CN212315539U - Recovery device of elemental sulfur in sulfur-containing hydrometallurgy slag - Google Patents
Recovery device of elemental sulfur in sulfur-containing hydrometallurgy slag Download PDFInfo
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Abstract
The utility model provides a recovery unit of elemental sulfur in metallurgical sediment of sulphur wet process. The device comprises a flotation unit, a sulfur melting unit, a heat preservation clarification unit and a filtering unit, wherein the flotation unit is provided with a sulfur-containing hydrometallurgical slag slurry inlet, a sulfur-rich material outlet and a desulfurized slag outlet, and is used for performing air flotation on the sulfur-containing hydrometallurgical slag slurry to obtain a sulfur-rich material and desulfurized slag; the sulfur melting unit is provided with a sulfur-rich material inlet and a sulfur melting material outlet, the sulfur-rich material inlet is connected with the sulfur-rich material outlet, and the sulfur melting unit is used for melting sulfur simple substances in the sulfur-rich material to obtain a sulfur melting material; the heat preservation clarification unit is provided with a sulfur melting material inlet and a clarified material outlet, and the sulfur melting material inlet is connected with the sulfur melting material outlet; the filtering unit is provided with a clarified material inlet and an elemental sulfur outlet, and the clarified material inlet is connected with the clarified material outlet. The utility model integrates the advantages of the flotation method and the thermal filtration method, and is a simple sulfur recovery process with low cost, simple operation and high sulfur recovery rate.
Description
Technical Field
The utility model relates to a resource recovery field of elemental sulfur particularly, relates to a recovery unit who contains elemental sulfur in metallurgical sediment of sulphur wet process.
Background
China is a large sulfur consuming country, but the sulfur resources in China are relatively deficient, and the sulfur has high external dependence. The sulfur-containing hydrometallurgical slag contains a large amount of elemental sulfur, such as chloridized leaching slag of sulfide ores, normal-pressure oxygen-enriched leaching slag, anode mud produced by nickel electrolysis and the like. Due to the lack of reasonable resource recovery technology, the sulfur-containing hydrometallurgical slag is stockpiled in a slag yard for a long time, which poses potential threat to local environment and has great potential safety hazard. Therefore, if the sulfur-containing hydrometallurgical slag can be reduced and recycled, the shortage of the sulfur market in China can be relieved, the burden on the local environment can be reduced, economic benefits can be generated, and sustainable development can be realized.
The current methods for recovering elemental sulfur from hazardous sulfur-containing wastes are largely divided into physical and chemical methods. Physical methods include flotation, high pressure decantation, granulation screening, melt filtration, and the like. The chemical method mainly comprises an organic solvent method, an inorganic solvent method and the like, wherein the organic solvent comprises kerosene, toluene, xylene, tetrachloroethylene and the like, and the inorganic solvent comprises ammonium sulfide, sodium sulfide and the like. The specific principles of these methods are as follows:
a flotation method: the principle is to separate elemental sulphur from other materials by exploiting the difference in hydrophilicity of the treated materials. In the flotation machine, the pulp is fully contacted with air through aeration. The elemental sulfur adheres to the surface of the bubbles due to the hydrophobicity and floats up to the surface layer along with the bubbles, and then is discharged through an overflow groove of a flotation machine, and the elemental sulfur product can be obtained after pressure filtration of a filter press or drying of a steam dryer. The flotation method has simple process, and can carry out flotation by adding a certain amount of light oil or without adding a medicament.
Granulation screening method: for example, chinese patent No. 201811280984.8 discloses a method for recovering sulfur from copper slag chlorine leaching slag, which comprises the steps of washing and slurrying a sulfur-containing material, heating to a temperature of 120 ℃ or higher to melt elemental sulfur into a liquid, and spraying cold water and stirring to obtain elemental sulfur particles. And finally, screening by using a screen with a certain mesh number, wherein the oversize is elemental sulfur particles, and the undersize is the desulfurized slag rich in precious metals.
A hot filtration method: the principle is that the viscosity of elemental sulfur is very low at 125-158 ℃, and is 0.0079-00096 Pa.s. In this temperature range, the elemental sulfur in the sulfur-containing material can be separated from the other solid materials by filtration.
The organic solvent method utilizes the characteristic that the solubility of sulfur in an organic solvent changes with the increase of temperature, such as kerosene, toluene, xylene, tetrachloroethylene, and the like. For example, the solubility of sulfur in kerosene increases with the increase of temperature, so elemental sulfur can be dissolved in an organic solvent by heating, an organic phase is obtained by solid-liquid separation, and the organic phase rich in elemental sulfur is cooled to separate out the elemental sulfur. Wherein, the kerosene can be recycled.
