CN117431411B - Smelting method of recycled aluminum - Google Patents
Smelting method of recycled aluminum Download PDFInfo
- Publication number
- CN117431411B CN117431411B CN202311774086.9A CN202311774086A CN117431411B CN 117431411 B CN117431411 B CN 117431411B CN 202311774086 A CN202311774086 A CN 202311774086A CN 117431411 B CN117431411 B CN 117431411B
- Authority
- CN
- China
- Prior art keywords
- smelting
- aluminum
- refining
- furnace
- raw material
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B21/00—Obtaining aluminium
- C22B21/0084—Obtaining aluminium melting and handling molten aluminium
- C22B21/0092—Remelting scrap, skimmings or any secondary source aluminium
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B21/00—Obtaining aluminium
- C22B21/06—Obtaining aluminium refining
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B7/00—Working 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
- C22B7/001—Dry processes
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B9/00—General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals
- C22B9/10—General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals with refining or fluxing agents; Use of materials therefor, e.g. slagging or scorifying agents
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
本发明提供了一种再生铝的熔炼方法,涉及再生铝合金熔炼领域。该再生铝的熔炼方法,包括以下步骤:将待再生的铝原料在580~680℃的条件下熔炼75~125min,得到熔化液;且在所述熔炼过程中,所述铝原料的上部区域位于氧化气氛喷火的范围内,所述铝原料的下部区域位于还原气氛喷火的范围内;将所述熔化液进行精炼,得到再生铝液。上述熔炼方法,在580~680℃的温度范围内,对待再生的铝原料进行熔炼。一方面,利用氧化气氛快速提升炉温,使得铝原料快速熔化提高熔炼效率。另一方面,通过铝原料下部还原气氛燃烧,减少对铝液和合金的烧损。采用上述的再生铝的熔炼方法,既可以提高再生铝的生产效率,同时又具有较低的烧损率。
The invention provides a method for smelting recycled aluminum and relates to the field of recycled aluminum alloy smelting. The smelting method of recycled aluminum includes the following steps: smelting the aluminum raw material to be regenerated at 580-680°C for 75-125 minutes to obtain a molten liquid; and during the smelting process, the upper area of the aluminum raw material is located Within the range of the flames of the oxidizing atmosphere, the lower region of the aluminum raw material is located within the range of the flames of the reducing atmosphere; the molten liquid is refined to obtain a regenerated aluminum liquid. The above-mentioned smelting method smelts the aluminum raw material to be recycled in the temperature range of 580 to 680°C. On the one hand, the oxidizing atmosphere is used to quickly increase the furnace temperature, causing the aluminum raw materials to quickly melt and improve the smelting efficiency. On the other hand, the lower part of the aluminum raw material is burned in the reducing atmosphere to reduce the burning loss of the aluminum liquid and alloy. Using the above-mentioned smelting method of recycled aluminum can not only improve the production efficiency of recycled aluminum, but also have a lower burning loss rate.
Description
技术领域Technical field
本发明涉及再生铝合金熔炼领域,尤其涉及再生铝的熔炼方法。The present invention relates to the field of recycled aluminum alloy smelting, and in particular to a method for smelting recycled aluminum.
背景技术Background technique
铝是一种可循环利用的资源,具有良好的回收性。再生铝是将废旧铝和废铝合金材料等经过重新熔炼,得到铝合金或铝金属。再生铝资源的开发利用,甚至保级使用,不仅能够节约能源、降低生产成本,相比原生铝可降低碳排放95%,而且能够减少环境污染、改善生态环境。因此,再生铝的工艺装备研究和铝产业未来高质量持续发展具有重要意义。Aluminum is a recyclable resource with good recyclability. Recycled aluminum is made by re-smelting scrap aluminum and scrap aluminum alloy materials to obtain aluminum alloy or aluminum metal. The development and utilization of recycled aluminum resources, or even the use of recycled aluminum, can not only save energy and reduce production costs, but also reduce carbon emissions by 95% compared with primary aluminum, and can also reduce environmental pollution and improve the ecological environment. Therefore, the research on process equipment for recycled aluminum and the future high-quality and sustainable development of the aluminum industry are of great significance.
再生铝熔炼时,通常采用高温熔炼技术实现废铝材料的充分熔解。但是,采用850℃以上的熔炼温度会使再生铝及其合金氧化烧损,造成废铝回收率降低,其值小于90%,影响产品质量,且能耗相当高,每吨产品的油耗一般在90公斤以上,甚至会达到100-120公斤。若采用低温熔炼法可以部分解决上述问题,但是,熔炼温度的降低必然会延长熔炼时间,影响再生铝的生产效率。When smelting recycled aluminum, high-temperature smelting technology is usually used to fully melt the scrap aluminum material. However, using a melting temperature above 850°C will cause oxidation and burning loss of recycled aluminum and its alloys, resulting in a reduction in the scrap aluminum recovery rate, which is less than 90%, affecting product quality, and the energy consumption is quite high. The fuel consumption per ton of product is generally More than 90 kg, even up to 100-120 kg. The above problems can be partially solved by using low-temperature smelting method. However, the reduction of smelting temperature will inevitably extend the smelting time and affect the production efficiency of recycled aluminum.
发明内容Contents of the invention
本发明的主要目的是提供一种再生铝的熔炼方法,以解决再生铝熔炼烧损高或者熔炼时间长的技术问题。The main purpose of the present invention is to provide a method for smelting recycled aluminum to solve the technical problems of high burning loss or long smelting time of recycled aluminum.
为实现上述目的,本发明提供了一种再生铝的熔炼方法,包括以下步骤:In order to achieve the above object, the present invention provides a method for smelting recycled aluminum, which includes the following steps:
将待再生的铝原料在580~680℃的条件下熔炼75~125min,得到熔化液。且在熔炼过程中,铝原料的上部区域位于氧化气氛喷火的范围内,铝原料的下部区域位于还原气氛喷火的范围内。The aluminum raw material to be regenerated is smelted at 580-680°C for 75-125 minutes to obtain a molten liquid. During the smelting process, the upper area of the aluminum raw material is located within the range of the oxidizing atmosphere and the lower area of the aluminum raw material is located within the range of the reducing atmosphere.
将熔化液进行精炼,得到再生铝液。The molten liquid is refined to obtain regenerated aluminum liquid.
根据本申请的实施方式,将待再生的铝原料在580~680℃的条件下熔炼75~125min的步骤包括:According to the embodiment of the present application, the steps of smelting the aluminum raw material to be regenerated at 580 to 680°C for 75 to 125 minutes include:
在铝原料加入后的10-25min内,在580-600℃的温度条件下进行第一阶段熔炼。Within 10-25 minutes after the aluminum raw materials are added, the first stage of melting is carried out at a temperature of 580-600°C.
将温度升温至650-680℃,保持25-50min,进行第二阶段熔炼。Raise the temperature to 650-680°C, keep it for 25-50 minutes, and proceed to the second stage of melting.
调节温度至580-630℃,保持熔炼40-50min,进行第三阶段熔炼。Adjust the temperature to 580-630°C, maintain melting for 40-50 minutes, and proceed to the third stage of melting.
根据本申请的实施方式,在第一阶段熔炼、第二阶段熔炼和第三阶段熔炼的过程中,搅拌熔化液,搅拌次数为2~8次。According to the embodiment of the present application, during the first stage smelting, the second stage smelting and the third stage smelting, the melt is stirred for 2 to 8 times.
根据本申请的实施方式,氧化气氛喷火为在天然气和助燃风的比例小于1比2的条件下进行燃烧喷火。According to an embodiment of the present application, the oxidizing atmosphere fire is performed under the condition that the ratio of natural gas to combustion air is less than 1:2.
