ELECTROLYSIS TANK USED FOR ALUMINUM ELECTROLYSIS AND ELECTROLYSIS PROCESS USING THE ELECTROLYZER

Abstract

An electrolytic cell for aluminum electrolysis includes a cell body, in which an anode and a cathode are arranged inside the cell body, the cell body is filled with an electrolyte, and at least a part of the anode is immersed in the electrolyte; the anode is arranged above the cell body, the cathode is arranged at the bottom of the electrolytic cell and is covered by aluminum liquid, the electrolyte is located between the anode and the cathode and covers the aluminum liquid; and an insulating layer is arranged on the inner sidewall of the cell body for isolating oxygen or the electrolyte from a carbon block. The anode contains Fe and Cu as primary components; and the electrolyte is composed of 30-38 wt % of NaF, 49-60 wt % of AlF₃, 1-5 wt % of LiF, 1-6 wt % of KF and 3-6 wt % of Al₂O₃, and the molar ratio of NaF to AlF₃ is 1.0-1.52.

Description

FIELD OF THE INVENTION

[0001] The present invention relates to an electrolytic cell for aluminum electrolysis and an electrolysis process using the electrolytic cell, belonging to non-ferrous metal smelting industry.

BACKGROUND OF THE INVENTION

[0002] In aluminum electrolysis industry, a traditional Hall-Heroult molten salt aluminum electrolysis process is typically adopted to perform electrolysis on the molten salts of cryolite-alumina in a prebaked carbon anode electrolytic cell typically by adopting, that is, cryolite Na₃AlF₆ fluoride salt melt is taken as flux, Al₂O₃ is dissolved in the fluoride salt, a carbon body is taken as an anode and vertically inserted into the electrolytic cell, a carbon body with aluminum liquid covering the bottom of the electrolytic cell is taken as a cathode, electrochemical reaction is carried out on the anode and cathode of the electrolytic cell at a high temperature ranging from 940 to 960° C. after a strong direct current is introduced, and the resultant aluminum liquid product covers the cathode at the bottom of the electrolytic cell. Due to high electrolysis temperature, the traditional aluminum electrolysis process has such characteristics as large volatilization amount of electrolyte, large oxidization loss of a carbon anode, large energy consumption and poor working environment.

[0003] In the prior art, in order to lower electrolysis temperature, a low temperature molten salt system for aluminum electrolysis is disclosed in Chinese patent document CN101671835A, the molten salt composition of the system includes AlF₃, Al₂O₃ and one or more salts selected from the group consisting of KF, NaF, MgF₂, CaF₂, NaCl, LiF, and BaF₂, and the electrolysis temperature of the electrolyte can be lowered to be within a wide area from 680 to 900° C. for the purpose of operations.

[0004] Addition of NaCl to the aforementioned electrolyte aims at lowering the liquidus temperature of the electrolyte, however, NaCl will lead to corrosion to metal parts like electrolytic cell accessories at the aforementioned electrolysis temperature, furthermore, NaCl is extremely liable to volatilization in the electrolysis process so as to form HCl toxic gas, so its application is difficult; in addition to addition of NaCl, decrease of the molar ratio of NaF to AlF₃ can also lower the liquidus temperature of the electrolyte in light of common knowledge in this art, but in the existing industry, the molar ratio of NaF to AlF₃ is generally larger than 2.2, this is because, if the molar ratio of NaF to AlF₃ further decreases, NaF and AlF₃ will lead to a `crusting` phenomenon of the cathode in the process of low-temperature electrolysis while the liquidus temperature of the electrolyte is lowered, the reason for this `crusting` phenomenon is that sodium ions and aluminum ions in the electrolyte will gather at the cathode in the electrolysis process to generate sodium cryolite, which is seldom molten at a low temperature due to its high melting point, as a result, the surface of the cathode is covered by a layer of refractory cryolite crust to affect normal electrolysis in the electrolysis process tremendously. Due to the above problems in the prior art, industrial application of the electrolyte is significantly limited, and it is an unsolved problem in the prior art to find a way of avoiding corrosion to electrolysis devices and damage to human body and ensuring proper electric conductivity and alumina solubility as well as no cathode `crusting` phenomenon of the prepared electrolyte while the liquidus temperature of the electrolyte is further lowered.

[0005] In addition to the high electrolysis temperature problem that needs to be solved, the carbon anode in the traditional electrolytic cell for aluminum electrolysis is ceaselessly consumed by oxidization in the electrolysis process, thus constant replacement for the carbon anode is required; moreover, carbon dioxide, carbon monoxide and other waste gases are continuously generated at the anode during aluminum electrolysis. Hence, to lessen the consumption of an anode material in the aluminum electrolysis process and simultaneously reduce the emission of waste gases, disclosed in the prior art is plenty of documents for research on anode material, e.g. disclosed in Chinese patent document CN1443877A is an inert anode material applied to aluminum, magnesium and rare earth electrolysis industries, this material is formed by binary or multi-element alloy composed of chromium, nickel, ferrum, cobalt, titanium, copper, aluminum, magnesium and other metals, and the preparation method thereof is a smelting or powder metallurgy method. The prepared anode material is good in electric and thermal conductivity and generates oxygen in the electrolysis process, wherein in Example 1, an anode is made of the alloy material composed of 37 wt % of cobalt, 18 wt % of copper, 19 wt % of nickel, 23 wt % of ferrum and 3 wt % of silver and is used for aluminum electrolysis, the anode has a current density of 1.0 A/cm² in the electrolysis process at 850° C. and the cell voltage is maintained within a range from 4.1V to 4.5V in the electrolysis process, the prepared aluminum has a purity of 98.35%.

