CN116177505A - A method for efficiently recovering indium and phosphorus in indium phosphide waste in a molten salt system - Google Patents

A method for efficiently recovering indium and phosphorus in indium phosphide waste in a molten salt system Download PDF

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CN116177505A
CN116177505A CN202310197897.0A CN202310197897A CN116177505A CN 116177505 A CN116177505 A CN 116177505A CN 202310197897 A CN202310197897 A CN 202310197897A CN 116177505 A CN116177505 A CN 116177505A
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phosphorus
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赵�卓
徐亮
姚超
葛涛
田勇攀
杨成
祝若鑫
韩琪
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Anhui University of Technology AHUT
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    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B25/00Phosphorus; Compounds thereof
    • C01B25/02Preparation of phosphorus
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    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
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    • 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
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Abstract

本发明属于有色金属冶金技术领域,具体涉及一种熔盐体系高效回收磷化铟废料中铟和磷的方法,该方法是在常压条件下,使磷化铟废料在熔盐体系中发生热分解,通过一步反应即可实现金属铟和单质磷的同步回收。本发明技术方案具有流程短、效率高、对设备要求低、成本低等特点,可以实现磷化铟废料的高效短流程综合回收;熔盐体系不参与化学反应,只是起到提供反应介质的作用,反应结束后回收的无机盐经简单的研磨、干燥处理后可以循环利用,整个反应过程理论上不消耗任何化学试剂,生产成本低,经济效益好;生产过程不产废气、废水、废渣,对环境友好。The invention belongs to the technical field of non-ferrous metal metallurgy, and specifically relates to a method for efficiently recovering indium and phosphorus in indium phosphide waste in a molten salt system. The method is to generate heat in a molten indium phosphide waste under normal pressure conditions. Decomposition, the simultaneous recovery of metal indium and elemental phosphorus can be realized through a one-step reaction. The technical scheme of the present invention has the characteristics of short process, high efficiency, low requirements for equipment, low cost, etc., and can realize the comprehensive recovery of indium phosphide waste with high efficiency and short process; the molten salt system does not participate in chemical reactions, but only serves as a reaction medium The inorganic salt recovered after the reaction can be recycled after simple grinding and drying treatment. The whole reaction process does not consume any chemical reagents in theory, the production cost is low, and the economic benefit is good; the production process does not produce waste gas, waste water, and waste residue. Environment friendly.

Description

一种熔盐体系高效回收磷化铟废料中铟和磷的方法A method for efficiently recovering indium and phosphorus in indium phosphide waste in a molten salt system

技术领域technical field

本发明属于有色金属冶金技术领域,具体涉及一种熔盐体系高效回收磷化铟废料中铟和磷的方法。The invention belongs to the technical field of nonferrous metal metallurgy, and in particular relates to a method for efficiently recovering indium and phosphorus in indium phosphide waste in a molten salt system.

背景技术Background technique

铟具有优异的物理化学性质,被广泛应用于半导体、电气元件、光电、通讯等领域。随着科技的进步和社会的发展,高新技术产业领域对铟的需求量逐年快速增加。然而,铟是一种稀散金属,地壳平均丰度仅为50-200ppb。铟在自然界中没有独立矿床,主要伴生于硫化锌矿石中,因此常以锌冶炼的副产品获得,但是铟在硫化锌矿中的含量也仅为1-100ppm。因此,铟的自然资源非常有限,难以满足行业对铟日益增长的需求,从二次资源中回收铟将是对有限铟一次资源的重要补充。Indium has excellent physical and chemical properties and is widely used in semiconductors, electrical components, optoelectronics, communications and other fields. With the progress of science and technology and the development of society, the demand for indium in the field of high-tech industries is increasing rapidly year by year. However, indium is a sparse metal with an average abundance in the earth's crust of only 50-200 ppb. Indium has no independent deposits in nature, and is mainly associated with zinc sulfide ore, so it is often obtained as a by-product of zinc smelting, but the content of indium in zinc sulfide ore is only 1-100ppm. Therefore, the natural resources of indium are very limited, and it is difficult to meet the industry's growing demand for indium. Recovering indium from secondary resources will be an important supplement to the limited indium primary resources.

磷化铟(InP)是一种重要的III-V族化合物半导体材料,具有较宽的禁带宽度、直接跃迁型能带结构、抗辐射能力强、电子迁移率高等优异的特性,广泛用于光纤通信、太阳能电池、集成电路以及高速高频器件等高新技术领域。然而,磷化铟脆性强、硬度低,在生产InP器件过程中报废率高达70%左右。另一方面,随着半导体行业的快速发展,磷化铟半导体器件也将大量更新迭代,产生大量磷化铟废料。因此,磷化铟废料是一种重要的铟二次资源,其高效综合回收对相关行业的可持续发展具有重要意义。Indium phosphide (InP) is an important III-V compound semiconductor material. It has excellent characteristics such as wide band gap, direct transition energy band structure, strong radiation resistance, and high electron mobility. It is widely used in High-tech fields such as optical fiber communication, solar cells, integrated circuits, and high-speed high-frequency devices. However, indium phosphide is brittle and has low hardness, and the scrap rate is as high as about 70% in the process of producing InP devices. On the other hand, with the rapid development of the semiconductor industry, a large number of indium phosphide semiconductor devices will be updated and iterated, resulting in a large amount of indium phosphide waste. Therefore, indium phosphide waste is an important secondary resource of indium, and its efficient and comprehensive recovery is of great significance to the sustainable development of related industries.

