WO2017107662A1 - Continuous metallurgical device and method - Google Patents

Continuous metallurgical device and method Download PDF

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Publication number
WO2017107662A1
WO2017107662A1 PCT/CN2016/103860 CN2016103860W WO2017107662A1 WO 2017107662 A1 WO2017107662 A1 WO 2017107662A1 CN 2016103860 W CN2016103860 W CN 2016103860W WO 2017107662 A1 WO2017107662 A1 WO 2017107662A1
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smelting
smelting chamber
chamber
gate
metallurgical
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PCT/CN2016/103860
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French (fr)
Chinese (zh)
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邱江波
夏明�
黄小兵
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天津闪速炼铁技术有限公司
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Publication of WO2017107662A1 publication Critical patent/WO2017107662A1/en

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    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B11/00Making pig-iron other than in blast furnaces
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B5/00General methods of reducing to metals
    • C22B5/02Dry methods smelting of sulfides or formation of mattes

Definitions

  • the invention belongs to the field of metallurgy, and particularly relates to a metallurgical device and a metallurgical method with a continuous structure, which can meet the requirements of pyrometallurgical smelting and refining of most metal minerals or secondary materials, and metal which needs to undergo multi-stage (secondary) smelting. Particularly effective.
  • the traditional metal smelting process often requires more than two smelting processes.
  • the steelmaking process generally requires blast furnace smelting, pretreatment, blowing, and refining processes, and each process is relatively dispersed.
  • a transporter such as a tanker or a crane.
  • This traditional dispersive metallurgical process and transport process has the following disadvantages: (1) multiple transfer processes cause the heat of the transferred melt to be dissipated in vain, and the energy consumption is very large; (2) the transport process requires special transportation tools and Manpower and material resources, low production efficiency and high cost; (3) The transportation process will cause gas and dust pollution, which is not conducive to environmental protection and human health. (4) The transshipment process cannot completely prevent the occurrence of a safety accident.
  • the invention provides a continuous metallurgical device and a metallurgical method for solving the problems in the prior art, which can break the relatively dispersed production process of the traditional metal smelting, realize the continuous production of metal smelting, has small land occupation, small investment, and can Low cost and low pollution.
  • the invention provides a continuous metallurgical device comprising a plurality of smelting chambers connected in series, and adjacent gate chambers are vertically arranged by a gate interval, the gates being movable in a vertical direction so as to be located on both sides thereof
  • the adjacent smelting chambers are completely separated or partially separated; for each of the smelting chambers, the lower part is a molten pool, the molten pool is provided with at least one slag discharging port communicating with the outside, and the upper part is provided with at least one block material feeding port And a flue; the first smelting chamber is also connected with a material main inlet having a falling space, and the last smelting chamber is also connected with a product outlet.
  • the number of the smelting chambers is preferably 3-5.
  • any adjacent smelting chambers are connected in parallel or stepwise, preferably in a stepped connection.
  • the smelting chamber located in front of the adjacent smelting chamber The height position of the melt layer in the molten pool partially coincides with the height position of the slag layer in the molten pool located in the subsequent smelting chamber.
  • each of the smelting chambers is independently provided with one or more of a auxiliary feeding port, a heating device, a bottom blowing nozzle, a side blowing nozzle, and a nozzle.
  • the auxiliary feeding port may be located at the middle top end of the smelting chamber where the smelting chamber is located;
  • the heating device may be an electromagnetic induction heating coil surrounding the side wall or the bottom of the smelting chamber where the smelting chamber is located or at the middle of the smelting chamber where the smelting chamber is located a heating electrode;
  • the bottom blowing nozzle is a nozzle disposed at the bottom of the smelting chamber where the smelting nozzle is located, and the side blowing nozzle is a plurality of nozzles distributed in parallel along the molten pool of the smelting chamber where the smelting chamber is located, the bottom blowing
  • the nozzle, the side blowing nozzle, and the nozzle are all capable of inputting materials or gases into the smelting chamber.
  • the gate can make the smelting chamber in a completely independent smelting process state when completely shut down according to the needs of smelting; or be in a semi-open state during the smelting process, and function as a partition wall in a part of the continuous smelting process; After the smelting of a certain process or smelting room is completed, the smelting raw materials directly enter the next smelting room or smelting process.
  • the main inlet of the first smelting chamber material is mainly used for the addition of powder or liquid or gaseous materials such as powder and fuel, and the input material is generally the basic raw material for the reaction, and the main inlet of the material is generally located in the first smelting chamber.
  • the block material feeding port is mainly used for adding bulk materials, generally materials that are difficult to be crushed, or materials that need to be added in each process, and thus are set in each smelting room, generally located in each smelting room.
  • the upper front side is close to the front gate.
  • the flue is used for the discharge of exhaust gas in each smelting process, and is generally located at the upper rear end of each smelting chamber, near the position of the rear gate.
  • the invention creates a continuous metallurgical device.
  • a brief smelting process is: smelting of ore powder (if powdering) and fuel (powder, liquid, gas), gas (such as air, oxygen, pure oxygen or other gases), The flux, etc., is sprayed into the first smelting chamber from the main inlet of the material, and the high-temperature metallurgical environment passing through the falling space is characterized by small particle size, large specific surface area, large contact area with gas in the space at high temperature, and fast reaction speed.
  • the material is first metallurgically; other materials that cannot be made into powder are added to the furnace from the bulk material feeding port of the first smelting chamber (the first feeding may be powder or block).
  • the material falls into the molten pool of the first smelting chamber, it continues to add the ingredients required for smelting at this stage through the bottom blowing nozzle, the side blowing nozzle, the nozzle, or the bulk material feeding port, for example: pulverized coal, oxygen, hot air , powder ore, flux, scrap metal, additives, blocks, etc.;
  • the flue gas is discharged from the flue of the first smelting chamber, and the slag is discharged from the slag discharge port.
  • an electrode can be added to the top of the bath, or a ring furnace body or electromagnetic induction heating at the bottom of the furnace can be selected.
  • the gate between the first smelting chamber and the second smelting chamber is closed or semi-opened (such as the slag layer or the melt layer of the first smelting chamber at the bottom end of the gate).
  • the slag is discharged from the slag discharge port, half the gate between the first smelting chamber and the second smelting chamber is opened, the gate between the second smelting chamber and the third smelting chamber is closed, and the purity is improved by the first smelting.
  • the latter melt flows into the second smelting chamber molten pool through the bottom of the gate, and the bottom blowing nozzle, the side blowing nozzle, the nozzle, or the block material feeding port of the second smelting chamber are added to the ingredients required for the smelting at this stage.
  • the flue gas is discharged from the flue of the second smelting chamber, and the slag is discharged from the slag discharge port.
  • the smelting is continued in the subsequent smelting chamber for smelting, and will not be described in detail here.