The inorganic solvent method includes an ammonium sulfide method and a sodium sulfide method. Ammonium sulfide is a good sulfur-dissolving reagent, and can react with elemental sulfur to produce ammonium polysulfide solution under a certain condition, and the filtered liquid phase is heated and decomposed into S0、NH3、H2S, precipitating simple substance at the bottom of decomposed liquid, and volatilizing NH3And H2And condensing the S to generate ammonium sulfide for recycling. The reaction formula is as follows:
x S0+(NH4)2S＝(NH4)2S(1+x)
(NH4)2S(1+x)＝2NH3+H2S+x S0
however, when the sulfur-containing hydrometallurgical slag is treated by the above methods, certain defects exist: the recovery process of the vacuum distillation method for treating the sulfur-containing hydrometallurgical slag has extremely high product purity, but the process has strict requirements on the tightness, heat preservation and the like of vacuum distillation equipment, so the equipment is relatively complex, the recovery cost is high, the economic benefit is low, and the industrial popularization is difficult to obtain. The flotation method is adopted to treat the sulfur-containing hydrometallurgical slag, and the sulfur product has low purity due to the complex components in the sulfur-containing hydrometallurgical slag. Compared with other processes, the sulfur recovery rate of the hot filtration method is low, the requirement on equipment heat-preservation operation is high, and the sulfur content in the residue is still high. The process has the advantages that the treatment amount is small, the material containing the noble metal is suitable for being treated by an organic solvent method, the recovery rate of sulfur is high and can reach about 97%, and the noble metal cannot be dissolved in the organic solvent, so that the loss of the noble metal is avoided. However, most organic solvents are flammable and explosive, and if residues with organic solvents attached to the surfaces are stacked in a slag yard, great potential safety hazards exist. Part of organic solvents, such as xylene, are smelly, toxic and volatile, which causes deterioration of the operating environment; tetrachloroethylene leaches out at a slower rate and is volatile. Inorganic solvent methods, such as ammonium sulfide and sodium sulfide, have the advantages of high leaching rate, simple process and recyclable reagent, but ammonium sulfide has a bad smell, and more importantly, precious metals are easily dissolved in an ammonium sulfide solution to cause loss.
For the above reasons, there is a need to provide a process for recovering elemental sulfur from sulfur-containing hydrometallurgical slag, which is more suitable for improving the sulfur recovery rate, and at the same time, simplifies the operation process, and avoids the use of toxic organic solvents, which are liable to cause precious metal loss.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide a recovery unit who contains elemental sulfur in metallurgical sediment of sulphur wet process to the rate of recovery that exists when retrieving the elemental sulfur in the metallurgical sediment of sulphur wet process among the solution prior art is low, the feature of environmental protection is poor and the operation is complicated scheduling problem.
In order to achieve the above object, according to an aspect of the present invention, there is provided a recovery apparatus for elemental sulfur in sulfur-containing hydrometallurgical slag, comprising: the flotation unit is provided with a sulfur-containing hydrometallurgical slag slurry inlet, a sulfur-rich material outlet and a desulfurized slag outlet and is used for performing air flotation on the sulfur-containing hydrometallurgical slag slurry to obtain a sulfur-rich material and desulfurized slag; the sulfur melting unit is provided with a sulfur-rich material inlet and a sulfur melting material outlet, the sulfur-rich material inlet is connected with the sulfur-rich material outlet, and the sulfur melting unit is used for melting elemental sulfur in the sulfur-rich material to obtain a sulfur melting material; the heat preservation clarification unit is provided with a sulfur melting material inlet and a clarified material outlet, and the sulfur melting material inlet is connected with the sulfur melting material outlet; and the filtering unit is provided with a clarified material inlet and an elemental sulfur outlet, and the clarified material inlet is connected with the clarified material outlet.
Further, the recovery device further comprises: the device comprises a washing unit, a sulfur-containing hydrometallurgy slag inlet, a washing water inlet and a washing material outlet, wherein the washing unit is used for washing the sulfur-containing hydrometallurgy slag; and the grinding unit is provided with a washing material inlet, a grinding water inlet and a grinding material outlet, the washing material inlet is connected with the washing material outlet, and the grinding material outlet is connected with the sulfur-containing hydrometallurgical slag slurry inlet of the flotation unit.