目前,关于磷化铟废料回收的研究相对有限。经检索:Currently, research on the recycling of indium phosphide scrap is relatively limited. Searched:

公开号为CN106586988B的中国专利文献公开了一种从磷化铟废料中综合回收铟和磷的方法,将磷化铟废料粉末置于真空管式炉中,在高温和真空条件下使磷化铟分解为铟和磷蒸汽,进一步对二者进行分别回收。该方法虽能实现磷化铟废料的短流程综合回收,但生产过程需要在高温、真空条件下实现,不仅能耗高,且需用到投资成本较高的真空冶炼设备,生产成本较高。The Chinese patent document with the publication number CN106586988B discloses a method for comprehensively recovering indium and phosphorus from indium phosphide waste. The indium phosphide waste powder is placed in a vacuum tube furnace to decompose indium phosphide under high temperature and vacuum conditions. Indium and phosphorus vapors are further recovered separately. Although this method can realize the short-process comprehensive recovery of indium phosphide waste, the production process needs to be realized under high temperature and vacuum conditions, which not only consumes high energy, but also requires the use of vacuum smelting equipment with high investment costs, resulting in high production costs.

公开号为CN106319224B的中国专利文献公开了一种磷化铟废料中回收铟的方法,采用浓盐酸和氯酸钠作为浸出剂使磷化铟废料充分溶解,进一步向浸出液中加入锌粉置换得到海绵铟。该工艺虽能有效从磷化铟废料中回收金属铟,但高酸度条件下的氯离子浸出体系不仅对设备腐蚀严重,且易挥发氯化氢气体污染生产环境;此外,采用锌粉置换铟的热力学推动力有限,过量的锌粉加入会降低海绵铟产品的纯度,且锌粉属于易制爆的管制类试剂,生产安全风险较高。The Chinese patent literature with the publication number CN106319224B discloses a method for recovering indium from indium phosphide waste. Concentrated hydrochloric acid and sodium chlorate are used as leaching agents to fully dissolve the indium phosphide waste, and zinc powder is further added to the leaching solution to replace it to obtain a sponge. indium. Although this process can effectively recover metal indium from indium phosphide waste, the chlorine ion leaching system under high acidity conditions not only severely corrodes the equipment, but also pollutes the production environment with volatile hydrogen chloride gas; in addition, the thermodynamic promotion of replacing indium with zinc powder The strength is limited, and the addition of excessive zinc powder will reduce the purity of the sponge indium product, and the zinc powder is a controlled reagent that is prone to explosives, and the production safety risk is high.

公开号为CN114380323A的中国专利文献公开了一种磷化铟中铟的回收方法,将磷化铟粉末与铁粉混合均匀后,在高温下进行固相反应,进一步通入氯化氢气体使铟选择性氯化生成易挥发的氯化铟,最后在气相中进行冷凝回收InCl3。该方法回收得到的氯化铟纯度较高,但整个回收工艺流程长、操作复杂、对设备要求高,且铟是以氯化铟的形式回收,需经进一步处理才能得到金属铟产品。The Chinese patent document with the publication number CN114380323A discloses a method for recovering indium in indium phosphide. After mixing indium phosphide powder and iron powder evenly, a solid phase reaction is carried out at high temperature, and hydrogen chloride gas is further introduced to make indium selective. Chlorination produces volatile indium chloride, and finally condenses in the gas phase to recover InCl 3 . The indium chloride recovered by this method has a high purity, but the whole recovery process is long, the operation is complicated, and the requirements for equipment are high, and the indium is recovered in the form of indium chloride, which requires further processing to obtain metal indium products.

综上所述,现有的磷化铟废料回收工艺仍有较大的优化和提升空间,有必要进一步开发操作简单、流程短、效率高、成本低、对环境友好的磷化铟废料综合回收工艺技术,支撑相关行业的可持续发展。In summary, the existing indium phosphide waste recycling process still has a lot of room for optimization and improvement, and it is necessary to further develop comprehensive recycling of indium phosphide waste with simple operation, short process, high efficiency, low cost, and environmental friendliness Process technology supports the sustainable development of related industries.

发明内容Contents of the invention

本发明的目的在于克服现有磷化铟废料综合回收工艺流程长、对设备要求高、效率低、生产成本高等问题,提供了一种熔盐体系高效回收磷化铟废料中铟和磷的方法。本发明的工艺技术具有流程短、效率高、对设备要求低、成本低等特点,可以实现磷化铟废料的高效短流程综合回收。The purpose of the present invention is to overcome the existing problems of long comprehensive recycling process of indium phosphide waste, high requirements on equipment, low efficiency, high production cost, etc., and provide a method for efficiently recycling indium and phosphorus in indium phosphide waste in a molten salt system . The process technology of the present invention has the characteristics of short flow, high efficiency, low requirements on equipment, low cost, etc., and can realize comprehensive recovery of indium phosphide waste with high efficiency and short flow.

