炭块的制备方法为:  The carbon anode of the profiled aluminum electrolytic cell with exhaust passage of the invention is composed of more than 20 monomers having the above-mentioned heterostructure anode carbon block, and the preparation method of the single anode carbon block is:
采用振动成型法或模压成型法制作阳极炭块生坯; 当采用振动成型法时, 其振模内的上 部重锤的下表面带有对应的凸起; 当采用模压成型法时, 其压模内的上模芯的下表面带有对 应的凸起; 在振动成型或模压成型时在阳极炭块生坯上制成炭碗、 凹槽和高度在 20~50cm的 深孔; 阳极炭块生坯出模并冷却后, 置入焙烧炉焙烧到 1100~1300°C, 制成顶部带有炭碗、 深孔和凹槽的阳极炭块焙烧体; 再在阳极炭块焙烧体底部物理切割开设沟槽, 并使沟槽与深 孔或者槽形通道连通, 形成通孔, 制成带有排气通道的异形结构铝电解槽阳极炭块; 所述的 对应的凸起是指与阳极炭块上的炭碗、 凹槽和通孔位置相应的凸起结构。  The anode carbon block green body is prepared by vibration molding or compression molding; when the vibration molding method is adopted, the lower surface of the upper weight in the vibration mode has a corresponding protrusion; when the molding method is used, the compression mold The lower surface of the upper core has a corresponding protrusion; a carbon bowl, a groove and a deep hole having a height of 20 to 50 cm are formed on the anode carbon block green body during vibration molding or press molding; After the blank is discharged from the mold and cooled, it is placed in a roasting furnace and fired at 1100~1300 °C to prepare an anode carbon block calcined body with a carbon bowl, a deep hole and a groove at the top; and then physically cut at the bottom of the anode carbon block calcined body. a groove, and the groove is communicated with the deep hole or the groove-shaped passage to form a through hole, and the anode carbon block of the aluminum-shaped electrolytic cell with the exhaust passage is formed; the corresponding protrusion refers to the anode carbon block The corresponding charcoal bowl, groove and through hole position corresponding convex structure.
本发明的带有排气通道的异形结构铝电解槽阳极炭块在使用前在凹槽上设置盖板, 横向 凹槽上设置横向盖板, 横向盖板盖在横向凹槽上, 横向盖板的长度与阳极炭块的宽度相同; 纵向凹槽的上方设置纵向盖板, 纵向盖板盖在纵向凹槽上, 纵向盖板的长度与阳极炭块的长 度相同; 当阳极炭块上同时有横向盖板和纵向盖板时, 纵向盖板与横向盖板连接构成一体结 构, 盖板之上覆盖冰晶石粉, 然后装配到铝电解槽中阳极爪上。  The anode carbon block of the special-shaped aluminum electrolytic cell with the exhaust passage of the invention is provided with a cover plate on the groove before use, a lateral cover plate is arranged on the lateral groove, and the transverse cover plate is disposed on the lateral groove, the transverse cover plate The length is the same as the width of the anode carbon block; the longitudinal cover is provided above the longitudinal groove, the longitudinal cover is on the longitudinal groove, and the length of the longitudinal cover is the same as the length of the anode carbon block; In the case of the transverse cover and the longitudinal cover, the longitudinal cover and the lateral cover are connected to form an integral structure, the cover is covered with cryolite powder, and then assembled to the anode claw of the aluminum electrolytic cell.
上述的盖板选用炭质材料或无机材料或金属材料, 选用的无机材料可以是耐火材料板或 耐火纤维板,选用的金属材料的材质为铝板或铁板;选用炭块或耐火材料板或耐火纤维板时, 其盖板的厚度为 5~20cm, 选用铝板或铁板时, 铝板或铁板的厚度为 l~4mm, 当选用铁板时, 铁板上可带孔, 孔上焊有上口高于阳极上表面所覆盖的电解质和氧化铝保温料厚度的铁管, 使之更有利于阳极气体排出槽外。  The above-mentioned cover plate is made of carbonaceous material or inorganic material or metal material, and the selected inorganic material may be refractory plate or refractory fiberboard, and the selected metal material is made of aluminum plate or iron plate; carbon block or refractory plate or refractory fiber board is selected. When the thickness of the cover plate is 5~20cm, when the aluminum plate or the iron plate is used, the thickness of the aluminum plate or the iron plate is l~4mm. When the iron plate is selected, the iron plate can be perforated, and the upper surface of the hole is welded with a high mouth. The electrolyte covered with the upper surface of the anode and the iron tube of the thickness of the alumina insulation material make it more advantageous for the anode gas to exit the tank.
本发明的带有排气通道的异形结构铝电解槽炭阳极的阳极炭块的工作原理是: 进行铝电 解时, 阳极炭块底面生成的 C02气体大部经由沟槽上升进入通孔中, 再由通孔汇集到阳极炭 块上表面的凹槽内, 进入到盖板和凹槽之间的空腔内, 并经由此空腔从盖板的端部或上部的 铁管排出到阳极炭块外。 The working principle of the anode carbon block of the carbon anode of the special-shaped aluminum electrolytic cell with the exhaust passage of the present invention is as follows: When performing aluminum electrolysis, most of the C0 2 gas generated on the bottom surface of the anode carbon block rises into the through hole through the groove. Then, the through hole is collected into the groove on the upper surface of the anode carbon block, enters into the cavity between the cover plate and the groove, and is discharged from the end of the cover plate or the upper iron pipe to the anode carbon through the cavity. Outside the block.
本发明的带有排气通道的异形结构铝电解槽阳极炭块具有制作工艺简便, 工作效率高等 特点, 经过试验, 采用该阳极炭块能够降低槽电压, 阳极产生的气体排放畅通均匀, 气体的 逸出对阴极铝液波动影响明显减少, 有利于电流效率的提高, 同时避免了小阳极炭块的脱落 现象, 具有良好的应用前景。 The anode carbon block of the special-shaped aluminum electrolytic cell with the exhaust passage of the invention has the characteristics of simple manufacturing process and high working efficiency. After the experiment, the anode carbon block can reduce the tank voltage, and the gas emissions generated by the anode are uniform and uniform, and the gas is The effect of the escape on the fluctuation of the cathode aluminum liquid is obviously reduced, which is beneficial to the improvement of the current efficiency, and avoids the falling off of the small anode carbon block, and has a good application prospect.