Further, the recovery device further comprises: the cyclone is arranged on a pipeline connected with the grinding material outlet and the sulfur-containing hydrometallurgy slag slurry inlet and is used for separating solid grinding materials in the grinding materials of the grinding unit products; and the slurry preparation unit is arranged on a pipeline connected with the cyclone and the inlet of the sulfur-containing hydrometallurgical slag slurry, and is used for preparing the solid grinding material and the water into the sulfur-containing hydrometallurgical slag slurry.
Further, the flotation unit comprises: the flotation machine is provided with a sulfur-containing hydrometallurgy slag slurry inlet, a sulfur-rich material slurry outlet and a desulfurization slag outlet; the filter press is provided with a sulfur-rich material slurry inlet and a sulfur-rich material outlet, and the sulfur-rich material slurry inlet is connected with the sulfur-rich material slurry outlet.
Further, the sulfur melting unit comprises: the sulfur melting kettle is provided with a sulfur-rich material inlet and a sulfur melting material outlet; the heating jacket is arranged outside the sulfur melting kettle and is provided with a first heat medium inlet; and the heating coil is arranged inside the sulfur melting kettle and is provided with a second heat medium inlet.
Further, the insulation clarification unit comprises: the clarifying tank is provided with a sulfur melting material inlet and a clarified material outlet, and the bottom of the clarifying tank is an inclined bottom; and the heat preservation unit is used for preserving heat of the clarification tank.
Furthermore, the filtering unit is a vacuum suction filter disc, a tubular filter or a plate and frame filter with heat preservation, and the filtering medium of the filtering unit is temperature-resistant cotton cloth, glass fiber or steel wire mesh.
The utility model provides a recovery unit who contains elemental sulfur in sulphur hydrometallurgy sediment utilizes the device to handle and contains sulphur hydrometallurgy sediment, and what adopt is that "aerify flotation-melting-clarification-filtration" process flow is in order to retrieve the elemental sulfur in the sulphur hydrometallurgy sediment. The flotation process retains the advantages of high recovery rate and low sulfur content of tailings in the flotation method, and elemental sulfur in the material is effectively enriched; the enriched material with high sulfur content obtained by the flotation process is also suitable for sulfur melting treatment, and the obtained elemental sulfur product has high quality. In addition, a clarifying step is added after the melting step, so that the load of hot filtration can be reduced, and the operating environment of subsequent hot filtration can be improved. Therefore, the utility model discloses avoid the toxicity, the flammability scheduling problem of high recovery cost, organic solvent method of vacuum distillation method, synthesized the advantage of flotation process and hot filtration method, be a low cost, easy and simple to handle, the high elemental sulfur recovery technology in the metallurgical sediment of sulphur wet process of sulphur recovery rate.
Drawings
The accompanying drawings, which form a part of the present application, are included to provide a further understanding of the invention, and are incorporated in and constitute a part of this specification, illustrate embodiments of the invention and together with the description serve to explain the invention and not to limit the invention. In the drawings:
fig. 1 shows a block diagram of a device for recovering elemental sulfur from sulfur-containing hydrometallurgical slag according to an embodiment of the present invention.
Wherein the figures include the following reference numerals:
10. a flotation unit; 11 a flotation machine; 12. a filter press; 20. a sulfur melting unit; 30. a heat preservation clarification unit; 40. a filtration unit; 50. a washing unit; 60. a grinding unit.
Detailed Description
It should be noted that the embodiments and features of the embodiments in the present application may be combined with each other without conflict. The present invention will be described in detail below with reference to the accompanying drawings in conjunction with embodiments.
As described in the background art, the problems of low recovery rate, poor environmental protection, complex operation and the like exist when the elemental sulfur in the sulfur-containing hydrometallurgical slag is recovered in the prior art.
In order to solve the above problem, the utility model provides a recovery unit of elemental sulfur in sulphur-containing hydrometallurgy sediment, as shown in fig. 1, this recovery unit includes flotation unit 10, sulphur melting unit 20, heat preservation clarification unit 30 and filter unit 40, flotation unit 10 has the import of sulphur-containing hydrometallurgy sediment thick liquids, rich sulphur material export and the export of desulfurization sediment, flotation unit 10 is used for aerifing the flotation so as to obtain rich sulphur material and desulfurization sediment to sulphur-containing hydrometallurgy sediment thick liquids; the sulfur melting unit 20 is provided with a sulfur-rich material inlet and a sulfur melting material outlet, the sulfur-rich material inlet is connected with the sulfur-rich material outlet, and the sulfur melting unit 20 is used for melting sulfur simple substances in the sulfur-rich material to obtain a sulfur melting material; the heat preservation clarification unit 30 is provided with a sulfur melting material inlet and a clarified material outlet, and the sulfur melting material inlet is connected with the sulfur melting material outlet; the filtering unit 40 has a clarified material inlet and an elemental sulfur outlet, with the clarified material inlet connected to the clarified material outlet.