为实现上述技术目的,达到上述技术效果,本发明是通过以下技术方案实现:In order to achieve the above-mentioned technical purpose and achieve the above-mentioned technical effect, the present invention is realized through the following technical solutions:

一种熔盐体系高效回收磷化铟废料中铟和磷的方法,在常压条件下,使磷化铟废料在熔盐体系中发生热分解,通过一步反应实现金属铟和单质磷的同步回收。A method for efficiently recovering indium and phosphorus in indium phosphide waste in a molten salt system. Under normal pressure, the indium phosphide waste is thermally decomposed in the molten salt system, and the simultaneous recovery of metal indium and elemental phosphorus is realized through a one-step reaction .

进一步地,具体操作包括如下步骤:Further, the specific operation includes the following steps:

1)将磷化铟废料粉末与无机盐体系按比例混合均匀;1) mixing the indium phosphide waste powder and the inorganic salt system in proportion;

2)将混合物置于管式炉中,升温至预定温度并恒温反应一段时间,整个过程在流动的惰性气氛保护条件下进行,生成的液态金属铟存在于熔盐中,而单质磷则随保护气体进入冷凝区,回收单质磷;2) Put the mixture in a tube furnace, raise the temperature to a predetermined temperature and react at a constant temperature for a period of time. The whole process is carried out under the protection of a flowing inert atmosphere. The liquid metal indium produced exists in the molten salt, and the elemental phosphorus is with the protection. The gas enters the condensation zone to recover elemental phosphorus;

3)反应结束后随炉冷却,将凝固的无机盐与金属铟分离,金属铟经洗涤、干燥后,得到金属铟产品;分离后的无机盐可循环使用。3) After the reaction is completed, cool with the furnace, and separate the solidified inorganic salt from the metal indium. After the metal indium is washed and dried, a metal indium product is obtained; the separated inorganic salt can be recycled.

进一步地,步骤1)中,所述磷化铟废料预先球磨至粒径≤300μm。Further, in step 1), the indium phosphide waste is pre-ball milled to a particle size of ≤300 μm.

进一步地,步骤1)中,所述无机盐体系为MClx-NCly二元共晶盐,其中,M和N为Li、Na、K、Ca中的任两种,x和y的值为1或2。Further, in step 1), the inorganic salt system is MCl x -NCl y binary eutectic salt, wherein M and N are any two of Li, Na, K, and Ca, and the values of x and y are 1 or 2.

进一步地,步骤1)中,所述无机盐体系和磷化铟废料的质量比控制在5-50:1。Further, in step 1), the mass ratio of the inorganic salt system to the indium phosphide waste is controlled at 5-50:1.

进一步地,步骤2)中,所述预定温度为MClx-NCly二元共晶盐的共晶点以上50-100℃,升温速率为5-30℃/min;升温至预定温度后,恒温反应时间为1-10h。Further, in step 2), the predetermined temperature is 50-100°C above the eutectic point of MCl x -NCly binary eutectic salt, and the heating rate is 5-30°C/min; The reaction time is 1-10h.

进一步地,步骤2)中,所述惰性保护气体为氩气、氮气、氦气中的一种,气体流速为1-5L/min。Further, in step 2), the inert protective gas is one of argon, nitrogen, and helium, and the gas flow rate is 1-5 L/min.

进一步地,步骤2)中,所述冷凝区回收单质磷的温度控制在50-90℃。Further, in step 2), the temperature of recovering elemental phosphorus in the condensation zone is controlled at 50-90°C.

进一步地,步骤3)中,采用去离子水对回收的金属铟进行洗涤4-8次。Further, in step 3), the recovered metal indium is washed 4-8 times with deionized water.

进一步地,步骤3)中,洗涤后的金属铟在60-100℃下干燥24-72h,得到金属铟产品。Further, in step 3), the washed metal indium is dried at 60-100° C. for 24-72 hours to obtain a metal indium product.

本发明的有益效果是:The beneficial effects of the present invention are:

1、本发明的一种熔盐体系高效回收磷化铟废料中铟和磷的方法,在熔盐体系中对磷化铟废料进行热分解,通过一步反应即可实现金属铟和单质磷的同步回收,生产流程短、效率高,可以实现磷化铟废料的高效短流程综合回收。1. A method for efficiently recovering indium and phosphorus in indium phosphide waste in a molten salt system of the present invention, in which the indium phosphide waste is thermally decomposed in the molten salt system, and the synchronization of metal indium and elemental phosphorus can be realized through a one-step reaction Recycling, short production process and high efficiency, can realize comprehensive recycling of indium phosphide waste with high efficiency and short process.