附图说明 DRAWINGS
图 1为本发明实施例 1的带有排气通道的异形结构铝电解槽炭阳极单体阳极炭块剖面结 构示意图;  1 is a schematic cross-sectional view showing a carbon anode single anode carbon block of a profiled aluminum electrolytic cell with an exhaust passage according to Embodiment 1 of the present invention;
图 2为图 1的 A-A面剖图;  Figure 2 is a cross-sectional view taken along line A-A of Figure 1;
图 3为图 1的 B-B面剖图;  Figure 3 is a cross-sectional view taken along line B-B of Figure 1;
图 4为图 1的 C-C面剖图;  Figure 4 is a cross-sectional view taken along line C-C of Figure 1;
图 5为图 1的 D-D面剖图;  Figure 5 is a cross-sectional view taken along line D-D of Figure 1;
图 6为图 1的 E-E面剖图;  Figure 6 is a cross-sectional view taken along line E-E of Figure 1;
图 7为本发明实施例 2的带有排气通道的异形结构铝电解槽单体阳极炭块剖面结构示意 图;  Figure 7 is a schematic cross-sectional view showing the structure of a single anode carbon block of an aluminum-shaped electrolytic cell having a profiled structure with an exhaust passage according to Embodiment 2 of the present invention;
图 8为图 7的 A-A面剖图;  Figure 8 is a cross-sectional view taken along line A-A of Figure 7;
图 9为图 7的 B-B面剖图;  Figure 9 is a cross-sectional view taken along line B-B of Figure 7;
图 10为图 7的 C-C面剖图;  Figure 10 is a cross-sectional view taken along line C-C of Figure 7;
图 11为图 7的 D-D面剖图;  Figure 11 is a cross-sectional view taken along line D-D of Figure 7;
图 12为图 7的 E-E面剖图;  Figure 12 is a cross-sectional view taken along line E-E of Figure 7;
图 13为本发明实施例 3的带有排气通道的异形结构铝电解槽阳极炭块剖面结构示意图; 图 14为图 13的 A-A面剖图;  Figure 13 is a cross-sectional view showing the structure of an anode carbon block of a profiled aluminum electrolytic cell with an exhaust passage according to Embodiment 3 of the present invention; Figure 14 is a cross-sectional view taken along line A-A of Figure 13;
图 15为图 13的 B-B面剖图;  Figure 15 is a cross-sectional view taken along line B-B of Figure 13;
图 16为图 13的 C-C面剖图;  Figure 16 is a cross-sectional view taken along line C-C of Figure 13;
图 17为图 13的 D-D面剖图;  Figure 17 is a cross-sectional view taken along line D-D of Figure 13;
图 18为图 13的 E-E面剖图;  Figure 18 is a cross-sectional view taken along line E-E of Figure 13;
图 19为本发明实施例 4的带有排气通道的异形结构铝 ;电解槽阳极炭块剖面结构示意图; 图 20为图 19的 A-A面剖图;  Figure 19 is a cross-sectional view showing the structure of the anode of the electrolytic cell with the exhaust passage; Figure 20 is a cross-sectional view of the A-A of Figure 19;
图 21为图 19的 B-B面剖图;  Figure 21 is a cross-sectional view taken along line B-B of Figure 19;
图 22为图 19的 C-C面剖图;  Figure 22 is a cross-sectional view taken along line C-C of Figure 19;
图 23为图 19的 D-D面剖图;  Figure 23 is a cross-sectional view taken along line D-D of Figure 19;
图 24为图 19的 E-E面剖图;  Figure 24 is a cross-sectional view taken along line E-E of Figure 19;
图 25为本发明实施例 5的带有排气通道的异形结构 ;电解槽阳极炭块剖面结构示意图; 图 26为图 25的 A-A面剖图; Figure 25 is a diagram showing a profiled structure of an anode having an exhaust passage according to Embodiment 5 of the present invention; Figure 26 is a cross-sectional view taken along line AA of Figure 25;
图 27为图 25的 B-B面剖图; Figure 27 is a cross-sectional view taken along line B-B of Figure 25;
图 28为图 25的 C-C面剖图; Figure 28 is a cross-sectional view taken along line C-C of Figure 25;
图 29为图 25的 D-D面剖图; Figure 29 is a cross-sectional view taken along line D-D of Figure 25;
图 30为图 25的 E-E面剖图; Figure 30 is a cross-sectional view taken along line E-E of Figure 25;
图 31为本发明实施例 6的带有排气通道的异形结构铝电解槽阳极炭块剖面结构示意图; 图 32为图 31的 A-A面剖图; Figure 31 is a cross-sectional view showing the structure of an anode carbon block of a profiled aluminum electrolytic cell with an exhaust passage according to Embodiment 6 of the present invention; and Figure 32 is a cross-sectional view taken along line A-A of Figure 31;
图 33为图 31的 B-B面剖图; Figure 33 is a cross-sectional view taken along line B-B of Figure 31;
图 34为图 31的 C-C面剖图; Figure 34 is a cross-sectional view taken along line C-C of Figure 31;
图 35为图 31的 D-D面剖图; Figure 35 is a cross-sectional view taken along line D-D of Figure 31;
图 36为图 31的 E-E面剖图; Figure 36 is a cross-sectional view taken along line E-E of Figure 31;
图 37为本发明实施例 7的带有排气通道的异形结构铝电解槽阳极炭块剖面结构示意图; 图 38为图 37的 A-A面剖图; Figure 37 is a cross-sectional view showing the structure of an anode carbon block of a profiled aluminum electrolytic cell with an exhaust passage according to Embodiment 7 of the present invention; and Figure 38 is a cross-sectional view taken along line A-A of Figure 37;
图 39为图 37的 B-B面剖图; Figure 39 is a cross-sectional view taken along line B-B of Figure 37;
图 40为图 37的 C-C面剖图; Figure 40 is a cross-sectional view taken along line C-C of Figure 37;
图 41为图 37的 D-D面剖图; Figure 41 is a cross-sectional view taken along line D-D of Figure 37;
图 42为图 37的 E-E面剖图; Figure 42 is a cross-sectional view taken along line E-E of Figure 37;
图 43为本发明实施例 8的带有排气通道的异形结构铝电解槽阳极炭块剖面结构示意图; 图 44为图 43的 A-A面剖图; Figure 43 is a cross-sectional view showing the structure of an anode carbon block of a profiled aluminum electrolytic cell with an exhaust passage according to Embodiment 8 of the present invention; and Figure 44 is a cross-sectional view taken along line A-A of Figure 43;
图 45为图 43的 B-B面剖图; Figure 45 is a cross-sectional view taken along line B-B of Figure 43;
图 46为图 43的 C-C面剖图; Figure 46 is a cross-sectional view taken along line C-C of Figure 43;
图 47为图 43的 D-D面剖图; Figure 47 is a cross-sectional view taken along line D-D of Figure 43;
图 48为图 43的 E-E面剖图; Figure 48 is a sectional view taken along line E-E of Figure 43;
图 49为本发明实施例 9的带有排气通道的异形结构铝电解槽阳极炭块剖面结构示意图; 图 50为图 49的 A-A面剖图; Figure 49 is a cross-sectional view showing the structure of an anode carbon block of a profiled structure aluminum electrolytic cell with an exhaust passage according to Embodiment 9 of the present invention; and Figure 50 is a cross-sectional view taken along line A-A of Figure 49;
图 51为图 49的 B-B面剖图; Figure 51 is a cross-sectional view taken along line B-B of Figure 49;
图 52为图 49的 C-C面剖图; Figure 52 is a cross-sectional view taken along line C-C of Figure 49;
图 53为图 49的 D-D面剖图; Figure 53 is a cross-sectional view taken along line D-D of Figure 49;
图 54为图 49的 E-E面剖图; Figure 54 is a sectional view taken along line E-E of Figure 49;
图 55 为本发明实施例 10 的带有排气通道的异形结构铝电解槽阳极炭块剖面结构示意 图; Figure 55 is a cross-sectional view showing the structure of an anode carbon block of a profiled aluminum electrolytic cell with an exhaust passage according to Embodiment 10 of the present invention; Figure
图 56为图 55的 A-A面剖图;  Figure 56 is a cross-sectional view taken along line A-A of Figure 55;
图 57为图 55的 C-C面剖图;  Figure 57 is a cross-sectional view taken along line C-C of Figure 55;
图中 1、 阳极炭块, 2、 炭碗, 3、 凹槽, 4、 通孔, 5、 沟槽, 6、 盖板。  Figure 1, anode carbon block, 2, charcoal bowl, 3, groove, 4, through hole, 5, groove, 6, cover.
