CN111592033A - A kind of preparation method of target grade gallium oxide - Google Patents
A kind of preparation method of target grade gallium oxide Download PDFInfo
- Publication number
- CN111592033A CN111592033A CN202010436819.8A CN202010436819A CN111592033A CN 111592033 A CN111592033 A CN 111592033A CN 202010436819 A CN202010436819 A CN 202010436819A CN 111592033 A CN111592033 A CN 111592033A
- Authority
- CN
- China
- Prior art keywords
- solution
- preparation
- gallium
- gallium oxide
- reaction
- 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
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G15/00—Compounds of gallium, indium or thallium
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/622—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/626—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/622—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/626—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
- C04B35/62605—Treating the starting powders individually or as mixtures
- C04B35/62645—Thermal treatment of powders or mixtures thereof other than sintering
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/30—Particle morphology extending in three dimensions
- C01P2004/32—Spheres
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/60—Particles characterised by their size
- C01P2004/61—Micrometer sized, i.e. from 1-100 micrometer
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/12—Surface area
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/80—Compositional purity
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Ceramic Engineering (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Catalysts (AREA)
Abstract
本发明涉及一种靶材级氧化镓的制备方法,属于半导体材料技术领域。本发明通过将A溶液和B溶液同时加入底液C溶液中,同时限定反应温度、A溶液和B溶液的浓度、A溶液和B溶液的加料速度、沉淀剂的种类,制备得到椭球形、粒度D50=1.5~2μm的氧化镓。本发明制备得到的氧化镓较棒状氧化镓具有较高的流动性和分散性,以满足靶材使用。且本发明制备得到的氧化镓具有以下特点:高比表面积,BET=10~15g/cm2;纯度高,可以达到99.995%;粒度小,D50=1.5~2μm。
The invention relates to a preparation method of target grade gallium oxide, and belongs to the technical field of semiconductor materials. The present invention prepares ellipsoid, particle size by simultaneously adding A solution and B solution into the bottom solution C solution, and simultaneously limiting the reaction temperature, the concentration of A solution and B solution, the feeding speed of A solution and B solution, and the type of precipitant. D50=1.5~2μm gallium oxide. The gallium oxide prepared by the present invention has higher fluidity and dispersibility than rod-shaped gallium oxide, so as to meet the target use. And the gallium oxide prepared by the invention has the following characteristics: high specific surface area, BET=10~15g/cm 2 ; high purity, which can reach 99.995%; small particle size, D50=1.5~2μm.
Description
技术领域technical field
本发明涉及一种靶材级氧化镓的制备方法,属于半导体材料技术领域。The invention relates to a preparation method of target grade gallium oxide, and belongs to the technical field of semiconductor materials.
背景技术Background technique
氧化镓(Ga2O3)是一种重要的宽禁带半导体材料,其具有五种晶体结构:α-Ga2O3、β-Ga2O3、γ-Ga2O3、ε-Ga2O3和δ-Ga2O3,在一定条件下可以相互转变。其中β-Ga2O3最为稳定,室温下呈单斜结构,空间结构为C2/m, β=103.83°。Ga2O3具有优良的光致发光性能、化学和热稳定性能等特性,广泛应用于敏材料、催化剂、光电子材料和荧光粉等领域。Gallium oxide (Ga 2 O 3 ) is an important wide-bandgap semiconductor material, which has five crystal structures: α-Ga 2 O 3 , β-Ga 2 O 3 , γ-Ga 2 O 3 , ε-Ga 2 O 3 and δ-Ga 2 O 3 can be transformed into each other under certain conditions. Among them, β-Ga 2 O 3 is the most stable, with a monoclinic structure at room temperature and a spatial structure of C2/m. β=103.83°. Ga 2 O 3 has excellent photoluminescence properties, chemical and thermal stability properties and other properties, and is widely used in the fields of sensitive materials, catalysts, optoelectronic materials and phosphors.
近年来,IGZO(氧化铟镓锌)在TFT-LCD显示器领域的应用,使得晶体管数量减少,提高了每个像素的透光率,使得显示器具有更高的能效水平,且效率更高。目前,射频/直流电(RF/DC)溅镀系统是主流的薄膜生长设备,影响溅镀透明导电薄膜品质的因素除了薄膜沉积工艺外,靶材的密度、导电性、晶粒大小、微结构与纯度起着至关重要的作用。例如靶材的密度低,即靶材表面或内部有微孔,镀膜过程会在靶材表面出现凸起,引起靶材局部能量过高,氧离子被撞击成游离态,形成高电阻区域,导致一些微颗粒进入薄膜中,降低薄膜品质,因此影响镀膜制成的稳定性。In recent years, the application of IGZO (Indium Gallium Zinc Oxide) in the field of TFT-LCD displays has reduced the number of transistors and improved the light transmittance of each pixel, resulting in a display with a higher level of energy efficiency and higher efficiency. At present, the radio frequency/direct current (RF/DC) sputtering system is the mainstream thin film growth equipment. In addition to the thin film deposition process, the factors affecting the quality of sputtered transparent conductive films are the density, conductivity, grain size, microstructure and Purity plays a vital role. For example, the density of the target is low, that is, there are micropores on the surface or inside of the target, and the coating process will cause bulges on the surface of the target, causing the local energy of the target to be too high, and the oxygen ions are hit into a free state, forming a high-resistance area, resulting in some Microparticles get into the film and reduce the quality of the film, thus affecting the stability of the coating made.