[0006] Compared with the carbon material, the alloy anode material in the technologies aforementioned has higher electric conductivity and lower corrosion amount in the electrolysis process and can be processed into random shapes, however, the alloy anode composed of the aforementioned components is still high in overvoltage, which results in large industrial power consumption and low product quality, besides, since a large quantity of expensive metal materials are used, the anode material is high in cost and cannot adapt to industrial needs.

[0007] In addition, a layer of oxide film is generated on the surface of the prepared alloy anode in the prior art, and if this oxide film is destroyed, the anode material exposed to the surface will be oxidized as a new oxide film. The oxide film on the surface of the alloy anode in the prior art has low oxidization resistance and is further liable to oxidization reaction to generate products that are likely to be corroded by the electrolyte, and the oxide film with low stability is liable to fall off the anode electrode in the electrolysis process; after the previous oxide film is corroded or falls off, the material of the alloy anode exposed to the surface will create a new oxide film by reaction, such replacement between new and old oxide films results in continuous consumption and poor corrosion resistance of the anode material; furthermore, the corroded or falling oxide film enters into liquid aluminum in the electrolysis process of alumina to degrade the purity of the final product aluminum, as a result, the manufactured aluminum product cannot meet the demand of national standards and accordingly cannot be directly used as a finished product.

SUMMARY OF THE INVENTION

[0008] The first technical problem to be solved by the present invention is that, the prior art is incapable of avoiding corrosion to electrolysis devices and damage to human body and ensuring proper electric conductivity and alumina solubility as well as no `crusting` phenomenon in the prepared electrolyte while the liquidus temperature of the electrolyte is further lowered. Thus the present invention provides an electrolytic cell, containing an electrolyte for aluminum electrolysis which is low in liquidus temperature, free from metal corrosion, not liable to volatilization, proper in electric conductivity and alumina solubility and free from cathode `crusting` phenomenon.

[0009] Simultaneously, the second technical problem to be solved by the present invention is that, an alloy anode composed of metal components in the prior art is high in overvoltage, power consumption in the aluminum electrolysis process is large and the metal components employed are high in price, resulting in cost increment of the alloy anode; in addition, an oxide film on the surface of the alloy anode in the prior art is low in oxidation resistance and liable to fall off, which leads to continuous consumption of the alloy anode and poor corrosion resistance, furthermore, the corroded or falling oxide film enters into liquid aluminum to degrade the purity of the final product aluminum; and therefore, provided is an electrolytic cell for aluminum electrolysis, which is low in overvoltage of the used inert anode material, low in price, strong in oxidation resistance and stability of the oxide film formed on the surface thereof and resistant to electrolyte corrosion.

[0010] Simultaneously, the present invention provides a process for aluminum electrolysis using the above electrolytic cell.

[0011] To solve the aforementioned technical problems, the present invention provides an electrolytic cell for aluminum electrolysis, comprising a cell body, wherein an anode and a cathode are arranged inside the cell body, the cell body is further filled with an electrolyte; the anode is arranged above the cell body, and at least a part of the anode is immersed in the electrolyte; the cathode is arranged at the bottom of the electrolytic cell and covered by a certain amount of aluminum liquid; the electrolyte is located between the anode and the cathode; the anode contains the components including Fe, Cu, Ni and Sn, wherein Fe and Cu serve as primary components; the electrolyte is composed of 30-38 wt % of NaF, 49-60 wt % of AlF₃, 1-5 wt % of LiF, 1-6 wt % of KF and 3-6 wt % of Al₂O₃, wherein the molar ratio of NaF to AlF₃ is 1.0-1.52.

[0012] The bottom surface of the anode is kept parallel to the cell body, and an insulating layer is arranged on the inner sidewall of the cell body and is used for isolating oxygen or the electrolyte from a carbon block.

[0013] A cell cover is arranged at the upper end of the cell body and is provided with a vent and a feeding hole; a cathode bar is arranged inside the cathode, one end of the anode penetrates through the cell cover and is connectedly provided with a binding post for connection with a power supply.

[0014] The mass ratio of Fe to Cu to Sn is (23-40):(36-60):(0.2-5).

[0015] The components of the anode further include Ni.

[0016] The anode is composed of Fe, Cu, Ni and Sn, wherein the content of Fe is 23-40 wt %, the content of Cu is 36-60%, the content of Ni is 14-28 wt % and the content of Sn is 0.2-5 wt %.

[0017] The components of the anode further include Al and Y.

[0018] The anode is composed of Fe, Cu, Ni, Sn, Al and Y, wherein the content of Fe is 23-40 wt %, the content of Cu is 36-60 wt %, the content of Ni is 14-28 wt %, the content of Al is more than zero and less than or equal to 4 wt %, the content of Y is more than zero and less than or equal to 2 wt %, and the content of Sn is 0.2-5 wt %.