具体实施方式 Detailed ways
本发明实施例中的炭碗的内径为 100~250mm, 深度为 100~200mm。  The carbon bowl in the embodiment of the present invention has an inner diameter of 100 to 250 mm and a depth of 100 to 200 mm.
实施例 1 Example 1
带有排气通道的异形结构铝电解槽阳极炭块剖面结构如图 1所示, A-A面结构如图 2 所示, B-B面结构如图 3所示, C-C面结构如图 4所示, D-D面结构如图 5所示, E-E面结 构如图 6所示; 阳极炭块 1的顶面边部设有倒角, 顶面上均匀分布有两排炭碗, 每排炭碗沿 阳极炭块纵向排列, 由 4个炭碗 2组成; 炭碗之间设有凹槽 3, 凹槽底部设有通孔 4与阳极 炭块底部的沟槽 5连通; 凹槽上方设有盖板 6;  The cross-sectional structure of the anode carbon block of the special-shaped aluminum electrolysis cell with exhaust passage is shown in Fig. 1. The structure of AA surface is shown in Fig. 2, the structure of BB surface is shown in Fig. 3, and the structure of CC surface is shown in Fig. 4. The surface structure is shown in Fig. 5. The EE surface structure is shown in Fig. 6. The top surface of the anode carbon block 1 is chamfered, and two rows of carbon bowls are uniformly distributed on the top surface, and each row of carbon bowls is along the anode carbon block. The longitudinal arrangement is composed of 4 carbon bowls 2; the carbon bowl is provided with a groove 3, the bottom of the groove is provided with a through hole 4 communicating with the groove 5 at the bottom of the anode carbon block; a cover plate 6 is arranged above the groove;
同一排炭碗上的相邻两个炭碗之间设有横向凹槽, 在两排炭碗之间设有纵向凹槽, 横向 凹槽与纵向凹槽互相连通;  There are lateral grooves between two adjacent carbon bowls on the same row of charcoal bowls, and longitudinal grooves are arranged between the two rows of carbon bowls, and the transverse grooves and the longitudinal grooves communicate with each other;
每个凹槽在阳极炭块底面相对应的位置上设有沟槽; 每个凹槽底部设有 3个通孔与该凹 槽相对应的沟槽连通。  Each groove is provided with a groove at a position corresponding to the bottom surface of the anode carbon block; and three through holes are provided at the bottom of each groove to communicate with the groove corresponding to the groove.
横向凹槽的轴线与阳极炭块的纵向轴线垂直, 横向凹槽的轴线位于相邻两个炭碗正中, 横向凹槽的两端通到阳极炭块两个长边上的倒角上;纵向凹槽的轴线与阳极炭块的轴线平行; 纵向凹槽位于相邻两排炭碗正中, 纵向凹槽的两端通到阳极炭块两个短边上的倒角上;  The axis of the transverse groove is perpendicular to the longitudinal axis of the anode carbon block, the axis of the transverse groove is located in the middle of two adjacent carbon bowls, and both ends of the transverse groove are open to the chamfers on the two long sides of the anode carbon block; The axis of the groove is parallel to the axis of the anode carbon block; the longitudinal groove is located in the middle of the adjacent two rows of carbon bowls, and both ends of the longitudinal groove are open to the chamfers on the two short sides of the anode carbon block;
各沟槽的顶部距阳极炭块顶部高度为 20~50cm, 底部通到阳极炭块的底表面, 其中与横 向凹槽相对应的沟槽为横向沟槽, 与纵向凹槽相对应的沟槽为纵向沟槽, 横向沟槽的长度与 阳极炭块宽度相等, 纵向沟槽的长度与阳极炭块长度相等, 各沟槽的宽度为 2.5~3.5cm; 各凹槽的横截面为倒置的三角形, 高度为 3~10cm, 顶面的宽度为 3~10cm;  The top of each groove is 20~50cm from the top of the anode carbon block, and the bottom part is connected to the bottom surface of the anode carbon block, wherein the groove corresponding to the lateral groove is a lateral groove, and the groove corresponding to the longitudinal groove For the longitudinal groove, the length of the transverse groove is equal to the width of the anode carbon block, the length of the longitudinal groove is equal to the length of the anode carbon block, and the width of each groove is 2.5 to 3.5 cm; the cross section of each groove is an inverted triangle , the height is 3~10cm, and the width of the top surface is 3~10cm;
通孔的纵轴线与阳极炭块底面垂直;  The longitudinal axis of the through hole is perpendicular to the bottom surface of the anode carbon block;
通孔为小通孔, 横截面为四个角为圆角的长方形, 面积为 10cm2; The through hole is a small through hole, and the cross section is a rectangle with four corners rounded, and the area is 10 cm 2 ;
制备方法为:  The preparation method is:
采用振动成型制作阳极炭块生坯, 振模内炭糊上部的重锤的下表面带有对应的凸起, 对 应凸起是指与阳极炭块上的炭碗、 凹槽和深孔位置相应的凸起结构, 在振动成型时在阳极炭 块生坯上制成炭碗凹槽和高度在 20~50cm的深孔, 然后将脱模后的这种阳极炭块生坯送到焙 烧炉中, 在 1100~1300°C的温度下进行焙烧, 制成带有炭碗、 凹槽和深孔的阳极炭块焙烧体; 然后再在阳极炭块焙烧体底部物理切割开设沟槽, 并使沟槽与深孔连通, 形成通孔, 制成带 有排气通道的异形结构铝电解槽阳极炭块; The anode carbon block green body is prepared by vibration molding, and the lower surface of the weight of the upper part of the carbon paste in the vibration mode has corresponding protrusions, and the corresponding protrusions are corresponding to the positions of the carbon bowl, the groove and the deep hole on the anode carbon block. The convex structure is formed into a carbon bowl groove and a deep hole having a height of 20 to 50 cm on the anode carbon block green body during vibration molding, and then the demolded anode carbon block green body is sent to the baking furnace. Roasting at a temperature of 1100 to 1300 ° C to produce an anode carbon block calcined body having a charcoal bowl, a groove and a deep hole; Then, a groove is physically cut at the bottom of the anode carbon block calcining body, and the groove is connected with the deep hole to form a through hole, and the anode carbon block of the special-shaped aluminum electrolytic cell with the exhaust passage is formed;
制成后在凹槽上设置盖板; 盖板搭在凹槽上, 使盖板与炭块形成一体, 在盖板和凹槽之 间形成断面为三角形的孔道。  After the preparation, a cover plate is arranged on the groove; the cover plate is placed on the groove, so that the cover plate is integrated with the carbon block, and a tunnel having a triangular cross section is formed between the cover plate and the groove.