  • different raw materials or auxiliary materials are added through the bottom blowing nozzle, the side blowing nozzle, the nozzle, or the block material feeding port, which can provide different metallurgical environments, and the metal is purified step by step in a continuously closed container. Until the expected metal product is obtained.
  • a specific continuous metallurgical process created by the present invention includes the following steps:
  • S1 smelting of the first smelting chamber: closing the first smelting chamber gate, forming the first smelting chamber to form an independent metallurgical unit, and adding raw materials from the main inlet of the material having the falling space in the first smelting chamber, the raw materials are
  • the first smelting room first undergoes space smelting, and then falls into the molten pool for smelting. In the smelting process, according to actual needs, it can pass through the block material feeding port, auxiliary feeding port, heating device, bottom blowing nozzle, and side blowing.
  • nozzles and nozzles add the auxiliary materials, heat and atmosphere necessary for smelting in a time-division manner to form a good metallurgical environment. After the material is slag in the molten pool and clarified and layered, a slag layer and a metal-rich layer are formed. Melt layer. The smelting flue gas is discharged from the flue of the first smelting chamber, and the slag is discharged from the slag discharging port of the first smelting chamber.
  • the beneficial effects created by the invention are as follows: (1) The structure and feeding mode created by the invention can meet the requirements of pyrometallurgical smelting and refining of most metal minerals or secondary materials, and for metals that need to undergo multi-stage (secondary) smelting, It is particularly effective; (2) The discrete processes in the traditional metallurgical process are connected into a whole, and the self-flow can be carried out by the gravity of the melt in the continuous connection state, avoiding energy dissipation, inefficiency and environmental pollution caused by the transfer process. (3) can fully utilize the heat of the first metallurgy, the whole process of metallurgy is sealed, the unorganized emission of gas and dust is close to zero, and the expected finished metal products can be directly obtained.
  • Figure 1 is a schematic view showing the construction of an embodiment of the present invention.
  • Iron fine powder, oxygen, pulverized coal, and flux are sprayed from the main inlet FQR into the smelting chamber T 1 , and coke is added from the bulk material feeding port K 1 , and the iron fine powder floats in a hot state with a large specific surface area.
  • the reduced ferrous oxide is completely reduced.
  • the gate G 1 is kept closed. After the slag iron is separated, the slag is discharged from the slag discharge port R 1 and the flue gas enters the flue Y 1 .
  • the gate G 3 is closed, the gate G 2 is half-opened, the molten iron flows into the molten pool Z 3 from the lower portion of the gate G 2 , and oxygen or iron concentrate is sprayed from the side blowing nozzle into the molten pool, and at the same time
  • the material feeding port K 3 is successively added with slag-forming materials such as lime and dolomite.
  • the iron concentrate, iron oxide scale and the like may be added from the bulk material feeding port K 3 while being blown. Or coolant.
  • the main purpose of this blowing process is to decarbonize while continuing to remove sulfur and phosphorus from the molten iron.
  • the flue gas enters the flue Y 3 and the slag is discharged from the slag discharge port R 3 .
  • G 3 After completion of the blowing and slag discharge is half open shutter G 3, G 3 a lower portion of the molten steel flows through the bath shutter Z 4, D 4 from the bottom-blowing lance for blowing the bath with stirring to argon, it is provided with a set of at F 4
  • the graphite electrode heats the molten pool, and in the process, a slag forming agent such as lime and fluorite is added through the bulk material feeding port K 4 .
  • a slag forming agent such as lime and fluorite is added through the bulk material feeding port K 4 .
  • the flue gas enters the flue Y 4 , and the molten slag is discharged from the slag discharge port R 4 , and the molten steel flows from the product outlet OUT into the tundish of the continuous casting workshop.
  • the above-mentioned continuous steelmaking process is more energy-saving and environmentally friendly and saves investment than the traditional dispersed "blast furnace-furnace pretreatment-converter blowing-LF refining" steel smelting process.
  • the copper concentrate ore, quartz flux and oxygen-enriched air are sprayed from the material main inlet FQR into the furnace chamber of the first smelting chamber of the continuous furnace, and the sulphide concentrate particles are in the oxidative turbulent airflow.
  • the oxidation reaction occurs rapidly, and a large amount of heat is released.
  • the particles suspended in the furnace cavity are melted, and then fall into the molten pool Z 1 to continue the copper-making sulfur (copper copper) and slagging reaction.
  • the middle gate G 1 remains closed.
  • the slag is discharged from the slag discharge port R 1 , and the SO 2 -rich flue gas enters the flue Y 1 .
  • the gate G 2 is closed, the gate G 1 is half-opened, copper and sulfur enter the molten pool Z 2 from the bottom of the gate G 1 , and air having a certain pressure is sent from the side blowing nozzle C 2 into the melting.
  • FeS is oxidized to FeO
  • Cu 2 S is oxidized and then reacted with Cu 2 S to become blister copper.
  • the blowing temperature can be maintained by the sulfide oxidation reaction, and the block is in the process.
  • a slagging agent such as quartz added to the material feed port K 2 .
  • the blown slag is discharged from the slag discharge port R 2 and the flue gas is blown into the flue Y2.
  • the bulk material feeding port K 3 adds flux such as quartz sand, lime or soda to the furnace, and utilizes the characteristics that most impurities have higher affinity with oxygen than copper, and the impurity oxide has a small solubility in copper, so that sulfur, iron, lead, Impurities such as zinc, nickel, arsenic, antimony, tin and antimony are oxidized to form slag, and the slag is discharged from the slag discharge port R 3 , and the flue gas enters the flue Y 3 .
  • the gate G 3 is half-opened, and the blister copper flows from the bottom of the gate G 3 into the molten pool Z 4 for reduction refining, and the heavy oil is atomized by steam or air from the side blowing nozzle C 4 into the copper liquid.
  • the charcoal powder or coke is added from the bulk material feeding port K 4 to cover the copper liquid surface, and the reducing agent such as heavy oil is thermally cracked into components such as H 2 , CO, C, etc., so that Cu 2 O is reduced to Cu.
  • the flue gas enters the flue Y 4 , and the refined copper melt is discharged from the molten pool Z 4 and can be electroplated or cast ingot.
