CN111979422B - Method for comprehensively recovering valuable metals in goethite slag - Google Patents

Method for comprehensively recovering valuable metals in goethite slag Download PDF

Info

Publication number
CN111979422B
CN111979422B CN202010655002.XA CN202010655002A CN111979422B CN 111979422 B CN111979422 B CN 111979422B CN 202010655002 A CN202010655002 A CN 202010655002A CN 111979422 B CN111979422 B CN 111979422B
Authority
CN
China
Prior art keywords
zinc
indium
iron
slag
roasting
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN202010655002.XA
Other languages
Chinese (zh)
Other versions
CN111979422A (en
Inventor
高文成
温建康
邓静娴
蔡镠璐
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
GRIMN Engineering Technology Research Institute Co Ltd
GRINM Resources and Environment Technology Co Ltd
Original Assignee
GRIMN Engineering Technology Research Institute Co Ltd
GRINM Resources and Environment Technology Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by GRIMN Engineering Technology Research Institute Co Ltd, GRINM Resources and Environment Technology Co Ltd filed Critical GRIMN Engineering Technology Research Institute Co Ltd
Priority to CN202010655002.XA priority Critical patent/CN111979422B/en
Publication of CN111979422A publication Critical patent/CN111979422A/en
Application granted granted Critical
Publication of CN111979422B publication Critical patent/CN111979422B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B7/00Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
    • C22B7/02Working-up flue dust
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B1/00Preliminary treatment of ores or scrap
    • C22B1/14Agglomerating; Briquetting; Binding; Granulating
    • C22B1/24Binding; Briquetting ; Granulating
    • C22B1/248Binding; Briquetting ; Granulating of metal scrap or alloys
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B19/00Obtaining zinc or zinc oxide
    • C22B19/20Obtaining zinc otherwise than by distilling
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B19/00Obtaining zinc or zinc oxide
    • C22B19/30Obtaining zinc or zinc oxide from metallic residues or scraps
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B58/00Obtaining gallium or indium
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Abstract

The invention provides a method for comprehensively recovering valuable metals in goethite slag, which comprises the following steps of: levigating goethite slag, and mixing the goethite slag: a chlorine-containing salt: carbon powder =1:0.05 to 1.0: proportioning the materials according to the mass ratio of 0.05-1.0; uniformly mixing the ingredients, and pelletizing, wherein the diameter of the pellets is 10-20mm; roasting and volatilizing at 500-1100 deg.c for 1-6 hr; collecting zinc-indium-containing dust generated in the volatilization process, and obtaining roasted calcine. After the reaction is finished, cooling the roasted calcine to room temperature, and then grinding the ore until the granularity is-200 meshes. And magnetically separating the ground material with the magnetic field intensity of 160-350 mT to obtain the iron concentrate product. The method provided by the invention can realize the high-efficiency volatilization recovery of the valuable metals zinc and indium in the goethite slag under the low-temperature thermal field, and the valuable metals zinc and indium are coupled with the magnetic field to obtain the iron ore concentrate product, and the method has the characteristics of high valuable metal recovery rate, simple and convenient operation, low energy consumption and the like.