经过试验, 采用该阳极炭块能够降低槽电压, 阳极产生的气体排放畅通均匀, 气体的逸 出对阴极铝液波动影响明显减少, 未发生阳极炭块的脱落现象。  After the experiment, the anode carbon block can reduce the tank voltage, the gas emissions generated by the anode are unimpeded, and the gas escape has a significant effect on the fluctuation of the cathode aluminum liquid, and the anode carbon block does not fall off.
实施例 2 Example 2
带有排气通道的异形结构铝电解槽阳极炭块剖面结构如图 7所示, A-A面结构如图 8 所示, B-B面结构如图 9所示, C-C面结构如图 10所示, D-D面结构如图 11所示, E-E面结 构如图 12所示; 阳极炭块 1的顶面边部设有倒角,顶面上均匀分布有一排炭碗沿阳极炭块纵 向排列, 一排炭碗由 4个炭碗 2组成; 炭碗之间设有凹槽 3, 凹槽底部设有通孔 4与阳极炭 块底部的沟槽 5连通; 凹槽上方设有盖板 6;  The cross-sectional structure of the anode carbon block of the profiled aluminum electrolytic cell with exhaust passage is shown in Fig. 7. The structure of the AA surface is shown in Fig. 8, the structure of the BB surface is shown in Fig. 9, and the structure of the CC surface is shown in Fig. 10. The surface structure is shown in Fig. 11, and the EE surface structure is shown in Fig. 12; the top surface of the anode carbon block 1 is chamfered, and a row of carbon bowls evenly distributed on the top surface is arranged along the longitudinal direction of the anode carbon block, and a row of carbon The bowl is composed of 4 carbon bowls 2; the carbon bowl is provided with a groove 3, the bottom of the groove is provided with a through hole 4 communicating with the groove 5 at the bottom of the anode carbon block; a cover plate 6 is arranged above the groove;
相邻两个炭碗之间设有横向凹槽; 每个凹槽在阳极炭块底面相对应的位置上设有沟槽; 每个凹槽底部设有 7个通孔与该凹槽相对应的沟槽连通;  A lateral groove is disposed between two adjacent carbon bowls; each groove is provided with a groove at a corresponding position on the bottom surface of the anode carbon block; and 7 through holes are provided at the bottom of each groove corresponding to the groove Groove connection;
横向凹槽的轴线与阳极炭块的纵向轴线垂直, 横向凹槽的轴线位于相邻两个炭碗正中, 横向凹槽的两端通到阳极炭块两个长边上的倒角处;  The axis of the transverse groove is perpendicular to the longitudinal axis of the anode carbon block, the axis of the transverse groove is located in the middle of two adjacent carbon bowls, and both ends of the transverse groove open to the chamfers on the two long sides of the anode carbon block;
沟槽的顶面距阳极炭块顶部高度为 20~50cm, 底面与阳极炭块的底面连通, 沟槽的长度 与阳极炭块宽度相等, 各沟槽的宽度为 2.5~3.5cm;  The top surface of the trench is 20~50cm from the top of the anode carbon block, and the bottom surface is connected with the bottom surface of the anode carbon block. The length of the groove is equal to the width of the anode carbon block, and the width of each groove is 2.5~3.5cm;
凹槽的横截面为倒置的三角形, 高度为 3~10cm; 顶面的宽度为 3~10cm; The cross section of the groove is an inverted triangle with a height of 3~10cm; the width of the top surface is 3~10cm ;
通孔的纵轴线与阳极炭块底面垂直;  The longitudinal axis of the through hole is perpendicular to the bottom surface of the anode carbon block;
通孔为小通孔, 横截面为四个角为圆角的长方形, 面积为 12cm2; The through hole is a small through hole, and the cross section is a rectangle with four corners rounded, and the area is 12 cm 2 ;
制备方法为:  The preparation method is:
采用模压成型法制作炭块, 其压模内的上模芯的下表面带有对应的凸起, 在模压成型时 在阳极炭块生坯上制成炭碗、 凹槽和高度在 20~50cm的深孔, 其余部分同实施例 1 ;  The carbon block is formed by compression molding, and the lower surface of the upper core in the stamper has corresponding protrusions, and the carbon bowl, the groove and the height are formed on the anode carbon block green body at the time of molding, and the height is 20-50 cm. The deep hole, the rest is the same as in Example 1;
在凹槽上设置横向盖板;  Providing a lateral cover plate on the groove;
经过试验, 采用该阳极炭块降低槽电压, 阳极产生的气体排放畅通均匀, 气体的逸出对 阴极铝液波动影响明显减少, 未发生阳极炭块的脱落现象。  After the test, the anode carbon block was used to reduce the cell voltage, and the gas emissions generated by the anode were unsteadily uniform, and the gas escaping significantly reduced the fluctuation of the cathode aluminum liquid, and the anode carbon block did not fall off.
实施例 3 Example 3
带有排气通道的异形结构铝电解槽阳极炭块剖面结构如图 13所示, A-A面结构如图 14 所示, B-B面结构如图 15所示, C-C面结构如图 16所示, D-D面结构如图 17所示, E-E面 结构如图 18所示; 结构同实施例 1, 不同点在于: 横向凹槽上设有两个通孔与相对应的沟槽 连通, 纵向凹槽上设有一个通孔与相对应的沟槽连通; The cross-sectional structure of the anode carbon block of the shaped aluminum electrolysis cell with exhaust passage is shown in Fig. 13, the AA surface structure is shown in Fig. 14, the BB surface structure is shown in Fig. 15, and the CC surface structure is shown in Fig. 16, DD The surface structure is shown in Figure 17, EE surface The structure is as shown in FIG. 18; the structure is the same as that in Embodiment 1, except that: the transverse groove is provided with two through holes communicating with the corresponding grooves, and the longitudinal groove is provided with a through hole and a corresponding groove. Connected
沟槽的顶面距阳极炭块顶部高度为 20~50cm, 沟槽的宽度为 2.5~3.5cm;  The top surface of the trench is 20~50cm from the top of the anode carbon block, and the width of the trench is 2.5~3.5cm;
凹槽的横截面为倒置的三角形, 高度为 3~10cm, 顶面的宽度为 3~10cm;  The cross section of the groove is an inverted triangle, the height is 3~10cm, and the width of the top surface is 3~10cm;
通孔为大通孔, 横截面为长方形, 横向凹槽内的两个通孔的横截面面积为 50 cm2, 纵向 凹槽内的通孔的面积为 390cm2; The through hole is a large through hole, the cross section is rectangular, the cross-sectional area of the two through holes in the transverse groove is 50 cm 2 , and the area of the through hole in the longitudinal groove is 390 cm 2 ;
制备方法同实施例 1 ;  The preparation method is the same as that in the embodiment 1;
在凹槽上设置盖板, 方法同实施例 1 ;  Providing a cover plate on the groove, the method is the same as in the embodiment 1;
经过试验, 采用该阳极炭块降低槽电压, 阳极产生的气体排放畅通均匀, 气体的逸出对 阴极铝液波动影响明显减少, 未发生阳极炭块的脱落现象。  After the test, the anode carbon block was used to reduce the cell voltage, and the gas emissions generated by the anode were unsteadily uniform, and the gas escaping significantly reduced the fluctuation of the cathode aluminum liquid, and the anode carbon block did not fall off.