  • the above continuous copper smelting process is more energy-saving and environmentally friendly and saves investment than the traditional dispersed "flash furnace-PS converter blowing-oxidizing refining-reduction refining" copper smelting process.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
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  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
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Abstract

A continuous metallurgical device and method. The continuous metallurgical device comprises a plurality of sequentially-connected metallurgical chambers (Tx). Every two adjacent metallurgical chambers (Tx) are separated by a vertically-disposed gate (Gx), and the gate (Gx) can move in a vertical direction, so that the adjacent metallurgical chambers (Tx) on two sides of the gate (Gx) are fully or partially separated. For each metallurgical chamber (Tx), the lower part of the metallurgical chamber (Tx) is a melting pool (Zx), at least one slag discharge opening (Rx) communicated with the outside is formed in the melting pool (Zx), and the upper part of the metallurgical chamber (Tx) is provided with at least one block material feeding opening (Kx) and a flue (Yx); and a material main inlet (FQR) provided with a falling space is further connected to the first metallurgical chamber (Tx), and a product outlet (OUT) is also connected to a last metallurgical chamber (Tx).

Description

一种连续冶金装置和冶金方法Continuous metallurgical device and metallurgical method 技术领域Technical field
本发明创造属于冶金领域,具体涉及一种具有连续结构的冶金装置和冶金方法,可以满足大部分金属矿物或二次原料的火法冶炼和精炼要求,对需要经过多级(次)冶炼的金属特别有效。The invention belongs to the field of metallurgy, and particularly relates to a metallurgical device and a metallurgical method with a continuous structure, which can meet the requirements of pyrometallurgical smelting and refining of most metal minerals or secondary materials, and metal which needs to undergo multi-stage (secondary) smelting. Particularly effective.
背景技术Background technique
传统的金属冶炼过程往往需要2个以上的冶炼工序,如炼钢过程一般需要高炉冶炼、预处理、吹炼以及精炼等工序,每一工序都相对分散。目前的冶金工艺中,在每一工序完成后,需要利用罐车、天车等运输工具将原料转运至下一工序。这种传统的分散冶金工序和转运过程具有如下弊端:(1)多次转运过程使得被转运的熔体热量被白白耗散,能耗十分巨大;(2)转运过程需要配备专门的运输工具以及人力、物力,生产效率低下、成本较大;(3)转运过程会造成气体和粉尘污染,不利于环境保护和人体健康。(4)转运过程无法彻底杜绝安全事故的发生。The traditional metal smelting process often requires more than two smelting processes. For example, the steelmaking process generally requires blast furnace smelting, pretreatment, blowing, and refining processes, and each process is relatively dispersed. In the current metallurgical process, after each process is completed, it is necessary to transport the raw materials to the next process by using a transporter such as a tanker or a crane. This traditional dispersive metallurgical process and transport process has the following disadvantages: (1) multiple transfer processes cause the heat of the transferred melt to be dissipated in vain, and the energy consumption is very large; (2) the transport process requires special transportation tools and Manpower and material resources, low production efficiency and high cost; (3) The transportation process will cause gas and dust pollution, which is not conducive to environmental protection and human health. (4) The transshipment process cannot completely prevent the occurrence of a safety accident.
发明内容Summary of the invention
本发明创造为解决现有技术中的问题,提供了一种连续冶金装置和冶金方法,能够打破传统金属冶炼相对分散的生产工序,实现金属冶炼的连续生产,具有占地少、投资小、能耗低、污染小等优势。The invention provides a continuous metallurgical device and a metallurgical method for solving the problems in the prior art, which can break the relatively dispersed production process of the traditional metal smelting, realize the continuous production of metal smelting, has small land occupation, small investment, and can Low cost and low pollution.
本发明创造提供的一种连续冶金装置,包括顺序连接的若干冶炼室,相邻冶炼室之间通过竖直设置的闸门间隔,所述闸门能够在竖直方向运动,从而实现将位于其两侧的相邻冶炼室进行完全间隔或部分间隔;对于每一所述冶炼室,下部为熔池,熔池中设有至少一个与外界连通的排渣口,上部设有至少一个块状物料投料口以及一个烟道;第一冶炼室上还连接有具有下落空间的物料主入口,最后一个冶炼室上还连接有产品出口。其中,所述冶炼室的数量优选为3-5个。The invention provides a continuous metallurgical device comprising a plurality of smelting chambers connected in series, and adjacent gate chambers are vertically arranged by a gate interval, the gates being movable in a vertical direction so as to be located on both sides thereof The adjacent smelting chambers are completely separated or partially separated; for each of the smelting chambers, the lower part is a molten pool, the molten pool is provided with at least one slag discharging port communicating with the outside, and the upper part is provided with at least one block material feeding port And a flue; the first smelting chamber is also connected with a material main inlet having a falling space, and the last smelting chamber is also connected with a product outlet. Among them, the number of the smelting chambers is preferably 3-5.
进一步,任意相邻冶炼室之间呈平行连接或阶梯连接,优选为阶梯连接。作为进一步的优选方案,在所述阶梯连接中,相邻冶炼室中位于前面的所述冶炼室 的熔池中熔体层的高度位置与位于后面的所述冶炼室的熔池中渣层的高度位置部分重合。Further, any adjacent smelting chambers are connected in parallel or stepwise, preferably in a stepped connection. As a further preferred solution, in the step connection, the smelting chamber located in front of the adjacent smelting chamber The height position of the melt layer in the molten pool partially coincides with the height position of the slag layer in the molten pool located in the subsequent smelting chamber.
进一步,所述冶炼室中各自还独立地设有辅加料口、加热装置、底吹喷管、侧吹喷管、喷嘴中的一种或多种。Further, each of the smelting chambers is independently provided with one or more of a auxiliary feeding port, a heating device, a bottom blowing nozzle, a side blowing nozzle, and a nozzle.
其中,所述辅加料口可位于其所在的冶炼室的中部顶端;所述加热装置可为环绕其所在的冶炼室的侧壁或底部的电磁感应加热线圈或位于其所在的冶炼室的中部顶端的加热电极;所述底吹喷管为设置于其所在的冶炼室底部的喷管,所述侧吹喷管为沿其所在的冶炼室的熔池平行分布的若干喷管,所述底吹喷管、侧吹喷管、喷嘴均能够向冶炼室中输入物料或气体。Wherein, the auxiliary feeding port may be located at the middle top end of the smelting chamber where the smelting chamber is located; the heating device may be an electromagnetic induction heating coil surrounding the side wall or the bottom of the smelting chamber where the smelting chamber is located or at the middle of the smelting chamber where the smelting chamber is located a heating electrode; the bottom blowing nozzle is a nozzle disposed at the bottom of the smelting chamber where the smelting nozzle is located, and the side blowing nozzle is a plurality of nozzles distributed in parallel along the molten pool of the smelting chamber where the smelting chamber is located, the bottom blowing The nozzle, the side blowing nozzle, and the nozzle are all capable of inputting materials or gases into the smelting chamber.