[0019] The molar ratio of NaF to AlF₃ is 1.12-1.52.

[0020] The liquidus temperature of the electrolyte is 620-670° C.

[0021] An electrolysis process using the electrolytic cell comprises the steps of:

(1) adding specified amounts of NaF, AlF₃, LiF, KF and Al₂O₃ to a melting furnace for mixing and melting to form a melt; or adding specified amounts of NaF, AlF₃, LiF and KF to a melting furnace for mixing and melting, and then adding Al₂O₃ to obtain a melt; and (2) raising the temperature of the melt prepared in step (1) to above 720-760° C., and then, pouring the melt into the electrolytic cell and carrying out electrolysis while the temperature is maintained at 720-760° C.

[0022] The electrolysis temperature is 730-750° C.

[0023] Al₂O₃ is quantitatively supplied in the electrolysis process.

[0024] The electrolysis process using the electrolytic cell comprises the steps of:

(1) adding specified amounts of NaF, AlF₃, LiF, KF and Al₂O₃ to a melting furnace for mixing and melting to form a melt; or adding specified amounts of NaF, AlF₃, LiF and KF to a melting furnace for mixing and melting, and then adding Al₂O₃ to obtain a melt; and (2) raising the temperature of the melt prepared in step (1) to above 720-760° C., and then, pouring the melt into the electrolytic cell and carrying out electrolysis while the temperature is maintained at 720-760° C.

[0025] The electrolysis temperature is 730-750° C.

[0026] Al₂O₃ is quantitatively supplied in the electrolysis process.

[0027] The electrolytic cell and the electrolysis process using the electrolytic cell in the present invention have the advantages below:

(1) The electrolytic cell for aluminum electrolysis in the present invention comprises a cell body, wherein an anode and a cathode are arranged inside the cell body, and the cell body is further filled with an electrolyte; the anode is arranged above the cell body, and at least a part of the anode is immersed in the electrolyte; the cathode is arranged at the bottom of the electrolytic cell and covered by a certain amount of aluminum liquid; the electrolyte is located between the anode and the cathode; the anode contains the components including Fe, Cu, Ni and Sn, wherein Fe and Cu serve as primary components; the electrolyte is composed of 30-38 wt % of NaF, 49-60 wt % of AlF₃, 1-5 wt % of LiF, 1-6 wt % of KF and 3-6 wt % of Al₂O₃, wherein the molar ratio of NaF to AlF₃ is 1.0-1.52.

[0028] The anode containing metal Sn and composed of the aforementioned metal components is high in electric conductivity and low in overvoltage, the cell voltage in the electrolysis process of the electrolytic cell is about 3.1-3.4V, power consumption in the aluminum electrolysis process is small, the power consumption for per ton of aluminum is not more than 11000 kwh, so the process cost is low; the anode material is alloy composed of Fe, Cu and Sn, so an oxide film formed on the surface of the anode in the electrolysis process is high in oxidation resistance and is hardly corroded by the electrolyte, and the formed oxide film is stable and not liable to fall off, therefore, the anode is imparted with quite high oxidation resistance and strong corrosion resistance so as to ensure the purity of aluminum products, that is, the purity of the produced aluminum can reach 99.8%. The following problems in the prior art are avoided: the alloy anode has high overvoltage, the oxide film on the alloy surface is low in oxidation resistance and liable to fall off, which leads to continuous consumption of the alloy anode and poor corrosion resistance, furthermore, the corroded or falling oxide film enters into liquid aluminum to degrade the purity of the final product aluminum. In addition, Fe and Cu serve as primary components of the alloy anode and their content proportions are quite high, and accordingly, the manufacturing cost of the anode material is lowered.

[0029] The used electrolyte employs a pure fluoride system, substance composition in the electrolyte is defined, the contents of these substances are further defined and the molar ratio of NaF to AlF₃ is 1.0-1.52, so that the liquidus temperature of the electrolyte is lowered to 640-670° C., as a result, electrolysis can be carried out at 720-760° C. according to the electrolysis process, which reduces volatilization loss of fluoride salt, avoids corrosion to electrolysis devices and damage to human body, improves working environment, greatly reduces energy consumption in the electrolysis process and achieves the aim of energy saving and emission reduction; meanwhile, in the present invention, proper amounts of LiF and KF are added and can be combined with sodium ions and aluminum ions in the electrolyte to form lithium cryolite and potassium cryolite with low melting points, thus the crusting phenomenon is avoided in the electrolysis process; compared with the existing industry, the electrolyte for aluminum electrolysis in the present invention has no CaF₂ and MgF₂ added therein, instead, KF in an appropriate proportion, which has the function of increasing alumina solubility and dissolution velocity, is added to a system in which the molar ratio of NaF to AlF₃ is 1.0-1.52, therefore, the shortcoming of low alumina solubility in the low-molar-ratio electrolyte is improved; in general, the electric conductivity of the electrolyte decreases as the temperature decreases, so typically, the electric conductivity at a low electrolysis temperature hardly meets the demand in a normal electrolysis process; the electrolysis temperature is lowered by lowering the liquidus temperature of the electrolyte in the present invention, however, the electric conductivity of the electrolyte at a low temperature can still meet the demand in the electrolysis process because LiF with a larger electric conductivity is added and component proportions in the electrolyte are optimized, thus enhancing the current efficiency in the electrolysis process. According to the invention, the content of LiF is defined as 1-5%, this is because too low content of LiF fails to improve electric conductivity and to prevent crusting, and too high content of LiF results in decrease of the alumina solubility, and the above two situations are effectively avoided by defining the content of LiF as 1-5% in the present invention; and there is no corrosion to a metal device when the electrolyte with the above proportions in the present invention is used, in this way, the service life of the electrolysis device is prolonged.