实施例 4 Example 4
带有排气通道的异形结构铝电解槽阳极炭块剖面结构如图 19所示, A-A面结构如图 20 所示, B-B面结构如图 21所示, C-C面结构如图 22所示, D-D面结构如图 23所示, E-E面 结构如图 24所示; 结构同实施例 1, 不同点在于: 每个凹槽底部设有 1个通孔与该凹槽相对 应的沟槽连通;  The cross-sectional structure of the anode carbon block of the shaped aluminum electrolysis cell with exhaust passage is shown in Fig. 19, the structure of the AA surface is shown in Fig. 20, the structure of the BB surface is shown in Fig. 21, and the structure of the CC surface is shown in Fig. 22, DD The surface structure is shown in FIG. 23, and the EE surface structure is as shown in FIG. 24; the structure is the same as that in Embodiment 1, except that: one through hole is provided at the bottom of each groove to communicate with the groove corresponding to the groove;
沟槽的顶面距阳极炭块顶部高度为 20~50cm, 各沟槽的宽度为 2.5~3.5cm;  The top surface of the trench is 20~50cm from the top of the anode carbon block, and the width of each trench is 2.5~3.5cm;
凹槽的横截面为倒置的三角形, 凹槽高度为 3~10cm, 顶面的宽度为 3~10cm; The cross section of the groove is an inverted triangle, the height of the groove is 3~10cm, and the width of the top surface is 3~10cm ;
通孔为大通孔, 横截面为长方形, 横向凹槽内的通孔面积为 100cm2, 纵向凹槽内的通孔 面积为 390cm2; 各通孔互相连通; The through hole is a large through hole, the cross section is rectangular, the through hole area in the lateral groove is 100 cm 2 , and the through hole area in the longitudinal groove is 390 cm 2 ; each through hole is connected to each other;
制备方法同实施例 2;  The preparation method is the same as in the embodiment 2;
在凹槽上设置盖板, 方法 同实施例 1 ;  Providing a cover plate on the groove, the method is the same as in the embodiment 1;
经过试验, 采用该阳极炭块降低槽电压, 阳极产生的气体排放畅通均匀, 气体的逸出对 阴极铝液波动影响明显减少, 未发生阳极炭块的脱落现象。  After the test, the anode carbon block was used to reduce the cell voltage, and the gas emissions generated by the anode were unsteadily uniform, and the gas escaping significantly reduced the fluctuation of the cathode aluminum liquid, and the anode carbon block did not fall off.
实施例 5 Example 5
带有排气通道的异形结构铝电解槽阳极炭块剖面结构如图 25所示, A-A面结构如图 26 所示, B-B面结构如图 27所示, C-C面结构如图 28所示, D-D面结构如图 29所示, E-E面 结构如图 30所示; 结构同实施例 1, 不同点在于: 每个横向凹槽内设有 1各通孔与相对应的 沟槽连通, 纵向凹槽内设有 4各通孔与相对应的沟槽连通;  The cross-sectional structure of the anode carbon block of the profiled aluminum electrolytic cell with exhaust passage is shown in Fig. 25. The structure of the AA surface is shown in Fig. 26, the structure of the BB surface is shown in Fig. 27, and the structure of the CC surface is shown in Fig. 28. The surface structure is shown in Fig. 29, and the EE surface structure is shown in Fig. 30; the structure is the same as that in the first embodiment, and the difference is that: each of the lateral grooves is provided with one through hole communicating with the corresponding groove, the longitudinal groove 4 through holes are communicated with corresponding grooves;
沟槽的顶面距阳极炭块顶部高度为 20~50cm, 各沟槽的宽度为 2.5~3.5cm;  The top surface of the trench is 20~50cm from the top of the anode carbon block, and the width of each trench is 2.5~3.5cm;
凹槽的横截面为倒置的三角形, 高度为 3~10cm, 顶面的宽度为 3~10cm; 通孔为大通孔, 横截面为长方形, 横向凹槽内的通孔的横截面面积为 lOOcm2, 纵向凹槽 内的通孔的面积为 300cm2; The cross section of the groove is an inverted triangle with a height of 3~10cm and a top surface width of 3~10cm ; The through hole is a large through hole, the cross section is rectangular, the cross hole area of the through hole in the horizontal groove is 100 cm 2 , and the area of the through hole in the longitudinal groove is 300 cm 2 ;
制备方法同实施例 1 ;  The preparation method is the same as that in the embodiment 1;
在凹槽上设置盖板, 方法同实施例 1 ;  Providing a cover plate on the groove, the method is the same as in the embodiment 1;
经过试验, 采用该阳极炭块降低槽电压, 阳极产生的气体排放畅通均匀, 气体的逸出对 阴极铝液波动影响明显减少, 未发生阳极炭块的脱落现象。  After the test, the anode carbon block was used to reduce the cell voltage, and the gas emissions generated by the anode were unsteadily uniform, and the gas escaping significantly reduced the fluctuation of the cathode aluminum liquid, and the anode carbon block did not fall off.
实施例 6 Example 6
带有排气通道的异形结构铝电解槽阳极炭块剖面结构如图 31所示, A-A面结构如图 32 所示, B-B面结构如图 33所示, C-C面结构如图 34所示, D-D面结构如图 35所示, E-E面 结构如图 36所示; 结构同实施例 1, 不同点在于: 每个横向凹槽底部设有 2个通孔与该凹槽 相对应的沟槽连通; 每个纵向凹槽内设有 4个通孔与相对应的沟槽连通;  The cross-sectional structure of the anode carbon block of the profiled aluminum electrolytic cell with the exhaust passage is shown in Fig. 31, the AA surface structure is shown in Fig. 32, the BB surface structure is shown in Fig. 33, and the CC surface structure is shown in Fig. 34, DD. The surface structure is shown in FIG. 35, and the EE surface structure is as shown in FIG. 36; the structure is the same as that in Embodiment 1, except that: two through holes are provided at the bottom of each lateral groove to communicate with the groove corresponding to the groove; Each of the longitudinal grooves is provided with four through holes communicating with corresponding grooves;
沟槽的顶面距阳极炭块顶部高度为 20~50cm, 宽度为 2.5~3.5cm;  The top surface of the trench is 20~50cm from the top of the anode carbon block, and the width is 2.5~3.5cm;
凹槽的横截面为倒置的三角形, 高度为 3~10cm, 顶面的宽度为 3~10cm; The cross section of the groove is an inverted triangle with a height of 3~10cm and a top surface width of 3~10cm ;
通孔为大通孔, 横截面为长方形, 面积为 50cm2; The through hole is a large through hole, and the cross section is rectangular, and the area is 50 cm 2 ;
制备方法同实施例 2;  The preparation method is the same as in the embodiment 2;
在凹槽上设置盖板, 方法同实施例 1 ;  Providing a cover plate on the groove, the method is the same as in the embodiment 1;
经过试验, 采用该阳极炭块降低槽电压, 阳极产生的气体排放畅通均匀, 气体的逸出对 阴极铝液波动影响明显减少, 未发生阳极炭块的脱落现象。  After the test, the anode carbon block was used to reduce the cell voltage, and the gas emissions generated by the anode were unsteadily uniform, and the gas escaping significantly reduced the fluctuation of the cathode aluminum liquid, and the anode carbon block did not fall off.