其中,所述熔池用于冶金材料的熔炼。所述闸门能够根据冶炼的需要,在完全关闭时使冶炼室处于完全独立的冶炼工序状态;或在冶炼过程中处于半开启状态,在部分连续的冶炼工序中充当隔墙的作用;又或者在某一工序或冶炼室的冶炼完成后开启,使冶炼原料直接进入下一冶炼室或冶炼工序。所述第一冶炼室物料主入口主要用于粉料、燃料等粉状或液态或气态物料的加入,投入的物料一般为反应的基础原料,所述物料主入口一般位于第一冶炼室的最前方。所述块状物料投料口主要用于块状物料的加入,一般为难以进行破碎处理的物料,或各个工序中需要辅助加入的物料,因而在各个冶炼室均有设置,一般位于各个冶炼室的前方上端,靠近前方闸门的位置。所述烟道用于各个冶炼工序中废气的排放,一般位于各个冶炼室的后方上端,靠近后方闸门的位置。Wherein the molten pool is used for the melting of metallurgical materials. The gate can make the smelting chamber in a completely independent smelting process state when completely shut down according to the needs of smelting; or be in a semi-open state during the smelting process, and function as a partition wall in a part of the continuous smelting process; After the smelting of a certain process or smelting room is completed, the smelting raw materials directly enter the next smelting room or smelting process. The main inlet of the first smelting chamber material is mainly used for the addition of powder or liquid or gaseous materials such as powder and fuel, and the input material is generally the basic raw material for the reaction, and the main inlet of the material is generally located in the first smelting chamber. In front. The block material feeding port is mainly used for adding bulk materials, generally materials that are difficult to be crushed, or materials that need to be added in each process, and thus are set in each smelting room, generally located in each smelting room. The upper front side is close to the front gate. The flue is used for the discharge of exhaust gas in each smelting process, and is generally located at the upper rear end of each smelting chamber, near the position of the rear gate.
需要说明的是,本发明创造中所述的“前”“后”“第一”“第二”等均是根据冶金装置在冶炼过程中的冶炼的走向方向而描述的。It should be noted that the “front”, “post”, “first”, “second” and the like described in the creation of the present invention are described in terms of the direction of smelting of the metallurgical apparatus during the smelting process.
本发明创造连续冶金装置一种简要的冶炼过程为:需要冶炼的矿粉(如果能制粉)与燃料(粉、液、气)、气体(如空气、富氧、纯氧或其他气体)、熔剂等,从物料主入口处喷入第一冶炼室内,利用粉料粒径小、比表面积大、在高温下与空间中气体接触面积大、反应速度快的特点,通过下落空间的高温冶金环境对物料进行首次冶金;不能制成粉料的其他物料从第一冶炼室的块状物料投料口处加入炉内(首次投料可以是粉料,也可以是块料)。物料在落入第一冶炼室的熔池后,继续通过底吹喷管、侧吹喷管、喷嘴、或块状物料投料口加入此阶段冶炼所需要的配料,例如:粉煤、氧气、热风、粉矿、熔剂、废金属、添加剂、块料等; 烟气从第一冶炼室的烟道排出,熔渣从排渣口排出。可以选择性在熔池顶部加入电极、或选择环炉身或位于炉底的电磁感应加热。冶炼过程中,根据冶炼需要关闭、或半开启(如使闸门底端位于第一冶炼室的渣层或熔体层)第一冶炼室和第二冶炼室之间的闸门。The invention creates a continuous metallurgical device. A brief smelting process is: smelting of ore powder (if powdering) and fuel (powder, liquid, gas), gas (such as air, oxygen, pure oxygen or other gases), The flux, etc., is sprayed into the first smelting chamber from the main inlet of the material, and the high-temperature metallurgical environment passing through the falling space is characterized by small particle size, large specific surface area, large contact area with gas in the space at high temperature, and fast reaction speed. The material is first metallurgically; other materials that cannot be made into powder are added to the furnace from the bulk material feeding port of the first smelting chamber (the first feeding may be powder or block). After the material falls into the molten pool of the first smelting chamber, it continues to add the ingredients required for smelting at this stage through the bottom blowing nozzle, the side blowing nozzle, the nozzle, or the bulk material feeding port, for example: pulverized coal, oxygen, hot air , powder ore, flux, scrap metal, additives, blocks, etc.; The flue gas is discharged from the flue of the first smelting chamber, and the slag is discharged from the slag discharge port. Optionally, an electrode can be added to the top of the bath, or a ring furnace body or electromagnetic induction heating at the bottom of the furnace can be selected. In the smelting process, according to the smelting needs, the gate between the first smelting chamber and the second smelting chamber is closed or semi-opened (such as the slag layer or the melt layer of the first smelting chamber at the bottom end of the gate).
冶炼完毕后,熔渣从排渣口排出,半开启第一冶炼室和第二冶炼室之间的闸门,关闭第二冶炼室和第三个冶炼室之间的闸门,经第一冶炼提高纯度后的熔体经闸门底部流入第二冶炼室熔池,第二冶炼室的底吹喷管、侧吹喷管、喷嘴、或块状物料投料口加入此阶段冶炼所需要的配料。烟气从第二冶炼室的烟道排出,熔渣从排渣口排出。After the smelting is completed, the slag is discharged from the slag discharge port, half the gate between the first smelting chamber and the second smelting chamber is opened, the gate between the second smelting chamber and the third smelting chamber is closed, and the purity is improved by the first smelting. The latter melt flows into the second smelting chamber molten pool through the bottom of the gate, and the bottom blowing nozzle, the side blowing nozzle, the nozzle, or the block material feeding port of the second smelting chamber are added to the ingredients required for the smelting at this stage. The flue gas is discharged from the flue of the second smelting chamber, and the slag is discharged from the slag discharge port.
冶炼完毕后,继续顺序进入后面的冶炼室进行冶炼,在此不再详述。每一个冶炼室,通过底吹喷管、侧吹喷管、喷嘴、或块状物料投料口加入不同的原料或辅料,可以提供不同的冶金环境,使金属在连续密闭的容器中逐级提纯,直至得到预期的金属产品。After the smelting is completed, the smelting is continued in the subsequent smelting chamber for smelting, and will not be described in detail here. In each smelting chamber, different raw materials or auxiliary materials are added through the bottom blowing nozzle, the side blowing nozzle, the nozzle, or the block material feeding port, which can provide different metallurgical environments, and the metal is purified step by step in a continuously closed container. Until the expected metal product is obtained.
