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CN106381395A - Method for recovering platinum group metal through car dead catalyst pyrogenic process - Google Patents

Method for recovering platinum group metal through car dead catalyst pyrogenic process Download PDF

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Publication number
CN106381395A
CN106381395A CN201610883402.XA CN201610883402A CN106381395A CN 106381395 A CN106381395 A CN 106381395A CN 201610883402 A CN201610883402 A CN 201610883402A CN 106381395 A CN106381395 A CN 106381395A
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platinum group
catalyst
group metals
slag
flux
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许开华
周继锋
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Green Us (tianjin) City Mineral Products Circulation Industry Development Co Ltd
GEM Co Ltd China
GEM Wuhan Urban Mining Resources Industrial Park Development Co Ltd
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Green Us (tianjin) City Mineral Products Circulation Industry Development Co Ltd
GEM Co Ltd China
GEM Wuhan Urban Mining Resources Industrial Park Development Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B7/00Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
    • C22B7/001Dry processes
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B11/00Obtaining noble metals
    • C22B11/02Obtaining noble metals by dry processes
    • C22B11/021Recovery of noble metals from waste materials
    • C22B11/026Recovery of noble metals from waste materials from spent catalysts
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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  • Engineering & Computer Science (AREA)
  • Metallurgy (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Catalysts (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

The invention discloses a method for recovering platinum group metal through a car dead catalyst pyrogenic process. The method comprises the steps that 1, a dead catalyst is pretreated firstly to remove a metal shell and impurities on the surface of the dead catalyst, and then the pretreated catalyst is subjected to crushing and fine grinding; 2, iron powder, carbon powder and calcium oxide are mixed uniformly for standby application according to the mass ratio of (2-3):(1-3):(12-30); 3, the catalyst obtained after fine grinding and mixed flux are mixed, then added into a plasma electric-arc furnace to be heated, gradually heated up to 1773 K-2073 K, and fully stirred until complete melting is achieved; and 4, melt is gradually cooled to room temperature to obtain an iron alloy with the platinum group metal enriched and flux slag. According to the method, the extraction process is simple, the technological process is short, the influence on environment is small, and the recovery rate of the platinum group metal Pt reaches 99.99%.

Description

汽车废催化剂火法回收铂族金属的方法Method for recovery of platinum group metals by fire method of waste automobile catalyst

技术领域technical field

本发明涉及一种汽车废催化剂中贵金属回收技术领域,更具体地,涉及一种汽车废催化剂火法回收铂族金属的方法。The invention relates to the technical field of recycling precious metals from automobile waste catalysts, and more specifically, to a method for recovering platinum group metals from automobile waste catalysts by fire method.

背景技术Background technique

资源匮乏和环境污染既是人类发展所面临的两大难题,也是我国实施可持续发展战略需要优先考虑的重大课题。截至2014年底,中国汽车保有量达1.54亿辆,位居世界第二,据工信部预测,到2020年我国汽车保有量将突破2亿,汽车尾气排放使得空气污染问题日益严峻,而汽车尾气净化催化剂正是解决汽车尾气排放问题的关键。按目前我国的汽车保有量和增长速度,预计未来几年内我国将迎来汽车报废的高峰,报废汽车废催化剂的处理数量也会大幅增加。Resource scarcity and environmental pollution are not only two major problems facing human development, but also major issues that need to be given priority in the implementation of sustainable development strategies in my country. As of the end of 2014, the number of automobiles in China reached 154 million, ranking second in the world. According to the prediction of the Ministry of Industry and Information Technology, the number of automobiles in my country will exceed 200 million by 2020. Automobile exhaust emissions make air pollution more and more serious, and automobile exhaust purification catalysts It is the key to solving the problem of automobile exhaust emissions. According to the current car ownership and growth rate in China, it is expected that my country will usher in the peak of car scrapping in the next few years, and the number of waste catalysts for scrapped cars will also increase significantly.