目前,商业市场销售的IGZO溅射靶材主要以固相反应热压烧结,做法是将In2O3、ZnO和Ga2O3三种粉体按一定比例混合、球磨均质、热压烧结等步骤,制成溅镀用IGZO靶材。此制备方法操作简单,但机械球磨混合的均匀性受各粉体的粒度和形貌的影响。In2O3、ZnO和Ga2O3粉体的粒度、形貌及流动性和分散性对均质的效果及热压过程起着决定性作用。 At present, the IGZO sputtering targets sold in the commercial market are mainly sintered by solid - phase reaction hot pressing. and other steps to prepare an IGZO target for sputtering. This preparation method is simple to operate, but the uniformity of mechanical ball milling is affected by the particle size and morphology of each powder. The particle size, morphology, fluidity and dispersibility of In 2 O 3 , ZnO and Ga 2 O 3 powders play a decisive role in the homogenization effect and the hot pressing process.
中国专利申请CN108821329A公开了一种高纯氧化镓制备方法,该方法采用硫酸和双氧水混合溶液溶解金属镓得到硫酸镓溶液,通过结晶提纯得到高纯度的硫酸镓晶体,在通过煅烧硫酸晶体得到高纯氧化镓。虽然该方法可以得到高纯度氧化镓,但在煅烧过程中产生含硫氧化物气体,同时所得产物结块,破碎后产品的均一性差,且硫酸盐分解温度高,耗能高。Chinese patent application CN108821329A discloses a method for preparing high-purity gallium oxide. The method uses a mixed solution of sulfuric acid and hydrogen peroxide to dissolve metal gallium to obtain a gallium sulfate solution, obtains high-purity gallium sulfate crystals through crystallization and purification, and obtains high-purity gallium sulfate crystals by calcining the sulfuric acid crystals. Gallium oxide. Although this method can obtain high-purity gallium oxide, sulfur-containing oxide gas is generated during the calcination process, and the obtained product is agglomerated, the homogeneity of the product after crushing is poor, and the sulfate decomposition temperature is high and energy consumption is high.
中国专利申请CN107010654B公开了一种单分散氧化镓粉末粉体及其高密度陶瓷靶材的制备方法。该发明使用99.99%以上的金属镓溶解于酸中,然后加入氨水沉淀、老化得到白色沉淀物,再经洗涤、过滤、干燥、煅烧等工序得到产物。但该方法煅烧温度高,所得产物微观颗粒易结团,产品均匀性降低。Chinese patent application CN107010654B discloses a monodispersed gallium oxide powder and a method for preparing a high-density ceramic target. In the invention, more than 99.99% of metal gallium is dissolved in acid, then ammonia water is added for precipitation and aging to obtain a white precipitate, and the product is obtained by washing, filtering, drying, calcining and other procedures. However, the calcination temperature of this method is high, the microscopic particles of the obtained product are easy to agglomerate, and the uniformity of the product is reduced.
发明内容SUMMARY OF THE INVENTION
本发明的目的在于克服上述现有技术的不足之处而提供一种靶材级氧化镓的制备方法,该方法合成的氧化镓为椭球形,具有较高的流动性和分散性,以满足靶材使用。The purpose of the present invention is to overcome the shortcomings of the above-mentioned prior art and provide a preparation method of target grade gallium oxide. material use.
为实现上述目的,本发明采取的技术方案为:一种靶材级氧化镓的制备方法,所述制备方法包括以下步骤:In order to achieve the above purpose, the technical solution adopted in the present invention is: a preparation method of target-grade gallium oxide, the preparation method comprising the following steps:
(1)A溶液配制:制备硝酸镓溶液,将硝酸镓溶液稀释至镓含量为25~55g/L(0.358~0.789mol/L),游离硝酸浓度为0.1%~10%,然后加入表面活性剂,得到A溶液;(1) Preparation of solution A: prepare a gallium nitrate solution, dilute the gallium nitrate solution to a gallium content of 25-55g/L (0.358-0.789mol/L) and a free nitric acid concentration of 0.1%-10%, and then add a surfactant , to obtain A solution;
(2)B溶液配制:将沉淀剂配制成质量分数为5%~15%的溶液,得到B溶液;(2) Preparation of solution B: the precipitant is prepared into a solution with a mass fraction of 5% to 15% to obtain solution B;
(3)底液配制:将B溶液加入纯水中,配制成底液C溶液;(3) Bottom liquid preparation: add B solution to pure water to prepare bottom liquid C solution;
(4)沉淀反应:将A溶液和B溶液同时加入底液C溶液中进行沉淀反应;(4) Precipitation reaction: A solution and B solution are added to the bottom liquid C solution simultaneously to carry out precipitation reaction;
(5)然后经陈化反应、离心洗涤、煅烧,得到靶材级氧化镓。(5) Then, through aging reaction, centrifugal washing and calcination, target grade gallium oxide is obtained.
