CN1091471C - Carbon block as cathode with compound titanium boride-carbon layer and its preparing process - Google Patents
Carbon block as cathode with compound titanium boride-carbon layer and its preparing process Download PDFInfo
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- CN1091471C CN1091471C CN00113420A CN00113420A CN1091471C CN 1091471 C CN1091471 C CN 1091471C CN 00113420 A CN00113420 A CN 00113420A CN 00113420 A CN00113420 A CN 00113420A CN 1091471 C CN1091471 C CN 1091471C
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Abstract
The present invention relates to a titanium boride and carbon composite layer cathode block for an aluminium electrolytic tank, which has the technical scheme that a titanium boride composite carbon paste layer is arranged on the surface of a base body of the cathode block, and the titanium boride composite layer and the base body of the cathode block are tightly combined together by vibratory formation. Then, the titanium boride composite layer and the base body of the cathode block are put in a roasting furnace and roasted together, and the titanium boride composite layer and the base body of the cathode block can be combined into an identical complex. The titanium boride and carbon composite layer is used as a working surface of the aluminium electrolytic tank, has the characteristics of good electrical conductivity, high thermal stability, strong electrolyte erosion resisting performance, good wettability for aluminium liquid, etc., and can effectively prolong the service life of the aluminium electrolytic tank. The titanium boride and carbon composite layer cathode block has the advantages of battery efficiency increase, energy saving and consumption reduction, and can be widely used as a cathode material of the aluminium electrolytic tank and an inner lining material of a refining blast furnace.
Description
The present invention relates to a kind of aluminium electrolytic industry cathode material and preparation method thereof.The cathode block that particularly relates to aluminium electrolyzer.
Electrolysis legal system aluminium is unique industry system aluminium method of system aluminium in the worldwide, Chinese patent specification sheets CN162008A has disclosed aluminium electrolysis cell cathode carbon block and preparation method thereof, and it mainly is to adopt the method for extrusion molding, ring-form calcining furnace roasting to produce whole cathode block for electricity section coal and coal-tar pitch mixture.Also having now the schungite carbon piece that generally uses is to be added by electric forging coal and synthetic graphite that coal-tar pitch is baking mixed to form, because it is low that conventional cathode carbon piece and schungite cathode block have resistivity, Heat stability is good, certain electrolyte-resistant and molten slag molten iron corrosive ability are arranged, be widely used in the liner of aluminium cell and metallurgical furnace, particularly be used as the cathode material of aluminium metallurgy industry electrolyzer in a large number.Numerous studies show that, start the initial stage at aluminium cell, sodium and ionogen are fast to the infiltration of conventional cathode carbon piece and schungite piece in particularly begin in electrolysis 200 minutes, it is to cause that the carbon piece expands and distortion, the key reason that causes the cathode block early damage, simultaneously also be to cause that furnace bottom resistance increases, the factor that cathode drop raises; There is its surface of conventional cathode carbon piece and schungite carbon piece to be difficult for moistening again by aluminium liquid, its not wettability can make a large amount of aluminium liquid in the electrolyzer be the state of converging, this aluminium that converges state acts on mutually with electromagnetic force and viscous force, cause the volatile fluctuation and the eddy current rotation of aluminium liquid, this enters ionogen with regard to the aluminium that makes the aluminium liquid layer easily and participates in secondary reaction or aluminium liquid layer moment and contact with the anode bottom and cause short circuit, and current efficiency is reduced.This shows, adopt the whole cathode material of making refining electrolytic bath for conventional cathode carbon piece and schungite carbon piece still to have certain defective, can cause the high and electrolyzer time limit of service shortening of power consumption.Titanium boride has good electroconductibility, thermostability, corrosion resistance, wet performance to aluminium liquid is good, little with the contact resistance of aluminium liquid, and absorbed electrolyte composition hardly, some producers are applied to aluminium electrolytic cell cathode to titanium boride and study, concrete way is to be that electric tank working surface-coated one deck titanium boride of being built into of conventional cathode carbon piece or schungite cathode block is stuck with paste in integral body, then by solidifying, carry out roasting with electrolyzer, make major defect in this way be: the thermal expansion in the calcination start-up course of coating and carbon block base body is shunk inconsistent, easily cause deep layer to peel off, come off, make the bottom land unfairness, irregular bottom land is under the washing away of aluminium liquid, further come off, lose the effect of titanium boride, cause the decline of aluminum products quality on the contrary.