还原气氛喷火为在天然气和助燃风的比例大于1比2的条件进行燃烧喷火。Reducing atmosphere flamethrowing is a combustion flamethrowing condition where the ratio of natural gas to combustion air is greater than 1:2.
根据本申请的实施方式,第一阶段的熔炼温度以5~10℃/min的速度升温至650-680℃。According to the embodiment of the present application, the melting temperature in the first stage is raised to 650-680°C at a rate of 5-10°C/min.
根据本申请的实施方式,在将待再生的铝原料进行熔炼之前还包括:According to the embodiment of the present application, before the aluminum raw material to be regenerated is smelted, it also includes:
将待再生的铝原料在500-600℃的条件下进行通过加热炉壁,反射烘烤;The aluminum raw material to be regenerated is passed through the heating furnace wall at 500-600°C for reflection baking;
继续将所述待再生的铝原料450-550℃的条件下进行长火焰直接烧烤,并通入经余热加热的空气吹离脱开的硬化漆膜或硬化油脂。Continue to directly grill the aluminum raw material to be regenerated at 450-550°C with a long flame, and blow off the separated hardened paint film or hardened grease with air heated by waste heat.
根据本申请的实施方式,反射烘烤的时长为10~15mim。According to the embodiment of the present application, the duration of reflection baking is 10~15mim.
在反射烘烤进行10~15分钟后,进行直接烧烤,直接烧烤的时长为15~25min。After reflection baking for 10 to 15 minutes, direct grilling is performed. The duration of direct grilling is 15 to 25 minutes.
根据本申请的实施方式,空气的流量为10~20 Nm³/h。According to the embodiment of the present application, the flow rate of air is 10~20 Nm³/h.
根据本申请的实施方式,将熔化液进行精炼的步骤包括:According to the embodiment of the present application, the step of refining the melt includes:
在炉内铝液温度680℃~720℃时,加入0.20%的精炼剂,精炼时间为10~15min以上,精炼时掀起的波浪高度在30~80mm之间,精炼之后静置8~12min扒渣。When the temperature of the aluminum liquid in the furnace is 680°C to 720°C, add 0.20% refining agent. The refining time is more than 10 to 15 minutes. The height of the waves set off during refining is between 30 to 80mm. After refining, let it stand for 8 to 12 minutes to remove the slag. .
根据本申请的实施方式,待再生的铝原料进行熔炼步骤发生于熔炼炉中,熔化液进行精炼的步骤发生于精炼炉中。According to the embodiment of the present application, the step of smelting the aluminum raw material to be regenerated occurs in the smelting furnace, and the step of refining the molten liquid occurs in the refining furnace.
在熔炼炉中的熔化液转移至精炼炉后,对熔炼炉进行扒铁、扒渣、清炉,然后进入下一个熔炼周期。After the molten liquid in the smelting furnace is transferred to the refining furnace, the smelting furnace is stripped of iron, slag, and cleaned, and then enters the next smelting cycle.
上述的再生铝的熔炼方法,在580~680℃的温度范围内,对待再生的铝原料进行熔炼。一方面,利用氧化气氛快速提升炉温,使得铝原料快速熔化提高熔炼效率。另一方面,通过铝原料下部还原气氛燃烧,减少对铝液和合金的烧损。采用上述的再生铝的熔炼方法,既可以提高再生铝的生产效率,同时又具有较低的烧损率。The above-mentioned smelting method of recycled aluminum smelts the aluminum raw material to be recycled in the temperature range of 580 to 680°C. On the one hand, the oxidizing atmosphere is used to quickly increase the furnace temperature, causing the aluminum raw materials to quickly melt and improve the smelting efficiency. On the other hand, the lower part of the aluminum raw material is burned in the reducing atmosphere to reduce the burning loss of the aluminum liquid and alloy. Using the above-mentioned smelting method of recycled aluminum can not only improve the production efficiency of recycled aluminum, but also have a lower burning loss rate.
附图说明Description of drawings
为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图示出的结构获得其他的附图。In order to explain the embodiments of the present invention or the technical solutions in the prior art more clearly, the drawings needed to be used in the description of the embodiments or the prior art will be briefly introduced below. Obviously, the drawings in the following description are only These are some embodiments of the present invention. For those of ordinary skill in the art, other drawings can be obtained based on the structures shown in these drawings without exerting creative efforts.
图1是本申请一实施方式的再生铝的熔炼方法的流程图。FIG. 1 is a flow chart of a method for smelting recycled aluminum according to an embodiment of the present application.
本发明目的的实现、功能特点及优点将结合实施方式,参照附图做进一步说明。The realization of the purpose, functional features and advantages of the present invention will be further described with reference to the embodiments and the accompanying drawings.
具体实施方式Detailed ways
下面将结合本发明实施方式中的附图,对本发明实施方式中的技术方案进行清楚、完整地描述,显然,所描述的实施方式仅仅是本发明的一部分实施方式,而不是全部的实施方式。基于本发明中的实施方式,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施方式,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only some of the embodiments of the present invention, not all of them. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts fall within the scope of protection of the present invention.
需要说明,本发明实施方式中所有方向性指示(诸如上、下……)仅用于解释在某一特定姿态(如附图所示)下各部件之间的相对位置关系、运动情况等,如果该特定姿态发生改变时,则该方向性指示也相应地随之改变。It should be noted that all directional indications (such as up, down...) in the embodiments of the present invention are only used to explain the relative positional relationship, movement, etc. between the components in a specific posture (as shown in the accompanying drawings). If the specific posture changes, the directional indication changes accordingly.
另外,在本发明中如涉及“第一”、“第二”等的描述仅用于描述目的,而不能理解为指示或暗示其相对重要性或者隐含指明所指示的技术特征的数量。由此,限定有“第一”、“第二”的特征可以明示或者隐含地包括至少一个该特征。In addition, descriptions such as "first", "second", etc. in the present invention are for descriptive purposes only and cannot be understood as indicating or implying their relative importance or implicitly indicating the number of indicated technical features. Therefore, features defined as "first" and "second" may explicitly or implicitly include at least one of these features.
并且,本发明各个实施方式之间的技术方案可以相互结合,但是必须是以本领域普通技术人员能够实现为基础,当技术方案的结合出现相互矛盾或无法实现时应当认为这种技术方案的结合不存在,也不在本发明要求的保护范围之内。Moreover, the technical solutions in the various embodiments of the present invention can be combined with each other, but it must be based on the realization by those of ordinary skill in the art. When the combination of technical solutions appears to be contradictory or cannot be realized, such combination of technical solutions should be considered. It does not exist and is not within the protection scope required by the present invention.
为实现上述目的,本发明提供了一种再生铝的熔炼方法,参见图1,包括以下步骤:In order to achieve the above object, the present invention provides a method for smelting recycled aluminum. See Figure 1, which includes the following steps:
S100:将待再生的铝原料在580~680℃的条件下熔炼75~150min,得到熔化液。且在熔炼过程中,铝原料的上部区域位于氧化气氛喷火的范围内,铝原料的下部区域位于还原气氛喷火的范围内。S100: Smelt the aluminum raw material to be regenerated at 580-680°C for 75-150 minutes to obtain a molten liquid. During the smelting process, the upper area of the aluminum raw material is located within the range of the oxidizing atmosphere and the lower area of the aluminum raw material is located within the range of the reducing atmosphere.
待再生的铝原料包括废旧铝和废铝合金材料或含铝的废料。通常将近似品类的铝原料或成分含量接近的同类型产品的铝原料进行同批次的熔炼。为了增加熔炼效率,待再生的铝原料以碎块进行投料,如通过步进式方式进行投料,以料堆形式存在。Aluminum raw materials to be recycled include scrap aluminum and scrap aluminum alloy materials or scrap containing aluminum. Usually, aluminum raw materials of similar categories or products of the same type with similar composition content are smelted in the same batch. In order to increase the smelting efficiency, the aluminum raw materials to be regenerated are fed in broken pieces, such as in a step-by-step manner, in the form of a pile.