目前,高纯度氧化镓行业通用采用的方法是氨水沉淀镓离子得到羟基氧化镓,再经煅烧得到氧化镓产品。但此种方法得到的氧化镓形貌为棒状,这种棒状结构流动性和分散性差,在制备靶材时,影响靶材的均匀性及密度。At present, the method commonly used in the high-purity gallium oxide industry is to precipitate gallium ions with ammonia to obtain gallium oxyhydroxide, and then calcine to obtain gallium oxide products. However, the morphology of the gallium oxide obtained by this method is rod-shaped, and the rod-shaped structure has poor fluidity and dispersibility, which affects the uniformity and density of the target material during the preparation of the target material.
本发明的制备方法旨在合成椭球形、粒度D50=1.5~2μm的氧化镓,通过将A溶液和B溶液同时加入底液C溶液中,同时限定反应温度、A溶液和B溶液的浓度、A溶液和B溶液的加料速度,以得到其粒度D50=1.5~2μm;通过限定沉淀剂的种类、A溶液和B溶液的浓度,以得到其形貌为椭球形。本发明制备得到的氧化镓较棒状氧化镓具有较高的流动性和分散性,以满足靶材使用。且本发明制备得到的氧化镓具有以下特点:高比表面积,BET=10~15g/cm2;纯度高,可以达到99.995%;粒度小,D50=1.5~2μm。The preparation method of the present invention aims to synthesize gallium oxide with an ellipsoid shape and a particle size of D50=1.5-2 μm. By adding the A solution and the B solution to the bottom liquid C solution at the same time, the reaction temperature, the concentration of the A solution and the B solution, the concentration of the A solution and the B solution are limited at the same time. The feeding speed of the solution and the B solution is to obtain its particle size D50=1.5-2 μm; by limiting the type of the precipitant and the concentration of the A solution and the B solution, the morphology is ellipsoid. The gallium oxide prepared by the present invention has higher fluidity and dispersibility than rod-shaped gallium oxide, so as to meet the target use. And the gallium oxide prepared by the invention has the following characteristics: high specific surface area, BET=10~15g/cm 2 ; high purity, which can reach 99.995%; small particle size, D50=1.5~2μm.
作为本发明所述制备方法的优选实施方式,所述步骤(1)中,硝酸镓溶液的制备方法为:将溶剂升温,加入金属镓搅拌;然后加入硝酸,搅拌反应,即得硝酸镓溶液。As a preferred embodiment of the preparation method of the present invention, in the step (1), the preparation method of the gallium nitrate solution is as follows: heating the solvent, adding metal gallium and stirring; then adding nitric acid, stirring and reacting to obtain a gallium nitrate solution.
优选地,所述步骤(1)中,硝酸镓溶液的制备方法为:将溶剂水加入反应釜内,升温至30℃以上,然后加入金属镓并搅拌使金属镓分散成液滴状;向反应釜内加入硝酸,在40~80℃下进行反应,持续搅拌直至反应结束,然后过滤除去未反应的固体杂质得到硝酸镓溶液。Preferably, in the step (1), the preparation method of the gallium nitrate solution is as follows: adding solvent water into the reaction kettle, raising the temperature to above 30°C, then adding metal gallium and stirring to disperse the metal gallium into droplets; Nitric acid is added into the kettle, the reaction is carried out at 40-80° C., and the stirring is continued until the reaction ends, and then unreacted solid impurities are removed by filtration to obtain a gallium nitrate solution.
优选地,金属镓的纯度为99.999%,金属镓与硝酸的摩尔比为1:4。Preferably, the purity of metal gallium is 99.999%, and the molar ratio of metal gallium to nitric acid is 1:4.
作为本发明所述制备方法的优选实施方式,所述金属镓与表面活性剂的质量比为(20~200):1。As a preferred embodiment of the preparation method of the present invention, the mass ratio of the metal gallium to the surfactant is (20-200):1.
作为本发明所述制备方法的优选实施方式,所述步骤(1)中,表面活性剂为十二烷基苯磺酸(LAS)、烷基苯磺酸钠(ABS)、α-烯烃磺酸盐(AOS)、仲烷基磺酸钠(SAS)中的至少一种。As a preferred embodiment of the preparation method of the present invention, in the step (1), the surfactant is dodecylbenzenesulfonic acid (LAS), sodium alkylbenzenesulfonate (ABS), α-olefinsulfonic acid At least one of salt (AOS) and sodium secondary alkyl sulfonate (SAS).
作为本发明所述制备方法的优选实施方式,所述步骤(2)中,沉淀剂为氨水、碳酸氢铵、氢氧化钠中的至少一种。As a preferred embodiment of the preparation method of the present invention, in the step (2), the precipitating agent is at least one of ammonia water, ammonium bicarbonate and sodium hydroxide.
更优选地,沉淀剂为氨水、氢氧化钠中的至少一种,使用该沉淀剂能形成椭球形的氧化镓。More preferably, the precipitating agent is at least one of ammonia water and sodium hydroxide, and ellipsoid gallium oxide can be formed by using the precipitating agent.
更优选地,沉淀剂为氨水,使用该沉淀剂能形成椭球形的氧化镓,且后处理操作简单。More preferably, the precipitating agent is ammonia water, ellipsoidal gallium oxide can be formed by using the precipitating agent, and the post-processing operation is simple.