Description

Method for comprehensively recovering valuable metals in goethite slag
Technical Field
The invention relates to comprehensive recovery of valuable metals zinc indium iron in goethite slag, in particular to a method for comprehensively recovering valuable metals in goethite slag.
Background
In the hydrometallurgical process of zinc, especially the zinc oxygen pressure leaching process, iron is leached into solution as an impurity element together with zinc. Iron is a foreign ion, and if the concentration of iron in the solution is greater than 20mg/L, it affects the zinc electrodeposition efficiency, increases the power consumption of the electrodeposition process, and poses serious hazards, and thus it needs to be economically and efficiently removed before electrodeposition. At present, the methods for removing iron from solution mainly include jarosite method, goethite method, hematite method and the like. The goethite method is a more common iron removal method in the zinc smelting industry, and has the advantages of complete precipitation, small slag amount, good iron slag filterability and the like, but has the outstanding problems of difficult control of mixed crystal forms of the iron slag, low iron content (35-45%) of the iron slag, high zinc content (8-15%) of the iron slag, difficult recycling of the iron slag, and the like.
At present, the treatment of the needle iron slag is generally carried out by adopting a rotary kiln volatilization-dust collection-kiln slag water quenching process. The method mainly comprises the steps of heating goethite slag in a rotary kiln to 1250 ℃ for volatilization, volatilizing valuable metals such as zinc and indium in smoke, recovering zinc and indium in a dust mode, and finally carrying out water quenching treatment on roasting slag. The method mainly has the following problems: 1) The volatilization rate of zinc and indium is not high, and especially when the goethite slag contains more zinc ferrite, the zinc ferrite can not be effectively decomposed by high-temperature volatilization to volatilize the zinc, so that part of zinc and indium are lost in water-quenched slag, and the waste of resources is caused; 2) The rotary kiln has higher volatilization temperature, so that the energy consumption is higher, and the cost is brought to the operation of enterprises; 3) Iron is not effectively utilized; roasted kiln slag is directly sold after water quenching, and iron resources cannot be effectively recycled.
Therefore, it is imperative to find a method for recovering valuable metals from goethite slag economically, reasonably and efficiently.
Disclosure of Invention
In view of the above problems, an object of the present invention is to provide a method for comprehensively recovering valuable metals from goethite slag, which can efficiently recover zinc, indium and iron elements from goethite slag and lay the foundation for the resource utilization of valuable metals.
In order to achieve the above object, the present invention provides a method for comprehensively recovering valuable metals from goethite slag, comprising the steps of:
1) Grinding goethite slag until the granularity is-200 meshes to-400 meshes, and mixing the fine powder according to the weight ratio of goethite slag: a chlorine-containing salt: carbon powder =1:0.05 to 1: 0.05-1 mass ratio; uniformly mixing the ingredients, and pelletizing, wherein the diameter of the pellets is 10-20mm;
2) Roasting the pellets in the step 1) at 500-1100 ℃ for 1-6 h, collecting zinc-indium-containing dust generated in the volatilization process, and obtaining roasted calcine;
in the roasting process of the goethite slag, metal zinc and indium, zinc chloride and indium chloride can be volatilized due to low boiling points of zinc, indium and compounds. The zinc and indium react with oxygen to produce zinc oxide and indium oxide, the volatile material (zinc-indium-containing dust) mainly contains zinc oxide, zinc chloride, zinc oxide, indium chloride, etc., and the indium and zinc in the volatile material are separated and purified by conventional method.
3) Cooling the roasted calcine obtained in the step 2) to room temperature, then grinding the calcine to the granularity of-200 meshes, and carrying out magnetic separation under the magnetic field intensity of 160-350 mT to obtain an iron ore concentrate product.
The residual magnetic separation tailings after the iron ore concentrate product is obtained through magnetic separation can be used as building materials, such as cement raw materials.
Further, the iron ore slag in the step 1): a chlorine-containing salt: the mass ratio of the carbon powder is 1:0.05 to 0.4:0.05 to 0.5.
Further, in the step 1), the chlorine-containing salt is one or more of sodium chloride, calcium chloride, potassium chloride, calcium chlorate, sodium chlorate, potassium chlorate, calcium hypochlorite, sodium perchlorate, potassium perchlorate and the like.
When a mixture of multiple chlorine-containing salts is used, any mass ratio between the chlorine-containing salts can be used.
Further, the roasting in the step 2) is carried out at 900-1100 ℃ for 2-4 h.
Furthermore, when the magnetic separation is carried out in the step 3), the magnetic field intensity is 200-300 mT.
Further, the goethite slag contains 20 to 60wt% of iron, 6 to 15wt% of zinc, and 0.01 to 0.5wt% of indium.
The invention provides a method for comprehensively recovering valuable metals in goethite slag, which utilizes a roasting system containing chloride and carbon powder to reduce the problem of high roasting volatilization temperature of the prior art and realize high-efficiency volatilization of zinc and indium; realizing the high-efficiency recovery of iron.
Among the key parameters that affect zinc, indium and iron recovery rates are goethite slag: a chlorine-containing salt: carbon powder mass ratio, roasting temperature, roasting time, magnetic separation strength and the like.