(2) In the electrolytic cell for aluminum electrolysis in the present invention, the anode is composed of Fe, Cu, Ni, Sn, Al and Y, wherein the content of Fe is 23-40 wt %, the content of Cu is 36-60 wt %, the content of Ni is 14-28 wt %, the content of Al is less than or equal to 4 wt %, the content of Y is less than or equal to 2 wt %, and the content of Sn is 0.2-5 wt %.

[0030] Similarly, the aforementioned inert alloy anode has the advantages of low material cost and high electric conductivity, in addition, the metal Al contained in the aforementioned inert alloy anode plays a role of oxidization resistance and can serve as a reducing agent for metallothermic reduction reaction with metal oxides in the inert anode alloy, thus preventing the metals in the inert alloy anode, i.e. primary components, from being oxidized, and causing reduction of the electric conductivity of the alloy anode; meanwhile, the metal Y added can be used for controlling a crystal structure for anode material formation in the preparation process of the inert anode, achieving the anti-oxidization purpose.

(3) In the electrolytic cell for aluminum electrolysis in the present invention, specified amounts of NaF, AlF₃, LiF, KF and Al₂O₃ are mixed, the resultant mixture is heated to form a melt; or specified amounts of NaF, AlF₃, LiF and KF are mixed, the resultant mixture is heated until the mixture is molten, and then Al₂O₃ is added to obtain a melt; afterwards, the melt prepared is electrolyzed at 720-760° C. Electrolysis temperature is directly associated with volatilization of the electrolyte, cathode crusting phenomenon, energy consumption of the process, electric conductivity and alumina solubility, and the inventor of the present invention, by long search, set the electrolysis temperature within a range from 720-760° C. in a matching way based on the components and content characteristics of the electrolyte in the present invention, thus the cathode crusting phenomenon is prevented and volatilization of the electrolyte and energy consumption of the electrolysis process are remarkably reduced while both the electric conductivity and the alumina solubility are increased, and the economic efficiency of the process is improved. Preferably, the electrolysis temperature is further set within a range from 730-750° C. in the present invention.

BRIEF DESCRIPTION OF THE DRAWINGS

[0031] For more easily understanding the contents of the present invention, further description will be made below to the technical solution of the present invention in conjunction with the drawing and the embodiments.

[0032] FIG. 1 is a structure diagram of the electrolytic cell for aluminum electrolysis in the present invention;

[0033] In this drawing, reference signs are as follows: 1 refers to cell body, 2 refers to anode, 3 refers to cathode, 4 refers to electrolyte, 5 refers to insulating layer, 6 refers to cell cover, 7 refers to vent, 8 refers to feeding hole, 9 refers to binding post, 10 refers to cathode bar and 11 refers to aluminum liquid.

DETAILED DESCRIPTION OF THE EMBODIMENTS

[0034] The electrolytic cell for aluminum electrolysis in the present invention is as shown in FIG. 1 and comprises a cell body 1, wherein an anode 2 and a cathode 3 are arranged inside the cell body 1, the anode 2 and the cathode 3 can be arranged in random ways in accordance with the actual need, in this embodiment, the anode 2 is arranged above the cell body 1, the bottom surface of the anode 2 is kept parallel to the cell body 1, the cathode 3 is arranged at the bottom of the electrolytic cell and covered by a certain amount of aluminum liquid 11; the cell body 1 is further filled with an electrolyte 4, immersion of the anode 2 and the cathode 3 in the electrolyte 4 depends on the selected electrolytic cell structure, in this embodiment, at least a part of the anode 2 is immersed in the electrolyte 4; the cathode 3 is arranged at the bottom of the electrolytic cell and covered by a certain amount of aluminum liquid 11; the electrolyte 4 is located between the anode 2 and the cathode 3 and covers the aluminum liquid 11; the anode 2 contains the components including Fe, Cu, Ni and Sn, wherein Fe and Cu serve as primary components, and the molar ratio of Fe to Cu to Sn is (23-40):(36-60):(0.2-5); the electrolyte 4 is composed of 30-38 wt % of NaF, 49-60 wt % of AlF₃, 1-5 wt % of LiF, 1-6 wt % of KF and 3-6 wt % of Al₂O₃, wherein the molar ratio of NaF to AlF₃ is 1.0-1.52, preferably 1.12-1.52, and the liquidus temperature of the electrolyte 4 is 620-670° C., preferably 640-670° C.