作为本发明所述制备方法的优选实施方式,所述步骤(3)中,底液C溶液的温度为40~70℃,底液C溶液的pH值为7.5~9.5。As a preferred embodiment of the preparation method of the present invention, in the step (3), the temperature of the bottom liquid C solution is 40-70° C., and the pH value of the bottom liquid C solution is 7.5-9.5.
作为本发明所述制备方法的优选实施方式,所述步骤(4)中,反应温度为40~70℃,底液C溶液与A溶液的体积比为1:(0.5~1.5),A溶液的加料速度为1~20L/min,调控B溶液的加料速度维持体系pH值为7.5~9.5,加料完成后持续搅拌1~3h,搅拌过程的温度为40~70℃、pH值为7.5~9.5。As a preferred embodiment of the preparation method of the present invention, in the step (4), the reaction temperature is 40 to 70° C., the volume ratio of the bottom liquid C solution to the A solution is 1:(0.5 to 1.5), and the volume ratio of the A solution is 1: (0.5 to 1.5). The feeding speed is 1-20 L/min, and the feeding speed of solution B is regulated to maintain the pH value of the system at 7.5-9.5. After the feeding is completed, the stirring is continued for 1-3 h. The temperature of the stirring process is 40-70 ° C and the pH value is 7.5-9.5.
沉淀反应中,底液C溶液与A溶液的体积比为1:(0.5~1.5),B溶液的用量范围不进行限定,通过调节B溶液的速度维持反应体系pH值为7.5~9.5,直到A溶液加料结束。In the precipitation reaction, the volume ratio of the bottom liquid C solution to the A solution is 1: (0.5~1.5), the dosage range of the B solution is not limited, and the pH value of the reaction system is maintained at 7.5~9.5 by adjusting the speed of the B solution, until A The solution addition was complete.
将A溶液和B溶液同时加入底液C溶液中,并通过调控B溶液的加料速度维持体系pH值为7.5~9.5,形成一个平衡的反应体系,利于粒度和形貌的控制。现有制备方法中均将B溶液直接加入A溶液中,镓离子浓度持续变化,形成的颗粒大小不一。Add solution A and solution B to the bottom solution C at the same time, and maintain the pH value of the system at 7.5-9.5 by adjusting the feeding speed of solution B to form a balanced reaction system, which is conducive to the control of particle size and morphology. In the existing preparation methods, the B solution is directly added to the A solution, the concentration of gallium ions is continuously changed, and the formed particles are of different sizes.
作为本发明所述制备方法的优选实施方式,所述步骤(5)中,陈化反应的温度为75~95℃,pH值为7.5~9.5,时间为1~8h。As a preferred embodiment of the preparation method of the present invention, in the step (5), the temperature of the aging reaction is 75-95° C., the pH value is 7.5-9.5, and the time is 1-8 h.
作为本发明所述制备方法的优选实施方式,所述步骤(5)中,洗涤直至洗涤水电导率小于100μS/cm。As a preferred embodiment of the preparation method of the present invention, in the step (5), washing is performed until the conductivity of the washing water is less than 100 μS/cm.
作为本发明所述制备方法的优选实施方式,所述步骤(5)中,煅烧温度为600~900℃,时间为4~12h。As a preferred embodiment of the preparation method of the present invention, in the step (5), the calcination temperature is 600-900° C., and the time is 4-12 hours.
与现有技术相比,本发明的有益效果为:本发明通过将A溶液和B溶液同时加入底液C溶液中,同时限定反应温度、A溶液和B溶液的浓度、A溶液和B溶液的加料速度、沉淀剂的种类,制备得到椭球形、粒度D50=1.5~2μm的氧化镓。本发明制备得到的氧化镓较棒状氧化镓具有较高的流动性和分散性,以满足靶材使用。且本发明制备得到的氧化镓具有以下特点:高比表面积,BET=10~15g/cm2;纯度高,可以达到99.995%;粒度小,D50=1.5~2μm。Compared with the prior art, the beneficial effects of the present invention are as follows: the present invention simultaneously limits the reaction temperature, the concentrations of the A solution and the B solution, the concentration of the A solution and the B solution by adding the A solution and the B solution to the bottom liquid C solution at the same time. According to the feeding speed and the type of precipitating agent, gallium oxide with ellipsoid shape and particle size D50=1.5-2 μm is prepared. The gallium oxide prepared by the present invention has higher fluidity and dispersibility than rod-shaped gallium oxide, so as to meet the target use. And the gallium oxide prepared by the invention has the following characteristics: high specific surface area, BET=10~15g/cm 2 ; high purity, which can reach 99.995%; small particle size, D50=1.5~2μm.
附图说明Description of drawings
图1为实施例1制备的氧化镓的SEM扫描电镜图。FIG. 1 is a SEM scanning electron microscope image of the gallium oxide prepared in Example 1. FIG.
图2为实施例2制备的氧化镓的SEM扫描电镜图。FIG. 2 is a SEM scanning electron microscope image of the gallium oxide prepared in Example 2. FIG.
图3为实施例3制备的氧化镓的SEM扫描电镜图。FIG. 3 is a SEM scanning electron microscope image of the gallium oxide prepared in Example 3. FIG.