本发明创造的一种具体的连续冶金方法包括下述步骤:A specific continuous metallurgical process created by the present invention includes the following steps:
S1:第一冶炼室冶炼:关闭所述第一冶炼室闸门,使所述第一冶炼室形成一个独立的冶金单元,从所述第一冶炼室具有下落空间的物料主入口加入原料,原料在第一冶炼室先经过空间冶炼,再落入熔池进行熔池冶炼,在冶炼过程中,根据实际需要,可通过块状物料投料口、辅加料口、加热装置、底吹喷管、侧吹喷管、喷嘴中的一种或多种方式分时段添加冶炼所必需的辅料、热量和气氛,形成良好的冶金环境,物料在熔池造渣并澄清分层后,形成渣层和富含金属熔体层。冶炼烟气从所述第一冶炼室烟道排出,渣从所述第一冶炼室排渣口排出。S1: smelting of the first smelting chamber: closing the first smelting chamber gate, forming the first smelting chamber to form an independent metallurgical unit, and adding raw materials from the main inlet of the material having the falling space in the first smelting chamber, the raw materials are The first smelting room first undergoes space smelting, and then falls into the molten pool for smelting. In the smelting process, according to actual needs, it can pass through the block material feeding port, auxiliary feeding port, heating device, bottom blowing nozzle, and side blowing. One or more ways of nozzles and nozzles add the auxiliary materials, heat and atmosphere necessary for smelting in a time-division manner to form a good metallurgical environment. After the material is slag in the molten pool and clarified and layered, a slag layer and a metal-rich layer are formed. Melt layer. The smelting flue gas is discharged from the flue of the first smelting chamber, and the slag is discharged from the slag discharging port of the first smelting chamber.
S2:第一冶炼室富含金属的熔体排放:原料在所述第一冶炼室冶炼完毕后,先关闭所述第二冶炼室闸门,然后提升所述第一冶炼室闸门,使其末端置于富含金属的熔体层中,让尽可能多的富含金属的熔体自流进入第二冶炼室,同时又保证所述第一冶炼室中的烟气和渣不会进入第二冶炼室,为达到上述目的,在排放过程中,可多次移动所述第一冶炼室闸门末端在富含金属熔体层的位置。富含金属的熔体排放完毕后,关闭所述第一冶炼室闸门。S2: melt-emission of metal rich in the first smelting chamber: after the smelting of the raw material in the first smelting chamber is completed, the gate of the second smelting chamber is closed, and then the gate of the first smelting chamber is lifted to be terminated In the metal-rich melt layer, as many metal-rich melts as possible flow into the second smelting chamber while ensuring that the flue gas and slag in the first smelting chamber do not enter the second smelting chamber In order to achieve the above purpose, in the discharging process, the end of the first smelting chamber gate may be moved at a position rich in the metal melt layer. After the metal-rich melt is discharged, the first smelting chamber gate is closed.
S3:第二冶炼室冶炼:在富含金属的熔体进入所述第二冶炼室,随后关闭第 一冶炼室闸门,此时第一冶炼室闸门、第二冶炼室炉壁及闭合的第二冶炼室闸门形成了一个独立的冶金单元,根据冶炼的实际需要,通过块状物料投料口、辅加料口、加热装置、底吹喷管、侧吹喷管、喷嘴中的一种或多种方式分时段添加冶炼所必需的辅料、热量和气氛,形成良好的冶金环境,以除去富含金属熔体中的部分杂质,精炼形成的渣从所述第二冶炼室排渣口排出,冶炼烟气从所述第二冶炼室烟道排出。S3: smelting in the second smelting chamber: entering the second smelting chamber in the metal-rich melt, and then closing the first A smelting chamber gate, at this time, the first smelting chamber gate, the second smelting chamber wall and the closed second smelting chamber gate form an independent metallurgical unit. According to the actual needs of smelting, through the block material feeding port and auxiliary feeding One or more of the mouth, heating device, bottom blowing nozzle, side blowing nozzle, and nozzle to add the necessary excipients, heat and atmosphere for the smelting to form a good metallurgical environment to remove the metal-rich melt. A part of the impurities, the slag formed by the refining is discharged from the slag discharge port of the second smelting chamber, and the smelting flue gas is discharged from the flue of the second smelting chamber.
S4:反复采用同步骤S2的熔体排放过程以及同步骤S3的冶炼步骤,使富含金属的熔体依次在后续冶炼室完成冶炼,直至在最后一个冶炼室完成冶炼(或精炼)。S4: repeatedly using the melt discharge process of the same step S2 and the smelting step of the same step S3, the metal-rich melt is sequentially smelted in the subsequent smelting chamber until the smelting (or refining) is completed in the last smelting chamber.
S5:产品的排放:在最后一个冶炼室完成冶炼的金属熔体从所述产品出口排出炉外。S5: Emission of the product: The molten metal that has been smelted in the last smelting chamber is discharged from the outlet of the product.
本发明创造的有益效果是:(1)本发明创造的结构和加料方式,可以满足大部分金属矿物或二次原料的火法冶炼和精炼要求,对需要经过多级(次)冶炼的金属,特别有效;(2)原来传统冶金工艺中离散的各个工序衔接成一个整体,连续连接状态下能够利用熔体自身重力进行自流,避免了因转运过程而造成的能量耗散、效率低下以及环境污染等问题;(3)能充分利用首次冶金的热量,冶金全过程密闭,气体和粉尘的无组织排放接近于零,能够直接获得预期的金属产品成品。The beneficial effects created by the invention are as follows: (1) The structure and feeding mode created by the invention can meet the requirements of pyrometallurgical smelting and refining of most metal minerals or secondary materials, and for metals that need to undergo multi-stage (secondary) smelting, It is particularly effective; (2) The discrete processes in the traditional metallurgical process are connected into a whole, and the self-flow can be carried out by the gravity of the melt in the continuous connection state, avoiding energy dissipation, inefficiency and environmental pollution caused by the transfer process. (3) can fully utilize the heat of the first metallurgy, the whole process of metallurgy is sealed, the unorganized emission of gas and dust is close to zero, and the expected finished metal products can be directly obtained.
附图说明DRAWINGS
图1是本发明创造一种实施方式的结构示意图。BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 is a schematic view showing the construction of an embodiment of the present invention.
图中,Tx-冶炼室;Ax-渣层;Bx-熔体层;Zx-熔池;Kx-块状物料投料口;Gx-闸门;Rx-排渣口;Yx-烟道;Fx-辅加料口、加热装置中的任一种;Dx-底吹喷管;Cx-侧吹喷管;FQR-物料主入口;OUT-产品出口;其中,下标x=1、2、……、N,分别表示顺序连接的冶炼室的顺序位置,如x=2时表示为第二冶炼室或其中的某个结构,特别地,对于闸门Gx的描述,则表示的是第x个冶炼室与第x+1个冶炼室之间的闸门。 In the figure, Tx-smelting chamber; Ax-slag layer; Bx-melt layer; Zx-melting pool; Kx-block material feeding port; Gx-gate; Rx-slag discharge port; Yx-flue; Fx-auxiliary Any one of a feeding port and a heating device; a Dx-bottom blowing nozzle; a Cx-side blowing nozzle; a FQR-material main inlet; an OUT-product outlet; wherein the subscript x=1, 2, ..., N , respectively, indicating the sequential positions of the sequentially connected smelting chambers, such as x=2, expressed as a second smelting chamber or a structure thereof, and in particular, for the description of the gate Gx, the xth smelting chamber and the A gate between x+1 smelting chambers.