The objective of the invention is to develop a kind of aluminium liquid contact surface integrated molding last layer titanium boride---cathode block of carbon composite layer at schungite carbon block base body, make it to have that resistivity is low, Heat stability is good, electrolyte-resistant etch, to characteristic such as the wettability of aluminium liquid is good.
Technology contents of the present invention mainly is to solve titanium boride---the prescription of carbon composite layer and preparation method's problem of cathode block thereof, makes full use of the various good characteristics of titanium boride material.First: titanium boride has good inertia and electroconductibility, thermostability and corrosion resistance, the composite bed of integrated molding titanium boride---carbon composite layer cathode block has the dauer effect of opposing sodium and electrolyte osmosis, thereby keeps the stable of electrode resistance rate; Second: titanium boride is easily moistening by aluminium liquid, make the aluminium liquid in the electrolyzer can not present the state of converging, thereby avoid taking place secondary reaction or short circuit and reduce current efficiency, also make the ionogen precipitation be difficult for being adsorbed on cathode surface, because of face is difficult for generating crust, keep regular in the groove for a long time.
The object of the present invention is achieved like this: produce in the schungite cathode block process in vibratory compaction, directly at a carbon block base dignity uniform titanium boride---carbon paste layer on the surface of aluminium liquid, through the vibratory compaction compacting this layer and carbon block base body are closely linked, the together roasting in the stoving oven of packing into then, the two is become in conjunction with consistent complex body, and titanium boride---carbon composite layer is as the working face of electrolyzer.
Schungite negative electrode carbon body matrix formulation weight percent is formed:
Electric calcined anthracite: 70～80%, synthetic graphite: 10～25%, binding agent: 5～20%.
Titanium boride---the percentage composition of carbon composite layer formulation weight is:
Electric calcined anthracite: 40～60%, titanium boride powder: 20～45%, binding agent: 15～35%.
Preparation process of the present invention is as follows:
1, get schungite carbon block base body and titanium boride---the carbon composite layer aggregate.
2, with above-mentioned two class aggregate fragmentations, screening, powder process, weighing and burden by weight percentage.
3, binding agent being dissolved the back weighing is added in above-mentioned two kinds of aggregates.
4, mix respectively and pinch.
5, earlier schungite piece batch mixing is carried out preliminary vibratory compaction processing, the uniform one deck of laminar surface has mixed the titanium boride of pinching thereon again---the carbon composite layer batching, and then carry out integral vibratory compaction.
6, with forming titanium boride---the carbon composite layer cathode block is sent into box roasting kiln roasting.
7, carry out machining after the cooling.
8, check, packing, warehouse-in.
Wherein key is to have introduced titanium boride in schungite carbon block base surface---carbon composite layer, composite bed thickness are 8～50mm.The granularity of electric calcined anthracite should be less than 2mm in titanium boride one carbon composite layer.Mix and pinch out 150 ℃ of thickener temperature, 155～160 ℃ of die temperatures, roasting ends 1300 ℃ of fiery temperature.Used binding agent is to be formed by two or more hybrid modulation in coal-tar pitch, washing oil, carbolineum, the coal tar wet goods.
Compared with the prior art, the present invention has following characteristics:
1, titanium boride---the electrolytic bath hall that the carbon composite layer cathode block is built by laying bricks or stones is regular in use, uses the pit degree not have the obvious sediment crust, and prolong the work-ing life of electrolyzer.