在待再生的铝原料较为洁净,杂质较少的情形下,如含有的油脂或漆较少,直接进行熔炼。When the aluminum raw material to be regenerated is relatively clean and contains few impurities, such as containing less grease or paint, it can be smelted directly.
待再生的铝原料的熔炼过程通常在熔炼炉中进行。在熔炼过程中,控制熔炼炉内的炉温为580~680℃。熔炼炉的热源主要为喷火嘴。喷火嘴燃烧使得熔炼炉的炉温升高。喷火嘴包括对铝原料的上部区域进行氧化气氛喷火的喷火嘴以及对铝原料的下部区域进行还原气氛喷火的喷火嘴,当然在一些实施例中,还包括在其他区域进行喷火的喷火嘴。The smelting process of the aluminum raw material to be regenerated is usually carried out in a smelting furnace. During the smelting process, the furnace temperature in the smelting furnace is controlled to be 580~680°C. The heat source of the smelting furnace is mainly the flame nozzle. The combustion of the flame nozzle increases the temperature of the smelting furnace. The flame nozzle includes a flame nozzle that sprays an oxidizing atmosphere on the upper area of the aluminum raw material and a flame nozzle that sprays a reducing atmosphere on the lower area of the aluminum raw material. Of course, in some embodiments, it also includes spraying in other areas. The spout of fire.
氧化气氛主要是指空气供给充分,燃料完全燃烧的情况下产生的一种火焰气氛。Oxidizing atmosphere mainly refers to a flame atmosphere produced when the air supply is sufficient and the fuel is completely burned.
还原气氛是指氢、一氧化碳和转化天然气等还原性气体为主要成分的气氛。这种气氛中通常不含有氧化性气体或含量极少。例如,转化天然气是由高纯度甲烷与少量氢气组成,燃烧时火焰清洁,不含氧化性成分。Reducing atmosphere refers to an atmosphere in which reducing gases such as hydrogen, carbon monoxide and converted natural gas are the main components. This atmosphere usually contains no or very small amounts of oxidizing gases. For example, converted natural gas is composed of high-purity methane and a small amount of hydrogen. It burns with a clean flame and contains no oxidizing components.
若熔炼炉非初次熔炼,则熔炼炉中包括上一周期熔炼形成的含铝的熔化液。料堆位于熔化液上。If the smelting furnace is not used for primary smelting, the smelting furnace includes the aluminum-containing molten liquid formed by the previous smelting cycle. The stockpile is located above the melt.
铝原料的上部区域位于氧化气氛喷火的范围内,即上部料块区域采用喷火嘴在氧化气氛下喷火燃烧熔化料块。铝原料的下部区域位于还原气氛喷火的范围内,即下部料块区域采用喷火嘴在还原气氛下喷火燃烧。由于料堆位于熔化液上,因此也可以理解为采用喷火嘴对准熔化液的液位区域进行燃烧,熔化液处于还原气氛下,从而防止熔化液过度氧化而造成烧损。The upper area of the aluminum raw material is located within the range of the flame in the oxidizing atmosphere, that is, the upper block area uses a flame nozzle to burn and melt the block in the oxidizing atmosphere. The lower area of the aluminum raw material is located within the range of the reducing atmosphere, that is, the lower block area uses a flame nozzle to burn and burn in the reducing atmosphere. Since the pile is located on the molten liquid, it can also be understood that the flame nozzle is used to aim at the liquid level area of the molten liquid to burn, and the molten liquid is in a reducing atmosphere, thereby preventing excessive oxidation of the molten liquid and causing burning damage.
具体而言,将主室炉膛内两侧布置喷火嘴对准炉膛内炉料喷火,利用炉膛内的上喷嘴对准炉料表面直接喷射火焰进行熔炼,火焰通过炉料之间空隙钻进炉料堆内部,将热量很快的传到炉料中间,使物料堆中间和底部的物料快速温度上升熔化。具体地,上喷嘴正对料堆中上部。Specifically, flame nozzles are arranged on both sides of the main chamber furnace to spray fire at the furnace materials. The upper nozzles in the furnace are used to directly spray flames on the surface of the furnace materials for melting. The flame penetrates into the furnace materials pile through the gaps between the furnace materials. , the heat is quickly transferred to the middle of the furnace material, causing the material in the middle and bottom of the material pile to quickly rise in temperature and melt. Specifically, the upper nozzle is facing the upper middle part of the pile.
炉膛两侧喷火嘴上下分区布置,上部料块区域通过上喷火嘴采用氧化气氛喷火燃烧熔化料块。下部料块区域通过下喷火嘴采用还原气氛燃烧。上部料块区域的火焰喷射角度为向下0~5°,对料堆中部,从而保证上喷嘴中心火焰加热料堆主体。The flame nozzles on both sides of the furnace are arranged in upper and lower zones. The upper block area uses the upper flame nozzle to burn and melt the material block using an oxidizing atmosphere. The lower block area is burned in a reducing atmosphere through the lower flame nozzle. The flame injection angle in the upper block area is 0~5° downward, towards the middle of the pile, thus ensuring that the flame in the center of the upper nozzle heats the main body of the pile.
下部料块区域的火焰喷射角度为向下10~15°对准料堆根部,从而保证下喷嘴火焰下部尽量覆盖铝合金液面。The flame injection angle in the lower block area is 10~15° downward and aimed at the root of the pile to ensure that the lower part of the lower nozzle flame covers the aluminum alloy liquid surface as much as possible.
上部料块区域的喷射位置与下部料块区域的喷射位置的高度差为500~800mm。下喷嘴距离初始铝液面400~800mm。由于火焰具有一定的长度,因此可以炉体内液面上200~800mm形成还原气氛区,而上部形成氧化气氛区。The height difference between the injection position of the upper block area and the injection position of the lower block area is 500~800mm. The distance between the lower nozzle and the initial aluminum liquid level is 400~800mm. Since the flame has a certain length, a reducing atmosphere zone can be formed at 200~800mm above the liquid surface in the furnace body, and an oxidizing atmosphere zone can be formed at the upper part.
S200:将熔化液进行精炼,得到再生铝液。S200: Refining the molten liquid to obtain regenerated aluminum liquid.
在该步骤中,熔化液精炼的主要目的是去除铝液中的杂质和气体,以提高铝的品质和成分均匀性。铝液中的杂质主要包括铁、硅、磷等有害元素,这些元素会对铝的性能产生不良影响。铝液中的氧、氢等气体也会影响铝液的性能和质量。In this step, the main purpose of melt refining is to remove impurities and gases in the aluminum liquid to improve the quality and composition uniformity of the aluminum. Impurities in liquid aluminum mainly include harmful elements such as iron, silicon, phosphorus, etc. These elements will have adverse effects on the performance of aluminum. Oxygen, hydrogen and other gases in the aluminum liquid will also affect the performance and quality of the aluminum liquid.
铝液精炼的工作原理主要有两种方式:化学精炼和物理精炼。化学精炼主要是利用一定的化学反应,在铝液中产生一些可挥发或溶解的化合物,从而将有害元素和气体去除。常用的方法有氯化精炼、氧化精炼、碳化精炼等。物理精炼主要是利用一些物理原理或技术手段,如通过搅拌或气泡冲击等方式使化合物挥发或溶解,再通过真空吸气等方式将气体排出,从而达到精炼目的。There are two main working principles of aluminum liquid refining: chemical refining and physical refining. Chemical refining mainly uses certain chemical reactions to produce some volatile or dissolved compounds in the aluminum liquid, thereby removing harmful elements and gases. Commonly used methods include chlorination refining, oxidation refining, carbonization refining, etc. Physical refining mainly uses some physical principles or technical means, such as stirring or bubble impact to volatilize or dissolve compounds, and then exhausting the gas through vacuum suction to achieve the purpose of refining.
