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 PDFInfo
- 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
- Authority
- CN
- China
- Prior art keywords
- platinum group
- catalyst
- group metals
- slag
- flux
- 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.)
- Pending
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
- 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
- C22B11/00—Obtaining noble metals
- C22B11/02—Obtaining noble metals by dry processes
- C22B11/021—Recovery of noble metals from waste materials
- C22B11/026—Recovery of noble metals from waste materials from spent catalysts
-
- 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
- Chemical & Material Sciences (AREA)
- 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
Description
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)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610883402.XA CN106381395A (en) | 2016-10-10 | 2016-10-10 | Method for recovering platinum group metal through car dead catalyst pyrogenic process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610883402.XA CN106381395A (en) | 2016-10-10 | 2016-10-10 | Method for recovering platinum group metal through car dead catalyst pyrogenic process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106381395A true CN106381395A (en) | 2017-02-08 |
Family
ID=57937219
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610883402.XA Pending CN106381395A (en) | 2016-10-10 | 2016-10-10 | Method for recovering platinum group metal through car dead catalyst pyrogenic process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106381395A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108950233A (en) * | 2018-06-27 | 2018-12-07 | 北京科技大学 | A method of rhodium is recycled from inactivation rhodium-containing homogeneous catalyst |
| 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 |
| CN110863104A (en) * | 2019-11-28 | 2020-03-06 | 北京科技大学 | Method for trapping agglomerate by using platinum group metal-containing waste catalyst iron |
| CN112342397A (en) * | 2020-11-06 | 2021-02-09 | 达塔仕南通信息科技有限公司 | Method for recovering metal platinum from platinum-carbon catalyst |
| CN113621828A (en) * | 2021-09-01 | 2021-11-09 | 南京德普瑞克环保科技股份公司 | Method for rapidly recovering precious metals from used three-way catalyst |
| CN114959292A (en) * | 2022-05-30 | 2022-08-30 | 广东先导稀材股份有限公司 | Method for enriching platinum group metals in zirconia slag by low-temperature pyrogenic process |
| CN115247231A (en) * | 2022-07-29 | 2022-10-28 | 贵研资源(易门)有限公司 | Method for separating platinum group metal-containing coating in waste automobile tail gas metal carrier catalyst |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5794533A (en) * | 1980-11-20 | 1982-06-12 | Engelhard Corp | Recovery of noble metal |
| CN102534226A (en) * | 2012-03-09 | 2012-07-04 | 干方良 | Method for extracting precious metal from spent automobile catalyst by concentration smelting-wet separation process |
| CN102796877A (en) * | 2012-08-27 | 2012-11-28 | 贵研铂业股份有限公司 | Method for enriching rhodium from rhodium-containing organic dead catalyst |
| CN103014352A (en) * | 2013-01-08 | 2013-04-03 | 昆明贵金属研究所 | Method for smelting and extracting platinum metal from alumina-supported petrochemical catalyst |
| CN103334010A (en) * | 2013-07-15 | 2013-10-02 | 贵研资源(易门)有限公司 | Method for fusing enriched precious metal from spent automotive catalyst |
| CN105861838A (en) * | 2015-01-23 | 2016-08-17 | 昆明冶金高等专科学校 | Method for enriching platinum from fluorine-containing failure platinum catalyst |
-
2016
- 2016-10-10 CN CN201610883402.XA patent/CN106381395A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5794533A (en) * | 1980-11-20 | 1982-06-12 | Engelhard Corp | Recovery of noble metal |
| CN102534226A (en) * | 2012-03-09 | 2012-07-04 | 干方良 | Method for extracting precious metal from spent automobile catalyst by concentration smelting-wet separation process |
| CN102796877A (en) * | 2012-08-27 | 2012-11-28 | 贵研铂业股份有限公司 | Method for enriching rhodium from rhodium-containing organic dead catalyst |
| CN103014352A (en) * | 2013-01-08 | 2013-04-03 | 昆明贵金属研究所 | Method for smelting and extracting platinum metal from alumina-supported petrochemical catalyst |
| CN103334010A (en) * | 2013-07-15 | 2013-10-02 | 贵研资源(易门)有限公司 | Method for fusing enriched precious metal from spent automotive catalyst |
| CN105861838A (en) * | 2015-01-23 | 2016-08-17 | 昆明冶金高等专科学校 | Method for enriching platinum from fluorine-containing failure platinum catalyst |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108950233A (en) * | 2018-06-27 | 2018-12-07 | 北京科技大学 | A method of rhodium is recycled from inactivation rhodium-containing homogeneous catalyst |