目前,很多国家对于废汽车尾气催化剂处理处置的主要目标大都是回收铂族金属,粗提工艺可分为火法和湿法两大类,是决定铂族金属能否高效回收的关键。湿法回收技术具有易操作、条件要求较低的优势,我国汽车尾气净化催化剂的回收技术目前以湿法工艺为主,然而,湿法回收工艺处理量小,对环境影响大,随着催化剂集中处置需求的提高,国家对于环保要求越来越高,湿法回收工艺已不能满足废汽车尾气催化剂处理的需要和环保的目的。At present, the main goal of many countries for the treatment and disposal of waste vehicle exhaust catalysts is mostly to recover platinum group metals. The rough extraction process can be divided into two categories: pyrolysis and wet methods, which are the key to determining whether platinum group metals can be recovered efficiently. Wet recovery technology has the advantages of easy operation and low condition requirements. The recovery technology of automobile exhaust purification catalyst in my country is currently dominated by wet process. However, wet recovery process has a small processing capacity and has a great impact on the environment. With the increase in disposal demand, the country has higher and higher requirements for environmental protection, and the wet recovery process can no longer meet the needs of waste vehicle exhaust catalyst treatment and the purpose of environmental protection.

发明内容Contents of the invention

针对现有技术中存在的问题,本发明的目的在于提供一种汽车废催化剂火法回收铂族金属的方法,该方法提取过程简单,工艺流程短,环境污染小,能满足大量处理废催化剂的需求。Aiming at the problems existing in the prior art, the object of the present invention is to provide a method for recovering platinum group metals by fire method of waste automobile catalysts. need.

本发明的汽车废催化剂火法回收铂族金属的方法,包括以下步骤:The method for reclaiming platinum group metals by fire method of automobile waste catalyst of the present invention comprises the following steps:

步骤(1):先将废催化剂进行预处理,除去废催化剂表面的金属外壳和易分离的杂质,再将预处理后的催化剂进行破碎细磨;Step (1): first pretreating the spent catalyst to remove the metal shell and easily separated impurities on the surface of the spent catalyst, and then crushing and finely grinding the pretreated catalyst;

步骤(2):制备混合熔剂:将铁粉、碳粉和氧化钙按质量比为2~3:1~3:12~30混合均匀备用;Step (2): Prepare mixed flux: mix iron powder, carbon powder and calcium oxide in a mass ratio of 2 to 3:1 to 3:12 to 30 evenly for later use;

步骤(3):将细磨后的催化剂和混合熔剂混合后加入等离子体电弧炉中进行加热,逐渐升温至1773K~2073K,充分搅拌至完全熔化,通过高温造渣后,得到的熔体上层为渣层,下层为含铂族金属的液态合金层;Step (3): After mixing the finely ground catalyst and mixed flux, add it to the plasma arc furnace for heating, gradually raise the temperature to 1773K ~ 2073K, fully stir until it is completely melted, and after high temperature slagging, the upper layer of the obtained melt is Slag layer, the lower layer is a liquid alloy layer containing platinum group metals;

步骤(4):对熔体逐步降温冷却至室温,得到富集铂族金属的铁合金,及熔剂渣体。Step (4): gradually lowering the temperature of the melt to room temperature to obtain a ferroalloy enriched in platinum group metals and flux slag.