具体实施方式detailed description
下面通过结合附图对本发明创造进行进一步说明。下面的实施例中描述的具体方案仅是为了说明本发明创造的内容,并不用于对本发明创造的限定。The invention will be further explained below by reference to the accompanying drawings. The specific embodiments described in the following examples are merely illustrative of the invention and are not intended to limit the invention.
实施例1连续炼钢Example 1 continuous steelmaking
铁精粉、氧气、粉煤、熔剂从物料主入口FQR处喷入冶炼室T1,焦炭从块状物料投料口K1加入,铁精粉以极大的比表面积状态弥撒漂浮于炽热且呈CO还原气分的连续炉第一冶炼室空间,迅速传热、传质,完成铁精矿的空间冶炼过程;经空间冶炼后,铁精粉中的高价铁氧化物被还原成金属铁及少部分低价铁氧化物,飘落在下部的熔池Z1中,熔池Z1分布有侧吹喷管C1,喷入氧气及粉煤,形成该区域的高温和强还原性环境,最难还原的氧化亚铁得以全部还原。在上述过程中,闸门G1一直保持关闭状态。在渣铁分离后,熔渣从排渣口R1排出炉外,烟气进入烟道Y1Iron fine powder, oxygen, pulverized coal, and flux are sprayed from the main inlet FQR into the smelting chamber T 1 , and coke is added from the bulk material feeding port K 1 , and the iron fine powder floats in a hot state with a large specific surface area. The space of the first smelting chamber of the continuous furnace for CO reduction gas, rapid heat transfer and mass transfer, completes the space smelting process of iron concentrate; after space smelting, the high-valent iron oxide in the iron concentrate is reduced to metallic iron and less Part of the low-cost iron oxide falls in the lower molten pool Z 1 , and the molten pool Z 1 is distributed with a side blowing nozzle C 1 , which is sprayed with oxygen and pulverized coal to form a high temperature and strong reducing environment in the area, which is the most difficult. The reduced ferrous oxide is completely reduced. In the above process, the gate G 1 is kept closed. After the slag iron is separated, the slag is discharged from the slag discharge port R 1 and the flue gas enters the flue Y 1 .
该炼铁过程完成并排渣完毕后,关闭闸门G2,半开启闸门G1,铁水经过闸门G1下部流入熔池Z2,在块状物料投料口K2先加入脱硅剂如氧化铁皮脱硅后,再从侧吹喷管C2喷入脱硫脱磷剂如苏打粉等,对铁水进行脱硫和脱磷。烟气进入烟道Y2,熔渣从排渣口R2排出炉外。After this process is complete and ironmaking slag discharge, close the gate G 2, semi-open gate G 1, the molten iron via the gate G 1 flows into the lower portion of the bath Z 2, the bulk material feed port was added to K 2 desilication removal agent such as iron oxide After the silicon is sprayed, a desulfurization and dephosphorization agent such as soda powder is sprayed from the side blowing nozzle C 2 to desulfurize and dephosphorize the molten iron. The flue gas enters the flue Y 2 and the slag exits the furnace from the slag discharge port R 2 .
经三脱并排渣完毕后,关闭闸门G3,半开启闸门G2,铁水从闸门G2下部流入熔池Z3,从侧吹喷管向熔池内喷入氧气或铁精粉,同时从块状物料投料口K3陆续加入造渣材料如石灰、白云石,为提高产量,如有必要,在吹炼的同时也可从块状物料投料口K3加入铁精矿、氧化铁皮等渣料或冷却剂。本吹炼过程主要目的是脱碳,同时继续脱除铁水中的硫和磷。烟气进入烟道Y3,熔渣从排渣口R3排出。After the detachment of the slag is completed, the gate G 3 is closed, the gate G 2 is half-opened, the molten iron flows into the molten pool Z 3 from the lower portion of the gate G 2 , and oxygen or iron concentrate is sprayed from the side blowing nozzle into the molten pool, and at the same time The material feeding port K 3 is successively added with slag-forming materials such as lime and dolomite. In order to increase the output, if necessary, the iron concentrate, iron oxide scale and the like may be added from the bulk material feeding port K 3 while being blown. Or coolant. The main purpose of this blowing process is to decarbonize while continuing to remove sulfur and phosphorus from the molten iron. The flue gas enters the flue Y 3 and the slag is discharged from the slag discharge port R 3 .
吹炼完成并排渣完毕后,半开启闸门G3,钢水经过闸门G3下部流入熔池Z4,从底吹喷管D4向熔池喷吹氩气进行搅拌,在F4处设有一组石墨电极对熔池进行加热,在此过程中,通过块状物料投料口K4加入石灰和荧石等造渣剂。通过此精炼流程,对钢水化学成分进行调整、消除非金属夹杂物和进行硫化物形态处理。烟气进入烟道Y4,熔渣从排渣口R4排出炉外,钢水从产品出口OUT流入连铸车间的中间包内。 After completion of the blowing and slag discharge is half open shutter G 3, G 3 a lower portion of the molten steel flows through the bath shutter Z 4, D 4 from the bottom-blowing lance for blowing the bath with stirring to argon, it is provided with a set of at F 4 The graphite electrode heats the molten pool, and in the process, a slag forming agent such as lime and fluorite is added through the bulk material feeding port K 4 . Through this refining process, the chemical composition of molten steel is adjusted, non-metallic inclusions are removed, and sulfide form processing is performed. The flue gas enters the flue Y 4 , and the molten slag is discharged from the slag discharge port R 4 , and the molten steel flows from the product outlet OUT into the tundish of the continuous casting workshop.
上述连续炼钢的工艺相对于传统的分散的“高炉-炉外预处理-转炉吹炼-LF精炼”钢铁冶炼工艺,更节能环保及节省投资。The above-mentioned continuous steelmaking process is more energy-saving and environmentally friendly and saves investment than the traditional dispersed "blast furnace-furnace pretreatment-converter blowing-LF refining" steel smelting process.