2, titanium boride---the electrolyzer operation that the carbon composite layer cathode block is built by laying bricks or stones is more steady, and current efficiency increases, and energy-saving and cost-reducing.
Embodiment: schungite piece matrix formulation by weight per-cent consists of: electric calcined anthracite 70%, synthetic graphite 15%, binding agent 15%.
Titanium boride---the percentage composition of carbon piece composite bed formulation by weight is: electric calcined anthracite 52.2%, titanium boride powder 28.8%, binding agent 19%.
Preparation process is as follows:
1, get schungite carbon piece and titanium boride by the composition of above-mentioned prescription---the aggregate of carbon composite layer.
2, with above-mentioned two class aggregate fragmentations, screening, powder process, and by the weight percent weighing and burden of above-mentioned prescription.
3, two kinds prepared aggregate in add the binding agent prepared respectively, binding agent is mixed by coal-tar pitch and carbolineum half and half and forms, sends into respectively to mix again and pinches fully mixed pinching in the pot.
4, earlier mixed the pinching of carbon block base body expected that sending into vibrating forming machine carries out preliminary vibratory compaction, the uniform one deck of laminar surface has mixed the titanium boride of pinching thereon again---the carbon composite layer batching, and then carry out integral vibratory compaction.
5, the titanium boride of forming---the carbon composite layer cathode block is sent into the roasting kiln roasting.
6, carry out machining after the cooling.
7, check, packing, warehouse-in.
Technology controlling and process:
The grain composition of schungite carbon block base body aggregate is:
Grade: 12～8mm, 8～4mm, 4～2mm, 2～0mm, the following powder of 200 orders
Content: 10 ± 2%, 17 ± 2%, 13 ± 2%, 16 ± 2%, 44 ± 2%.
The grade of electric calcined anthracite is 0～2mm in titanium boride---the carbon composite layer.
Mixing and pinching out the thickener temperature is 150 ℃, and die temperature is 155～166 ℃.
Composite bed thickness is controlled at 15 ± 5mm after the moulding.
Roasting ends fiery temperature: 1300 ℃.
Claims (3)
1, a kind of titanium boride---carbon composite layer cathode block, it is characterized in that matrix is the schungite cathode block, it is electric calcined anthracite 70%～80%, synthetic graphite 10～25%, binding agent 5～20% that the matrix formulation weight percent is formed, the matrix working face is titanium boride a---carbon composite layer, titanium boride---the percentage composition of carbon composite layer formulation weight is electric calcined anthracite 40～60%, titanium boride 20～45%, binding agent 15～35%.
The thickness of 2, titanium boride according to claim 1---the carbon composite layer cathode block is characterized in that titanium boride---carbon composite layer working face is 8～50mm.
3, a kind of titanium boride---carbon composite layer cathode block preparation method is characterized in that preparation process is as follows:
A, by the prescription composition be on the waiting list schungite carbon piece and titanium boride---the aggregate of carbon composite layer, wherein schungite carbon block base body formulation weight per-cent consists of electric calcined anthracite 70～80%, synthetic graphite 10～25%, binding agent 5～20%, titanium boride---and the percentage composition of carbon composite layer formulation by weight is electric calcined anthracite 40～60%, titanium boride powder 20～45%, binding agent 15～35%;
B, with above-mentioned two class aggregate fragmentations, screening, powder process, and by the weight percent weighing and burden of above-mentioned prescription;
The grain composition that will accomplish schungite carbon block base body aggregate on the technology is:
Grade: 12～8mm, 8～4mm, 4～2mm, 2～0mm, the following powder of 200 orders.
Content: 10 ± 2%, 17 ± 2%, 13 ± 2%, 16 ± 2,44 ± 2%.