本发明的有益效果:本发明以铁粉作为铂族金属元素的捕集剂,碳粉作为还原剂,氧化钙作为助熔剂,利用火法进行高温熔融造渣,铂族金属被铁捕捉形成铂钯铑铁合金,熔渣比重较轻会漂浮在比重较重的铂钯铑铁合金上方,实现渣层与金属合金分离,达到铂族金属富集的效果,碳粉、氧化钙等助剂会熔解在熔渣中。该方法的铂族金属中Pt的回收率达到99.99%,Pd的回收率达到99.22%以上,Rh的回收率达到90.12%以上,较单纯的湿法回收率有所提高,且提取过程简单,工艺流程短,对环境影响小,有广阔的工业运用前景。Beneficial effects of the present invention: In the present invention, iron powder is used as a collector of platinum group metal elements, carbon powder is used as a reducing agent, calcium oxide is used as a flux, and high-temperature melting slagging is carried out by fire method, and platinum group metals are captured by iron to form platinum For palladium-rhodium-iron alloy, the slag with a lighter specific gravity will float above the heavier platinum-palladium-rhodium-iron alloy to separate the slag layer from the metal alloy and achieve the effect of enriching platinum group metals. Additives such as carbon powder and calcium oxide will be melted in the in the slag. In this method, the recovery rate of Pt in platinum group metals reaches 99.99%, the recovery rate of Pd reaches more than 99.22%, and the recovery rate of Rh reaches more than 90.12%, which is improved compared with the simple wet recovery rate, and the extraction process is simple and the process The process is short, the impact on the environment is small, and it has broad industrial application prospects.

具体实施方式detailed description

下面结合具体实施例对本发明进行详细描述,本部分的描述仅是示范性和解释性,不应对本发明的保护范围有任何的限制作用。The present invention will be described in detail below in conjunction with specific embodiments. The description in this part is only exemplary and explanatory, and should not have any limiting effect on the protection scope of the present invention.

本发明的汽车废催化剂火法回收铂族金属的方法,包括以下步骤:The method for reclaiming platinum group metals by fire method of automobile waste catalyst of the present invention comprises the following steps:

步骤(1):先将废催化剂进行预处理,除去废催化剂表面的金属外壳和易分离的杂质,再将预处理后的催化剂进行破碎细磨;Step (1): first pretreating the spent catalyst to remove the metal shell and easily separated impurities on the surface of the spent catalyst, and then crushing and finely grinding the pretreated catalyst;

步骤(2):制备混合熔剂:将铁粉、碳粉和氧化钙按质量比为2~3:1~3:12~30混合均匀备用;Step (2): Prepare mixed flux: mix iron powder, carbon powder and calcium oxide in a mass ratio of 2 to 3:1 to 3:12 to 30 evenly for later use;

步骤(3):将细磨后的催化剂和混合熔剂混合后加入等离子体电弧炉中进行加热,逐渐升温至1773K~2073K,充分搅拌至完全熔化,通过高温造渣后,铁粉作为铂族金属铂钯铑(Pt、Pd、Rh)的捕集剂会将铂族金属捕捉形成铂钯铑液态铁合金,液态铁合金的比重比较重,会沉降在熔体的下层,碳粉、氧化钙等助剂会熔解在熔渣中,熔渣比重轻,会漂浮在铁合金上方形成渣层;Step (3): After mixing the finely ground catalyst and mixed flux, add it to the plasma arc furnace for heating, gradually raise the temperature to 1773K-2073K, stir fully until it is completely melted, and after high-temperature slagging, iron powder is used as platinum group metal Platinum-palladium-rhodium (Pt, Pd, Rh) collectors will capture platinum group metals to form platinum-palladium-rhodium liquid iron alloy, which has a relatively heavy specific gravity and will settle in the lower layer of the melt. Additives such as carbon powder and calcium oxide It will be melted in the slag, which has a light specific gravity and will float above the ferroalloy to form a slag layer;

步骤(4):对熔体逐步降温冷却至室温,得到富集铂族金属的铁合金,及熔剂渣体。将分层后的液态铁合金和溶剂渣体降温固化后,即可进行分离,可用磁选的方法回收溶剂渣体中的少量磁性物料。Step (4): gradually lowering the temperature of the melt to room temperature to obtain a ferroalloy enriched in platinum group metals and flux slag. After the layered liquid iron alloy and solvent slag are cooled and solidified, they can be separated, and a small amount of magnetic materials in the solvent slag can be recovered by magnetic separation.