[0035] As a variable embodiment on this basis, in order to isolate the inner sidewall of the cell body 1 from the electrolyte 4 and oxygen to prevent transfer of electrons between the sidewall of the cell body 1 and the electrolyte 4 and corrosion of the electrolyte 4 to the sidewall of the cell body 1, an insulating layer 5 is arranged on the inner sidewall of the cell body 1 and is made of any commercially available insulating material that is resistant to high temperature and corrosion of the electrolyte 4, e.g. corundum, aluminate spinel refractory and the like. In this embodiment, a carbon block is arranged between the inner sidewall of the cell body 1 and the insulating layer 5, and the carbon block and the cathode 3 are integrally formed. Undoubtedly, the carbon block and the cathode 3 can also be arranged in a separated manner.

[0036] On this basis, in order to isolate the electrolysis environment for the electrolytic cell from outside without impediment to exhaust and feeding, a cell cover 6 is arranged at the upper end of the cell body 1 and is provided with a vent 7 and a feeding hole 8 thereon, the sizes and positions of the vent 7 and the feeding hole can be randomly determined in accordance with the actual need, and in this embodiment, the vent 7 is arranged next to the anode 2.

[0037] Further, in order to facilitate connection of the anode 2 and the cathode 3 with a power supply, a cathode bar 10 is arranged on the cathode 3 at the bottom of the electrolytic cell and is used for connection with the power supply of the cathode 3; one end of the anode 2 penetrates through the cell cover 6 and is connected and provided with a binding post 9 for connection with the power supply of the anode 2; and the cathode 10 and the binding post 9 can be made of any material with good electric conductivity, including steel, iron and alloy materials, etc.

[0038] On this basis, in order to improve the combination firmness among metals Fe, Cu and Sn, the components of the anode 2 further include Ni, preferably the anode 2 is composed of Fe, Cu, Ni and Sn, wherein the content Fe is 23-40 wt %, the content of Cu is 36-60 wt %, the content of Ni is 14-28 wt % and the content of Sn is 0.2-5 wt %.

[0039] The anode 2 may be preferably composed of Fe, Cu, Ni, Sn, Al and Y, the added Al can prevent other primary metal components of the anode 2 from oxidation and improve the oxidization resistance, the component Y can be used for regulating and controlling the structure of the prepared alloy crystal in order to achieve the anti-oxidization purpose, wherein the content of Fe is 23-40 wt %, the content of Cu is 36-60 wt %, the content of Ni is 14-28 wt %, the content of Al is less than or equal to 4 wt %, the content of Y is less than or equal to 2 wt %, and the content of Sn is 0.2-5 wt %.

[0040] The electrolysis temperature is 720-760° C. when the aforementioned electrolytic cell is used for aluminum electrolysis, preferably 730-750° C.

[0041] Description is made below in conjunction with the embodiments.

Embodiment 1

[0042] Fe, Cu, Ni and Sn metal blocks are mixed based on 23 wt % of Fe, 60 wt % of Cu, 14 wt % of Ni and 3 wt % of Sn, the mixture is molten by heating at high temperature and then subjected to casting to obtain an anode 1. The anode 1 has a density of 8.3/cm³, a specific resistivity of 68 μΩcm and a melting point of 1360° C.

[0043] The components of the electrolyte in this embodiment are as follows: 32% of NaF, 57% of AlF₃, 3% of LiF, 4% of KF and 4% of Al₂O₃, wherein the molar ratio of NaF to aluminum fluoride AlF₃ is 1.12. The liquidus temperature of the electrolyte in this embodiment is 640° C. according to measurement. The electrolyte has an electric conductivity of about 1.7 Ω¹cm^-1, a density of about 2.03 g/cm³ and an alumina saturation concentration of 5%.

[0044] The process using the electrolyte in the present invention for aluminum electrolysis is as follows:

(1) by means of the anode 1 and the carbon body cathode, melting the aforementioned amounts of NaF, AlF₃, LiF, KF and Al₂O₃ in a melting furnace so as to form a melt; and (2) raising the temperature of the melt prepared in step (1) to above 720° C. in the melting furnace, then pouring the melt into the electrolytic cell, switching on the power supplies of the anode and the cathode, and carrying out electrolysis for 40 hours while the temperature is maintained at 720° C., wherein Al₂O₃ is quantitatively supplied in the electrolysis process.

[0045] There is no crust at the bottom of the cell body in the electrolysis process, the cell voltage of the electrolytic cell is 3.1 V, the power consumption for per ton of aluminum is 10040 kwh in the electrolysis process, and the prepared aluminum has a purity of 99.85%.

Embodiment 2

[0046] Fe, Cu, Ni and Sn metal blocks are mixed based on 40 wt % of Fe, 36 wt % of Cu, 19 wt % of Ni and 5 wt % of Sn, the mixture is molten by heating at high temperature and then subjected to casting to obtain an anode 2. The anode has a density of 8.1/cm³, a specific resistivity of 76.8 μΩcm and a melting point of 1386° C.

[0047] The components of the electrolyte in this embodiment are as follows: 38% of NaF, 50% of AlF₃, 2% of LiF, 5% of KF and 5% of Al₂O₃, wherein the molar ratio of NaF to aluminum fluoride AlF₃ is 1.52.