The device is used for treating the sulfur-containing hydrometallurgical slag, and the process flow of 'aeration flotation-melting-clarification-filtration' is adopted to recover elemental sulfur in the sulfur-containing hydrometallurgical slag. The flotation process retains the advantages of high recovery rate and low sulfur content of tailings in the flotation method, and elemental sulfur in the material is effectively enriched; the enriched material with high sulfur content obtained by the flotation process is also suitable for sulfur melting treatment, and the obtained elemental sulfur product has high quality. In addition, a clarifying step is added after the melting step, so that the load of hot filtration can be reduced, and the operating environment of subsequent hot filtration can be improved. Therefore, the utility model discloses avoid the toxicity, the flammability scheduling problem of high recovery cost, organic solvent method of vacuum distillation method, synthesized the advantage of flotation process and hot filtration method, be a low cost, easy and simple to handle, the high elemental sulfur recovery technology in the metallurgical sediment of sulphur wet process of sulphur recovery rate.
In order to further improve the elemental sulfur recovery effect, in a preferred embodiment, the recovery apparatus further comprises a washing unit 50 and a grinding unit 60, the washing unit 50 comprises a sulfur-containing hydrometallurgical slag inlet, a washing water inlet and a washing material outlet, and the washing unit 50 is used for washing the sulfur-containing hydrometallurgical slag; the grinding unit 60 has a washed material inlet, a ground water inlet and a ground material outlet, the washed material inlet being connected to the washed material outlet and the ground material outlet being connected to the sulphur-containing hydrometallurgical slag slurry inlet of the flotation unit 10. Thus, part of soluble salts contained in the sulfur-containing hydrometallurgical slag can be removed by water washing and then fed to the grinding unit 60 for wet grinding, so that the degree of monomer separation of elemental sulfur from other materials can be increased, and the flotation effect can be improved. Preferably, the grinding unit 60 is a ball mill. The ball mill performs wet ball milling, and can better separate elemental sulfur in the slag.
In a preferred embodiment, the recycling apparatus further comprises a cyclone and a slurry preparation unit, the cyclone is disposed on a pipeline connecting the ground material outlet and the sulfur-containing hydrometallurgical slag slurry inlet, and the cyclone is used for separating solid ground material from the ground material produced by the grinding unit 60; and the slurry preparation unit is arranged on a pipeline connected with the cyclone and the inlet of the sulfur-containing hydrometallurgical slag slurry, and is used for preparing the solid grinding material and the water into the sulfur-containing hydrometallurgical slag slurry. Therefore, the ground materials after wet grinding enter a cyclone for cyclone classification, solid materials in the materials are separated, and then the materials and water are prepared into slurry in a slurry preparation unit, so that the subsequent flotation process can be carried out.
The flotation unit 10 preferably comprises a flotation machine 11 and a filter press 12, wherein the flotation machine 11 is provided with a sulfur-containing hydrometallurgical slag slurry inlet, a sulfur-rich material slurry outlet and a desulfurized slag outlet; the filter press 12 has a sulfur-rich material slurry inlet and a sulfur-rich material outlet, the sulfur-rich material slurry inlet being connected to the sulfur-rich material slurry outlet. Thus, after the slurry enters the flotation machine 11 for flotation, the obtained sulfur-rich material slurry enters the filter press 12 for treatment, and then the sulfur-rich material can be obtained. The particular flotation machine 11 may be of a type commonly used in the art, such as flotation machine 11 having a flotation cell into which the slurry is fed and into which a quantity of air is introduced to agitate the slurry to cause bubbling of the slurry. Obtaining tailings, namely desulfurization slag, at the lower part of the flotation tank; and collecting the upper bubbles by using a bubble scraper to obtain the sulfur-rich material slurry.
Preferably, the flotation unit 10 further comprises a drying unit disposed on the conduit connecting the sulfur-rich material outlet and the sulfur-rich material inlet. Therefore, the sulfur-rich material slurry can be dried and then enters a subsequent melting process. Preferably the drying unit is a steam dryer.