即在本申请中通过在熔炼室上下产生氧化和还原气氛区,在580~680℃的温度范围内,对再生铝料进行熔炼;一方面,利用氧化气氛快速提升炉温,低温喷射的火舌和高温烟气很容易熔化物料堆的表层料堆块和钻入铝料堆内部实现熔化处理,缩小废铝料堆内外温差,尽量保持恒温的环境,提高熔炼效率;另一方面,通过料堆下部还原气氛燃烧,减少对铝液和合金的烧损。采用上述结合的技术从投料到铝锭浇铸完成,时间可控制在3小时左右,比采用传统熔炼技术所用的时间缩短了2小时,大大提高了再生铝锭的生产效率,本发明技术可使产量提高50%以上,烧损率降低50%,耗油量减少10%以上,烟气排放处理负荷减少60%。That is, in this application, the recycled aluminum material is smelted in the temperature range of 580 to 680°C by generating oxidation and reduction atmosphere zones above and below the smelting chamber; on the one hand, the oxidation atmosphere is used to quickly increase the furnace temperature, and the low-temperature injection flame tongue and The high-temperature flue gas can easily melt the surface material pile blocks of the material pile and drill into the inside of the aluminum material pile to achieve melting treatment, reduce the temperature difference between the inside and outside of the scrap aluminum material pile, try to maintain a constant temperature environment, and improve the melting efficiency; on the other hand, through the lower part of the material pile, Combustion in reducing atmosphere reduces burning loss of aluminum liquid and alloy. Using the above combined technology, the time from feeding to aluminum ingot casting can be controlled to about 3 hours, which is 2 hours shorter than the time used by traditional smelting technology, which greatly improves the production efficiency of recycled aluminum ingots. The technology of the present invention can increase the output Increase by more than 50%, reduce burnout rate by 50%, reduce fuel consumption by more than 10%, and reduce flue gas emission treatment load by 60%.
而若熔炼炉为初次熔炼,熔炼炉中则不包括含铝的熔化液。其与熔炼炉中包括熔化液的情形类似,因此其各区域的火焰喷射角度、喷射位置以及喷射位置高度差也可参考设置,有益效果也预制类似,也不再赘述。If the smelting furnace is used for primary smelting, the melt containing aluminum will not be included in the smelting furnace. It is similar to the situation where the melt is included in the smelting furnace. Therefore, the flame injection angle, injection position and height difference of the injection position in each area can also be set as a reference. The beneficial effects are also similar and will not be described again.
上述的再生铝的熔炼方法,在580~680℃的温度范围内,对待再生的铝原料进行熔炼。一方面,利用氧化气氛快速提升炉温,使得铝原料快速熔化提高熔炼效率。另一方面,通过铝原料下部还原气氛燃烧,减少对铝液和合金的烧损。采用上述的再生铝的熔炼方法,既可以提高再生铝的生产效率,同时又具有较低的烧损率。The above-mentioned smelting method of recycled aluminum smelts the aluminum raw material to be recycled in the temperature range of 580 to 680°C. On the one hand, the oxidizing atmosphere is used to quickly increase the furnace temperature, causing the aluminum raw materials to quickly melt and improve the smelting efficiency. On the other hand, the lower part of the aluminum raw material is burned in the reducing atmosphere to reduce the burning loss of the aluminum liquid and alloy. Using the above-mentioned smelting method of recycled aluminum can not only improve the production efficiency of recycled aluminum, but also have a lower burning loss rate.
在一些实施例中,将待再生的铝原料在580~680℃的条件下熔炼75-125min的步骤包括:In some embodiments, the step of smelting the aluminum raw material to be regenerated at 580-680°C for 75-125 minutes includes:
在铝原料加入后的10-25min内,在580-600℃的温度条件下进行第一阶段熔炼。Within 10-25 minutes after the aluminum raw materials are added, the first stage of melting is carried out at a temperature of 580-600°C.
将温度升温至650-680℃,保持25-50min,进行第二阶段熔炼。Raise the temperature to 650-680°C, keep it for 25-50 minutes, and proceed to the second stage of melting.
调节温度至580-630℃,保持熔炼40-50min,进行第三阶段熔炼。Adjust the temperature to 580-630°C, maintain melting for 40-50 minutes, and proceed to the third stage of melting.
即通过调控炉膛两侧对准物料堆的喷火嘴的喷火温度实现熔炼过程,在一个熔炼周期内,开始10-25min内,以580-600℃的温度进行低温喷火过程(第一阶段熔炼),对铝合金低温软化处理,随后再迅速升温至650-680℃(第二阶段熔炼),加快铝堆的熔炼,运行25-50min后,最后控制在580-630℃,继续熔炼40-50min(第三阶段熔炼)。That is, the smelting process is realized by regulating the flame spray temperature of the flame nozzles on both sides of the furnace that are aligned with the material pile. Within a smelting cycle, the low-temperature flame spray process is carried out at a temperature of 580-600°C within the first 10-25 minutes (the first stage Smelting), soften the aluminum alloy at low temperature, and then quickly raise the temperature to 650-680℃ (second stage smelting) to speed up the smelting of the aluminum pile. After running for 25-50 minutes, it is finally controlled at 580-630℃ and continues smelting for 40- 50min (third stage smelting).
在一些实施例中,在第一阶段熔炼、第二阶段熔炼和第三阶段熔炼的过程中,搅拌熔化液,搅拌次数为2~8次。该种方式有利于促进熔化。In some embodiments, during the first stage smelting, the second stage smelting and the third stage smelting, the melt is stirred for 2 to 8 times. This method is beneficial to promote melting.
在一些实施例中,氧化气氛喷火为在天然气和助燃风的比例小于1比2的条件下进行燃烧喷火。优选地,氧化气氛为天然气和助燃风的比例为1比3。当然,也可以将天然气用燃烧油、煤气替换,其与助燃风的比例要求类似。In some embodiments, the oxidizing atmosphere fire is performed under the condition that the ratio of natural gas to combustion air is less than 1:2. Preferably, the ratio of the oxidizing atmosphere to natural gas and combustion air is 1:3. Of course, natural gas can also be replaced with combustion oil or coal gas, and the ratio requirements for combustion air are similar.
还原气氛喷火为在天然气和助燃风的比例大于1比2的条件进行燃烧喷火。优选地,还原气氛为天然气和助燃风的比例为1比1.5。当然,也可以将天然气用燃烧油、煤气替换,其与助燃风的比例要求类似。Reducing atmosphere flamethrowing is a combustion flamethrowing condition where the ratio of natural gas to combustion air is greater than 1:2. Preferably, the ratio of the reducing atmosphere to natural gas and combustion air is 1:1.5. Of course, natural gas can also be replaced with combustion oil or coal gas, and the ratio requirements for combustion air are similar.
在一些实施例中,第一阶段的熔炼温度以5-10℃/min的速度升温至650-680。In some embodiments, the melting temperature in the first stage is increased to 650-680°C at a rate of 5-10°C/min.
在一些实施例中,参见图1,在将待再生的铝原料进行熔炼之前还包括:In some embodiments, referring to Figure 1, before the aluminum raw material to be regenerated is smelted, it also includes:
将待再生的铝原料在500-600℃的条件下进行通过加热炉壁,反射烘烤;The aluminum raw material to be regenerated is passed through the heating furnace wall at 500-600°C for reflection baking;
继续将所述待再生的铝原料450-550℃的条件下进行长火焰(超过料堆心部)直接烧烤,并通入经余热加热的空气吹离脱开的硬化漆膜或硬化油脂。Continue to directly grill the aluminum raw material to be regenerated at 450-550°C with a long flame (exceeding the core of the stockpile), and introduce air heated by waste heat to blow away the separated hardened paint film or hardened grease.