上述技术方案中,所述步骤(1)中,将催化剂破碎细磨至颗粒粒径小于或等于200目,粉碎得越细,铁捕捉铂族金属越充分,且熔化的时间越短,可以节省造渣时间。In the above technical scheme, in the step (1), the catalyst is crushed and finely ground to a particle size of less than or equal to 200 mesh, the finer the crushing, the more sufficient the iron captures the platinum group metals, and the shorter the melting time, it can save Slagging time.

上述技术方案中,所述步骤(3)中,细磨后的催化剂和混合溶剂按质量比为5~15:1~3加入到等离子体电弧炉中。In the above technical solution, in the step (3), the finely ground catalyst and the mixed solvent are added to the plasma arc furnace at a mass ratio of 5-15:1-3.

上述技术方案中,所述步骤(3)中,在搅拌过程中不断地加入氧化钙直至造渣完成,氧化钙作为助熔剂,可降低熔渣的粘稠度,提高造渣效率。In the above technical solution, in the step (3), calcium oxide is continuously added during the stirring process until the slagging is completed, and the calcium oxide is used as a flux to reduce the viscosity of molten slag and improve the slagging efficiency.

实施例1Example 1

先切割除去废催化剂表面的金属外壳和易分离的膨胀棉等杂质,再将催化剂进行破碎细磨至100目;称取20g铁粉、10g碳粉和120g氧化钙、2250g催化剂混合均匀后加入等离子体电弧炉中进行加热,逐渐升温至1773K,充分搅拌至完全熔化,在搅拌过程中可以不断地缓慢加入氧化钙直至造渣完成,造渣时间为30min,通过高温造渣后,熔渣自动漂浮在上层,含铂族金属的液态合金比重较重沉在下层,故得到的熔体上层为渣层,下层为含铂族金属的液态合金层;对熔体逐步降温冷却至室温,渣层中的熔渣和合金层中的重金属会逐渐固化并分离,最终得到富集铂族金属的铁合金及熔剂渣体。对铁合金中的铂族金属铂钯铑分别进行含量检测,得到铂的回收率达到99.99%,钯的回收率达到99.22%,铑的回收率达到90.12%。First cut and remove impurities such as the metal shell on the surface of the spent catalyst and easily separated expanded cotton, and then crush and finely grind the catalyst to 100 mesh; weigh 20g of iron powder, 10g of carbon powder, 120g of calcium oxide, and 2250g of catalyst and mix them evenly before adding plasma Heating in a body electric arc furnace, gradually raising the temperature to 1773K, fully stirring until it is completely melted, during the stirring process, calcium oxide can be continuously and slowly added until the slagging is completed, and the slagging time is 30 minutes. In the upper layer, the specific gravity of the liquid alloy containing platinum group metals is relatively heavy and sinks in the lower layer, so the upper layer of the obtained melt is a slag layer, and the lower layer is a liquid alloy layer containing platinum group metals; the melt is gradually cooled to room temperature, and the slag layer The heavy metals in the molten slag and the alloy layer will gradually solidify and separate, and finally obtain the iron alloy and flux slag enriched in platinum group metals. The contents of the platinum group metals platinum, palladium and rhodium in the iron alloy are detected respectively, and the recovery rate of platinum reaches 99.99%, the recovery rate of palladium reaches 99.22%, and the recovery rate of rhodium reaches 90.12%.