具体实施方式Detailed ways
为更好地说明本发明的目的、技术方案和优点,下面将结合具体实施例对本发明作进一步说明。In order to better illustrate the purpose, technical solutions and advantages of the present invention, the present invention will be further described below with reference to specific embodiments.
实施例1Example 1
一种靶材级氧化镓的制备方法,包括以下步骤:A preparation method of target grade gallium oxide, comprising the following steps:
(1)A溶液配制:向钛制反应釜内加入400L纯化水,升温至40℃,然后加入35.75kg纯度为99.999%液态金属镓,然后开启搅拌使金属镓分散,接着以匀速加入优级纯硝酸进行溶解反应,其金属镓与硝酸的摩尔比为1:4,持续反应至溶液清亮透明,加入纯化水定容至650L,经过精密过滤器过滤后得到镓含量为55g/L硝酸镓溶液,游离酸度为10%;然后向溶液中加入178.75gABS,搅拌至完全溶解后,得到A溶液;(1) Preparation of solution A: add 400L of purified water to the titanium reaction kettle, raise the temperature to 40°C, then add 35.75kg of liquid metal gallium with a purity of 99.999%, then start stirring to disperse the metal gallium, and then add premium pure gallium at a uniform speed The nitric acid is dissolved, and the molar ratio of metal gallium to nitric acid is 1:4, and the reaction is continued until the solution is clear and transparent, and purified water is added to make up the volume to 650L. The free acidity is 10%; then add 178.75g ABS to the solution, and stir until completely dissolved to obtain solution A;
(2)B溶液配制:向沉淀剂储罐中加入800L纯化水,再加入200kg含量为25wt%优级纯氨水,形成质量分数为5%的溶液,搅拌均匀后,得到B溶液;(2) B solution preparation: add 800L of purified water to the precipitant storage tank, then add 200kg of 25wt% premium pure ammonia water to form a solution with a mass fraction of 5%, and after stirring evenly, obtain B solution;
(3)底液配制:向反应釜内加入955L纯化水,升温至40℃,加入2L溶液B将pH值调至9.5,得到底液C溶液;(3) bottom liquid preparation: add 955L of purified water in the reactor, be warming up to 40 ℃, add 2L of solution B and adjust the pH value to 9.5 to obtain bottom liquid C solution;
(4)沉淀反应:将A溶液和B溶液同时加入到底液C溶液中,加料过程控制反应温度为40℃、pH值为9.5,A溶液的加料速度为1L/min,调控B溶液的加料速度维持体系pH值为9.5,加料完成后持续搅拌2h;(4) Precipitation reaction: A solution and B solution were added to the bottom solution C at the same time, the reaction temperature of the feeding process was controlled to be 40 ° C, the pH value was 9.5, the feeding speed of the A solution was 1L/min, and the feeding speed of the B solution was regulated. The pH value of the system was maintained at 9.5, and the stirring was continued for 2h after the addition of materials;
(5)陈化反应:升温至75℃,停止搅拌,保持温度75℃陈化6h,陈化过程保持体系pH值为9.5;(5) Ageing reaction: heat up to 75°C, stop stirring, maintain the temperature at 75°C for ageing for 6 hours, and keep the pH value of the system at 9.5 during the ageing process;
抽滤洗涤:陈化反应结束后开启搅拌使浆料均匀,然后将浆料打入离心机,然后通入纯化水洗涤直至洗涤水电导率小于100μS/cm,高速离心甩干、卸料;Suction filtration and washing: After the aging reaction is completed, turn on the stirring to make the slurry uniform, then put the slurry into the centrifuge, and then pass into the purified water for washing until the conductivity of the washing water is less than 100 μS/cm, high-speed centrifugal drying, and discharging;
煅烧:将甩干后的物料转移至石英舟,装入管式气氛炉,通入一定流量的氮气和氧混合气体,在600℃煅烧12h,冷却至80℃以下后出料,得到靶材级氧化镓44.5kg,收率98%。Calcination: transfer the dried material to a quartz boat, load it into a tubular atmosphere furnace, introduce a certain flow of nitrogen and oxygen mixed gas, calcinate at 600 °C for 12 hours, cool down to below 80 °C and discharge to obtain a target grade Gallium oxide 44.5kg, yield 98%.
将本实施例制备得到的氧化镓取样送检杂质,ICP-MS测试结果如表1所示,SEM扫描电镜图如图1所示。由表1和图1可知,产品纯度达到99.995%,粒度D50为1.9μm,比表面积BET为13.8g/cm2,SEM形貌为椭球状。The gallium oxide prepared in this example was sampled and sent for inspection of impurities, the ICP-MS test results are shown in Table 1, and the SEM scanning electron microscope image is shown in FIG. 1 . It can be seen from Table 1 and Figure 1 that the product has a purity of 99.995%, a particle size D50 of 1.9 μm, a specific surface area BET of 13.8 g/cm 2 , and an ellipsoidal SEM morphology.