实施例2连续炼铜Example 2 Continuous Copper Smelting
铜精矿经干燥破碎后,将铜精矿矿粉、石英熔剂和富氧空气从物料主入口FQR喷入连续炉第一冶炼室炉腔内,硫化铜精矿颗粒在氧化性的紊流气流中呈悬浮状态,快速的发生氧化反应,同时放出大量热,悬浮在炉腔内的物料颗粒熔融后,落入熔池Z1继续进行造铜硫(冰铜)和造渣反应,在上述过程中闸门G1一直保持关闭状态。在铜硫和渣澄清分层后,从排渣口R1排出炉渣,富含SO2的烟气进入烟道Y1After the copper concentrate is dried and crushed, the copper concentrate ore, quartz flux and oxygen-enriched air are sprayed from the material main inlet FQR into the furnace chamber of the first smelting chamber of the continuous furnace, and the sulphide concentrate particles are in the oxidative turbulent airflow. In the suspended state, the oxidation reaction occurs rapidly, and a large amount of heat is released. The particles suspended in the furnace cavity are melted, and then fall into the molten pool Z 1 to continue the copper-making sulfur (copper copper) and slagging reaction. The middle gate G 1 remains closed. After the copper sulphur and the slag are clarified and stratified, the slag is discharged from the slag discharge port R 1 , and the SO 2 -rich flue gas enters the flue Y 1 .
在铜硫分离完成并排渣完毕后,关闭闸门G2,半开启闸门G1,铜硫从闸门G1底部进入熔池Z2,将具有一定压力的空气从侧吹喷管C2送入熔池Z2中,使FeS氧化成FeO,而Cu2S经氧化后又与Cu2S相互反应变成粗铜,吹炼温度可以靠硫化物氧化反应来维持温度,在此过程中从块状物料投料口K2加入的造渣剂如石英等。吹炼渣从排渣口R2排出,吹炼烟气进入烟道Y2。After the copper and sulfur separation is completed and the slag is discharged, the gate G 2 is closed, the gate G 1 is half-opened, copper and sulfur enter the molten pool Z 2 from the bottom of the gate G 1 , and air having a certain pressure is sent from the side blowing nozzle C 2 into the melting. In the pool Z 2 , FeS is oxidized to FeO, and Cu 2 S is oxidized and then reacted with Cu 2 S to become blister copper. The blowing temperature can be maintained by the sulfide oxidation reaction, and the block is in the process. A slagging agent such as quartz added to the material feed port K 2 . The blown slag is discharged from the slag discharge port R 2 and the flue gas is blown into the flue Y2.
吹炼过程完成并排渣完毕后,关闭闸门G3,半开启闸门G2,粗铜从闸门G2底部流入熔池Z3中进行氧化精炼,从侧吹喷管C3鼓入空气,同时从块状物料投料口K3口向炉内加入熔剂如石英砂、石灰或苏打,利用多数杂质与氧亲和力大于铜,且杂质氧化物在铜中溶解度很小的特性,使硫、铁、铅、锌、镍、砷、锑、锡和铋等杂质氧化后造渣,熔渣从排渣口R3排出,烟气进入烟道Y3After the completion of the blowing process and the completion of the slag discharge, the gate G 3 is closed, the gate G 2 is half-opened, and the blister copper flows from the bottom of the gate G 2 into the molten pool Z 3 for oxidative refining, and the air is blown from the side blowing nozzle C 3 while The bulk material feeding port K 3 adds flux such as quartz sand, lime or soda to the furnace, and utilizes the characteristics that most impurities have higher affinity with oxygen than copper, and the impurity oxide has a small solubility in copper, so that sulfur, iron, lead, Impurities such as zinc, nickel, arsenic, antimony, tin and antimony are oxidized to form slag, and the slag is discharged from the slag discharge port R 3 , and the flue gas enters the flue Y 3 .
氧化精炼完成并排渣完毕后,半开启闸门G3,粗铜从闸门G3底部流入熔池Z4中进行还原精炼,用蒸汽或空气将重油雾化从侧吹喷管C4吹入铜液中,从块状物料投料口K4加入木炭粉或焦丁覆盖于铜液面上,重油等还原剂受热裂解为H2、CO、C等成分,使Cu2O还原成Cu。烟气进入烟道Y4,精炼铜熔体从熔池Z4中放出,可以铸板电解或铸锭销售。After the oxidizing refining is completed and the slag is completed, the gate G 3 is half-opened, and the blister copper flows from the bottom of the gate G 3 into the molten pool Z 4 for reduction refining, and the heavy oil is atomized by steam or air from the side blowing nozzle C 4 into the copper liquid. In the middle, the charcoal powder or coke is added from the bulk material feeding port K 4 to cover the copper liquid surface, and the reducing agent such as heavy oil is thermally cracked into components such as H 2 , CO, C, etc., so that Cu 2 O is reduced to Cu. The flue gas enters the flue Y 4 , and the refined copper melt is discharged from the molten pool Z 4 and can be electroplated or cast ingot.
上述连续炼铜的工艺相对于传统的分散的“闪速炉-PS转炉吹炼-氧化精炼-还原精炼”铜冶炼工艺,更节能环保及节省投资。The above continuous copper smelting process is more energy-saving and environmentally friendly and saves investment than the traditional dispersed "flash furnace-PS converter blowing-oxidizing refining-reduction refining" copper smelting process.
以上所述仅为本发明创造的较佳实施例而已,并不用以限制本发明创造,凡 在本发明创造的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明创造的保护范围之内。 The above description is only a preferred embodiment of the present invention and is not intended to limit the creation of the present invention. All modifications, equivalent substitutions, improvements, etc., made within the spirit and scope of the invention are intended to be included within the scope of the invention.

Claims (7)

  1. 一种连续冶金装置,包括顺序连接的若干冶炼室,相邻冶炼室之间通过竖直设置的闸门间隔,所述闸门能够在竖直方向运动,从而实现将位于其两侧的相邻冶炼室进行完全间隔或部分间隔;对于每一所述冶炼室,下部为熔池,熔池中设有至少一个与外界连通的排渣口,上部设有至少一个块状物料投料口以及一个烟道;第一冶炼室上还连接有具有下落空间的物料主入口,最后一个冶炼室上还连接有产品出口。A continuous metallurgical device comprising a plurality of smelting chambers connected in series, and adjacent gate chambers are vertically arranged by a gate interval, the gates being movable in a vertical direction, thereby realizing adjacent smelting chambers to be located on both sides thereof Performing a complete interval or a partial interval; for each of the smelting chambers, the lower portion is a molten pool, the molten pool is provided with at least one slag discharge port communicating with the outside, and the upper portion is provided with at least one block material feeding port and a flue; The main smelting chamber is also connected with a material main inlet having a falling space, and the last smelting chamber is also connected with a product outlet.
  2. 根据权利要求1所述的一种连续冶金装置,其特征在于,所述冶炼室的数量优选为3-5个。A continuous metallurgical apparatus according to claim 1, wherein the number of said smelting chambers is preferably 3-5.
  3. 根据权利要求1所述的一种连续冶金装置,其特征在于,任意相邻所述冶炼室之间呈平行连接或阶梯连接,优选为阶梯连接。A continuous metallurgical apparatus according to any of the preceding claims, wherein any adjacent said smelting chambers are connected in parallel or in a stepwise connection, preferably in a stepped connection.