实施例2Example 2

先切割除去废催化剂表面的金属外壳和易分离的膨胀棉等杂质,再将催化剂进行破碎细磨至100目;称取30g铁粉、30g碳粉和300g氧化钙、700g催化剂混合均匀后加入等离子体电弧炉中进行加热,逐渐升温至2073K,充分搅拌至完全熔化,在搅拌过程中可以不断地缓慢加入氧化钙直至造渣完成,造渣时间为20min,通过高温造渣后,熔渣自动漂浮在上层,含铂族金属的液态合金比重较重沉在下层,故得到的熔体上层为渣层,下层为含铂族金属的液态合金层;对熔体逐步降温冷却至室温,渣层中的熔渣和合金层中的重金属会逐渐固化并分离,最终得到富集铂族金属的铁合金及熔剂渣体。对铁合金中的铂族金属铂钯铑分别进行含量检测,得到铂的回收率达到99.99%,钯的回收率达到99.42%,铑的回收率达到90.52%。First cut and remove impurities such as the metal shell on the surface of the spent catalyst and easily separated expanded cotton, and then crush and finely grind the catalyst to 100 mesh; weigh 30g of iron powder, 30g of carbon powder, 300g of calcium oxide, and 700g of catalyst and mix them evenly before adding plasma Heating in a body electric arc furnace, gradually raising the temperature to 2073K, fully stirring until it is completely melted, during the stirring process, calcium oxide can be continuously and slowly added until the slagging is completed, the slagging time is 20min, and the slag will automatically float after the high temperature slagging In the upper layer, the specific gravity of the liquid alloy containing platinum group metals is relatively heavy and sinks in the lower layer, so the upper layer of the obtained melt is a slag layer, and the lower layer is a liquid alloy layer containing platinum group metals; the melt is gradually cooled to room temperature, and the slag layer The heavy metals in the molten slag and the alloy layer will gradually solidify and separate, and finally obtain the iron alloy and flux slag enriched in platinum group metals. The contents of the platinum group metals platinum, palladium and rhodium in the iron alloy are detected respectively, and the recovery rate of platinum reaches 99.99%, the recovery rate of palladium reaches 99.42%, and the recovery rate of rhodium reaches 90.52%.

实施例3Example 3

先切割除去废催化剂表面的金属外壳和易分离的膨胀棉等杂质,再将催化剂进行破碎细磨至200目;称取20g铁粉、20g碳粉和120g氧化钙、1200g催化剂混合均匀后加入等离子体电弧炉中进行加热,逐渐升温至1873K,充分搅拌至完全熔化,在搅拌过程中可以不断地缓慢加入氧化钙直至造渣完成,造渣时间为30min,通过高温造渣后,熔渣自动漂浮在上层,含铂族金属的液态合金比重较重沉在下层,故得到的熔体上层为渣层,下层为含铂族金属的液态合金层;对熔体逐步降温冷却至室温,渣层中的熔渣和合金层中的重金属会逐渐固化并分离,最终得到富集铂族金属的铁合金及熔剂渣体。对铁合金中的铂族金属铂钯铑分别进行含量检测,得到铂的回收率达到99.99%,钯的回收率达到99.62%,铑的回收率达到90.52%。First cut and remove impurities such as the metal shell on the surface of the spent catalyst and easily separated expanded cotton, and then crush and finely grind the catalyst to 200 mesh; weigh 20g of iron powder, 20g of carbon powder, 120g of calcium oxide, and 1200g of catalyst and mix them evenly before adding plasma Heating in a solid electric arc furnace, gradually raising the temperature to 1873K, fully stirring until completely melted, during the stirring process, calcium oxide can be continuously and slowly added until the slagging is completed, and the slagging time is 30 minutes. After slagging at high temperature, the slag will automatically float In the upper layer, the specific gravity of the liquid alloy containing platinum group metals is relatively heavy and sinks in the lower layer, so the upper layer of the obtained melt is a slag layer, and the lower layer is a liquid alloy layer containing platinum group metals; the melt is gradually cooled to room temperature, and the slag layer The heavy metals in the molten slag and the alloy layer will gradually solidify and separate, and finally obtain the iron alloy and flux slag enriched in platinum group metals. The contents of the platinum group metals platinum, palladium and rhodium in the iron alloy are detected respectively, and the recovery rate of platinum reaches 99.99%, the recovery rate of palladium reaches 99.62%, and the recovery rate of rhodium reaches 90.52%.