当待再生的铝原料具有较多的漆膜或油脂时,在熔炼前需要进行脱漆去脂。When the aluminum raw material to be regenerated has a large amount of paint film or grease, it needs to be depainted and degreased before smelting.
脱漆去脂技术操作过程为,在处理室内两侧顶部布置喷火嘴对准炉膛内炉壁和废铝产品/碎块喷火,使火舌50%覆盖炉膛膛壁面上,火舌通过炉膛膛壁反射传热对铝料堆周围及表面温度进行传递烘烤,炉温500-600℃。所述低温喷火脱漆,燃烧喷火嘴正对废铝块部分,采用高比例通量空气,采用低温直接烧烤,炉温450-550℃;同时大通量空气将表面脱开的硬化漆膜或硬化油脂吹到处理室下面收集器,通过高温反射烘烤10-15分钟和低温烧烤15-25分钟去除掉80%表面油漆和油脂。The operation process of paint removal and degreasing technology is to arrange flame nozzles on the top of both sides of the processing chamber to spray fire on the furnace wall and scrap aluminum products/pieces, so that the flame tongue covers 50% of the furnace wall surface, and the flame tongue passes through the furnace wall Reflective heat transfer transfers and bakes the surrounding and surface temperature of the aluminum pile, and the furnace temperature is 500-600°C. In the low-temperature spray paint removal, the combustion flame nozzle is facing the scrap aluminum block, using high-proportion flux air, using low-temperature direct barbecue, the furnace temperature is 450-550°C; at the same time, large-flux air will separate the hardened paint from the surface The film or hardened grease is blown to the collector below the treatment chamber, and 80% of the surface paint and grease is removed through high-temperature reflection baking for 10-15 minutes and low-temperature grilling for 15-25 minutes.
而相关技术中,再生铝表面有机涂层和油脂的通常高温燃烧去除的比较经济的做法,会产生大量二噁英等有害废弃物,产生大量VOCs排放物和环境污染。Among related technologies, the relatively economical method of removing organic coatings and grease on the surface of recycled aluminum by high-temperature combustion will produce a large amount of harmful wastes such as dioxins, as well as a large amount of VOCs emissions and environmental pollution.
在一些实施例中,反射烘烤的时长为10-15分钟。在反射烘烤进行10-15分钟后,进行直接烧烤,直接烧烤的时长为15-25分钟。In some embodiments, the duration of reflective baking is 10-15 minutes. After reflection baking for 10-15 minutes, direct grilling is performed. The duration of direct grilling is 15-25 minutes.
在一些实施例中,空气的流量为10~20 Nm³/h,脱漆室形成5~12Pa的微正压。即脱漆去脂的腔室具有一定的微正压,从而有利于排出硬化漆膜或硬化油脂。In some embodiments, the air flow rate is 10~20 Nm³/h, and the paint stripping chamber forms a slight positive pressure of 5~12Pa. That is, the chamber for stripping paint and degreasing has a certain slight positive pressure, which is conducive to discharging the hardened paint film or hardened grease.
在一些实施例中,将熔化液进行精炼的步骤包括:In some embodiments, the step of refining the melt includes:
在一些实施例中,待再生的铝原料进行熔炼步骤发生于熔炼炉中,熔化液进行精炼的步骤发生于精炼炉中。In some embodiments, the step of smelting the aluminum raw material to be regenerated occurs in a smelting furnace, and the step of refining the molten liquid occurs in a refining furnace.
在熔炼炉中的熔化液转移至精炼炉后,对熔炼炉进行扒铁、扒渣、清炉,然后进入下一个熔炼周期。After the molten liquid in the smelting furnace is transferred to the refining furnace, the smelting furnace is stripped of iron, slag, and cleaned, and then enters the next smelting cycle.
将上述熔炼炉中1/3至1/2的熔化液在10-15min内通过下部溜槽转移至下层精炼炉进行精炼,并对铝液转移后的上层熔炼炉进行扒铁、扒渣、清炉,然后进入下一个熔炼周期。Transfer 1/3 to 1/2 of the molten liquid in the above-mentioned smelting furnace to the lower refining furnace through the lower chute within 10-15 minutes for refining, and perform iron removal, slag removal, and furnace cleaning on the upper smelting furnace after the aluminum liquid has been transferred , and then enter the next smelting cycle.
在脱漆去脂、熔炼和精炼三个炉室的侧面主排烟气通道上设换热器,对参与燃烧的压缩空气进行换热、加热,提升余热利用水平,排烟通道后端设除尘和脱氮脱硫等环保设备。A heat exchanger is installed on the main exhaust gas channel on the side of the three furnace chambers of depainting, degreasing, smelting and refining to heat exchange and heat the compressed air participating in combustion to improve the utilization level of waste heat. A dust collector is installed at the rear end of the exhaust channel. and environmental protection equipment such as denitrification and desulfurization.
以下结合具体的实施例对本申请的具体技术方案进行说明。The specific technical solutions of the present application will be described below with reference to specific examples.
实施例Example
1)脱漆去脂:1) Remove paint and grease:
将成分含量接近的同类型产品或碎块,通过辊道或传输链分批步进脱漆去脂室(也叫高温预处理l)进行高温烘烤脱漆去脂。The same type of products or fragments with similar component content are sent to the depainting and degreasing chamber (also called high-temperature pretreatment l) in batches through rollers or conveyor chains for high-temperature baking, depainting and degreasing.
在炉温550℃的条件下反射烘烤15分钟,并且当反射烘烤进行至10分钟后,开启低温直接烧烤,其中炉温500℃,时长为15分钟。在低温直接烧烤过程中,以20 Nm³/h,的流量通入空气将表面脱开的硬化漆膜或硬化油脂吹到处理室下面收集器。Reflection baking is performed at an oven temperature of 550°C for 15 minutes, and when the reflection baking progresses to 10 minutes, low-temperature direct grilling is turned on, with the oven temperature being 500°C and the duration being 15 minutes. During the low-temperature direct grilling process, air is introduced at a flow rate of 20 Nm³/h to blow the hardened paint film or hardened grease off the surface to the collector below the treatment chamber.
2)粗炼:将上述脱漆去脂的铝原料投入熔炼炉(主室),采用气氛分区低温喷火相结合的熔炼技术对再生铝进行熔炼;2) Rough smelting: Put the above-mentioned depainted and degreased aluminum raw materials into the smelting furnace (main chamber), and use the smelting technology combining atmosphere zoned low-temperature flame spray to smelt the recycled aluminum;
在铝原料加入后的10min内,在590-600℃的温度条件下进行第一阶段熔炼。Within 10 minutes after the aluminum raw materials are added, the first stage of melting is carried out at a temperature of 590-600°C.
将温度升温至670-680℃,保持25min,进行第二阶段熔炼。Raise the temperature to 670-680°C, keep it for 25 minutes, and proceed to the second stage of melting.
调节温度至620-630℃,保持熔炼40min,进行第三阶段熔炼。Adjust the temperature to 620-630°C, maintain melting for 40 minutes, and proceed to the third stage of melting.