[0048] The performances of the electrolyte in this embodiment are measured and the measurement result is that the liquidus temperature of the electrolyte in this embodiment is 670° C. The electrolyte has an electric conductivity of about 1.8 Ω^-1cm^-1, a density of about 2.05 g/cm³ and an alumina saturation concentration of 6%.

[0049] The process using the electrolyte in the present invention for aluminum electrolysis is as follows:

(1) by means of the anode 2 and the carbon body cathode, melting the aforementioned amounts of NaF, AlF₃, LiF and KF in a melting furnace, and then adding the aforementioned amount of Al₂O₃ to obtain a melt by melting; and (2) raising the temperature of the melt prepared in step (1) to above 760° C. in the melting furnace, then pouring the melt into the electrolytic cell, switching on the power supplies of the anode and the cathode, and carrying out electrolysis for 40 hours while the temperature is maintained at 760° C.

[0050] There is no crust at the bottom of the cell body in the electrolysis process, the cell voltage of the electrolytic cell is 3.39V, the power consumption for per ton of aluminum is 10979 kwh in the electrolysis process, and the prepared aluminum has a purity of 99.82%.

Embodiment 3

[0051] Fe, Cu, Ni and Sn metal blocks are mixed based on 25 wt % of Fe, 46.8 wt % of Cu, 28 wt % of Ni and 0.2 wt % of Sn, the mixture is molten by heating at high temperature and then subjected to casting to obtain an anode 3. The anode has a density of 8.2/cm³, a specific resistivity of 72 μΩcm and a melting point of 1350° C.

[0052] The components of the electrolyte in this embodiment are as follows: 32% of NaF, 57% of AlF₃, 3% of LiF, 4% of KF and 4% of Al₂O₃, wherein the molar ratio of NaF to aluminum fluoride AlF₃ is 1.12.

[0053] The performances of the electrolyte in this embodiment are measured and the measurement result is that the liquidus temperature of the electrolyte in this embodiment is 640° C. The electrolyte has an electric conductivity of about 1.6 Ω^-1cm^-1, a density of about 2.03 g/cm³ and an alumina saturation concentration of 5%.

[0054] The process using the electrolyte in the present invention for aluminum electrolysis is as follows:

(1) by means of the anode 3 and the carbon body cathode, melting the aforementioned amounts of NaF, AlF₃, LiF, KF and Al₂O₃ in a melting furnace so as to form a melt; and (2) raising the temperature of the melt prepared in step (1) to above 730° C. in the melting furnace, then pouring the melt into the electrolytic cell, switching on the power supplies of the anode and the cathode, and carrying out electrolysis for 40 hours while the temperature is maintained at 730° C., wherein Al₂O₃ is quantitatively supplied in the electrolysis process.

[0055] There is no crust at the bottom of the cell body in the electrolysis process, the cell voltage of the electrolytic cell is 3.15V, the power consumption for per ton of aluminum is 10202 kwh in the electrolysis process, and the prepared aluminum has a purity of 99.85%.

Embodiment 4

[0056] Fe, Cu, Ni and Sn metal blocks are mixed based on 24.2 wt % of Fe, 60 wt % of Cu, 14 wt % of Ni and 0.2 wt % of Sn, the mixture is molten by heating at high temperature, 1.8 wt % of Al metal block is then added for continuous melting and mixing, and finally, 0.8 wt % of Y metal block is added for melting and mixing and an anode 4 is obtained by casting of the mixture. The anode has a density of 8.3/cm³, a specific resistivity of 68 μΩcm and a melting point of 1360° C.

[0057] The components of the electrolyte in this embodiment are as follows: 32% of NaF, 57% of AlF₃, 3% of LiF, 4% of KF and 4% of Al₂O₃, wherein the molar ratio of NaF to aluminum fluoride AlF₃ is 1.12.

[0058] The performances of the electrolyte in this embodiment are measured and the measurement result is that the liquidus temperature of the electrolyte in this embodiment is 640° C. The electrolyte has an electric conductivity of about 1.8 Ω^-1cm^-1, a density of about 2.04 g/cm³ and an alumina saturation concentration of 6%.

[0059] The process using the electrolyte in the present invention for aluminum electrolysis is as follows:

(1) by means of the anode 4 and the carbon body cathode, melting the aforementioned amounts of NaF, AlF₃, LiF, KF and Al₂O₃ in a melting furnace so as to form a melt; and (2) raising the temperature of the melt prepared in step (1) to above 750° C. in the melting furnace, then pouring the melt into the electrolytic cell, switching on the power supplies of the anode and the cathode, and carrying out electrolysis for 40 hours while the temperature is maintained at 750° C., wherein Al₂O₃ is quantitatively supplied in the electrolysis process.

[0060] There is no crust at the bottom of the cell body in the electrolysis process, the cell voltage of the electrolytic cell is 3.12V, the power consumption for per ton of aluminum is 10105 kwh in the electrolysis process, and the prepared aluminum has a purity of 99.8%.