In a preferred embodiment, the sulfur melting unit 20 comprises a sulfur melting kettle, a heating jacket and a heating coil, wherein the sulfur melting kettle is provided with a sulfur-rich material inlet and a sulfur melting material outlet; the heating jacket is arranged outside the sulfur melting kettle and is provided with a first heat medium inlet; the heating coil is arranged inside the sulfur melting kettle and is provided with a second heat medium inlet. Like this, can utilize heating jacket and the dual heating mode of coil pipe to carry out the melting of rich sulphur material for temperature environment is more even, and heating efficiency is higher, thereby is favorable to improving the recovery effect and the recovery efficiency of sulphur simple substance.
More preferably, the sulfur melting unit 20 further includes a ventilation device for discharging volatile matters in the melting process to improve the operating environment of the plant and workers.
In a preferred embodiment, the heat-insulating and clarifying unit 30 comprises a clarification tank and a heat-insulating unit, wherein the clarification tank is provided with a molten sulfur material inlet and a clarified material outlet, and the bottom of the clarification tank is an inclined bottom; the heat preservation unit is used for preserving heat of the clarification tank. Therefore, tailings generated in the clarification process of the sulfur melting material can be concentrated at the inclined bottom, and people can regularly clean slag at the bottom of the clarification tank through slag dragging equipment along with long-time operation of the equipment.
The clarified and separated liquid sulfur is further separated from impurities through a filtering process to reach the first-grade standard (S0> 99.9%). In order to further improve the filtering effect, in a preferred embodiment, the filtering unit 40 is a vacuum suction filter disc, a tubular filter or a plate and frame filter with heat insulation, and the filtering medium of the filtering unit 40 is temperature-resistant cotton cloth, glass fiber or steel wire mesh.
According to another aspect of the utility model, still provide a recovery method of elemental sulfur in sulphur-containing hydrometallurgy sediment, it includes with the step: performing air flotation on the sulfur-containing hydrometallurgy slag slurry to obtain a sulfur-rich material and desulfurized slag; melting the sulfur-rich material to melt sulfur in the sulfur-rich material to form a molten sulfur material; carrying out heat preservation clarification treatment on the sulfur melting material to obtain a clarified material; filtering and clarifying the material to obtain an elemental sulfur product.
The method is used for treating the sulfur-containing hydrometallurgical slag, and the process flow of 'aeration flotation-melting-clarification-filtration' is adopted to recover elemental sulfur in the sulfur-containing hydrometallurgical slag. The flotation process retains the advantages of high recovery rate and low sulfur content of tailings in the flotation method, and elemental sulfur in the material is effectively enriched; the enriched material with high sulfur content obtained by the flotation process is also suitable for sulfur melting treatment, and the obtained elemental sulfur product has high quality. In addition, a clarifying step is added after the melting step, so that the load of hot filtration can be reduced, and the operating environment of subsequent hot filtration can be improved. Therefore, the utility model discloses avoid the toxicity, the flammability scheduling problem of high recovery cost, organic solvent method of vacuum distillation method, synthesized the advantage of flotation process and hot filtration method, be a low cost, easy and simple to handle, the high elemental sulfur recovery technology in the metallurgical sediment of sulphur wet process of sulphur recovery rate.
In order to further enhance the elemental sulfur recovery effect, in a preferred embodiment, the recovery method further comprises the following steps before the aeration flotation step: washing and filtering the sulfur-containing hydrometallurgy slag to obtain a washing material; and wet grinding the washing material to obtain a ground material. Thus, part of soluble salts contained in the sulfur-containing hydrometallurgical slag can be removed by washing with water, and then wet grinding can improve the monomer separation degree of elemental sulfur from other materials, so as to improve the flotation effect. Preferably, in the step of washing, the weight ratio of the sulfur-containing hydrometallurgical slag to water is 1: 3-6, and the washing is carried out for 30-50 min at the temperature of 60-85 ℃. So that soluble salt impurities carried in the slag can be more fully removed. Preferably, in the wet grinding step, the weight ratio of the washing materials to water is 1: 2-3, and more preferably, a ball mill is adopted for the wet grinding step. The ball mill performs wet ball milling, and can better separate elemental sulfur in the slag.
In a preferred embodiment, after the wet milling step, the milled material is subjected to cyclone classification to separate solid material from the washed material, and preferably the solid material has a material content of more than 70% by weight with a particle size of less than 200 mesh. And then mixing the solid material and water to prepare sulfur-containing hydrometallurgy slag slurry for an air flotation step, wherein the weight ratio of the solid material to the water is preferably 1: 4-8, and the time of the air flotation is preferably 10-60 min. The flotation effect of the elemental sulfur is better when the solid material is used for flotation. And the weight ratio of the solid material to the water is controlled within the range, so that the flotation effect is further improved, and the recovery rate of the elemental sulfur is further improved.