The chlorine-containing salt is added into a reaction system, so that the phase containing zinc and indium is intensively decomposed, the system is easier to volatilize, and the reaction temperature (1200-1300 ℃) of the traditional magnetizing roasting is reduced, so that the volatilization rates of zinc and indium can be obviously improved.
The addition of the carbon powder can effectively promote the generation of a magnetic iron-containing phase within a parameter limit range, can promote the decomposition of zinc ferrite in the goethite slag by combining the roasting temperature and the roasting time, provides conditions for obtaining iron ore concentrate by subsequent magnetic separation, and can play a role in increasing the iron recovery rate by combining the change of the magnetic field strength within the parameter limit range.
In addition, goethite slag: when the mass ratio of the chlorine-containing salt, the roasting temperature and the roasting time are changed within the parameter limit range, the volatilization rates of zinc and indium are gradually influenced after being increased; the goethite slag, the carbon powder mass ratio, the roasting temperature, the roasting time and the magnetic field intensity play a role in increasing the iron recovery rate when changing within the parameter limit range.
The low-temperature thermal field means that the goethite slag can react when the roasting temperature is controlled to be 500-1100 ℃, so that the reaction temperature of roasting at 1200-1300 ℃ in the original production process is reduced, and the energy consumption and the production cost are effectively reduced.
The invention has the beneficial effects that:
the invention provides a method for comprehensively recovering valuable metals in goethite, which can realize the high-efficiency volatilization recovery of zinc and indium in the goethite under a low-temperature thermal field, solves the problems of overhigh volatilization temperature, low volatilization rate of zinc and indium, ineffective utilization of iron and the like of the goethite, realizes the comprehensive recovery of the zinc, indium and iron in the goethite, has the volatilization rate of zinc of more than 70 percent, the volatilization rate of indium of more than 75 percent and the iron grade of an iron ore concentrate product of more than 60 percent, greatly improves the resource utilization rate and realizes the resource utilization of solid wastes. The method provided by the invention has the advantages of simple process flow, simple and convenient operation, low raw material cost, no pollution to the environment, great environmental benefit and economic benefit, and capability of meeting the requirement of current green metallurgy on clean production.
Drawings
FIG. 1 is a process flow diagram for the integrated recovery of valuable metals from goethite slag according to the present invention.
Detailed Description
The invention is described in detail below with reference to the figures and the embodiments. The following examples are only illustrative of the present invention, and the scope of the present invention shall include the full contents of the claims, not limited to the examples.
Example 1
The contents of iron in the goethite slag in Guangdong province are 36.88% of iron, 12.08% of zinc and 0.02% of indium, and the main chemical detection results and the phase analysis results are shown in tables 1-3. Grinding 100g of goethite slag to the granularity of-200 meshes to-400 meshes according to the process flow shown in figure 1, mixing the ground goethite slag with 10g of calcium chloride and 45g of carbon powder, pelletizing, wherein the pellet granularity is 10-20mm, roasting in a tubular furnace, controlling the roasting temperature at 900 ℃ and the roasting time at 2h. Collecting the volatilized zinc-indium-containing dust in the roasting process. And grinding the obtained material to the granularity of-200 meshes after roasting, and carrying out magnetic separation under the condition that the magnetic field intensity is 200mT to obtain an iron ore concentrate product. In the experimental process, chemical element detection and analysis are carried out on the contents of zinc, indium and iron in the roasted material, the zinc-indium-containing dust, the iron concentrate and the magnetic separation tailings respectively, and the recovery rate is calculated.
According to calculation, the recovery rate of zinc is 71.1%, the recovery rate of indium is 78.2%, and the grade of iron ore concentrate is 60.2%.
TABLE 1 analysis of chemical elements of certain goethite slag
Figure BDA0002576447310000041
TABLE 2 phase analysis results of some goethite slag iron
Figure BDA0002576447310000042
TABLE 3 phase analysis results of certain goethite slag Zinc
Figure BDA0002576447310000043
Example 2
The contents of iron in the goethite slag in Guangdong province are 36.88% of iron, 12.08% of zinc and 0.02% of indium, and the main chemical detection results and the phase analysis results are shown in tables 1-3. Grinding 100g of goethite slag to the granularity of-200 meshes to-400 meshes according to the process flow shown in figure 1, mixing with 5g of sodium chloride and 50g of carbon powder, pelletizing, wherein the pellet granularity is 10-20mm, roasting in a tubular furnace, controlling the roasting temperature at 900 ℃ and the roasting time at 2h. Collecting the volatilized zinc-indium-containing dust in the roasting process. And grinding the obtained material to the granularity of-200 meshes after roasting, and carrying out magnetic separation under the condition that the magnetic field intensity is 160mT to obtain an iron ore concentrate product. In the experimental process, the content of zinc, indium and iron in the roasted material, the zinc-indium-containing dust, the iron concentrate and the magnetic separation tailings needs to be respectively detected and analyzed by chemical elements, and the recovery rate is calculated.