实施例 7 Example 7
带有排气通道的异形结构铝电解槽阳极炭块剖面结构如图 37所示, A-A面结构如图 38 所示, B-B面结构如图 39所示, C-C面结构如图 40所示, D-D面结构如图 41所示, E-E面 结构如图 42所示; 结构同实施例 6, 不同点在于: 三个横向凹槽分别与纵向凹槽连接的三个 交点处还分别设有一个小通孔, 小通孔横截面为圆形, 面积为 11cm2; The profile structure of the anode carbon block of the profiled aluminum reduction cell with exhaust passage is shown in Fig. 37, the AA surface structure is shown in Fig. 38, the BB surface structure is shown in Fig. 39, and the CC surface structure is shown in Fig. 40, DD The surface structure is shown in Fig. 41, and the EE surface structure is as shown in Fig. 42; the structure is the same as that in the embodiment 6, and the difference is that: three lateral grooves are respectively provided with a small pass at the three intersections of the longitudinal grooves. The hole and the small through hole have a circular cross section with an area of 11 cm 2 ;
制备方法同实施例 1 ;  The preparation method is the same as that in the embodiment 1;
在凹槽上设置盖板, 方法同实施例 1 ;  Providing a cover plate on the groove, the method is the same as in the embodiment 1;
经过试验, 采用该阳极炭块降低槽电压, 阳极产生的气体排放畅通均匀, 气体的逸出对 阴极铝液波动影响明显减少, 未发生阳极炭块的脱落现象。  After the test, the anode carbon block was used to reduce the cell voltage, and the gas emissions generated by the anode were unsteadily uniform, and the gas escaping significantly reduced the fluctuation of the cathode aluminum liquid, and the anode carbon block did not fall off.
实施例 8 Example 8
带有排气通道的异形结构铝电解槽阳极炭块剖面结构如图 43所示, A-A面结构如图 44 所示, B-B面结构如图 45所示, C-C面结构如图 46所示, D-D面结构如图 47所示, E-E面 结构如图 48所示, 阳极炭块 1的顶面边部设有倒角, 顶面上均匀分布有两排炭碗, 每排炭碗 沿阳极炭块纵向排列, 由 4个炭碗 2组成; 炭碗之间设有凹槽 3, 凹槽底部设有通孔 4与阳 极炭块底部的沟槽 5连通, 凹槽上方设有盖板 6; The cross-sectional structure of the anode carbon block of the profiled aluminum electrolytic cell with the exhaust passage is shown in Fig. 43, the AA surface structure is shown in Fig. 44, the BB surface structure is shown in Fig. 45, and the CC surface structure is shown in Fig. 46, DD The surface structure is shown in Figure 47, EE surface The structure is as shown in Fig. 48, the top side of the anode carbon block 1 is chamfered, and two rows of carbon bowls are uniformly distributed on the top surface, and each row of carbon bowls is arranged along the longitudinal direction of the anode carbon block, and is composed of four carbon bowls 2. a groove 3 is provided between the carbon bowls, and a through hole 4 is formed in the bottom of the groove to communicate with the groove 5 at the bottom of the anode carbon block, and a cover plate 6 is disposed above the groove;
凹槽为在两排炭碗之间的纵向凹槽; 凹槽在阳极炭块底面相对应的位置上设有沟槽; 凹 槽底部设有 1个通孔与沟槽连通;  The groove is a longitudinal groove between the two rows of carbon bowls; the groove is provided with a groove at a position corresponding to the bottom surface of the anode carbon block; and a through hole is provided at the bottom of the groove to communicate with the groove;
纵向凹槽的轴线与阳极炭块的轴线平行; 纵向凹槽位于相邻两排炭碗正中, 纵向凹槽的 两端通到阳极炭块两个短边上的倒角位置上;  The axis of the longitudinal groove is parallel to the axis of the anode carbon block; the longitudinal groove is located in the middle of the adjacent two rows of carbon bowls, and the two ends of the longitudinal groove are open to the chamfered position on the two short sides of the anode carbon block;
沟槽的顶面距阳极炭块顶部高度为 20~50cm, 底面与阳极炭块的底面连通, 沟槽的宽度 为 2.5~3.5cm; The top surface of the trench is 20~50cm from the top of the anode carbon block, and the bottom surface is connected with the bottom surface of the anode carbon block, and the width of the groove is 2.5~3.5cm ;
凹槽的横截面为倒置的三角形, 高度为 3~10cm, 顶面的宽度为 3~10cm;  The cross section of the groove is an inverted triangle, the height is 3~10cm, and the width of the top surface is 3~10cm;
通孔的纵轴线与阳极炭块底面垂直;  The longitudinal axis of the through hole is perpendicular to the bottom surface of the anode carbon block;
通孔为大通孔, 横截面为长方形, 面积为 390cm2; The through hole is a large through hole, and the cross section is rectangular, and the area is 390 cm 2 ;
制备方法同实施例 2;  The preparation method is the same as in the embodiment 2;
在凹槽上设置纵向盖板, 方法同实施例 1。  A longitudinal cover is provided on the groove in the same manner as in the first embodiment.
经过试验, 采用该阳极炭块降低槽电压, 阳极产生的气体排放畅通均匀, 气体的逸出对 阴极铝液波动影响明显减少, 未发生阳极炭块的脱落现象。  After the test, the anode carbon block was used to reduce the cell voltage, and the gas emissions generated by the anode were unsteadily uniform, and the gas escaping significantly reduced the fluctuation of the cathode aluminum liquid, and the anode carbon block did not fall off.
实施例 9 Example 9
带有排气通道的异形结构铝电解槽阳极炭块剖面结构如图 49所示, A-A面结构如图 50 所示, B-B面结构如图 51所示, C-C面结构如图 52所示, D-D面结构如图 53所示, E-E面 结构如图 54所示; 结构同实施例 2, 不同点在于:  The cross-sectional structure of the anode carbon block of the profiled aluminum electrolytic cell with the exhaust passage is shown in Fig. 49, the structure of the AA surface is shown in Fig. 50, the structure of the BB surface is shown in Fig. 51, and the structure of the CC surface is shown in Fig. 52, DD The surface structure is shown in Fig. 53, and the EE surface structure is as shown in Fig. 54; the structure is the same as that in the second embodiment, and the difference is:
每个凹槽底部设有 1个通孔与该凹槽相对应的沟槽连通;  a through hole is provided at the bottom of each groove to communicate with a groove corresponding to the groove;
沟槽的顶面距阳极炭块顶部高度为 20~50cm, 沟槽的宽度为 2.5~3.5cm;  The top surface of the trench is 20~50cm from the top of the anode carbon block, and the width of the trench is 2.5~3.5cm;
凹槽的横截面为倒置的三角形, 高度为 3~10cm, 顶面的宽度为 3~10cm; The cross section of the groove is an inverted triangle with a height of 3~10cm and a top surface width of 3~10cm ;
通孔为大通孔, 横截面为长方形, 面积为 100cm2; The through hole is a large through hole, and the cross section is rectangular, and the area is 100 cm 2 ;
制备方法同实施例 1 ;  The preparation method is the same as that in the embodiment 1;
在凹槽上设置横向盖板, 方法同实施例 1 ;  a lateral cover is disposed on the groove, the method is the same as in Embodiment 1;
经过试验, 采用该阳极炭块降低槽电压, 阳极产生的气体排放畅通均匀, 气体的逸出对 阴极铝液波动影响明显减少, 未发生阳极炭块的脱落现象。  After the test, the anode carbon block was used to reduce the cell voltage, and the gas emissions generated by the anode were unsteadily uniform, and the gas escaping significantly reduced the fluctuation of the cathode aluminum liquid, and the anode carbon block did not fall off.