  4. 根据权利要求1所述的一种连续冶金装置,其特征在于,所述冶炼室中各自还独立地设有辅加料口、加热装置、底吹喷管、侧吹喷管、喷嘴中的一种或多种。A continuous metallurgical apparatus according to claim 1, wherein each of said smelting chambers is independently provided with one of a auxiliary feeding port, a heating device, a bottom blowing nozzle, a side blowing nozzle, and a nozzle. Or a variety.
  5. 根据权利要求4所述的一种连续冶金装置,其特征在于,所述辅加料口位于其所在的冶炼室的中部顶端;所述加热装置可为环绕其所在的冶炼室的侧壁或底部的电磁感应加热线圈或位于其所在的冶炼室的中部顶端的加热电极;所述底吹喷管为设置于其所在的冶炼室底部的喷管,所述侧吹喷管为沿其所在的冶炼室的熔池平行分布的若干喷管。A continuous metallurgical apparatus according to claim 4, wherein said auxiliary feed port is located at a central top end of a smelting chamber in which it is located; said heating means may be located around a side wall or bottom of a smelting chamber in which it is located An electromagnetic induction heating coil or a heating electrode at a central portion of a smelting chamber in which it is located; the bottom blowing nozzle is a nozzle disposed at a bottom of a smelting chamber where the smelting nozzle is located, and the side blowing nozzle is a smelting chamber along which it is located The nozzles of the molten pool are distributed in parallel.
  6. 根据权利要求1所述的一种连续冶金装置,其特征在于,所述块状物料投料口位于各个冶炼室的前方上端,靠近前方闸门的位置;所述烟道位于各个冶炼室的后方上端,靠近后方闸门的位置。A continuous metallurgical apparatus according to claim 1, wherein said block material feeding port is located at an upper front end of each smelting chamber, adjacent to a position of the front gate; said flue is located at a rear upper end of each smelting chamber, Close to the position of the rear gate.
  7. 一种连续冶金方法,其特征在于,包括如下步骤:A continuous metallurgy method, comprising the steps of:
    S1:第一冶炼室冶炼:关闭所述第一冶炼室闸门,使所述第一冶炼室形成一个独立的冶金单元,从所述第一冶炼室具有下落空间的物料主入口加入原料,原料在第一冶炼室先经过空间冶炼,再落入熔池进行熔池冶炼,在冶炼过程中,通过块状物料投料口、辅加料口、加热装置、底吹喷管、侧吹喷管、喷嘴中的一种或多种方式分时段添加冶炼所必需的辅料、热量和气氛,形成良好的冶金环境,物料在熔池造渣并澄清分层后,形成渣层和富含金属熔体层;冶炼烟气从所述第 一冶炼室烟道排出,渣从所述第一冶炼室排渣口排出;S1: smelting of the first smelting chamber: closing the first smelting chamber gate, forming the first smelting chamber to form an independent metallurgical unit, and adding raw materials from the main inlet of the material having the falling space in the first smelting chamber, the raw materials are The first smelting room first undergoes space smelting, and then falls into the molten pool for smelting in the molten pool. During the smelting process, through the bulk material feeding port, the auxiliary feeding port, the heating device, the bottom blowing nozzle, the side blowing nozzle, and the nozzle One or more ways to add the auxiliary materials, heat and atmosphere necessary for smelting in a time-division manner to form a good metallurgical environment. After the material is slag in the molten pool and clarified and layered, a slag layer and a metal-rich melt layer are formed; Smoke from the said a smelting chamber flue is discharged, and the slag is discharged from the slag discharging port of the first smelting chamber;
    S2:第一冶炼室富含金属的熔体排放:原料在所述第一冶炼室冶炼完毕后,先关闭所述第二冶炼室闸门,然后提升所述第一冶炼室闸门,并多次移动所述第一冶炼室闸门末端在富含金属熔体层的位置,使其末端置于富含金属的熔体层中,让尽可能多的富含金属的熔体自流进入第二冶炼室,同时又保证所述第一冶炼室中的烟气和渣不会进入第二冶炼室,富含金属的熔体排放完毕后,关闭所述第一冶炼室闸门;S2: Melt discharge rich in metal in the first smelting chamber: after the smelting of the raw material in the first smelting chamber is completed, the gate of the second smelting chamber is closed, and then the gate of the first smelting chamber is lifted and moved multiple times The end of the first smelting chamber gate is at a position rich in a metal melt layer, and the end is placed in a metal-rich melt layer, allowing as much metal-rich melt as possible to flow into the second smelting chamber. At the same time, it is ensured that the flue gas and slag in the first smelting chamber do not enter the second smelting chamber, and after the metal-rich melt is discharged, the first smelting chamber gate is closed;
    S3:第二冶炼室冶炼:在富含金属的熔体进入所述第二冶炼室,随后关闭第一冶炼室闸门,此时第一冶炼室闸门、第二冶炼室炉壁及闭合的第二冶炼室闸门形成了一个独立的冶金单元,通过块状物料投料口、辅加料口、加热装置、底吹喷管、侧吹喷管、喷嘴中的一种或多种方式分时段添加冶炼所必需的辅料、热量和气氛,形成良好的冶金环境,除去富含金属熔体中的部分杂质,精炼形成的渣从所述第二冶炼室排渣口排出,冶炼烟气从所述第二冶炼室烟道排出;S3: second smelting room smelting: entering the second smelting chamber in the metal-rich melt, and then closing the first smelting chamber gate, at this time, the first smelting chamber gate, the second smelting chamber wall and the closed second The smelting chamber gate forms an independent metallurgical unit, which is necessary to add smelting time by means of one or more of the block material feeding port, the auxiliary feeding port, the heating device, the bottom blowing nozzle, the side blowing nozzle and the nozzle. Excipients, heat and atmosphere form a good metallurgical environment, remove some impurities in the metal-rich melt, and the slag formed by refining is discharged from the slag discharge port of the second smelting chamber, and the smelting flue gas is from the second smelting chamber Flue discharge;
    S4:反复采用同步骤S2的熔体排放过程以及同步骤S3的冶炼步骤,使富含金属的熔体依次在后续冶炼室完成冶炼,直至在最后一个冶炼室完成冶炼(或精炼);S4: repeatedly using the melt discharge process of the same step S2 and the smelting step of the same step S3, so that the metal-rich melt is sequentially smelted in the subsequent smelting chamber until the smelting (or refining) is completed in the last smelting chamber;
    S5:产品的排放:在最后一个冶炼室完成冶炼的金属熔体从所述产品出口排出炉外。 S5: Emission of the product: The molten metal that has been smelted in the last smelting chamber is discharged from the outlet of the product.
PCT/CN2016/103860 2015-12-25 2016-10-29 Continuous metallurgical device and method WO2017107662A1 (en)

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