According to calculation, the recovery rate of zinc is 73.4%, the recovery rate of indium is 75.5%, and the grade of iron ore concentrate is 64.2%.
Example 3
The contents of iron in the goethite slag in Guangdong province are 36.88% of iron, 12.08% of zinc and 0.02% of indium, and the main chemical detection results and the phase analysis results are shown in tables 1-3. Grinding 100g of goethite slag to the granularity of-200 meshes to-400 meshes according to the process flow shown in figure 1, mixing with 15g of potassium chloride and 40g of carbon powder, pelletizing, wherein the pellet granularity is 10-20mm, roasting in a tubular furnace, controlling the roasting temperature at 900 ℃ and the roasting time at 2h. Collecting the volatilized zinc-indium-containing dust in the roasting process. And grinding the obtained material after roasting until the granularity is-200 meshes, and carrying out magnetic separation under the condition that the magnetic field intensity is 240mT to obtain an iron ore concentrate product. In the experimental process, the content of zinc, indium and iron in the roasted material, the zinc-indium-containing dust, the iron concentrate and the magnetic separation tailings needs to be respectively detected and analyzed by chemical elements, and the recovery rate is calculated.
According to calculation, the recovery rate of zinc is 81.2%, the recovery rate of indium is 76.1%, and the grade of iron ore concentrate is 63.1%.
Example 4
The contents of iron in the goethite slag in Guangdong province are 36.88% of iron, 12.08% of zinc and 0.02% of indium, and the main chemical detection results and the phase analysis results are shown in tables 1-3. Grinding 100g of the goethite slag to the granularity of-200 meshes to-400 meshes according to the process flow shown in figure 1, mixing with 20g of calcium chlorate and 35g of carbon powder, pelletizing, wherein the pellet granularity is 10-20mm, roasting in a tubular furnace, controlling the roasting temperature at 900 ℃ and the roasting time at 3h. Collecting the volatilized zinc-indium-containing dust in the roasting process. And grinding the obtained material after roasting until the granularity is-200 meshes, and carrying out magnetic separation under the magnetic field intensity of 270mT to obtain an iron ore concentrate product. In the experimental process, the content of zinc, indium and iron in the roasted material, the zinc-indium-containing dust, the iron concentrate and the magnetic separation tailings needs to be respectively detected and analyzed by chemical elements, and the recovery rate is calculated.
According to calculation, the recovery rate of zinc is 82.8%, the recovery rate of indium is 75.8%, and the grade of iron ore concentrate is 61.2%.
Example 5
The contents of iron in the goethite slag in Guangdong province are 36.88% of iron, 12.08% of zinc and 0.02% of indium, and the main chemical detection results and the phase analysis results are shown in tables 1-3. Grinding 100g of the goethite slag to the granularity of-200 meshes to-400 meshes according to the process flow shown in the figure 1, mixing with 25g of sodium chlorate and 30g of carbon powder, pelletizing, wherein the pellet granularity is 10-20mm, placing the pellets into a tubular furnace for roasting, controlling the roasting temperature to be 1000 ℃ and the roasting time to be 3 hours. Collecting the volatilized zinc-indium-containing dust in the roasting process. And grinding the obtained material to the granularity of-200 meshes after roasting, and carrying out magnetic separation under the magnetic field intensity of 300mT to obtain an iron ore concentrate product. In the experimental process, the content of zinc, indium and iron in the roasted material, the zinc-indium-containing dust, the iron concentrate and the magnetic separation tailings needs to be respectively detected and analyzed by chemical elements, and the recovery rate is calculated.
The recovery rate of zinc is 83.2%, the recovery rate of indium is 77.3%, and the grade of iron ore concentrate is 62.8%.
Example 6
The contents of iron in the goethite slag in Guangdong province are 36.88% of iron, 12.08% of zinc and 0.02% of indium, and the main chemical detection results and the phase analysis results are shown in tables 1-3. Grinding 100g of the needle iron slag to the granularity of-200 meshes to-400 meshes according to the process flow shown in figure 1, mixing with 30g of potassium chlorate and 25g of carbon powder, pelletizing, wherein the pellet granularity is 10-20mm, placing the pellets into a tubular furnace for roasting, controlling the roasting temperature to be 1000 ℃ and the roasting time to be 3 hours. Collecting the volatilized zinc-indium-containing dust in the roasting process. And grinding the obtained material to the granularity of-200 meshes after roasting, and carrying out magnetic separation under the magnetic field intensity of 320mT to obtain an iron ore concentrate product. In the experimental process, chemical element detection and analysis are carried out on the contents of zinc, indium and iron in the roasted material, the zinc-indium-containing dust, the iron concentrate and the magnetic separation tailings respectively, and the recovery rate is calculated.
The recovery rate of zinc is 83.9%, the recovery rate of indium is 78.4%, and the grade of iron ore concentrate is 60.9%.
Example 7