实施例 10 Example 10
带有排气通道的异形结构铝电解槽阳极炭块剖面结构如图 55所示, A-A面结构如图 56 所示, C-C面结构如图 57所示; 阳极炭块顶面边部设有倒角, 顶面上均匀分布有一排或两 排炭碗 2, 每排炭碗 2沿阳极炭块 1纵向排列, 由 4个炭碗组 2成; 炭碗 2之间设有凹槽 3, 阳极炭块 1底部设有沟槽 5; 凹槽 3底部设置通孔 4与沟槽 5连通, 通孔 4的长度与阳极炭 块 1的长度相同, 通孔 4与沟槽 5连接在一起, 将阳极炭块在纵向断开形成两个相同的小阳 极炭块; The profile structure of the anode carbon block of the shaped aluminum electrolysis cell with the exhaust passage is shown in Fig. 55, and the AA surface structure is shown in Fig. 56. As shown, the CC surface structure is shown in Fig. 57; the top surface of the anode carbon block is chamfered, and one or two rows of carbon bowls 2 are evenly distributed on the top surface, and each row of carbon bowls 2 are arranged longitudinally along the anode carbon block 1. 4, 4 carbon charcoal set; groove 3 is arranged between the carbon bowl 2, the bottom of the anode carbon block 1 is provided with a groove 5; the bottom of the groove 3 is provided with a through hole 4 communicating with the groove 5, the through hole 4 The length is the same as the length of the anode carbon block 1, the through hole 4 is connected with the groove 5, and the anode carbon block is broken in the longitudinal direction to form two identical small anode carbon blocks;
凹槽为纵向凹槽, 位于两排炭碗之间;  The groove is a longitudinal groove located between the two rows of charcoal bowls;
沟槽的顶面距阳极炭块顶部高度为 40cm, 沟槽的宽度为 3cm;  The top surface of the trench is 40 cm from the top of the anode carbon block, and the width of the trench is 3 cm;
凹槽的横截面为倒置的三角形, 高度为 6cm, 顶面的宽度为 6m; The cross section of the groove is an inverted triangle with a height of 6 cm and a top surface having a width of 6 m .
通道宽度与沟槽相同, 长度为 150cm, 横截面积为 450cm2; The channel width is the same as the groove, the length is 150cm, and the cross-sectional area is 450cm 2 ;
制备方法为: 采用振动成型法制作阳极炭块生坯; 振模内的上部重锤的下表面带有对应 的凸起, 在振动成型时在阳极炭块生坯上制成炭碗、 凹槽以及高度在 40cm且长度与阳极炭 块相同的深孔; 阳极炭块生坯出模并冷却后, 置入焙烧炉焙烧到 1100~1300°C, 制成带有炭 块、 深孔和凹槽的阳极炭块焙烧体; 再在阳极炭块焙烧体底部物理切割开设沟槽, 并使沟槽 与深孔连通, 将一个阳极炭块分割成两个小阳极炭块, 制成带有排气通道的异形结构铝电解 槽阳极炭块; 在凹槽上设置横向盖板, 方法同实施例 1 ;  The preparation method comprises the following steps: preparing the anode carbon block green body by vibration molding; the lower surface of the upper weight in the vibration mode has corresponding protrusions, and forming a carbon bowl and a groove on the anode carbon block green body during vibration molding. And a deep hole having a height of 40 cm and the same length as the anode carbon block; the anode carbon block green body is discharged from the mold and cooled, and then placed in a roasting furnace and fired to 1100 to 1300 ° C to form a carbon block, a deep hole and a groove. The anode carbon block is fired; then the groove is physically cut at the bottom of the anode carbon block calcined body, and the groove is connected with the deep hole, and an anode carbon block is divided into two small anode carbon blocks to be made with exhaust gas. Amorphous structure of the channel aluminum electrolytic cell anode carbon block; a lateral cover plate is arranged on the groove, the method is the same as the embodiment 1;
经过试验, 采用该阳极炭块降低槽电压, 阳极产生的气体排放畅通均匀, 气体的逸出对 阴极铝液波动影响明显减少, 未发生阳极炭块的脱落现象。  After the test, the anode carbon block was used to reduce the cell voltage, and the gas emissions generated by the anode were unsteadily uniform, and the gas escaping significantly reduced the fluctuation of the cathode aluminum liquid, and the anode carbon block did not fall off.

Claims

权 利 要 求 书 Claim
1、 一种带有排气通道的异形结构铝电解槽阳极炭块, 顶面边部设有倒角, 顶面上均匀分 布有一排或两排炭碗, 每排炭碗沿阳极炭块纵向排列, 由 3~5个炭碗组成; 其特征在于炭碗 之间设有凹槽, 阳极炭块底部设有沟槽; 其中凹槽底部设有通孔与阳极炭块底部的沟槽连通。 1. An anode carbon block with a profiled structure aluminum electrolysis cell with an exhaust passage, a chamfered surface at the top surface, and a row or two rows of carbon bowls evenly distributed on the top surface, each row of carbon bowls along the anode carbon block longitudinal direction Arranged, consisting of 3~5 carbon bowls; characterized by a groove between the carbon bowls, and a groove at the bottom of the anode carbon block; wherein the bottom of the groove is provided with a through hole communicating with the groove at the bottom of the anode carbon block.
2、根据权利要求 1所述的带有排气通道的异形结构铝电解槽阳极炭块,其特征在于所述 的阳极炭块顶面上设有一排炭碗, 相邻两个炭碗之间设有横向凹槽; 或所述的阳极炭块顶面 上设有两排炭碗, 在两排炭碗之间设有纵向凹槽, 或者同一排的相邻两个炭碗之间设有横向 凹槽, 或同时设有上述两种凹槽。  2. The anode carbon block of a profiled aluminum electrolysis cell with an exhaust passage according to claim 1, wherein a carbon row is arranged on the top surface of the anode carbon block, and between two adjacent carbon bowls. a lateral groove is provided; or two rows of carbon bowls are arranged on the top surface of the anode carbon block, and longitudinal grooves are arranged between the two rows of carbon bowls, or between two adjacent carbon bowls of the same row The transverse grooves, or both of the above grooves are provided.
3、根据权利要求 1所述的带有排气通道的异形结构铝电解槽阳极炭块,其特征在于所述 的沟槽位于每个凹槽在阳极炭块底面相对应的位置; 每个凹槽底部设有至少一个通孔与该凹 槽相对应的沟槽连通。  3. The anode carbon block of a profiled structure aluminum electrolytic cell with an exhaust passage according to claim 1, wherein said groove is located at a position corresponding to each groove on the bottom surface of the anode carbon block; The bottom of the groove is provided with at least one through hole communicating with a groove corresponding to the groove.