在整个粗炼过程中,保持上部料块区域采用氧化气氛喷火燃烧熔化料块,天然气和助燃风的比例大于1比2。保持下部还原气氛燃烧,天然气和助燃风的比例小于1比2。在熔炼过程中步进式加料,平稳搅拌熔化液2-8次。其中,上喷嘴的设置位置与下喷嘴的设置位置高度差为500~800mm。下喷嘴距离初始铝液面400~800mm。During the entire rough refining process, the upper block area is maintained to be burned and melted by oxidizing atmosphere, and the ratio of natural gas to combustion air is greater than 1:2. Keep the lower reducing atmosphere burning, and the ratio of natural gas and combustion air is less than 1:2. Add materials step by step during the melting process and stir the melt steadily 2-8 times. Among them, the height difference between the setting position of the upper nozzle and the setting position of the lower nozzle is 500~800mm. The distance between the lower nozzle and the initial aluminum liquid level is 400~800mm.
3)精炼:将上述熔炼炉中1/3至1/2的熔化液在10-15min内通过下部溜槽转移至下层精炼炉进行精炼,并对铝液转移后的上层熔炼炉进行扒铁、扒渣、清炉,然后进入下一个熔炼周期。3) Refining: Transfer 1/3 to 1/2 of the molten liquid in the above-mentioned smelting furnace to the lower refining furnace through the lower chute within 10-15 minutes for refining, and perform scraping and scraping of the upper smelting furnace after the aluminum liquid has been transferred. slag, clear the furnace, and then enter the next smelting cycle.
整个粗炼过程的时长为75分钟,烧损为1.6%。The entire rough refining process lasts 75 minutes and the burn loss is 1.6%.
实施例Example
1)脱漆去脂:1) Remove paint and grease:
将成分含量接近的同类型产品或碎块,通过辊道或传输链分批步进脱漆去脂室(也叫高温预处理l)进行高温烘烤脱漆去脂。The same type of products or fragments with similar component content are sent to the depainting and degreasing chamber (also called high-temperature pretreatment l) in batches through rollers or conveyor chains for high-temperature baking, depainting and degreasing.
在炉温500℃的条件下反射烘烤20分钟,并且当反射烘烤进行至15分钟后,开启低温直接烧烤,其中炉温450℃,时长为25分钟。在低温直接烧烤过程中,以15Nm³/h,的流量通入空气将表面脱开的硬化漆膜或硬化油脂吹到处理室下面收集器。Reflection baking is performed at an oven temperature of 500°C for 20 minutes, and when the reflection baking progresses to 15 minutes, low-temperature direct grilling is turned on, with the oven temperature being 450°C and the duration being 25 minutes. During the low-temperature direct grilling process, air is introduced at a flow rate of 15Nm³/h to blow the hardened paint film or hardened grease off the surface to the collector below the treatment chamber.
2)粗炼:将上述脱漆去脂的铝原料投入熔炼炉(主室),采用气氛分区低温喷火相结合的熔炼技术对再生铝进行熔炼;2) Rough smelting: Put the above-mentioned depainted and degreased aluminum raw materials into the smelting furnace (main chamber), and use the smelting technology combining atmosphere zoned low-temperature flame spray to smelt the recycled aluminum;
在铝原料加入后的25min内,在580-590℃的温度条件下进行第一阶段熔炼。Within 25 minutes after the aluminum raw materials are added, the first stage of melting is carried out at a temperature of 580-590°C.
将温度升温至650-660℃,保持50min,进行第二阶段熔炼。Raise the temperature to 650-660°C, keep it for 50 minutes, and proceed to the second stage of melting.
调节温度至580-590℃,保持熔炼50min,进行第三阶段熔炼。Adjust the temperature to 580-590°C, maintain melting for 50 minutes, and proceed to the third stage of melting.
在整个粗炼过程中,保持上部料块区域采用氧化气氛喷火燃烧熔化料块,天然气和助燃风的比例大于1比2。保持下部还原气氛燃烧,天然气和助燃风的比例小于1比2。在熔炼过程中步进式加料,平稳搅拌熔化液2-8次。其中,上喷嘴的设置位置与下喷嘴的设置位置高度差为500~800mm。下喷嘴距离初始铝液面400~800mm。During the entire rough refining process, the upper block area is maintained to be burned and melted by oxidizing atmosphere, and the ratio of natural gas to combustion air is greater than 1:2. Keep the lower reducing atmosphere burning, and the ratio of natural gas and combustion air is less than 1:2. Add materials step by step during the melting process and stir the melt steadily 2-8 times. Among them, the height difference between the setting position of the upper nozzle and the setting position of the lower nozzle is 500~800mm. The distance between the lower nozzle and the initial aluminum liquid level is 400~800mm.
3)精炼:将上述熔炼炉中1/3至1/2的熔化液在10-15min内通过下部溜槽转移至下层精炼炉进行精炼,并对铝液转移后的上层熔炼炉进行扒铁、扒渣、清炉,然后进入下一个熔炼周期。3) Refining: Transfer 1/3 to 1/2 of the molten liquid in the above-mentioned smelting furnace to the lower refining furnace through the lower chute within 10-15 minutes for refining, and perform scraping and scraping of the upper smelting furnace after the aluminum liquid has been transferred. slag, clear the furnace, and then enter the next smelting cycle.
整个粗炼过程的时长为125分钟,烧损为1.7%。The entire rough refining process lasts 125 minutes and the burning loss is 1.7%.
实施例Example
1)脱漆去脂:1) Remove paint and grease:
将成分含量接近的同类型产品或碎块,通过辊道或传输链分批步进脱漆去脂室(也叫高温预处理l)进行高温烘烤脱漆去脂。The same type of products or fragments with similar component content are sent to the depainting and degreasing chamber (also called high-temperature pretreatment l) in batches through rollers or conveyor chains for high-temperature baking, depainting and degreasing.
在炉温500℃的条件下反射烘烤25分钟,并且当反射烘烤进行至12分钟后,开启低温直接烧烤,其中炉温500℃,时长为20分钟。在低温直接烧烤过程中,以15 Nm³/h的流量通入空气将表面脱开的硬化漆膜或硬化油脂吹到处理室下面收集器。Reflection baking is performed at an oven temperature of 500°C for 25 minutes, and when the reflection baking progresses to 12 minutes, low-temperature direct grilling is turned on, with the oven temperature being 500°C and the duration being 20 minutes. During the low-temperature direct grilling process, air is introduced at a flow rate of 15 Nm³/h to blow the hardened paint film or hardened grease off the surface to the collector below the treatment chamber.
2)粗炼:将上述脱漆去脂的铝原料投入熔炼炉(主室),采用气氛分区低温喷火相结合的熔炼技术对再生铝进行熔炼;2) Rough smelting: Put the above-mentioned depainted and degreased aluminum raw materials into the smelting furnace (main chamber), and use the smelting technology combining atmosphere zoned low-temperature flame spray to smelt the recycled aluminum;
在铝原料加入后的15min内,在590-600℃的温度条件下进行第一阶段熔炼。Within 15 minutes after the aluminum raw materials are added, the first stage of melting is carried out at a temperature of 590-600°C.
将温度升温至660-670℃,保持40min,进行第二阶段熔炼。Raise the temperature to 660-670°C, keep it for 40 minutes, and proceed to the second stage of melting.
调节温度至600-610℃,保持熔炼45min,进行第三阶段熔炼。Adjust the temperature to 600-610°C, maintain melting for 45 minutes, and proceed to the third stage of melting.
在整个粗炼过程中,保持上部料块区域采用氧化气氛喷火燃烧熔化料块,天然气和助燃风的比例大于1比2。保持下部还原气氛燃烧,天然气和助燃风的比例小于1比2。在熔炼过程中步进式加料,平稳搅拌熔化液2-8次。其中,上喷嘴的设置位置与下喷嘴的设置位置高度差为500~800mm。下喷嘴距离初始铝液面400~800mm。During the entire rough refining process, the upper block area is maintained to be burned and melted by oxidizing atmosphere, and the ratio of natural gas to combustion air is greater than 1:2. Keep the lower reducing atmosphere burning, and the ratio of natural gas and combustion air is less than 1:2. Add materials step by step during the melting process and stir the melt steadily 2-8 times. Among them, the height difference between the setting position of the upper nozzle and the setting position of the lower nozzle is 500~800mm. The distance between the lower nozzle and the initial aluminum liquid level is 400~800mm.