The contents of iron in the goethite slag in Guangdong province are 36.88% of iron, 12.08% of zinc and 0.02% of indium, and the main chemical detection results and the phase analysis results are shown in tables 1-3. Grinding 100g of goethite slag to the granularity of-200 meshes to-400 meshes according to the process flow shown in figure 1, mixing with 35g of calcium hypochlorite and 20g of carbon powder, pelletizing, wherein the pellet granularity is 10-20mm, roasting in a tubular furnace, controlling the roasting temperature to be 1000 ℃, and roasting for 4 hours. Collecting the volatilized zinc-indium-containing dust in the roasting process. And grinding the obtained material to the granularity of-200 meshes after roasting, and carrying out magnetic separation under the magnetic field intensity of 340mT to obtain an iron ore concentrate product. In the experimental process, the content of zinc, indium and iron in the roasted material, the zinc-indium-containing dust, the iron concentrate and the magnetic separation tailings needs to be respectively detected and analyzed by chemical elements, and the recovery rate is calculated.
The calculation shows that the recovery rate of zinc is 84.9%, the recovery rate of indium is 76.8%, and the grade of iron ore concentrate is 61.8%.
Example 8
The contents of iron in the goethite slag in Guangdong province are 36.88% of iron, 12.08% of zinc and 0.02% of indium, and the main chemical detection results and the phase analysis results are shown in tables 1-3. Grinding 100g of goethite slag to the granularity of-200 meshes to-400 meshes according to the process flow shown in figure 1, mixing with 40g of sodium perchlorate and 15g of carbon powder, pelletizing, wherein the pellet granularity is 10-20mm, roasting in a tubular furnace, controlling the roasting temperature to be 1000 ℃, and roasting for 4 hours. Collecting the volatilized zinc-indium-containing dust in the roasting process. And grinding the obtained material after roasting until the granularity is-200 meshes, and carrying out magnetic separation under the magnetic field intensity of 350mT to obtain an iron ore concentrate product. In the experimental process, the content of zinc, indium and iron in the roasted material, the zinc-indium-containing dust, the iron concentrate and the magnetic separation tailings needs to be respectively detected and analyzed by chemical elements, and the recovery rate is calculated.
The recovery rate of zinc is 84.3%, the recovery rate of indium is 75.5%, and the grade of iron ore concentrate is 64.7%.
Example 9
The contents of iron in the goethite slag in Guangdong province are 36.88% of iron, 12.08% of zinc and 0.02% of indium, and the main chemical detection results and the phase analysis results are shown in tables 1-3. Grinding 100g of goethite slag to the granularity of-200 meshes to-400 meshes according to the process flow shown in figure 1, mixing with 30g of potassium perchlorate and 10g of carbon powder, pelletizing, wherein the pellet granularity is 10-20mm, roasting in a tubular furnace, controlling the roasting temperature at 1100 ℃ and the roasting time at 4h. Collecting the volatilized zinc-indium-containing dust in the roasting process. And grinding the obtained material to the granularity of-200 meshes after roasting, and carrying out magnetic separation under the condition that the magnetic field intensity is 200mT to obtain an iron ore concentrate product. In the experimental process, chemical element detection and analysis are carried out on the contents of zinc, indium and iron in the roasted material, the zinc-indium-containing dust, the iron concentrate and the magnetic separation tailings respectively, and the recovery rate is calculated.
According to calculation, the recovery rate of zinc is 87.1%, the recovery rate of indium is 78.2%, and the grade of iron ore concentrate is 65.2%.
Comparative example 1:
the contents of iron in the goethite slag in Guangdong province are 36.88% of iron, 12.08% of zinc and 0.02% of indium, and the main chemical detection results and the phase analysis results are shown in tables 1-3. 100g of the goethite slag is not mixed with chlorine-containing salt and carbon powder, the rest is ground to the granularity of-200 meshes to-400 meshes and pelletized according to the process flow shown in figure 1, the pellet granularity is 10-20mm, the pellets are placed into a tubular furnace for roasting, the roasting temperature is controlled to be 1000 ℃, and the roasting time is 4 hours. Collecting the volatilized zinc-indium-containing dust in the roasting process. And grinding the obtained roasted product to the granularity of-200 meshes after roasting is finished, and carrying out magnetic separation under the condition that the magnetic field intensity is 200mT to obtain an iron ore concentrate product. In the experimental process, the content of zinc, indium and iron in the roasted material, the zinc-indium-containing dust, the iron concentrate and the magnetic separation tailings needs to be respectively detected and analyzed by chemical elements, and the recovery rate is calculated.
The recovery rate of zinc is 20.88%, the recovery rate of indium is 21.2%, and the grade of iron ore concentrate is 45.3%.
In conclusion, the method for comprehensively recovering valuable metals from the goethite slag can efficiently recover zinc, indium and iron elements in the goethite slag, the recovery rate of zinc is more than 70%, the recovery rate of indium is more than 75%, the grade of iron ore concentrate is more than 60%, the utilization rate of resources is greatly improved, and a foundation is laid for solid waste resource utilization of the goethite slag. The method has the advantages of simple operation of the technological process, wide source of the required raw materials, low cost, easy operation of the experiment, low requirement on equipment, low energy consumption, environmental friendliness, great environmental benefit and economic benefit, and capability of meeting the requirement of the current green metallurgy on clean production.
The invention has not been described in detail and is part of the common general knowledge of a person skilled in the art.