4、根据权利要求 2所述的带有排气通道的异形结构铝电解槽阳极炭块,其特征在于横向 凹槽的轴线与阳极炭块的纵向轴线垂直, 横向凹槽的轴线位于阳极炭块纵向方向上的相邻两 个炭碗正中, 横向凹槽的两端通到阳极炭块两个长边上的倒角处; 纵向凹槽的轴线与阳极炭 块的轴线平行; 纵向凹槽位于阳极炭块纵向方向上的相邻两排炭碗正中, 纵向凹槽的两端通 到阳极炭块两个短边上的倒角处。  4. The anode carbon block of a profiled aluminum electrolysis cell with an exhaust passage according to claim 2, wherein the axis of the transverse groove is perpendicular to the longitudinal axis of the anode carbon block, and the axis of the transverse groove is located at the anode carbon block. The two adjacent carbon bowls in the longitudinal direction are centered, and both ends of the transverse grooves open to the chamfers on the two long sides of the anode carbon block; the axis of the longitudinal grooves is parallel to the axis of the anode carbon block; the longitudinal grooves are located The two rows of carbon bowls in the longitudinal direction of the anode carbon block are centered, and both ends of the longitudinal groove are passed to the chamfers on the two short sides of the anode carbon block.
5、根据权利要求 1所述的带有排气通道的异形结构铝电解槽阳极炭块,其特征在于所述 的沟槽的顶部距阳极炭块顶部高度为 20~50cm, 沟槽的底部通到阳极炭块的底表面, 各沟槽 的宽度为 1.0~3.5cm。  5. The anode carbon block of a profiled aluminum electrolysis cell with an exhaust passage according to claim 1, wherein the top of the groove is 20 to 50 cm from the top of the anode carbon block, and the bottom of the groove is open. To the bottom surface of the anode carbon block, the width of each groove is 1.0 to 3.5 cm.
6、根据权利要求 1所述的带有排气通道的异形结构铝电解槽阳极炭块,其特征在于所述 的凹槽的横截面为倒置的等腰三角形或倒置的等腰梯形, 凹槽高度为 3~10cm;所述的横截面 为倒置的等腰三角形的凹槽,其顶面宽度为 3~10cm;所述的横截面为倒置的等腰梯形的凹槽, 其顶面宽度为 5~10cm, 底面的宽度为 3~8cm。  6. The abnormally structured aluminum electrolytic cell anode carbon block with an exhaust passage according to claim 1, wherein said groove has a cross section of an inverted isosceles triangle or an inverted isosceles trapezoid, a groove. The height is 3~10cm; the cross section is an inverted isosceles triangle groove having a top surface width of 3~10cm; the cross section is an inverted isosceles trapezoidal groove, and the top surface width is 5~10cm, the width of the bottom surface is 3~8cm.
7、根据权利要求 1所述的带有排气通道的异形结构铝电解槽阳极炭块,其特征在于所述 的通孔在凹槽底部, 且其纵轴线与阳极炭块底面垂直。  7. The abnormally structured aluminum electrolytic cell anode carbon block with an exhaust passage according to claim 1, wherein the through hole is at the bottom of the groove, and the longitudinal axis thereof is perpendicular to the bottom surface of the anode carbon block.
8、根据权利要求 1所述的带有排气通道的异形结构铝电解槽阳极炭块,其特征在于所述 的通孔分为小通孔和大通孔, 小通孔的横截面为圆形、 或椭圆形、 或方形或长方形, 面积为 3~18cm2, 其中所述的横截面为方形或长方形的小通孔, 方形或长方形的四个角为圆角; 所述 的大通孔的横截面为长方形, 面积为 18~500cm28. The abnormally structured aluminum electrolytic cell anode carbon block with an exhaust passage according to claim 1, wherein the through hole is divided into a small through hole and a large through hole, and the small through hole has a circular cross section. Or elliptical, or square or rectangular, having an area of 3 to 18 cm 2 , wherein the cross section is a square or rectangular small through hole, and the four corners of the square or rectangle are rounded; the horizontal of the large through hole The cross section is rectangular and the area is 18~500cm 2 .
9、根据权利要求 1所述的一种带有排气通道的异形结构铝电解槽阳极炭块,其特征在于 当通孔的长度与阳极炭块的长度相同时, 通孔与沟槽连接在一起, 将一个阳极炭块在纵向断 开形成两个相同的小阳极炭块。 9. The anode carbon block of a profiled aluminum electrolytic cell with an exhaust passage according to claim 1, wherein when the length of the through hole is the same as the length of the anode carbon block, the through hole is connected to the groove. Together, an anode carbon block is broken in the longitudinal direction. Open two identical small anode carbon blocks.
10、 权利要求 1所述的带有排气通道的异形结构铝电解槽阳极炭块的制备方法, 其特征 在于: 采用振动成型法或模压成型法制作阳极炭块生坯; 当采用振动成型法时, 其振模内的 上部重锤的下表面带有对应的凸起; 当采用模压成型法时, 其压模内的上模芯的下表面带有 对应的凸起; 在振动成型或模压成型时在阳极炭块生坯上制成炭碗、 凹槽和高度在 20~50cm 的深孔; 阳极炭块生坯出模并冷却后, 置入焙烧炉焙烧到 1100~1300°C, 制成顶部带有炭碗、 深孔和凹槽的阳极炭块焙烧体; 再在阳极炭块焙烧体底部物理切割开设沟槽, 并使沟槽与深 孔或者槽形通道连通, 形成通孔, 制成带有排气通道的异形结构铝电解槽阳极炭块; 所述的 对应的凸起是指与阳极炭块上的炭碗、 凹槽和通孔位置相应的凸起结构。  10 . The method for preparing an anode carbon block of a profiled aluminum electrolytic cell with an exhaust passage according to claim 1 , wherein: the anode carbon block green body is formed by a vibration molding method or a compression molding method; When the upper surface of the upper weight in the vibration mode has a corresponding protrusion; when the molding method is used, the lower surface of the upper core in the compression mold has a corresponding protrusion; in vibration molding or molding During the molding, a carbon bowl, a groove and a deep hole with a height of 20 to 50 cm are formed on the anode carbon block green body; the anode carbon block green body is discharged from the mold and cooled, and then placed in a roasting furnace and fired to 1100 to 1300 ° C. An anode carbon block calcined body having a carbon bowl, a deep hole and a groove at the top; and a groove is physically cut at the bottom of the anode carbon block calcined body, and the groove is connected with the deep hole or the grooved passage to form a through hole. The anode carbon block of the profiled aluminum electrolytic cell with the exhaust passage is formed; the corresponding protrusion refers to the convex structure corresponding to the position of the carbon bowl, the groove and the through hole on the anode carbon block.
PCT/CN2012/078394 2011-09-05 2012-07-09 Aluminum electrolytic tank anode carbon block of irregularly-shaped structure with exhaust passage and preparation method thereof WO2013034024A1 (en)

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CN201110260656.3A CN102345141B (en) 2011-09-05 2011-09-05 Aluminum electrolytic tank anode carbon block of irregularly-shaped structure with exhaust passage and preparation method thereof
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