2、本发明的一种熔盐体系高效回收磷化铟废料中铟和磷的方法,熔盐介质可以为反应过程提供类真空的无氧环境,使得磷化铟废料热分解回收金属铟和单质磷的过程在常压条件下即可实现,采用冶金行业常用的普通管式炉即可达到预期效果,无需使用传统方法中所必须的真空冶金设备,对设备要求低,可以大幅降低反应所需能耗和设备投资成本;另外,熔盐介质可以为反应过程提供微重力场环境,使磷化铟废料粉末在熔盐体系中充分均匀分散,有利于提高反应速率和转化率,金属铟和单质磷的回收率高。2. A method for efficiently recovering indium and phosphorus in indium phosphide waste in a molten salt system of the present invention. The molten salt medium can provide a vacuum-like oxygen-free environment for the reaction process, so that indium phosphide waste can be thermally decomposed to recover metal indium and elemental substances The process of phosphorus can be realized under normal pressure conditions, and the expected effect can be achieved by using ordinary tube furnaces commonly used in the metallurgical industry. There is no need to use vacuum metallurgical equipment necessary in traditional methods, and the requirements for equipment are low, which can greatly reduce the reaction requirements. Energy consumption and equipment investment cost; in addition, the molten salt medium can provide a microgravity field environment for the reaction process, so that the indium phosphide waste powder can be fully and uniformly dispersed in the molten salt system, which is conducive to improving the reaction rate and conversion rate. The recovery rate of phosphorus is high.

3、本发明的一种熔盐体系高效回收磷化铟废料中铟和磷的方法,熔盐体系不参与化学反应,只是起到提供反应介质的作用,反应结束后回收的无机盐经简单的研磨、干燥处理后可以循环利用,整个反应过程理论上不消耗任何化学试剂,生产成本低,经济效益好;生产过程不产废气、废水、废渣,对环境友好。3. A method for efficiently reclaiming indium and phosphorus in indium phosphide waste in a molten salt system of the present invention. The molten salt system does not participate in chemical reactions, but only serves as a reaction medium. After the reaction, the recovered inorganic salt undergoes simple It can be recycled after grinding and drying. The whole reaction process theoretically does not consume any chemical reagents, with low production cost and good economic benefits. The production process does not produce waste gas, waste water, and waste residue, which is environmentally friendly.

当然,实施本发明的任一产品并不一定需要同时达到以上的所有优点。Of course, implementing any product of the present invention does not necessarily need to achieve all the above advantages at the same time.

具体实施方式Detailed ways

下面将对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有作出创造性劳动前提下所获得的所有其它实施例,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. Obviously, the described embodiments are only some of the embodiments of the present invention, but not all of them. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without creative efforts fall within the protection scope of the present invention.

本发明的相关具体实施例如下:Relevant specific embodiments of the present invention are as follows:

本发明提供了一种熔盐体系高效回收磷化铟废料中铟和磷的方法,在常压条件下,使磷化铟废料在熔盐体系中发生热分解,通过一步反应即可实现金属铟和单质磷的同步回收。本发明技术方案具有流程短、效率高、对设备要求低、成本低等特点,可以实现磷化铟废料的高效短流程综合回收。本发明的生产工艺具体包括以下步骤:The invention provides a method for efficiently recovering indium and phosphorus in indium phosphide waste in a molten salt system. Under normal pressure, the indium phosphide waste is thermally decomposed in the molten salt system, and metal indium can be realized through one-step reaction. and simultaneous recovery of elemental phosphorus. The technical scheme of the invention has the characteristics of short process, high efficiency, low requirements on equipment, low cost, etc., and can realize comprehensive recovery of indium phosphide waste materials in an efficient short process. Production technology of the present invention specifically comprises the following steps:

1)将预先球磨至300μm以下的磷化铟废料粉末与无机盐体系按比例混合均匀,无机盐体系组成为MClx-NCly(M,N=Li、Na、K、Ca;x,y=1或2)二元共晶盐,控制无机盐体系与磷化铟废料的质量比在5:1至50:1之间。1) Mix the indium phosphide waste powder that has been ball-milled to be below 300 μm in proportion with the inorganic salt system, and the inorganic salt system is composed of MCl x -NCl y (M, N = Li, Na, K, Ca; x, y = 1 or 2) Binary eutectic salt, controlling the mass ratio of the inorganic salt system to the indium phosphide waste between 5:1 and 50:1.

2)将混合物置于管式炉中,以5-30℃/min的速率升温至MClx-NCly二元混合体系共晶点以上50-100℃,并恒温反应1-10h,整个过程在流动的惰性气氛保护条件下进行,惰性保护气体为氩气、氮气、氦气中的一种,气体流速为1-5L/min,生成的液态金属铟存在于熔盐中,而单质磷则随保护气体进入温度为50-90℃的冷凝区,回收单质磷。2) Put the mixture in a tube furnace, raise the temperature to 50-100°C above the eutectic point of the MCl x -NCl y binary mixed system at a rate of 5-30°C/min, and react at a constant temperature for 1-10h. The whole process is at It is carried out under the protection condition of flowing inert atmosphere. The inert protection gas is one of argon, nitrogen and helium. The gas flow rate is 1-5L/min. The liquid metal indium generated exists in the molten salt, and the elemental phosphorus is The protective gas enters the condensation zone with a temperature of 50-90°C to recover elemental phosphorus.