以上所述,仅是本发明的较佳实施例而已,并非对本发明的技术范围作出任何限制,故凡是依据本发明的技术实质对以上实施例所作的任何细微修改、等同变化与修饰,均仍属于本发明的技术方案范围内。The above description is only a preferred embodiment of the present invention, and does not make any limitation to the technical scope of the present invention, so any minor modifications, equivalent changes and modifications made to the above embodiments according to the technical essence of the present invention are still valid. It belongs to the scope of the technical solution of the present invention.

Claims (4)

1.一种汽车废催化剂火法回收铂族金属的方法,其特征在于,包括以下步骤:1. A method for reclaiming platinum group metals by fire method of automobile waste catalyst, is characterized in that, comprises the following steps: 步骤(1):先将废催化剂进行预处理,除去废催化剂表面的金属外壳和易分离的杂质,再将预处理后的催化剂进行破碎细磨;Step (1): first pretreating the spent catalyst to remove the metal shell and easily separated impurities on the surface of the spent catalyst, and then crushing and finely grinding the pretreated catalyst; 步骤(2):制备混合熔剂:将铁粉、碳粉和氧化钙按质量比为2~3:1~3:12~30混合均匀备用;Step (2): Prepare mixed flux: mix iron powder, carbon powder and calcium oxide in a mass ratio of 2 to 3:1 to 3:12 to 30 evenly for later use; 步骤(3):将细磨后的催化剂和混合熔剂混合后加入等离子体电弧炉中进行加热,逐渐升温至1773K~2073K,充分搅拌至完全熔化,通过高温造渣后,得到的熔体上层为渣层,下层为含铂族金属的液态合金层;Step (3): After mixing the finely ground catalyst and mixed flux, add it to the plasma arc furnace for heating, gradually raise the temperature to 1773K ~ 2073K, fully stir until it is completely melted, and after high temperature slagging, the upper layer of the obtained melt is Slag layer, the lower layer is a liquid alloy layer containing platinum group metals; 步骤(4):对熔体逐步降温冷却至室温,得到富集铂族金属的铁合金,及熔剂渣体。Step (4): gradually lowering the temperature of the melt to room temperature to obtain a ferroalloy enriched in platinum group metals and flux slag. 2.如权利要求1所述的汽车废催化剂火法回收铂族金属的方法,其特征在于:所述步骤(1)中,将催化剂破碎细磨至颗粒粒径小于或等于200目。2. The method for recovering platinum group metals from waste automobile catalysts by fire method according to claim 1, characterized in that: in the step (1), the catalyst is crushed and finely ground until the particle size is less than or equal to 200 mesh. 3.如权利要求1所述的汽车废催化剂火法回收铂族金属的方法,其特征在于:所述步骤(3)中,细磨后的催化剂和混合溶剂按质量比为5~15:1~3加入到等离子体电弧炉中。3. The method for recovering platinum group metals by fire method of waste automobile catalyst as claimed in claim 1, characterized in that: in the step (3), the finely ground catalyst and the mixed solvent are in a mass ratio of 5 to 15:1 ~3 into the plasma arc furnace. 4.如权利要求1所述的汽车废催化剂火法回收铂族金属的方法,其特征在于:所述步骤(3)中,在搅拌过程中不断地加入氧化钙直至造渣完成。4. The method for recovering platinum group metals by fire from automobile waste catalysts as claimed in claim 1, characterized in that: in the step (3), calcium oxide is continuously added during the stirring process until the slagging is completed.
CN201610883402.XA 2016-10-10 2016-10-10 Method for recovering platinum group metal through car dead catalyst pyrogenic process Pending CN106381395A (en)

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CN109338107A (en) * 2018-11-12 2019-02-15 五邑大学 Method for comprehensive recovery of waste three-way catalysts for environmental protection and recycling
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