In order to further improve the separation effect of elemental sulfur, in a limited implementation manner, in the step of melting the sulfur-rich material, the sulfur-rich material is heated to 130-160 ℃, and the temperature is maintained for 0.5-2 hours, so that a sulfur-melted material is obtained. In this way, elemental sulfur can be more fully melted and separated from other impurities. Preferably, the recovery process further comprises the step of drying the sulphur-rich material prior to the melt processing step.
In a preferred embodiment, the step of filtering the clarified material is performed by vacuum suction filtration, tube filtration or plate and frame filtration.
More preferably, the treatment time of the heat preservation and clarification step is 1-2 h, so that the liquid sulfur is better separated from the slag.
The present application is described in further detail below with reference to specific examples, which should not be construed as limiting the scope of the invention as claimed.
Example 1
100g of sulfur-containing hydrometallurgical slag is taken, 500mL of water is added according to the solid-to-liquid ratio of 1:5, and the mixture is washed for 30min at the temperature of 70 ℃. And carrying out solid-liquid separation by a vacuum pump filter to obtain washed slag. And mixing the washed slag with water according to the ratio of 1:2, and adding the mixture into a ball mill for ball milling for 2 hours.
Pouring the obtained ore pulp into a flotation tank of a flotation machine, adding water according to the solid-liquid ratio of 1:5, stirring and aerating for 30 min. Obtaining tailings, namely desulfurization slag, at the lower part of the flotation tank; and collecting the upper bubbles by using a bubble scraper to obtain sulfur-rich material slurry, and performing liquid-solid separation and drying on the slurry to obtain the sulfur-rich material.
Directly adding the sulfur-rich material into a sulfur melting kettle, heating to 140 ℃, and preserving heat for 1 h. The liquid sulfur was then filtered to yield a sulfur product with a purity of 99.92% and a calculated sulfur recovery of 96.43%.
Example 2
100g of sulfur-containing hydrometallurgical slag is taken, 500mL of water is added according to the solid-to-liquid ratio of 1:5, and the mixture is washed for 30min at the temperature of 70 ℃. And carrying out solid-liquid separation by a vacuum pump filter to obtain washed slag. And mixing the washed slag with water according to the ratio of 1:2, and adding the mixture into a ball mill for ball milling for 2 hours.
Pouring the obtained ore pulp into a flotation tank of a flotation machine, adding water according to the solid-liquid ratio of 1:6, stirring and aerating for 40 min. Obtaining tailings, namely desulfurization slag, at the lower part of the flotation tank; and collecting the upper bubbles by using a bubble scraper to obtain sulfur-rich material slurry, and performing liquid-solid separation and drying on the slurry to obtain the sulfur-rich material.
Directly adding the sulfur-rich material into a sulfur melting kettle, heating to 150 ℃, and preserving heat for 1.5 h. The liquid sulfur was then filtered to yield a sulfur product with a purity of 99.90% and a calculated sulfur recovery of 97.71%.
Example 3
100g of sulfur-containing hydrometallurgical slag is taken, 500mL of water is added according to the solid-to-liquid ratio of 1:5, and the mixture is washed for 30min at the temperature of 70 ℃. And carrying out solid-liquid separation by a vacuum pump filter to obtain washed slag. And mixing the washed slag with water according to the ratio of 1:2, and adding the mixture into a ball mill for ball milling for 2 hours.
Pouring the obtained ore pulp into a flotation tank of a flotation machine, adding water according to the solid-liquid ratio of 1:5, stirring and aerating for 60 min. Obtaining tailings, namely desulfurization slag, at the lower part of the flotation tank; and collecting the upper bubbles by using a bubble scraper to obtain sulfur-rich material slurry, and performing liquid-solid separation and drying on the slurry to obtain the sulfur-rich material.
Directly adding the sulfur-rich material into a sulfur melting kettle, heating to 150 ℃, and preserving heat for 2 hours. The liquid sulfur was then filtered to yield a sulfur product with a purity of 99.91% and a calculated sulfur recovery of 98.10%.
Example 4
100g of sulfur-containing hydrometallurgical slag is taken, 500mL of water is added according to the solid-to-liquid ratio of 1:3, and the mixture is washed for 30min at the temperature of 60 ℃. And carrying out solid-liquid separation by a vacuum pump filter to obtain washed slag. And mixing the washed slag with water according to the ratio of 1:2, and adding the mixture into a ball mill for ball milling for 2 hours.