3)反应结束后随炉冷却,将凝固的无机盐与金属铟分离,金属铟经去离子水洗涤4-8次后,在60-100℃下干燥24-72h,得到金属铟产品。3) Cool in the furnace after the reaction, separate the solidified inorganic salt from the metal indium, wash the metal indium 4-8 times with deionized water, and dry at 60-100°C for 24-72h to obtain the metal indium product.

下面结合具体实施例对本发明进一步进行描述。The present invention will be further described below in conjunction with specific embodiments.

实施例1Example 1

本实施例提供一种熔盐体系高效回收磷化铟废料中铟和磷的方法,具体包括以下步骤:This embodiment provides a method for efficiently recycling indium and phosphorus in indium phosphide waste in a molten salt system, which specifically includes the following steps:

1)将预先球磨至300μm以下的磷化铟废料粉末与LiCl-NaCl二元共晶盐混合均匀,控制无机盐体系与磷化铟废料的质量比为5:1。1) Mix the indium phosphide waste powder pre-milled to be below 300 μm with the LiCl-NaCl binary eutectic salt, and control the mass ratio of the inorganic salt system to the indium phosphide waste to be 5:1.

2)将混合物置于管式炉中,以30℃/min的速率升温至620℃,并恒温反应1h,整个过程在流动的氩气气氛保护条件下进行,气体流速为1L/min,生成的液态金属铟存在于熔盐中,而单质磷则随保护气体进入温度为50℃的冷凝区,回收单质磷。2) Put the mixture in a tube furnace, raise the temperature to 620°C at a rate of 30°C/min, and react at a constant temperature for 1h. The liquid metal indium exists in the molten salt, while the elemental phosphorus enters the condensation zone with a temperature of 50°C along with the protective gas to recover the elemental phosphorus.

3)反应结束后随炉冷却,将凝固的无机盐与金属铟分离,金属铟经去离子水洗涤4次后,在60℃下干燥72h,得到金属铟产品。3) Cool in the furnace after the reaction, separate the solidified inorganic salt from the metal indium, wash the metal indium four times with deionized water, and dry at 60°C for 72 hours to obtain the metal indium product.

采用本实施例的方法,通过王水溶解结合电感耦合等离子体质谱仪(ICP-MS)和X射线荧光光谱仪(XRF)分析金属铟和单质磷的回收率及纯度,结果为金属铟和单质磷的回收率分别为98.5%和97.8%,金属铟和单质磷的纯度分别为99.95%和99.23%。Using the method of this embodiment, the recovery rate and purity of metal indium and elemental phosphorus were analyzed by aqua regia dissolution combined with inductively coupled plasma mass spectrometer (ICP-MS) and X-ray fluorescence spectrometer (XRF), and the result was metal indium and elemental phosphorus The recoveries are 98.5% and 97.8%, respectively, and the purity of metal indium and elemental phosphorus are 99.95% and 99.23%, respectively.

实施例2Example 2

本实施例提供一种熔盐体系高效回收磷化铟废料中铟和磷的方法,具体包括以下步骤:This embodiment provides a method for efficiently recycling indium and phosphorus in indium phosphide waste in a molten salt system, which specifically includes the following steps:

1)将预先球磨至300μm以下的磷化铟废料粉末与LiCl-KCl二元共晶盐混合均匀,控制无机盐体系与磷化铟废料的质量比为50:1。1) Mix the indium phosphide waste powder pre-milled to be below 300 μm with the LiCl-KCl binary eutectic salt, and control the mass ratio of the inorganic salt system to the indium phosphide waste to 50:1.

2)将混合物置于管式炉中,以5℃/min的速率升温至450℃,并恒温反应10h,整个过程在流动的氮气气氛保护条件下进行,气体流速为5L/min,生成的液态金属铟存在于熔盐中,而单质磷则随保护气体进入温度为90℃的冷凝区,回收单质磷。2) Put the mixture in a tube furnace, heat up to 450°C at a rate of 5°C/min, and react at a constant temperature for 10 hours. The whole process is carried out under the protection of a flowing nitrogen atmosphere, and the gas flow rate is 5L/min. The resulting liquid Metal indium exists in molten salt, while elemental phosphorus enters the condensation zone with a temperature of 90°C along with the protective gas to recover elemental phosphorus.

3)反应结束后随炉冷却,将凝固的无机盐与金属铟分离,金属铟经去离子水洗涤8次后,在100℃下干燥24h,得到金属铟产品。3) Cool in the furnace after the reaction, separate the solidified inorganic salt from the metal indium, wash the metal indium 8 times with deionized water, and dry at 100° C. for 24 hours to obtain the metal indium product.