3)精炼:将上述熔炼炉中1/3至1/2的熔化液在10-15min内通过下部溜槽转移至下层精炼炉进行精炼,并对铝液转移后的上层熔炼炉进行扒铁、扒渣、清炉,然后进入下一个熔炼周期。3) Refining: Transfer 1/3 to 1/2 of the molten liquid in the above-mentioned smelting furnace to the lower refining furnace through the lower chute within 10-15 minutes for refining, and perform scraping and scraping of the upper smelting furnace after the aluminum liquid has been transferred. slag, clear the furnace, and then enter the next smelting cycle.
整个粗炼过程的时长为100min,烧损为<1.5%。The duration of the entire rough refining process is 100 minutes, and the burning loss is <1.5%.
实施例Example
1)脱漆去脂:1) Remove paint and grease:
将成分含量接近的同类型产品或碎块,通过辊道或传输链分批步进脱漆去脂室(也叫高温预处理l)进行高温烘烤脱漆去脂。The same type of products or fragments with similar component content are sent to the depainting and degreasing chamber (also called high-temperature pretreatment l) in batches through rollers or conveyor chains for high-temperature baking, depainting and degreasing.
在炉温550℃的条件下反射烘烤22分钟,并且当反射烘烤进行至18分钟后,开启低温直接烧烤,其中炉温530℃,时长为18分钟。在低温直接烧烤过程中,以16 Nm³/h的流量通入空气将表面脱开的硬化漆膜或硬化油脂吹到处理室下面收集器。Reflection baking was performed at an oven temperature of 550°C for 22 minutes, and when the reflection baking progressed to 18 minutes, low-temperature direct grilling was turned on, with the oven temperature being 530°C and a duration of 18 minutes. During the low-temperature direct grilling process, air is introduced at a flow rate of 16 Nm³/h to blow the hardened paint film or hardened grease off the surface to the collector below the treatment chamber.
2)粗炼:将上述脱漆去脂的铝原料投入熔炼炉(主室),采用气氛分区低温喷火相结合的熔炼技术对再生铝进行熔炼;2) Rough smelting: Put the above-mentioned depainted and degreased aluminum raw materials into the smelting furnace (main chamber), and use the smelting technology combining atmosphere zoned low-temperature flame spray to smelt the recycled aluminum;
在铝原料加入后的20min内,在590-600℃的温度条件下进行第一阶段熔炼。Within 20 minutes after the aluminum raw materials are added, the first stage of melting is carried out at a temperature of 590-600°C.
将温度升温至670-680℃,保持25min,进行第二阶段熔炼。Raise the temperature to 670-680°C, keep it for 25 minutes, and proceed to the second stage of melting.
调节温度至620-630℃,保持熔炼40min,进行第三阶段熔炼。Adjust the temperature to 620-630°C, maintain melting for 40 minutes, and proceed to the third stage of melting.
在整个粗炼过程中,保持上部料块区域采用氧化气氛喷火燃烧熔化料块,天然气和助燃风的比例大于1比2。保持下部还原气氛燃烧,天然气和助燃风的比例小于1比2。在熔炼过程中步进式加料,平稳搅拌熔化液2-8次。其中,上喷嘴的设置位置与下喷嘴的设置位置高度差为500~800mm。下喷嘴距离初始铝液面400~800mm。During the entire rough refining process, the upper block area is maintained to be burned and melted by oxidizing atmosphere, and the ratio of natural gas to combustion air is greater than 1:2. Keep the lower reducing atmosphere burning, and the ratio of natural gas and combustion air is less than 1:2. Add materials step by step during the melting process and stir the melt steadily 2-8 times. Among them, the height difference between the setting position of the upper nozzle and the setting position of the lower nozzle is 500~800mm. The distance between the lower nozzle and the initial aluminum liquid level is 400~800mm.
3)精炼:将上述熔炼炉中1/3至1/2的熔化液在10-15min内通过下部溜槽转移至下层精炼炉进行精炼,并对铝液转移后的上层熔炼炉进行扒铁、扒渣、清炉,然后进入下一个熔炼周期。3) Refining: Transfer 1/3 to 1/2 of the molten liquid in the above-mentioned smelting furnace to the lower refining furnace through the lower chute within 10-15 minutes for refining, and perform scraping and scraping of the upper smelting furnace after the aluminum liquid has been transferred. slag, clear the furnace, and then enter the next smelting cycle.
整个粗炼过程的时长为85分钟,烧损为1.6%。The entire rough refining process lasts 85 minutes, and the burning loss is 1.6%.
实施例Example
1)脱漆去脂:1) Remove paint and grease:
将成分含量接近的同类型产品或碎块,通过辊道或传输链分批步进脱漆去脂室(也叫高温预处理l)进行高温烘烤脱漆去脂。The same type of products or fragments with similar component content are sent to the depainting and degreasing chamber (also called high-temperature pretreatment l) in batches through rollers or conveyor chains for high-temperature baking, depainting and degreasing.
在炉温550℃的条件下反射烘烤20分钟,并且当反射烘烤进行至15分钟后,开启低温直接烧烤,其中炉温500℃,时长为20分钟。在低温直接烧烤过程中,以18 Nm³/h的流量通入空气将表面脱开的硬化漆膜或硬化油脂吹到处理室下面收集器。Reflection baking is performed at an oven temperature of 550°C for 20 minutes, and when the reflection baking progresses to 15 minutes, low-temperature direct grilling is turned on, with the oven temperature being 500°C and the duration being 20 minutes. During the low-temperature direct grilling process, air is introduced at a flow rate of 18 Nm³/h to blow the hardened paint film or hardened grease off the surface to the collector below the treatment chamber.
2)粗炼:将上述脱漆去脂的铝原料投入熔炼炉(主室),采用气氛分区低温喷火相结合的熔炼技术对再生铝进行熔炼。2) Rough smelting: Put the above-mentioned depainted and degreased aluminum raw materials into the smelting furnace (main chamber), and use the smelting technology combining atmosphere zoned low-temperature flame spray to smelt the recycled aluminum.
在铝原料加入后的15min内,在590-600℃的温度条件下进行第一阶段熔炼。Within 15 minutes after the aluminum raw materials are added, the first stage of melting is carried out at a temperature of 590-600°C.
将温度升温至650-660℃,保持35min,进行第二阶段熔炼。Raise the temperature to 650-660°C, keep it for 35 minutes, and proceed to the second stage of melting.
调节温度至580-590℃,保持熔炼50min,进行第三阶段熔炼。Adjust the temperature to 580-590°C, maintain melting for 50 minutes, and proceed to the third stage of melting.
在整个粗炼过程中,保持上部料块区域采用氧化气氛喷火燃烧熔化料块,天然气和助燃风的比例大于1比2。保持下部还原气氛燃烧,天然气和助燃风的比例小于1比2。在熔炼过程中步进式加料,平稳搅拌熔化液2-8次。其中,上喷嘴的设置位置与下喷嘴的设置位置高度差为500~800mm。下喷嘴距离初始铝液面400~800mm。During the entire rough refining process, the upper block area is maintained to be burned and melted by oxidizing atmosphere, and the ratio of natural gas to combustion air is greater than 1:2. Keep the lower reducing atmosphere burning, and the ratio of natural gas and combustion air is less than 1:2. Add materials step by step during the melting process and stir the melt steadily 2-8 times. Among them, the height difference between the setting position of the upper nozzle and the setting position of the lower nozzle is 500~800mm. The distance between the lower nozzle and the initial aluminum liquid level is 400~800mm.