| 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 |
| CN110863104A (en) * | 2019-11-28 | 2020-03-06 | 北京科技大学 | Method for trapping agglomerate by using platinum group metal-containing waste catalyst iron |
| CN110863104B (en) * | 2019-11-28 | 2021-04-13 | 北京科技大学 | Method for trapping agglomerate by using platinum group metal-containing waste catalyst iron |
| CN112342397A (en) * | 2020-11-06 | 2021-02-09 | 达塔仕南通信息科技有限公司 | Method for recovering metal platinum from platinum-carbon catalyst |
| CN112342397B (en) * | 2020-11-06 | 2023-11-28 | 达塔仕南通信息科技有限公司 | A method for recovering metallic platinum from platinum carbon catalyst |
| CN113621828A (en) * | 2021-09-01 | 2021-11-09 | 南京德普瑞克环保科技股份公司 | Method for rapidly recovering precious metals from used three-way catalyst |
| CN114959292A (en) * | 2022-05-30 | 2022-08-30 | 广东先导稀材股份有限公司 | Method for enriching platinum group metals in zirconia slag by low-temperature pyrogenic process |
| CN114959292B (en) * | 2022-05-30 | 2024-05-24 | 广东先导稀材股份有限公司 | A method for low-temperature pyrometallurgical enrichment of platinum group metals in zirconium oxide slag |
| CN115247231A (en) * | 2022-07-29 | 2022-10-28 | 贵研资源(易门)有限公司 | Method for separating platinum group metal-containing coating in waste automobile tail gas metal carrier catalyst |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106381395A (en) | Method for recovering platinum group metal through car dead catalyst pyrogenic process | |
| CN101509077B (en) | Method for extracting platinum, palladium, rhodium from automotive catalyst of ore phase reconstruction | |
| CN102534226B (en) | Method for extracting precious metal from spent automobile catalyst by concentration smelting-wet separation process | |
| CN108441647A (en) | A kind of method that pyrogenic process recycles noble metal platinum in automobile dead catalyst | |
| KR101226612B1 (en) | A method for concentrating and recovering precious metals from spent mobile phone pcbs and spent auto-catalysts using waste nonferrous slag | |
| CN107400784A (en) | A kind of method that platinum group metal is reclaimed from spent auto-catalysts | |
| CN104178634A (en) | Method for efficiently and cleanly recovering platinum group metals from spent automobile catalyst | |
| CN110257642A (en) | A kind of resource utilization method of secondary aluminium alloy ash | |
| CN106011477A (en) | Method for recycling platinum group metal from ineffective automobile catalysts | |
| CN105861851A (en) | Method for enriching platinum group metal secondary resource with high efficiency | |
| CN104988314A (en) | Method of recovering platinum group metals based on copper capture | |
| CN107557587A (en) | A kind of method of microwave heating melting trapping platinum group metal | |
| CN104313336B (en) | Zinc-containing pyrite cinder processing method | |
| CN106282568A (en) | A kind of method being enriched with platinum group metal from spent automotive exhaust catalysts metallic carrier | |
| CN116043028B (en) | A method for recovering platinum group metals from automobile waste catalysts using nickel-iron tailings as flux | |
| CN116555581A (en) | A method for adding cobalt sulfate to smelting and trapping platinum group metals in ruthenium residue | |
| CN106834765B (en) | A method of preparing silicon-containing alloy with the silicon carbide cutting waste material of crystalline silicon | |
| CN114058852B (en) | Method for co-processing copper-containing electroplating sludge and spent automobile catalyst | |
| CN109402316B (en) | Financial-division comprehensive recovery method for rapidly reducing supergravity slag from neodymium-iron-boron waste acid leaching slag | |
| CN113245347B (en) | Impurity removing method for solid waste of silicate and application thereof | |
| CN111705223B (en) | Method for co-processing lead glass and waste catalyst | |
| CN116814974A (en) | Method for recovering platinum group metals in spent automobile catalysts using ferronickel tailings as flux and fire method | |
| CN101082093A (en) | Method for remelting and circulating utilization of waste foamed aluminium | |
| CN102643994A (en) | Waste cathode-ray tube cone glass machinery activation wet-process sulphur treatment method | |
| CN114774705A (en) | A method for recovering iron and zinc and preparing refractory raw materials by utilizing copper smelting slag |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170208 |
|
| RJ01 | Rejection of invention patent application after publication |