采用本实施例的方法,通过王水溶解结合电感耦合等离子体质谱仪(ICP-MS)和X射线荧光光谱仪(XRF)分析金属铟和单质磷的回收率及纯度,结果为金属铟和单质磷的回收率分别为97.6%和97.2%,金属铟和单质磷的纯度分别为99.93%和99.18%。Using the method of this embodiment, the recovery rate and purity of metal indium and elemental phosphorus were analyzed by aqua regia dissolution combined with inductively coupled plasma mass spectrometer (ICP-MS) and X-ray fluorescence spectrometer (XRF), and the result was metal indium and elemental phosphorus The recoveries were 97.6% and 97.2%, respectively, and the purity of metal indium and elemental phosphorus were 99.93% and 99.18%, respectively.

实施例3Example 3

本实施例提供一种熔盐体系高效回收磷化铟废料中铟和磷的方法,具体包括以下步骤:This embodiment provides a method for efficiently recycling indium and phosphorus in indium phosphide waste in a molten salt system, which specifically includes the following steps:

1)将预先球磨至300μm以下的磷化铟废料粉末与LiCl-CaCl2二元共晶盐混合均匀,控制无机盐体系与磷化铟废料的质量比为15:1。1) Mix the indium phosphide waste powder pre-milled to be below 300 μm with the LiCl-CaCl 2 binary eutectic salt, and control the mass ratio of the inorganic salt system to the indium phosphide waste to be 15:1.

2)将混合物置于管式炉中,以10℃/min的速率升温至550℃,并恒温反应3h,整个过程在流动的氦气气氛保护条件下进行,气体流速为2L/min,生成的液态金属铟存在于熔盐中,而单质磷则随保护气体进入温度为60℃的冷凝区,回收单质磷。2) Put the mixture in a tube furnace, raise the temperature to 550°C at a rate of 10°C/min, and react at a constant temperature for 3 hours. The whole process is carried out under the protection condition of a flowing helium atmosphere, and the gas flow rate is 2L/min. Liquid metal indium exists in molten salt, while elemental phosphorus enters the condensation zone with a temperature of 60°C along with the protective gas to recover elemental phosphorus.

3)反应结束后随炉冷却,将凝固的无机盐与金属铟分离,金属铟经去离子水洗涤5次后,在70℃下干燥60h,得到金属铟产品。3) Cool in the furnace after the reaction, separate the solidified inorganic salt from the metal indium, wash the metal indium five times with deionized water, and dry at 70°C for 60 hours to obtain the metal indium product.

采用本实施例的方法,通过王水溶解结合电感耦合等离子体质谱仪(ICP-MS)和X射线荧光光谱仪(XRF)分析金属铟和单质磷的回收率及纯度,结果为金属铟和单质磷的回收率分别为98.8%和98.2%,金属铟和单质磷的纯度分别为99.97%和99.36%。Using the method of this embodiment, the recovery rate and purity of metal indium and elemental phosphorus were analyzed by aqua regia dissolution combined with inductively coupled plasma mass spectrometer (ICP-MS) and X-ray fluorescence spectrometer (XRF), and the result was metal indium and elemental phosphorus The recoveries are 98.8% and 98.2%, respectively, and the purity of metal indium and elemental phosphorus are 99.97% and 99.36%, respectively.

实施例4Example 4

本实施例提供一种熔盐体系高效回收磷化铟废料中铟和磷的方法,具体包括以下步骤:This embodiment provides a method for efficiently recycling indium and phosphorus in indium phosphide waste in a molten salt system, which specifically includes the following steps:

1)将预先球磨至300μm以下的磷化铟废料粉末与NaCl-KCl二元共晶盐混合均匀,控制无机盐体系与磷化铟废料的质量比为30:1。1) Mix the indium phosphide waste powder pre-milled to be below 300 μm with the NaCl-KCl binary eutectic salt, and control the mass ratio of the inorganic salt system to the indium phosphide waste to be 30:1.

2)将混合物置于管式炉中,以15℃/min的速率升温至700℃,并恒温反应6h,整个过程在流动的氦气气氛保护条件下进行,气体流速为3L/min,生成的液态金属铟存在于熔盐中,而单质磷则随保护气体进入温度为70℃的冷凝区,回收单质磷。2) Put the mixture in a tube furnace, heat up to 700°C at a rate of 15°C/min, and react at a constant temperature for 6 hours. The whole process is carried out under the protection condition of a flowing helium atmosphere, and the gas flow rate is 3L/min. The generated Liquid metal indium exists in molten salt, while elemental phosphorus enters the condensation zone with a temperature of 70°C along with the protective gas to recover elemental phosphorus.

3)反应结束后随炉冷却,将凝固的无机盐与金属铟分离,金属铟经去离子水洗涤6次后,在80℃下干燥48h,得到金属铟产品。3) Cool in the furnace after the reaction, separate the solidified inorganic salt from the metal indium, wash the metal indium 6 times with deionized water, and dry at 80° C. for 48 hours to obtain the metal indium product.