Pouring the obtained ore pulp into a flotation tank of a flotation machine, adding water according to the solid-liquid ratio of 1:4, stirring and aerating for 10 min. Obtaining tailings, namely desulfurization slag, at the lower part of the flotation tank; and collecting the upper bubbles by using a bubble scraper to obtain sulfur-rich material slurry, and performing liquid-solid separation and drying on the slurry to obtain the sulfur-rich material.
Directly adding the sulfur-rich material into a sulfur melting kettle, heating to 130 ℃, and preserving heat for 1 h. The liquid sulfur was then filtered to yield a sulfur product with a purity of 97.71% and a calculated sulfur recovery of 98.41%.
Example 5
100g of sulfur-containing hydrometallurgical slag is taken, 500mL of water is added according to the solid-to-liquid ratio of 1:6, and washing is carried out for 30min at the temperature of 85 ℃. And carrying out solid-liquid separation by a vacuum pump filter to obtain washed slag. And mixing the washed slag with water according to the ratio of 1:3, and adding the mixture into a ball mill for ball milling for 2 hours.
Pouring the obtained ore pulp into a flotation tank of a flotation machine, adding water according to the solid-liquid ratio of 1:8, stirring and aerating for 50 min. Obtaining tailings, namely desulfurization slag, at the lower part of the flotation tank; and collecting the upper bubbles by using a bubble scraper to obtain sulfur-rich material slurry, and performing liquid-solid separation and drying on the slurry to obtain the sulfur-rich material.
Directly adding the sulfur-rich material into a sulfur melting kettle, heating to 160 ℃, and preserving heat for 2 hours. The liquid sulfur was then filtered to yield a sulfur product with a purity of 99.90% and a calculated sulfur recovery of 95.51%.
Example 6
100g of sulfur-containing hydrometallurgical slag is taken, 500mL of water is added according to the solid-to-liquid ratio of 1:8, and the mixture is washed for 30min at the temperature of 90 ℃. And carrying out solid-liquid separation by a vacuum pump filter to obtain washed slag. And mixing the washed slag with water according to the ratio of 1:4, and adding the mixture into a ball mill for ball milling for 2 hours.
Pouring the obtained ore pulp into a flotation tank of a flotation machine, adding water according to the solid-liquid ratio of 1:8, stirring and aerating for 60 min. Obtaining tailings, namely desulfurization slag, at the lower part of the flotation tank; and collecting the upper bubbles by using a bubble scraper to obtain sulfur-rich material slurry, and performing liquid-solid separation and drying on the slurry to obtain the sulfur-rich material.
Directly adding the sulfur-rich material into a sulfur melting kettle, heating to 180 ℃, and preserving heat for 2 hours. The liquid sulfur was then filtered to yield a sulfur product with a purity of 99.95% and a calculated sulfur recovery of 93.11%.
Comparative example 1
100g of sulfur-containing hydrometallurgical slag is taken, 500mL of water is added according to the solid-to-liquid ratio of 1:5, and the mixture is washed for 30min at the temperature of 70 ℃. And carrying out solid-liquid separation by a vacuum pump filter to obtain washed slag. And mixing the washed slag with water according to the ratio of 1:2, and adding the mixture into a ball mill for ball milling for 2 hours.
Pouring the obtained ore pulp into a flotation tank of a flotation machine, adding water according to the solid-liquid ratio of 1:5, stirring and aerating for 30 min. Obtaining tailings, namely desulfurization slag, at the lower part of the flotation tank; and collecting the upper bubbles by using a bubble scraper to obtain sulfur-rich material slurry, and performing liquid-solid separation and drying on the slurry to obtain a sulfur product with the purity of 83.45% and the sulfur recovery rate of 97.71%.
Comparative example 2
100g of sulfur-containing hydrometallurgical slag is taken, 500mL of water is added according to the solid-to-liquid ratio of 1:5, and the mixture is washed for 30min at the temperature of 70 ℃. And carrying out solid-liquid separation by a vacuum pump filter to obtain washed slag. And mixing the washed slag with water according to the ratio of 1:2, and adding the mixture into a ball mill for ball milling for 2 hours.
And directly adding the obtained ore pulp into a sulfur melting kettle, heating to 140 ℃, and preserving heat for 1 h. The liquid sulfur was then filtered to yield a sulfur product with a purity of 93.89% and a calculated sulfur recovery of 86.11%.
From the above description, it can be seen that the above-mentioned embodiments of the present invention achieve the following technical effects:
compared with the utility model, the purity of the sulfur product obtained by the flotation method is obviously reduced, and the sulfur recovery rate is slightly increased; the purity of the sulfur product obtained by independently adopting a hot-melting sulfur method is slightly reduced, and the sulfur recovery rate is obviously reduced.
The above description is only a preferred embodiment of the present invention and is not intended to limit the present invention, and various modifications and changes may be made by those skilled in the art. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (7)
1. The utility model provides a recovery unit of elemental sulfur in metallurgical sediment of sulphur wet process which characterized in that includes:
the flotation unit (10) is provided with a sulfur-containing hydrometallurgical slag slurry inlet, a sulfur-rich material outlet and a desulfurized slag outlet, and the flotation unit (10) is used for performing air flotation on the sulfur-containing hydrometallurgical slag slurry to obtain a sulfur-rich material and desulfurized slag;
the sulfur melting unit (20) is provided with a sulfur-rich material inlet and a sulfur melting material outlet, the sulfur-rich material inlet is connected with the sulfur-rich material outlet, and the sulfur melting unit (20) is used for melting sulfur simple substances in the sulfur-rich material to obtain a sulfur melting material;
the heat preservation clarification unit (30) is provided with a sulfur melting material inlet and a clarification material outlet, and the sulfur melting material inlet is connected with the sulfur melting material outlet;
a filter unit (40) having a clarified material inlet and an elemental sulfur outlet, the clarified material inlet being connected to the clarified material outlet.
2. The recycling apparatus according to claim 1, further comprising:
the device comprises a washing unit (50), a sulfur-containing hydrometallurgical slag inlet, a washing water inlet and a washing material outlet, wherein the washing unit (50) is used for washing the sulfur-containing hydrometallurgical slag;
a grinding unit (60) having a scrubbing material inlet, a grinding water inlet and a grinding material outlet, the scrubbing material inlet being connected to the scrubbing material outlet, the grinding material outlet being connected to the sulphur-containing hydrometallurgical slag slurry inlet of the flotation unit (10).
3. The recycling apparatus according to claim 2, further comprising:
a cyclone arranged in the conduit connecting the mill feed outlet with the sulphur-containing hydrometallurgical slag slurry inlet, for separating solid mill feed from the mill feed of the product of the mill unit (60);
and the slurry preparation unit is arranged on a pipeline connected with the cyclone and the sulfur-containing hydrometallurgical slag slurry inlet and is used for preparing the solid grinding material and water into the sulfur-containing hydrometallurgical slag slurry.
4. A recovery device according to any of claims 1 to 3, characterized in that the flotation unit (10) comprises:
a flotation machine (11) having the sulphur-containing hydrometallurgical slag slurry inlet, a sulphur-rich material slurry outlet and the desulphurised slag outlet;
the filter press (12) is provided with a sulfur-rich material slurry inlet and a sulfur-rich material outlet, and the sulfur-rich material slurry inlet is connected with the sulfur-rich material slurry outlet.
5. A recovery device according to any one of claims 1 to 3, characterized in that the sulphur melting unit (20) comprises:
the sulfur melting kettle is provided with a sulfur-rich material inlet and a sulfur melting material outlet;
the heating jacket is arranged outside the sulfur melting kettle and is provided with a first heat medium inlet;
and the heating coil is arranged inside the sulfur melting kettle and is provided with a second heat medium inlet.
6. A recovery device according to any of claims 1 to 3, characterized in that the thermo-refining unit (30) comprises:
the clarifying pool is provided with the sulfur melting material inlet and the clarifying material outlet, and the bottom of the clarifying pool is an inclined bottom;
and the heat preservation unit is used for preserving heat of the clarification tank.
7. A recycling apparatus according to any one of claims 1 to 3, characterized in that the filter unit (40) is a vacuum suction disc, a tube filter or a plate and frame filter with insulation, and the filter medium of the filter unit (40) is temperature-resistant cotton cloth, glass fiber or steel wire mesh.
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111392696A (en) * | 2020-04-26 | 2020-07-10 | 中国恩菲工程技术有限公司 | Device and method for recovering elemental sulfur in sulfur-containing hydrometallurgy slag |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111392696A (en) * | 2020-04-26 | 2020-07-10 | 中国恩菲工程技术有限公司 | Device and method for recovering elemental sulfur in sulfur-containing hydrometallurgy slag |
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