The grade of electric calcined anthracite is 0～2mm in titanium boride---the carbon composite layer;
C, add the binding agent prepared respectively in two kinds of aggregates that prepared, binding agent is mixed by coal-tar pitch and carbolineum half and half and forms, sends into respectively to mix to pinch fully to mix in the pot again and pinches, and mixed to pinch out the thickener temperature be 150 ℃, and die temperature is 155～160 ℃;
D, elder generation mix the carbon block base body to pinch and expect that sending into vibratory compaction carries out preliminary vibratory compaction, and the uniform one deck of laminar surface has mixed the titanium boride of pinching thereon again---the carbon composite layer batching, and then carry out integral vibratory compaction;
E, the titanium boride of forming---the carbon composite layer cathode block is sent into the roasting kiln roasting, and roasting ends 1300 ℃ of fiery temperature;
F. carry out machining after the cooling;
G, check, packing, warehouse-in.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN00113420A CN1091471C (en) | 2000-05-08 | 2000-05-08 | Carbon block as cathode with compound titanium boride-carbon layer and its preparing process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN00113420A CN1091471C (en) | 2000-05-08 | 2000-05-08 | Carbon block as cathode with compound titanium boride-carbon layer and its preparing process |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1273284A CN1273284A (en) | 2000-11-15 |
| CN1091471C true CN1091471C (en) | 2002-09-25 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN00113420A Expired - Fee Related CN1091471C (en) | 2000-05-08 | 2000-05-08 | Carbon block as cathode with compound titanium boride-carbon layer and its preparing process |
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| CN (1) | CN1091471C (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100366800C (en) * | 2004-12-28 | 2008-02-06 | 中国铝业股份有限公司 | Preparation method of TiB2 composite layer cathode carbon block |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101255568B (en) * | 2007-12-07 | 2010-11-10 | 中南大学 | Particle gradation functional gradient TiB2/C composite cathode for aluminium electrolysis and preparation method thereof |
| DE102011004012A1 (en) * | 2011-02-11 | 2012-08-16 | Sgl Carbon Se | Surface profiled graphite cathode block with an abrasion resistant surface |
| DE102011004013A1 (en) * | 2011-02-11 | 2012-08-16 | Sgl Carbon Se | Graphitized cathode block with an abrasion resistant surface |
| DE102011004001A1 (en) * | 2011-02-11 | 2012-08-16 | Sgl Carbon Se | Hard material-containing surface profiled cathode block |
| DE102011004014A1 (en) * | 2011-02-11 | 2012-08-16 | Sgl Carbon Se | Cathode block with a covering layer containing hard material |
| CN108390020B (en) * | 2018-03-28 | 2023-10-13 | 天能电池集团股份有限公司 | Lead accumulator polar plate suppression device |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN85205776U (en) * | 1985-12-31 | 1986-10-22 | 东北工学院 | Tib2 composite layers-type cathode for ai electrolysis |
| CN2079618U (en) * | 1990-01-11 | 1991-06-26 | 东北工学院 | Al cell with tib anode construction |
| CN1062008A (en) * | 1990-12-08 | 1992-06-17 | 东北工学院 | A kind of aluminium electrolysis cell cathode carbon block and preparation method thereof |
-
2000
- 2000-05-08 CN CN00113420A patent/CN1091471C/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN85205776U (en) * | 1985-12-31 | 1986-10-22 | 东北工学院 | Tib2 composite layers-type cathode for ai electrolysis |
| CN2079618U (en) * | 1990-01-11 | 1991-06-26 | 东北工学院 | Al cell with tib anode construction |
| CN1062008A (en) * | 1990-12-08 | 1992-06-17 | 东北工学院 | A kind of aluminium electrolysis cell cathode carbon block and preparation method thereof |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100366800C (en) * | 2004-12-28 | 2008-02-06 | 中国铝业股份有限公司 | Preparation method of TiB2 composite layer cathode carbon block |
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| Publication number | Publication date |
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| CN1273284A (en) | 2000-11-15 |
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