表1Table 1
实施例2Example 2
一种靶材级氧化镓的制备方法,包括以下步骤:A preparation method of target grade gallium oxide, comprising the following steps:
(1)A溶液配制:向钛制反应釜内加入400L纯化水,升温至40℃,然后加入16.25kg纯度为99.999%液态金属镓,然后开启搅拌使金属镓分散,接着以匀速加入优级纯硝酸进行溶解反应,其金属镓与硝酸的摩尔比为1:4,持续反应至溶液清亮透明,加入纯化水定容至650L,经过精密过滤器过滤后得到镓含量为25g/L硝酸镓溶液,游离酸度为5%;然后向溶液中加入812.5g ABS,搅拌至完全溶解后,得到A溶液;(1) Preparation of solution A: add 400L of purified water to the titanium reaction kettle, raise the temperature to 40°C, then add 16.25kg of liquid metal gallium with a purity of 99.999%, then start stirring to disperse the metal gallium, and then add premium pure gallium at a uniform speed The nitric acid is dissolved, and the molar ratio of metal gallium to nitric acid is 1:4, and the reaction is continued until the solution is clear and transparent, and purified water is added to make up the volume to 650L. The free acidity is 5%; then add 812.5g ABS to the solution, stir until it is completely dissolved, and obtain solution A;
(2)B溶液配制:向沉淀剂储罐中加入225L纯化水,再加入25kg分析纯氢氧化钠,形成质量分数为10%的溶液,搅拌均匀后,得到B溶液;(2) B solution preparation: add 225L of purified water to the precipitant storage tank, then add 25kg of analytically pure sodium hydroxide to form a solution with a mass fraction of 10%, and after stirring evenly, obtain B solution;
(3)底液配制:向反应釜内加入650L纯化水,升温至50℃,加入10mL溶液B将pH值调至8.0,得到底液C溶液;(3) Bottom liquid preparation: add 650L purified water in the reactor, be warming up to 50 ℃, add 10mL solution B to adjust pH value to 8.0, obtain bottom liquid C solution;
(4)沉淀反应:将A溶液和B溶液同时加入到底液C溶液中,加料过程控制反应温度为50℃、pH值为8.0,A溶液的加料速度为20L/min,调控B溶液的加料速度维持体系pH值为8.0,加料完成后持续搅拌2h;(4) Precipitation reaction: A solution and B solution are added into the bottom solution C solution simultaneously, the reaction temperature of the feeding process is controlled to be 50 ° C, the pH value is 8.0, the feeding speed of the A solution is 20L/min, and the feeding speed of the B solution is regulated and controlled. The pH value of the system was maintained at 8.0, and the stirring was continued for 2h after the addition of materials;
(5)陈化反应:升温至80℃,停止搅拌,保持温度80℃陈化4h,陈化过程保持体系pH值为8.0;(5) Ageing reaction: heat up to 80°C, stop stirring, keep the temperature at 80°C for ageing for 4 hours, and keep the pH value of the system at 8.0 during the ageing process;
抽滤洗涤:陈化反应结束后开启搅拌使浆料均匀,然后将浆料打入离心机,然后通入纯化水洗涤直至洗涤水电导率小于10μS/cm,高速离心甩干、卸料;Suction filtration and washing: After the aging reaction is completed, turn on the stirring to make the slurry uniform, then put the slurry into a centrifuge, and then pour into purified water for washing until the conductivity of the washing water is less than 10 μS/cm, high-speed centrifugal drying, and discharging;
煅烧:将甩干后的物料转移至石英舟,装入管式气氛炉,通入一定流量的氮气和氧混合气体,在700℃煅烧8h,冷却至80℃以下后出料,得到靶材级氧化镓31.6kg,收率99%。Calcination: transfer the dried material to a quartz boat, load it into a tubular atmosphere furnace, introduce a certain flow of nitrogen and oxygen mixed gas, calcinate at 700°C for 8 hours, cool down to below 80°C and discharge to obtain a target grade Gallium oxide 31.6kg, yield 99%.
将本实施例制备得到的氧化镓取样送检杂质,ICP-MS测试结果如表2所示,SEM扫描电镜图如图2所示。由表2和图2可知,产品纯度达到99.995%,粒度D50为1.8μm,比表面积BET为14.0g/cm2,SEM形貌为椭球状。The gallium oxide prepared in this example was sampled and sent for inspection of impurities. The ICP-MS test results are shown in Table 2, and the SEM scanning electron microscope image is shown in FIG. 2 . It can be seen from Table 2 and Figure 2 that the product has a purity of 99.995%, a particle size D50 of 1.8 μm, a specific surface area BET of 14.0 g/cm 2 , and an ellipsoidal SEM morphology.