Embodiment 5

[0061] Fe, Cu, Ni and Sn metal blocks are mixed based on 40 wt % of Fe, 36 wt % of Cu, 14.9 wt % of Ni and 5 wt % of Sn, the mixture is molten by heating at high temperature, 0.1 wt % of Al metal block is then added for continuous melting and mixing, and finally, 0.1 wt % of Y metal block is added for melting and mixing and an anode 5 is obtained by casting of the mixture. The anode has a density of 8.1/cm³, a specific resistivity of 76.8 μΩcm and a melting point of 1386° C.

[0062] The components of the electrolyte in this embodiment are as follows: 30% of NaF, 60% of AlF₃, 1% of LiF, 6% of KF and 3% of Al₂O₃, wherein the molar ratio of NaF to aluminum fluoride AlF₃ is 1.0.

[0063] The performances of the electrolyte in this embodiment are measured and the measurement result is that the liquidus temperature of the electrolyte in this embodiment is 620° C. The electrolyte has an electric conductivity of about 1.6 Ω^-1cm^-1, a density of about 2.03 g/cm³ and an alumina saturation concentration of 5%.

[0064] The process using the electrolyte in the present invention for aluminum electrolysis is as follows:

(1) by means of the anode 5 and the carbon body cathode, melting the aforementioned amounts of NaF, AlF₃, LiF, KF and Al₂O₃ in a melting furnace so as to form a melt; and (2) raising the temperature of the melt prepared in step (1) to above 720° C. in the melting furnace, then pouring the melt into the electrolytic cell, switching on the power supplies of the anode and the cathode, and carrying out electrolysis for 40 hours while the temperature is maintained at 720° C., wherein Al₂O₃ is quantitatively supplied in the electrolysis process.

[0065] There is no crust at the bottom of the cell body in the electrolysis process, the cell voltage of the electrolytic cell is 3.27V, the power consumption for per ton of aluminum is 10591 kwh in the electrolysis process, and the prepared aluminum has a purity of 99.81%.

Embodiment 6

[0066] Fe, Cu, Ni and Sn metal blocks are mixed based on 25 wt % of Fe, 38 wt % of Cu, 28 wt % of Ni and 4 wt % of Sn, the mixture is molten by heating at high temperature, 4 wt % of Al metal block is then added for continuous melting and mixing, and finally, 1 wt % of Y metal block is added for melting and mixing and an anode 6 is obtained by casting of the mixture. The anode has a density of 8.2/cm³, a specific resistivity of 70 μΩcm and a melting point of 1365° C.

[0067] The components of the electrolyte in this embodiment are as follows: 38% of NaF, 54% of AlF₃, 4% of LiF, 1% of KF and 3% of Al₂O₃, wherein the molar ratio of NaF to aluminum fluoride AlF₃ is 1.4.

[0068] The performances of the electrolyte in this embodiment are measured and the measurement result is that: the liquidus temperature of the electrolyte in this embodiment is 670° C. The electrolyte has an electric conductivity of about 1.8 Ω^-1cm^-1, a density of about 2.05 g/cm³ and an alumina saturation concentration of 6%.

[0069] The process using the electrolyte in the present invention for aluminum electrolysis is as follows:

(1) by means of the anode 6 and the carbon body cathode, melting the aforementioned amounts of NaF, AlF₃, LiF, KF and Al₂O₃ in a melting furnace so as to form a melt; and (2) raising the temperature of the melt prepared in step (1) to above 760° C. in the melting furnace, then pouring the melt into the electrolytic cell, switching on the power supplies of the anode and the cathode, and carrying out electrolysis for 40 hours while the temperature is maintained at 760° C., wherein Al₂O₃ is quantitatively supplied in the electrolysis process.

[0070] There is no crust at the bottom of the cell body in the electrolysis process, the cell voltage of the electrolytic cell is 3.35V, the power consumption for per ton of aluminum is 10850 kwh in the electrolysis process, and the prepared aluminum has a purity of 99.83%.

Embodiment 7

[0071] Fe, Cu, Ni and Sn metal blocks are mixed based on 40 wt % of Fe, 36.5 wt % of Cu, 18 wt % of Ni and 3 wt % of Sn, the mixture is molten by heating at high temperature, 1.5 wt % of Al metal block is then added for continuous melting and mixing, and finally, 1 wt % of Y metal block is added for melting and mixing and an anode 7 is obtained by casting of the mixture. The anode has a density of 8.1/cm³, a specific resistivity of 76.8 μΩcm and a melting point of 1386° C.

[0072] The components of the electrolyte in this embodiment are as follows: 34% of NaF, 49% of AlF₃, 5% of LiF, 6% of KF and 6% of Al₂O₃, wherein the molar ratio of NaF to aluminum fluoride AlF₃ is 1.39.

[0073] The performances of the electrolyte in this embodiment are measured and the measurement result is that the liquidus temperature of the electrolyte in this embodiment is 660° C. The electrolyte has an electric conductivity of about 1.8 Ω^-1cm^-1, a density of about 2.05 g/cm³ and an alumina saturation concentration of 6%.