采用本实施例的方法,通过王水溶解结合电感耦合等离子体质谱仪(ICP-MS)和X射线荧光光谱仪(XRF)分析金属铟和单质磷的回收率及纯度,结果为金属铟和单质磷的回收率分别为97.6%和96.8%,金属铟和单质磷的纯度分别为99.94%和99.46%。Using the method of this embodiment, the recovery rate and purity of metal indium and elemental phosphorus were analyzed by aqua regia dissolution combined with inductively coupled plasma mass spectrometer (ICP-MS) and X-ray fluorescence spectrometer (XRF), and the result was metal indium and elemental phosphorus The recoveries were 97.6% and 96.8%, respectively, and the purity of metal indium and elemental phosphorus were 99.94% and 99.46%, respectively.

实施例5Example 5

本实施例提供一种熔盐体系高效回收磷化铟废料中铟和磷的方法,具体包括以下步骤:This embodiment provides a method for efficiently recycling indium and phosphorus in indium phosphide waste in a molten salt system, which specifically includes the following steps:

1)将预先球磨至300μm以下的磷化铟废料粉末与NaCl-CaCl2二元共晶盐混合均匀,控制无机盐体系与磷化铟废料的质量比为40:1。1) Mix the indium phosphide waste powder pre-milled to be below 300 μm with the NaCl-CaCl 2 binary eutectic salt, and control the mass ratio of the inorganic salt system to the indium phosphide waste to 40:1.

2)将混合物置于管式炉中,以20℃/min的速率升温至550℃,并恒温反应8h,整个过程在流动的氩气气氛保护条件下进行,气体流速为4L/min,生成的液态金属铟存在于熔盐中,而单质磷则随保护气体进入温度为80℃的冷凝区,回收单质磷。2) Put the mixture in a tube furnace, raise the temperature to 550°C at a rate of 20°C/min, and react at a constant temperature for 8 hours. The whole process is carried out under the protection condition of a flowing argon atmosphere, and the gas flow rate is 4L/min. The liquid metal indium exists in the molten salt, while the elemental phosphorus enters the condensation zone with a temperature of 80°C along with the protective gas to recover the elemental phosphorus.

3)反应结束后随炉冷却,将凝固的无机盐与金属铟分离,金属铟经去离子水洗涤7次后,在90℃下干燥36h,得到金属铟产品。3) Cool in the furnace after the reaction, separate the solidified inorganic salt from the metal indium, wash the metal indium 7 times with deionized water, and dry at 90° C. for 36 hours to obtain the metal indium product.

采用本实施例的方法,通过王水溶解结合电感耦合等离子体质谱仪(ICP-MS)和X射线荧光光谱仪(XRF)分析金属铟和单质磷的回收率及纯度,结果为金属铟和单质磷的回收率分别为99.2%和98.7%,金属铟和单质磷的纯度分别为99.98%和99.38%。Using the method of this embodiment, the recovery rate and purity of metal indium and elemental phosphorus were analyzed by aqua regia dissolution combined with inductively coupled plasma mass spectrometer (ICP-MS) and X-ray fluorescence spectrometer (XRF), and the result was metal indium and elemental phosphorus The recoveries are 99.2% and 98.7%, respectively, and the purity of metal indium and elemental phosphorus are 99.98% and 99.38%, respectively.

以上公开的本发明优选实施例只是用于帮助阐述本发明。优选实施例并没有详尽叙述所有的细节,也不限制该发明仅为具体实施方式。显然,根据本说明书的内容,可作很多的修改和变化。本说明书选取并具体描述这些实施例,是为了更好地解释本发明的原理和实际应用,从而使所属技术领域技术人员能很好地理解和利用本发明。本发明仅受权利要求书及其全部范围和等效物的限制。The preferred embodiments of the invention disclosed above are only to help illustrate the invention. The preferred embodiments do not exhaust all details nor limit the invention to specific implementations. Obviously, many modifications and variations can be made based on the contents of this specification. This description selects and specifically describes these embodiments in order to better explain the principle and practical application of the present invention, so that those skilled in the art can well understand and utilize the present invention. The invention is to be limited only by the claims, along with their full scope and equivalents.

Claims (10)