3)精炼:将上述熔炼炉中1/3至1/2的熔化液在10-15min内通过下部溜槽转移至下层精炼炉进行精炼,并对铝液转移后的上层熔炼炉进行扒铁、扒渣、清炉,然后进入下一个熔炼周期。3) Refining: Transfer 1/3 to 1/2 of the molten liquid in the above-mentioned smelting furnace to the lower refining furnace through the lower chute within 10-15 minutes for refining, and perform scraping and scraping of the upper smelting furnace after the aluminum liquid has been transferred. slag, clear the furnace, and then enter the next smelting cycle.
在本实施例中,整个粗炼过程的时长为100分钟,烧损为1.8%。In this embodiment, the duration of the entire rough refining process is 100 minutes, and the burning loss is 1.8%.
对比例1Comparative example 1
与实施例5的区别在于,在整个粗炼过程中上部料块区域和下部料块区域均为氧化气氛。其余同实施例5。在本实施例中,整个粗炼过程的时长为100分钟,烧损为3.0%。The difference from Example 5 is that both the upper block area and the lower block area are in an oxidizing atmosphere during the entire roughing process. The rest is the same as in Embodiment 5. In this embodiment, the duration of the entire rough refining process is 100 minutes, and the burning loss is 3.0%.
对比例2Comparative example 2
与实施例5的区别在于,在粗炼步骤中,在铝原料加入后的15min内,在590-600℃的温度条件下进行第一阶段熔炼。The difference from Example 5 is that in the rough refining step, the first stage smelting is performed at a temperature of 590-600°C within 15 minutes after the aluminum raw material is added.
将温度升温至840-850℃,保持35min,进行第二阶段熔炼。Raise the temperature to 840-850°C, keep it for 35 minutes, and proceed to the second stage of melting.
调节温度至840-850℃,保持熔炼50min,进行第三阶段熔炼。Adjust the temperature to 840-850°C, maintain melting for 50 minutes, and proceed to the third stage of melting.
其中,上喷嘴的设置位置与下喷嘴的设置位置高度差为500~800mm。下喷嘴距离初始铝液面400~800mm。Among them, the height difference between the setting position of the upper nozzle and the setting position of the lower nozzle is 500~800mm. The distance between the lower nozzle and the initial aluminum liquid level is 400~800mm.
其余同实施例5。在本实施例中,整个粗炼过程的时长为100分钟,烧损为3.5%。The rest is the same as in Embodiment 5. In this embodiment, the duration of the entire rough refining process is 100 minutes, and the burning loss is 3.5%.
通过比较上述的实施例和对比例证明,本申请的再生铝的熔炼方法既可以提高再生铝的生产效率,同时又具有较低的烧损率。Comparing the above examples and comparative examples proves that the recycled aluminum smelting method of the present application can not only improve the production efficiency of recycled aluminum, but also have a lower burning loss rate.
本发明的上述技术方案中,以上仅为本发明的优选实施例,并非因此限制本发明的专利范围,凡是在本发明的技术构思下,利用本发明说明书及附图内容所作的等效结构变换,或直接/间接运用在其他相关的技术领域均包括在本发明的专利保护范围。Among the above technical solutions of the present invention, the above are only preferred embodiments of the present invention and do not limit the patent scope of the present invention. Under the technical concept of the present invention, equivalent structural transformations can be made using the contents of the description and drawings of the present invention. , or direct/indirect application in other related technical fields are included in the scope of patent protection of the present invention.
Claims (8)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202311774086.9A CN117431411B (en) | 2023-12-22 | 2023-12-22 | Smelting method of recycled aluminum |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202311774086.9A CN117431411B (en) | 2023-12-22 | 2023-12-22 | Smelting method of recycled aluminum |
Publications (2)
Publication Number | Publication Date |
---|---|
CN117431411A CN117431411A (en) | 2024-01-23 |
CN117431411B true CN117431411B (en) | 2024-03-01 |
Family
ID=89550258
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202311774086.9A Active CN117431411B (en) | 2023-12-22 | 2023-12-22 | Smelting method of recycled aluminum |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN117431411B (en) |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20090114039A (en) * | 2008-04-29 | 2009-11-03 | 윤수현 | Apparatus and method for melting aluminum for recycle |
CN102839288A (en) * | 2012-10-09 | 2012-12-26 | 南通曼特威金属材料有限公司 | Low-temperature rapidly-smelting process for regenerative aluminum alloy |
CN113528825A (en) * | 2021-06-25 | 2021-10-22 | 江西华赣瑞林稀贵金属科技有限公司 | Method for smelting and recovering valuable metals by electronic waste and multi-metal solid waste |
CN116463519A (en) * | 2023-04-24 | 2023-07-21 | 天津圣金特汽车配件有限公司 | Aluminum alloy smelting process |
-
2023
- 2023-12-22 CN CN202311774086.9A patent/CN117431411B/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20090114039A (en) * | 2008-04-29 | 2009-11-03 | 윤수현 | Apparatus and method for melting aluminum for recycle |
CN102839288A (en) * | 2012-10-09 | 2012-12-26 | 南通曼特威金属材料有限公司 | Low-temperature rapidly-smelting process for regenerative aluminum alloy |
CN113528825A (en) * | 2021-06-25 | 2021-10-22 | 江西华赣瑞林稀贵金属科技有限公司 | Method for smelting and recovering valuable metals by electronic waste and multi-metal solid waste |
CN116463519A (en) * | 2023-04-24 | 2023-07-21 | 天津圣金特汽车配件有限公司 | Aluminum alloy smelting process |
Also Published As
Publication number | Publication date |
---|---|
CN117431411A (en) | 2024-01-23 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA2028769C (en) | Glassmelting method with reduced nox generation | |
CN1091870C (en) | Non-oxidizing heating method and apparatus therefor | |
CN109852760A (en) | Smelting method for improving scrap steel ratio by preheating scrap steel in converter | |
CN111518986B (en) | Steelmaking method of scrap steel smelting system by utilizing primary combustion heat energy | |
CN109357268B (en) | Process method for treating waste paint buckets by utilizing hot air oxygen-enriched natural gas in shaft furnace | |
JP7142154B2 (en) | Method for refining low-nitrogen steel using electric furnace | |
JP6357104B2 (en) | Starting the smelting process | |
CN117431411B (en) | Smelting method of recycled aluminum | |
CN215863419U (en) | Plasma melting furnace with stirring function | |
CN212713622U (en) | System for smelting scrap steel by utilizing once-combustion heat energy | |
CN1325672C (en) | Lead smelting method and apparatus implementing the same | |
JP4372838B2 (en) | Improved energy input method for bulk scrap | |
NO953834L (en) | Process for heat treatment of waste material, especially garbage, and rotary kiln for carrying out the process | |
JPH0368082B2 (en) | ||
JPH0233779B2 (en) | ||
TWI881534B (en) | Method for producing molten iron | |
RU2160320C1 (en) | Method of reworking secondary materials containing precious metals | |
CN212299976U (en) | Environment-friendly heating furnace | |
SU1668441A1 (en) | Method for extraction of aluminum out of secondary aluminum-containing raw material in reverberatory furnace | |
JP2560668B2 (en) | Smelting and refining method | |
JPH10310813A (en) | Melting method and melting equipment for cold iron source | |
SU1756362A1 (en) | Process for reduction roasting of siderite ore in shaft furnace | |
SU1201322A1 (en) | Method of producing steel from scrap | |
JPH0631686B2 (en) | Exhaust gas heat recovery method and apparatus for melting furnace | |
CN118460857A (en) | Zinc leaching slag treatment method and device |
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 |