[0074] The process using the electrolyte in the present invention for aluminum electrolysis is as follows:

(1) by means of the anode 7 and the carbon body cathode, melting the aforementioned amounts of NaF, AlF₃, LiF, KF and Al₂O₃ in a melting furnace so as to form a melt; and (2) raising the temperature of the melt prepared in step (1) to above 760° C. in the melting furnace, then pouring the melt into the electrolytic cell, switching on the power supplies of the anode and the cathode, and carrying out electrolysis for 40 hours while the temperature is maintained at 760° C., wherein Al₂O₃ is quantitatively supplied in the electrolysis process.

[0075] There is no crust at the bottom of the cell body in the electrolysis process, the cell voltage of the electrolytic cell is 3.38V, the power consumption for per ton of aluminum is 10947 kwh in the electrolysis process, and the prepared aluminum has a purity of 99.8%.

[0076] The electrolytic cell in the aforementioned embodiments is any of the electrolytic cells in the present invention.

[0077] Detailed description has been made to the specific contents of the present invention in the aforementioned embodiments, and it should be understood by those skilled in this art that modifications and detail variations in any form based upon the present invention pertain to the contents that the present invention seeks to protect.

Claims

1. An electrolytic cell for aluminum electrolysis, comprising: a cell body, an anode and a cathode being arranged inside the cell body, the cell body being further filled with an electrolyte; the anode being arranged above the cell body, and at least a part of the anode being immersed in the electrolyte; the cathode being arranged at the bottom of the electrolytic cell and covered by a certain amount of aluminum liquid; the electrolyte being located between the anode and the cathode; wherein the anode contains the components including Fe, Cu, Ni and Sn, wherein Fe and Cu serve as primary components; and the electrolyte is composed of 30-38 wt % of NaF, 49-60 wt % of AlF₃, 1-5 wt % of LiF, 1-6 wt % of KF and 3-6 wt % of Al₂O₃, wherein the molar ratio of NaF to AlF₃ is 1.0-1.52.

2. The electrolytic cell according to claim 1, wherein the bottom surface of the anode is kept parallel to the cell body, and an insulating layer is arranged on the inner sidewall of the cell body and is used for isolating oxygen or the electrolyte from a carbon block.

3. The electrolytic cell according to claim 1, wherein a cell cover is arranged at the upper end of the cell body and is provided with a vent and a feeding hole; a cathode bar is arranged inside the cathode, one end of the anode penetrates through the cell cover and is connected and provided with a binding post for connection with a power supply.

4. The electrolytic cell according to claim 1, wherein the mass ratio of Fe to Cu to Sn is (23-40):36-60):(0.2-5).

5. The electrolytic cell according to claim 1, wherein the components of the anode further include Ni.

6. The electrolytic cell according to claim 5, wherein the anode is composed of Fe, Cu, Ni and Sn, wherein the content of Fe is 23-40 wt %, the content of Cu is 36-60 wt %, the content of Ni is 14-28 wt % and the content of Sn is 0.2-5 wt %.

7. The electrolytic cell according to claim 5, wherein the components of the anode further include Al and Y.

8. The electrolytic cell according to claim 7, wherein the anode is composed of Fe, Cu, Ni, Sn, Al and Y, wherein the content of Fe is 23-40 wt %, the content of Cu is 36-60 wt %, the content of Ni is 14-28 wt %, the content of Al is more than zero and less than or equal to 4 wt %, the content of Y is more than zero and less than or equal to 2 wt %, and the content of Sn is 0.2-5 wt %.

9. The electrolytic cell according to claim 1, wherein the molar ratio of NaF to AlF₃ is 1.12-1.52.

10. The electrolytic cell according to claim 1, wherein the liquidus temperature of the electrolyte is 620-670.degree. C.

11. An electrolysis process using the electrolytic cell according to claim 1, comprising the steps of: (1) adding specified amounts of NaF, AlF₃, LiF, KF and Al₂O₃ to a melting furnace for mixing and melting to form a melt; or adding specified amounts of NaF, AlF₃, LiF and KF to a melting furnace for mixing and melting, and then adding Al₂O₃ to obtain a melt; and (2) raising the temperature of the melt prepared in step (1) to above 720-760.degree. C., and then, pouring the melt into the electrolytic cell and carrying out electrolysis while the temperature is maintained at 720-760.degree. C.

12. The electrolysis process according to claim 11, wherein the electrolysis temperature is 730-750.degree. C.

13. The electrolysis process according to claim 11, wherein Al₂O₃ is quantitatively supplied in the electrolysis process.

14. The electrolytic cell according to claim 2, wherein a cell cover is arranged at the upper end of the cell body and is provided with a vent and a feeding hole; a cathode bar is arranged inside the cathode, one end of the anode penetrates through the cell cover and is connected and provided with a binding post for connection with a power supply.

15. The electrolytic cell according to claim 2, wherein the mass ratio of Fe to Cu to Sn is (23-40):(36-60):(0.2-5).

16. The electrolytic cell according to claim 3, wherein the mass ratio of Fe to Cu to Sn is (23-40):(36-60):(0.2-5).

17. The electrolytic cell according to claim 2, wherein the components of the anode further include Ni.

18. The electrolytic cell according to claim 3, wherein the components of the anode further include Ni.

19. The electrolytic cell according to claim 4, wherein the components of the anode further include Ni.

20. The electrolytic cell according to claim 1, wherein the components of the anode further include Al and Y.

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