表2Table 2
实施例3Example 3
一种靶材级氧化镓的制备方法,包括以下步骤:A preparation method of target-grade gallium oxide, comprising the following steps:
(1)A溶液配制:向钛制反应釜内加入400L纯化水,升温至40℃,然后加入26kg纯度为99.999%液态金属镓,然后开启搅拌使金属镓分散,接着以匀速加入优级纯硝酸进行溶解反应,其金属镓与硝酸的摩尔比为1:4,持续反应至溶液清亮透明,加入纯化水定容至650L,经过精密过滤器过滤后得到镓含量为40g/L硝酸镓溶液,游离酸度为0.1%;然后向溶液中加入260g ABS,搅拌至完全溶解后,得到A溶液;(1) Preparation of solution A: add 400L of purified water to the titanium reaction kettle, heat up to 40°C, then add 26kg of liquid metal gallium with a purity of 99.999%, then start stirring to disperse the metal gallium, and then add high-grade pure nitric acid at a uniform speed Carry out the dissolution reaction, the molar ratio of metal gallium to nitric acid is 1:4, continue to react until the solution is clear and transparent, add purified water to make up the volume to 650L, and filter through a precision filter to obtain a gallium content of 40g/L gallium nitrate solution, free The acidity is 0.1%; then add 260g ABS to the solution, stir until completely dissolved, and obtain solution A;
(2)B溶液配制:向沉淀剂储罐中加入1700L纯化水,再加入300kg碳酸氢铵,形成质量分数为15%的溶液,搅拌均匀后,得到B溶液;(2) Preparation of solution B: add 1700L of purified water to the precipitant storage tank, then add 300kg of ammonium bicarbonate to form a solution with a mass fraction of 15%, and stir to obtain solution B;
(3)底液配制:向反应釜内加入450L纯化水,升温至70℃,加入3L溶液B将pH值调至7.5,得到底液C溶液;(3) bottom liquid preparation: add 450L of purified water in the reactor, be warming up to 70 ℃, add 3L of solution B to adjust pH value to 7.5, obtain bottom liquid C solution;
(4)沉淀反应:将A溶液和B溶液同时加入到底液C溶液中,加料过程控制反应温度为70℃、pH值为7.5,A溶液的加料速度为10L/min,调控B溶液的加料速度维持体系pH值为7.5,加料完成后持续搅拌2h;(4) Precipitation reaction: A solution and B solution are added into the bottom solution C solution simultaneously, the reaction temperature of the feeding process is controlled to be 70 ° C, the pH value is 7.5, the feeding speed of the A solution is 10L/min, and the feeding speed of the B solution is regulated and controlled. The pH value of the system was maintained at 7.5, and the stirring was continued for 2h after the addition of materials;
(5)陈化反应:升温至95℃,停止搅拌,保持温度95℃陈化6h,陈化过程保持体系pH值为7.5;(5) Ageing reaction: the temperature was raised to 95°C, the stirring was stopped, the temperature was maintained at 95°C for 6 hours, and the pH value of the system was maintained at 7.5 during the ageing process;
抽滤洗涤:陈化反应结束后开启搅拌使浆料均匀,然后将浆料打入离心机,然后通入纯化水洗涤直至洗涤水电导率小于10μS/cm,高速离心甩干、卸料;Suction filtration and washing: After the aging reaction is completed, turn on the stirring to make the slurry uniform, then put the slurry into a centrifuge, and then pour into purified water for washing until the conductivity of the washing water is less than 10 μS/cm, high-speed centrifugal drying, and discharging;
煅烧:将甩干后的物料转移至石英舟,装入管式气氛炉,通入一定流量的氮气和氧混合气体,在900℃煅烧4h,冷却至80℃以下后出料,得到靶材级氧化镓45.5kg,收率96.6%。Calcination: transfer the dried material to a quartz boat, load it into a tubular atmosphere furnace, introduce a certain flow of nitrogen and oxygen mixed gas, calcinate at 900 °C for 4 hours, cool to below 80 °C and discharge to obtain a target grade Gallium oxide 45.5kg, yield 96.6%.
将本实施例制备得到的氧化镓取样送检杂质,ICP-MS测试结果如表3所示,SEM扫描电镜图如图3所示。由表3和图3可知,产品纯度达到99.995%,粒度D50为1.7μm,比表面积BET为14.5g/cm2,SEM形貌为椭球状。The gallium oxide prepared in this example was sampled and sent for inspection of impurities. The ICP-MS test results are shown in Table 3, and the SEM scanning electron microscope image is shown in FIG. 3 . It can be seen from Table 3 and Figure 3 that the product has a purity of 99.995%, a particle size D50 of 1.7 μm, a specific surface area BET of 14.5 g/cm 2 , and an ellipsoidal SEM morphology.
表3table 3
最后所应当说明的是,以上实施例仅用以说明本发明的技术方案而非对本发明保护范围的限制,尽管参照较佳实施例对本发明作了详细说明,本领域的普通技术人员应当理解,可以对本发明的技术方案进行修改或者等同替换,而不脱离本发明技术方案的实质和范围。Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention and not to limit the protection scope of the present invention. Although the present invention is described in detail with reference to the preferred embodiments, those of ordinary skill in the art should understand that, The technical solutions of the present invention may be modified or equivalently replaced without departing from the spirit and scope of the technical solutions of the present invention.