1.一种熔盐体系高效回收磷化铟废料中铟和磷的方法,其特征在于,在常压条件下,使磷化铟废料在熔盐体系中发生热分解,通过一步反应实现金属铟和单质磷的同步回收。1. A method for efficiently reclaiming indium and phosphorus in indium phosphide waste in a molten salt system, characterized in that, under normal pressure conditions, the indium phosphide waste is thermally decomposed in the molten salt system, and metal indium is realized by one-step reaction and simultaneous recovery of elemental phosphorus. 2.根据权利要求1所述的一种熔盐体系高效回收磷化铟废料中铟和磷的方法,其特征在于,具体操作包括如下步骤:2. the method for efficiently reclaiming indium and phosphorus in a kind of molten salt system according to claim 1 in the indium phosphide waste material, is characterized in that, concrete operation comprises the steps: 1)将磷化铟废料粉末与无机盐体系按比例混合均匀;1) mixing the indium phosphide waste powder and the inorganic salt system in proportion; 2)将混合物置于管式炉中,升温至预定温度并恒温反应一段时间,整个过程在流动的惰性气氛保护条件下进行,生成的液态金属铟存在于熔盐中,而单质磷则随保护气体进入冷凝区,回收单质磷;2) Put the mixture in a tube furnace, raise the temperature to a predetermined temperature and react at a constant temperature for a period of time. The whole process is carried out under the protection of a flowing inert atmosphere. The liquid metal indium produced exists in the molten salt, and the elemental phosphorus is with the protection. The gas enters the condensation zone to recover elemental phosphorus; 3)反应结束后随炉冷却,将凝固的无机盐与金属铟分离,金属铟经洗涤、干燥后,得到金属铟产品;分离后的无机盐可循环使用。3) After the reaction is completed, cool with the furnace, and separate the solidified inorganic salt from the metal indium. After the metal indium is washed and dried, a metal indium product is obtained; the separated inorganic salt can be recycled. 3.根据权利要求2所述的一种熔盐体系高效回收磷化铟废料中铟和磷的方法,其特征在于:步骤1)中,所述磷化铟废料预先球磨至粒径≤300μm。3. A method for efficiently recovering indium and phosphorus in indium phosphide waste in a molten salt system according to claim 2, characterized in that in step 1), the indium phosphide waste is pre-ball milled to a particle size ≤ 300 μm. 4.根据权利要求2所述的一种熔盐体系高效回收磷化铟废料中铟和磷的方法,其特征在于:步骤1)中,所述无机盐体系为MClx-NCly二元共晶盐,其中,M和N为Li、Na、K、Ca中的任两种,x和y的值为1或2。4. the method for efficiently reclaiming indium and phosphorus in a kind of molten salt system according to claim 2, is characterized in that: in step 1), described inorganic salt system is MCl x -NCl y binary total A crystal salt, wherein M and N are any two of Li, Na, K, and Ca, and the values of x and y are 1 or 2. 5.根据权利要求4所述的一种熔盐体系高效回收磷化铟废料中铟和磷的方法,其特征在于:步骤1)中,所述无机盐体系和磷化铟废料的质量比控制在5-50:1。5. the method for efficiently reclaiming indium and phosphorus in a kind of molten salt system according to claim 4, is characterized in that: in step 1), the mass ratio control of described inorganic salt system and indium phosphide waste material In 5-50:1. 6.根据权利要求4所述的一种熔盐体系高效回收磷化铟废料中铟和磷的方法,其特征在于:步骤2)中,所述预定温度为MClx-NCly二元共晶盐的共晶点以上50-100℃,升温速率为5-30℃/min;升温至预定温度后,恒温反应时间为1-10h。6. The method for efficiently reclaiming indium and phosphorus in indium phosphide waste in a kind of molten salt system according to claim 4, characterized in that: in step 2), the predetermined temperature is MCl x -NCl y binary eutectic 50-100°C above the eutectic point of the salt, the heating rate is 5-30°C/min; after the temperature is raised to the predetermined temperature, the constant temperature reaction time is 1-10h. 7.根据权利要求2所述的一种熔盐体系高效回收磷化铟废料中铟和磷的方法,其特征在于:步骤2)中,所述惰性保护气体为氩气、氮气、氦气中的一种,气体流速为1-5L/min。7. The method for efficiently reclaiming indium and phosphorus in indium phosphide waste in a kind of molten salt system according to claim 2, characterized in that: in step 2), the inert protective gas is argon, nitrogen, helium One, the gas flow rate is 1-5L/min. 8.根据权利要求2所述的一种熔盐体系高效回收磷化铟废料中铟和磷的方法,其特征在于:步骤2)中,所述冷凝区回收单质磷的温度控制在50-90℃。8. A method for efficiently recycling indium and phosphorus in indium phosphide waste in a molten salt system according to claim 2, characterized in that: in step 2), the temperature for recovering elemental phosphorus in the condensation zone is controlled at 50-90 ℃. 9.根据权利要求2所述的一种熔盐体系高效回收磷化铟废料中铟和磷的方法,其特征在于:步骤3)中,采用去离子水对回收的金属铟进行洗涤4-8次。9. The method for efficiently reclaiming indium and phosphorus in indium phosphide waste in a molten salt system according to claim 2, characterized in that: in step 3), the recovered metal indium is washed with deionized water for 4-8 Second-rate. 10.根据权利要求2所述的一种熔盐体系高效回收磷化铟废料中铟和磷的方法,其特征在于:步骤3)中,洗涤后的金属铟在60-100℃下干燥24-72h,得到金属铟产品。10. A method for efficiently reclaiming indium and phosphorus in indium phosphide waste in a molten salt system according to claim 2, characterized in that: in step 3), the washed metal indium is dried at 60-100°C for 24- 72h, the indium metal product was obtained.
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