Claims (1)

1. A method for comprehensively recovering valuable metals in goethite slag is characterized by comprising the following steps:
1) Grinding the goethite slag until the granularity is 200-400 meshes of sieve size, and mixing the goethite slag: a chlorine-containing salt: carbon powder =1:0.05 to 0.4: 0.1-0.5 weight ratio; uniformly mixing the ingredients and then pelletizing, wherein the diameter of the pellets is 10-20mm;
2) Roasting the pellets in the step 1) at 900-1100 ℃ for 2-4 h, collecting zinc-indium-containing dust generated in the volatilization process, and obtaining roasted calcine;
3) Cooling the roasted product obtained in the step 2) to room temperature, then grinding the roasted product to a granularity of-200 meshes, and carrying out magnetic separation under the condition that the magnetic field intensity is 200-300 mT to obtain an iron ore concentrate product;
wherein, the chlorine-containing salt in the step 1) is one or more of sodium chloride, calcium chloride, potassium chloride, calcium chlorate, sodium chlorate, potassium chlorate, calcium hypochlorite, sodium perchlorate and potassium perchlorate;
the ferrosilicon slag contains 20-60 wt% of iron, 6-15wt% of zinc and 0.01-0.5wt% of indium.
CN202010655002.XA 2020-07-09 2020-07-09 Method for comprehensively recovering valuable metals in goethite slag Active CN111979422B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202010655002.XA CN111979422B (en) 2020-07-09 2020-07-09 Method for comprehensively recovering valuable metals in goethite slag

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202010655002.XA CN111979422B (en) 2020-07-09 2020-07-09 Method for comprehensively recovering valuable metals in goethite slag

Publications (2)

Publication Number Publication Date
CN111979422A CN111979422A (en) 2020-11-24
CN111979422B true CN111979422B (en) 2022-10-21

Family

ID=73438527

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202010655002.XA Active CN111979422B (en) 2020-07-09 2020-07-09 Method for comprehensively recovering valuable metals in goethite slag

Country Status (1)

Country Link
CN (1) CN111979422B (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103194602A (en) * 2013-03-25 2013-07-10 中南大学 Method for removing iron and recovering iron-enriched iron scum in wet-method zinc smelting process
EP3587599A1 (en) * 2018-06-29 2020-01-01 Vito NV Process for recovering non-ferrous metals from industrial mineral residues