Claims (10)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202010436819.8A CN111592033A (en) | 2020-05-21 | 2020-05-21 | A kind of preparation method of target grade gallium oxide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202010436819.8A CN111592033A (en) | 2020-05-21 | 2020-05-21 | A kind of preparation method of target grade gallium oxide |
Publications (1)
Publication Number | Publication Date |
---|---|
CN111592033A true CN111592033A (en) | 2020-08-28 |
Family
ID=72187450
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202010436819.8A Pending CN111592033A (en) | 2020-05-21 | 2020-05-21 | A kind of preparation method of target grade gallium oxide |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN111592033A (en) |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4351821A (en) * | 1980-06-27 | 1982-09-28 | Rhone-Poulenc Industries | Preparation of gallium oxide |
US5066617A (en) * | 1986-07-23 | 1991-11-19 | Nippon Steel Corporation | Method for producing plzt powder |
CN104190423A (en) * | 2014-09-25 | 2014-12-10 | 四川理工学院 | A kind of preparation method of spherical α-Fe2O3 |
CN107010654A (en) * | 2017-05-05 | 2017-08-04 | 华中科技大学 | A kind of preparation method of single dispersing gallium oxide powder and its high density ceramic target |
CN107973332A (en) * | 2018-01-23 | 2018-05-01 | 包头科日稀土材料有限公司 | A kind of method for preparing high rare-earth content basic carbonate cerium |
CN110937622A (en) * | 2019-11-12 | 2020-03-31 | 中铝山东有限公司 | Method for preparing 4N gallium oxide from sponge gallium |
-
2020
- 2020-05-21 CN CN202010436819.8A patent/CN111592033A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4351821A (en) * | 1980-06-27 | 1982-09-28 | Rhone-Poulenc Industries | Preparation of gallium oxide |
US5066617A (en) * | 1986-07-23 | 1991-11-19 | Nippon Steel Corporation | Method for producing plzt powder |
CN104190423A (en) * | 2014-09-25 | 2014-12-10 | 四川理工学院 | A kind of preparation method of spherical α-Fe2O3 |
CN107010654A (en) * | 2017-05-05 | 2017-08-04 | 华中科技大学 | A kind of preparation method of single dispersing gallium oxide powder and its high density ceramic target |
CN107973332A (en) * | 2018-01-23 | 2018-05-01 | 包头科日稀土材料有限公司 | A kind of method for preparing high rare-earth content basic carbonate cerium |
CN110937622A (en) * | 2019-11-12 | 2020-03-31 | 中铝山东有限公司 | Method for preparing 4N gallium oxide from sponge gallium |
Non-Patent Citations (4)
Title |
---|
ALINE V等: "Study of intense photoluminescence from monodispersed β-Ga2O3 ellipsoidal structures", 《CERAMICS INTERNATIONAL》 * |
JING-JING SHAN等: "Sintering behavior and microstructural evolution of the monodispersed β-gallium oxide micro-particles with different morphology and size", 《CERAMICS INTERNATIONAL》 * |
曾令可等: "《纳米陶瓷技术》", 31 August 2006, 华南理工大学出版社 * |
王胜等: "纳米氧化铟的制备", 《有色金属(冶炼部分)》 * |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Gao et al. | Phase and shape controlled VO 2 nanostructures by antimony doping | |
CN111362298B (en) | A preparation method of indium oxide spherical powder with controllable particle shape | |
CN104646683B (en) | Controllable ball shape silver powder of a kind of granularity and preparation method thereof | |
CN102554265B (en) | A kind of preparation method of adjustable particle size monodisperse high crystalline silver powder | |
CN108910932B (en) | A kind of method for preparing narrow distribution ultrafine yttrium oxide by sodium carbonate precipitation | |
CN111717938B (en) | Narrowly distributed small-particle-size nickel-cobalt-aluminum hydroxide and preparation method thereof | |
CN106216710A (en) | A kind of preparation method of high-tap density high-crystallinity silver powder | |
CN105645959B (en) | Y2O3The spraying codepostion preparation method of base transparent ceramic powder | |
CN109019656A (en) | The production method of nano rareearth oxidate powder body | |
CN108585014A (en) | A series of micro-/ nano rare earth materials and preparation method thereof | |
CN111439778A (en) | Preparation method of nano-grade gallium oxide | |
CN101979326A (en) | A kind of micron-scale ultrafine ammonium paratungstate and preparation method thereof | |
KR101473716B1 (en) | Manufacturing method of gallium oxide of high purity spherical for minimalize of loss of gallium and high purity spherical gallium oxide therefrom | |
CN104876258A (en) | Method for preparing custerite phase copper, zinc, tin and sulfur semiconductor nanocrystals | |
KR20130070092A (en) | Method for producing yttrium oxide powders and yttrium oxide powders prepared by the method | |
ES2968773A2 (en) | Method for preparing ternary precursor | |
JP5588815B2 (en) | Gallium oxide powder | |
CN101870491A (en) | Co-precipitation method for preparation of yttrium aluminum garnet nanopowder in a narrow pH range | |
CN111592033A (en) | A kind of preparation method of target grade gallium oxide | |
CN108706618A (en) | Utilize the method for micro-emulsion method for preparing nano aluminium oxide | |
CN101591176A (en) | A kind of synthetic Gd 3Ga 5O 12(GGG) the nanocrystalline method of crystalline ceramics | |
CN112110732A (en) | Method for preparing aluminum nitride powder by using soluble carbon source | |
CN116986625A (en) | Preparation method of in-situ precipitation self-dispersion indium oxide powder | |
CN108046323A (en) | A kind of preparation method of niobium oxide | |
TWI531537B (en) | Indium-gallium-zinc oxide, method for producing the same, and its application |
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 | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20200828 |
|
RJ01 | Rejection of invention patent application after publication |