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB0900677D0 (en) * 2009-01-16 2009-02-25 Minex Technologies Ltd Metal recovery process
CN102134655A (en) * 2010-12-29 2011-07-27 昆明理工大学 Method for separating zinc and indium and iron from indium-enriched high-iron high-zinc calcine through reduction-magnetic separation
RU2568797C2 (en) * 2014-07-07 2015-11-20 Владимир Иванович Лунёв Fuel and metallurgical granules, and method of their production and metal coating
CN106929667A (en) * 2017-03-13 2017-07-07 江苏省冶金设计院有限公司 A kind of method for processing zinc leaching residue
CN107201442A (en) * 2017-06-06 2017-09-26 江苏省冶金设计院有限公司 A kind of system and method for handling zinc leaching residue
CN107419107A (en) * 2017-08-17 2017-12-01 江苏省冶金设计院有限公司 A kind of method and system for handling zinc leaching residue
CN109266841B (en) * 2018-11-27 2020-05-05 广东工业大学 Roasting treatment method of iron tailings

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103194602A (en) * 2013-03-25 2013-07-10 中南大学 Method for removing iron and recovering iron-enriched iron scum in wet-method zinc smelting process
EP3587599A1 (en) * 2018-06-29 2020-01-01 Vito NV Process for recovering non-ferrous metals from industrial mineral residues

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
Microwave assisted alkaline roasting-water leaching for the valorisation of goethite sludge from zinc refining process;ThomasAbo Atia 等;《Hydrometallurgy》;20200131;1-9 *
浸锌渣综合利用现状及发展趋势;王福生等;《天津化工》;20100530(第03期);5-7 *

Also Published As

Publication number Publication date
CN111979422A (en) 2020-11-24

Similar Documents

Publication Publication Date Title
CN110564970A (en) Process method for recovering potassium, sodium and zinc from blast furnace cloth bag ash
CN109266841B (en) Roasting treatment method of iron tailings
CN108315559B (en) A kind of method of steel plant's Zinc-Bearing Wastes separation of Zinc
Gang et al. Selective reduction process of zinc ferrite and its application in treatment of zinc leaching residues
CN102242253A (en) Method for treating poor-tin middling ore and recovering iron-making raw material
Wang et al. Characteristics of the reduction behavior of zinc ferrite and ammonia leaching after roasting
CN106048251A (en) Technological method for cleaning and efficiently treating arsenic matte
CN102220479A (en) Beneficiation method for comprehensive recovery of valuable metals from sulfuric acid residues through chlorination and segregation
CN111088433A (en) Method for enriching and recovering thallium from lead smelting system
CN104152671B (en) A kind of method of being prepared ironmaking iron ore concentrate by Iron Ore Containing Tin
CN113862464B (en) Method for recovering copper and scattered metal in black copper sludge
CN111154975A (en) Method for treating arsenic-antimony-containing gold-carrying material
CN111996364B (en) Method for recovering gold from cyanidation tailings and synchronously magnetizing iron
CN111979422B (en) Method for comprehensively recovering valuable metals in goethite slag
CN115433840B (en) Method for separating and recovering tungsten and tin in fine-fraction black-white tungsten-tin bulk concentrate
CN111593205A (en) Method for recovering cobalt from cobalt-containing sulfuric acid residue
CN108950195B (en) Method for extracting valuable metals from zinc concentrate oxidizing slag by using chlorine-containing wastewater
CN112813277B (en) Method for separating and recovering valuable metals from copper smelting slag through chlorination roasting
CN111440908B (en) Method for converting titanium component in titanium-containing blast furnace slag into ilmenite
CN110564969B (en) Method for comprehensively recovering lead, zinc and iron in blast furnace gas ash
CN111485101B (en) Method for recovering iron from iron-containing ore
CN111575500A (en) Method for treating zinc-containing dangerous solid waste and zinc ore by combining chlorination roasting with ammonia process electrodeposition
CN114480859A (en) Method for cooperatively utilizing all components of red mud and iron ore sintering dedusting ash
CN107419107A (en) A kind of method and system for handling zinc leaching residue
CN102912124A (en) Method for recovering nickel, cobalt, manganese and iron by hydrochloric acid leaching of nickel oxide ore

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant