CN104178801B - A kind of High Temperature High Pressure hydro-thermal still containing foam metal crystallization parts - Google Patents
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Abstract
本发明公开了一种含有泡沫金属结晶部件的高温高压水热釜,包括置于高压釜釜体内的水热反应容器,该水热反应容器内存在溶解区和结晶区,在结晶区设置有利于晶体生长的结晶部件,该结晶部件由泡沫金属制成。通过在结晶区中设置由泡沫金属制成的结晶部件,利用泡沫金属具有的高比表面积等结构特点,产生大量的适宜晶体附着的成核位点,而且泡沫金属内部细密的网孔能够起到抓紧晶粒防止其滑落到溶解区的作用,在吸取传统温差式水热釜中以金属丝、金属片作为结晶承载体的优点的同时,解决其有效成核面积小,已长成晶粒掉落,对流过于强烈,输运受阻等缺陷,极大程度地增加了结晶效率,并促进使晶粒进一步长大,同时晶体产量也得到进一步提高。
The invention discloses a high-temperature and high-pressure hydrothermal kettle containing foamed metal crystallization parts, which includes a hydrothermal reaction vessel placed in the autoclave body. There is a dissolution zone and a crystallization zone in the hydrothermal reaction vessel, and the setting in the crystallization zone is beneficial to A crystalline part for crystal growth, the crystalline part being made of metal foam. By setting crystallization parts made of metal foam in the crystallization area, using the structural characteristics of metal foam such as high specific surface area, a large number of nucleation sites suitable for crystal attachment are generated, and the fine mesh inside the metal foam can play a role Grasp the role of the crystal grains to prevent them from slipping into the dissolution zone. While absorbing the advantages of using metal wires and metal sheets as the crystallization carrier in the traditional temperature difference hydrothermal kettle, it solves the problem that the effective nucleation area is small and the grains that have grown into Defects such as falling, strong convection, and hindered transport greatly increase the crystallization efficiency, promote the further growth of crystal grains, and further increase the crystal yield.
Description
技术领域technical field
本发明涉及人工方法生长晶体的装置,具体涉及一种含有泡沫金属结晶部件的高温高压水热釜。The invention relates to a device for artificially growing crystals, in particular to a high-temperature and high-pressure hydrothermal kettle containing foamed metal crystal parts.
背景技术Background technique
人工生长晶体方法的研究早在十九世纪末期就已开始,迄今已有超过百年的历史,生长单晶的方法主要有助熔剂法、水热法、气相法、区熔法等,其中,水热法生长出来的晶体具有热应力小、宏观缺陷小、晶体均匀性好、透过率高等特点。水热法生长晶体具体是将原料(溶质)溶解在溶剂中,采取适当的措施造成溶液的过饱和状态(稀薄相饱和蒸汽压升高),使固相颗粒在其中成核长大,最终得到完整晶体的方法。The research on the method of artificially growing crystals began as early as the end of the nineteenth century, and has a history of more than one hundred years. The methods for growing single crystals mainly include flux method, hydrothermal method, gas phase method, zone melting method, etc. Among them, water The crystals grown by the thermal method have the characteristics of small thermal stress, small macroscopic defects, good crystal uniformity, and high transmittance. The hydrothermal crystal growth method specifically dissolves the raw material (solute) in the solvent, and takes appropriate measures to cause the supersaturated state of the solution (the saturated vapor pressure of the dilute phase increases), so that the solid phase particles nucleate and grow in it, and finally obtain method for intact crystals.
水热法具有很多优势,如可以使晶体在远低于其熔点的温度下生长,解决某些晶体不到熔点就分解或远低于熔点发生晶型转变的难题;水热法生长晶体过程可以降低溶液粘度,克服某些晶体在熔盐法生长过程中冷却粘度大,易于形成玻璃体的缺点;水热法生长晶体容易生长得到大块的、均匀性晶体,并且通常都会有较为完整的外形和晶胞;水热法生长晶体可直接观察晶体生长过程,有利于准确研究生长动力学和热力学;但是,还存在以下不足:The hydrothermal method has many advantages, such as allowing the crystal to grow at a temperature far below its melting point, and solving the problem that some crystals decompose before the melting point or crystal transformation occurs far below the melting point; the crystal growth process of the hydrothermal method can be Reduce the viscosity of the solution and overcome the disadvantages of high cooling viscosity of some crystals during the molten salt growth process and easy formation of glass bodies; hydrothermal growth crystals are easy to grow to obtain large, uniform crystals, and usually have a relatively complete shape and Unit cell; crystal growth by hydrothermal method can directly observe the crystal growth process, which is conducive to the accurate study of growth kinetics and thermodynamics; however, there are still the following shortcomings:
1、在水热实际生长过程中需要有籽晶创造成核位点来完成晶核的进一步长大,而籽晶培育需要很长周期,粒径尺寸、体积的扩展也耗时耗力,能够达到水热生长使用尺度的籽晶少之又少,更有甚者,一些新型晶体尚无籽晶或很难得到籽晶(无自发成核的现象),在实际生长中需要有结晶装置完成晶体成核步骤。1. In the actual hydrothermal growth process, it is necessary to have seed crystals to create nucleation sites to complete the further growth of crystal nuclei, and seed crystal cultivation requires a long period, and the expansion of particle size and volume is also time-consuming and labor-intensive. There are very few seed crystals that reach the scale used for hydrothermal growth. What's more, some new crystals have no seed crystals or are difficult to obtain seed crystals (no spontaneous nucleation phenomenon), and a crystallization device is required to complete the actual growth. Crystal nucleation step.
2、在水热结晶中,高压釜内部有剧烈的营养盐输运过程,输运是从高压釜热端向冷端,营养盐在冷端冷却回流至热端,如此循环往复,结晶过程一般就发生在营养盐的冷凝过程(某些晶体有反向温度系数,可能在加热过程结晶),现今的高性能高压釜虽然能准确控温,拉开温差,但是很难做到放大冷凝(加热)结晶过程段,减缓釜内溶液对流。2. In hydrothermal crystallization, there is a violent nutrient transport process inside the autoclave. The transport is from the hot end to the cold end of the autoclave, and the nutrient salt is cooled at the cold end and flows back to the hot end. In this way, the crystallization process is normal. It happens in the condensation process of nutrient salts (some crystals have a reverse temperature coefficient and may crystallize during the heating process). Although today's high-performance autoclaves can accurately control the temperature and widen the temperature difference, it is difficult to achieve amplified condensation (heating ) in the crystallization process section to slow down the convection of the solution in the kettle.
3、为了解决水热结晶过程对流剧烈的问题,国内外已经有在溶解区和结晶区之间加装内挡板设备,内挡板在一定意义上减缓了营养盐的输运,放大了冷凝结晶过程,使结晶量增加,晶核增大,但是,晶核形成后会随着重力作用及输运作用力迁移至溶解区或挡板位置,晶核利用率并不高。实际生长过程中经常会出现晶核难以长大(在釜内反复溶解结晶),晶粒阻塞挡板孔造成生长停滞的现象。3. In order to solve the problem of severe convection in the hydrothermal crystallization process, internal baffle equipment has been installed between the dissolution zone and the crystallization zone at home and abroad. The internal baffle slows down the transportation of nutrient salts in a certain sense and enlarges the condensation The crystallization process increases the amount of crystallization and the crystal nucleus. However, after the formation of the crystal nucleus, it will migrate to the dissolution zone or the position of the baffle with the force of gravity and transportation, and the utilization rate of the crystal nucleus is not high. In the actual growth process, it often occurs that the crystal nuclei are difficult to grow (repeatedly dissolving crystals in the kettle), and the crystal grains block the baffle holes and cause growth stagnation.
4、已有文献报道使用经过缠绕或折叠的金属片、金属丝等来产生结晶区域,增大结合位点面积,虽然起到了承接晶粒、减缓溶液对流的作用,但是金属片、金属丝的密度较大,单位比表面积却很小,匹配晶体晶胞的指数面利用率依旧不高;另一方面,如果采用大面积的金属片、金属丝,会阻碍营养盐的输运。4. It has been reported in the literature that wound or folded metal sheets and wires are used to generate crystallization regions and increase the area of the binding sites. The density is high, but the unit specific surface area is small, and the utilization rate of the index surface matching the crystal unit cell is still not high; on the other hand, if large-area metal sheets and wires are used, the transportation of nutrients will be hindered.
发明内容Contents of the invention
本发明要解决的技术问题是提供一种含有泡沫金属结晶部件的高温高压水热釜。采用该高压釜可以使难结晶或不结晶材料更易于形成晶核,并使晶粒更快速地长大,同时提高晶体的产量。The technical problem to be solved by the present invention is to provide a high-temperature and high-pressure hydrothermal kettle containing foamed metal crystal parts. The use of the autoclave can make crystal nucleation easier for difficult-to-crystallization or non-crystallization materials, make crystal grains grow faster, and increase crystal output at the same time.
本发明所述的含有泡沫金属结晶部件的高温高压水热釜,包括置于高压釜釜体内的水热反应容器,该水热反应容器内存在溶解区和结晶区,在结晶区设置有利于晶体生长的结晶部件,该结晶部件由泡沫金属制成。The high-temperature and high-pressure hydrothermal kettle containing foamed metal crystallization parts according to the present invention includes a hydrothermal reaction vessel placed in the autoclave body. There is a dissolution zone and a crystallization zone in the hydrothermal reaction vessel. A grown crystalline part made of metal foam.
本发明所述技术方案中涉及的泡沫金属材料具有比重小、高孔隙率、比表面积大和较大孔径的结构特征。本发明在结晶区中设置采用泡沫金属制成的结晶部件,利用泡沫金属具有的高比表面积等结构特点,产生大量的适宜晶体附着的成核位点,而且泡沫金属内部细密的网孔能够起到抓紧晶粒的作用,极大程度地增加了结晶效率,并促进使晶粒进一步长大,同时晶体产量也得到进一步提高。The metal foam material involved in the technical solution of the present invention has the structural characteristics of small specific gravity, high porosity, large specific surface area and large pore diameter. In the present invention, crystallization parts made of metal foam are arranged in the crystallization area, and a large number of nucleation sites suitable for crystal attachment are generated by utilizing the structural characteristics such as high specific surface area of metal foam, and the fine mesh inside the metal foam can act The effect of grasping the crystal grains has greatly increased the crystallization efficiency, and promoted the further growth of the grains, and the crystal yield has also been further improved.
上述技术方案中,优选采用具有下述结构参数的泡沫金属来制作结晶部件:孔径为0.01~10mm,孔隙率为50%~98%,通孔率≥90%,体积密度为0.05~1g/cm3,以获得更高的结晶效率及晶体产量,同时更利于生长得到更大尺寸的晶体。In the above technical solution, it is preferable to use metal foam with the following structural parameters to make the crystalline part: the pore diameter is 0.01-10mm, the porosity is 50%-98%, the through-porosity ≥ 90%, and the bulk density is 0.05-1g/cm 3 , to obtain higher crystallization efficiency and crystal yield, and at the same time, it is more conducive to the growth of crystals with larger sizes.
上述技术方案中,所述的泡沫金属通常为泡沫铝、泡沫铜、泡沫镍、泡沫铁、泡沫银、泡沫金、泡沫铂或泡沫合金,其中的的泡沫合金具体可以是铜锡泡沫合金、铜锌泡沫合金、钛镍泡沫合金或铝镁泡沫合金等。In the above technical scheme, the metal foam is usually aluminum foam, copper foam, nickel foam, iron foam, silver foam, gold foam, platinum foam or foam alloy, wherein the foam alloy can specifically be copper tin foam alloy, copper foam Zinc foam alloy, titanium-nickel foam alloy or aluminum-magnesium foam alloy, etc.
上述技术方案中,所述的结晶部件可以是由泡沫金属制成的具有各种形状或结构,空心或实心的部件。由于泡沫金属体积密度低、质轻、易于折叠和裁剪,因而易于将其制作成任意形状的结晶部件。具体地,结晶部件可以是由泡沫金属制作的呈现出直线结构、片状结构、盘形结构、齿状结构、柱状结构、锥状结构、螺旋结构或实心结构的任意形状。In the above technical solution, the crystallized part may be a hollow or solid part made of metal foam with various shapes or structures. Because metal foam has low bulk density, light weight, and is easy to fold and cut, it is easy to make it into crystalline parts of any shape. Specifically, the crystalline part can be made of metal foam and exhibit any shape of linear structure, sheet structure, disc structure, tooth structure, column structure, cone structure, helical structure or solid structure.
上述技术方案中,所述的结晶部件可以将通过贵金属丝连接于水热反应容器的容器盖上。所述的贵金属丝通常为金丝、银丝、钛丝或铂丝等。In the above technical solution, the crystallization part can be connected to the container cover of the hydrothermal reaction container through precious metal wires. The precious metal wires are usually gold wires, silver wires, titanium wires or platinum wires.
本发明所述的技术方案中,除结晶部件以外的结构均与现有技术中常规的水热法高压釜的结构相同,在此不再一一详述。本发明所述的技术方案中,所述的水热反应容器为现有技术中常用的贵金属衬套管,具体可以是黄金衬套管、银衬套管或者是铂金衬套管。In the technical solution of the present invention, the structure other than the crystallization part is the same as that of the conventional hydrothermal autoclave in the prior art, and will not be described in detail here. In the technical solution of the present invention, the hydrothermal reaction vessel is a noble metal bushing tube commonly used in the prior art, specifically a gold bushing tube, a silver bushing tube or a platinum bushing tube.
本发明所述的技术方案中,用泡沫金属制成的结晶部件在放入高压釜进行使用之前需要进行预处理,具体的预处理步骤是:将泡沫金属制成的结晶部件先在超声条件下用无水乙醇清洗,然后用酸液(通常为0.1~1mol/L的盐酸溶液或硫酸溶液)清洗除氧化膜,再用碱液(通常为0.5~4mol/L的氢氧化钠溶液或氢氧化钾溶液)清洗除油,之后真空干燥即可。对干燥后的结晶部件进行称重,根据泡沫金属的密度换算体积,高压釜内填充溶液时需要扣除结晶部件占用的体积以免造成压力失衡。In the technical solution of the present invention, the crystalline parts made of metal foam need to be pretreated before being put into an autoclave for use. Clean with absolute ethanol, then use acid solution (usually 0.1-1mol/L hydrochloric acid solution or sulfuric acid solution) to clean and remove the oxide film, and then use lye (usually 0.5-4mol/L sodium hydroxide solution or Potassium solution) to clean and degrease, then vacuum dry. The dried crystalline parts are weighed, and the volume is converted according to the density of the metal foam. When filling the autoclave with the solution, the volume occupied by the crystalline parts needs to be deducted to avoid pressure imbalance.
本发明所述的高压釜在实际生长晶体时,需要根据选用的矿化剂来选择用于制作结晶部件的泡沫金属,选择的原则是所选择的泡沫金属不能与水热反应容器中的矿化剂发生化学反应。When the autoclave of the present invention actually grows crystals, it is necessary to select the metal foam used to make the crystal part according to the selected mineralizer. The agent reacts chemically.
与现有技术相比,本发明的特点在于在结晶区中设置采用泡沫金属制成的结晶部件,这产生了以下几个方面的有益效果:Compared with the prior art, the present invention is characterized in that crystallization parts made of metal foam are arranged in the crystallization area, which produces the following beneficial effects:
首先,泡沫金属制成的结晶部件热传导性能好,不会造成热传递不均匀,局部过冷过热等现象,而且能够耐受高温高压高PH超临界水热、溶剂热环境,是极度稳定的结晶附着体材料;另外,由于泡沫金属体积密度低、质轻,易于折叠和裁剪,因而易于将其制作成任意形状的结晶部件;First of all, the crystalline parts made of metal foam have good thermal conductivity, will not cause uneven heat transfer, local overcooling and overheating, etc., and can withstand high temperature, high pressure, high PH supercritical hydrothermal and solvent thermal environments, and are extremely stable crystals Attachment material; In addition, because metal foam has low bulk density, light weight, and is easy to fold and cut, it is easy to make it into crystal parts of any shape;
其次,利用泡沫金属具有的高比表面积等结构特点,产生大量的适宜晶体附着的成核位点,而且泡沫金属内部细密的网孔能够起到抓紧晶粒防止其滑落到溶解区的作用,在吸取传统温差式水热釜中以金属丝、金属片作为结晶承载体的优点的同时,解决其有效成核面积小,已长成晶粒掉落,对流过于强烈,输运受阻等缺陷,极大程度地增加了结晶效率,并促进使晶粒进一步长大,同时晶体产量也得到进一步提高。Secondly, using the structural characteristics of metal foam such as high specific surface area, a large number of nucleation sites suitable for crystal attachment are generated, and the fine mesh inside the metal foam can hold the crystal grains to prevent them from slipping into the dissolution zone. While absorbing the advantages of using metal wires and metal sheets as the crystallization carrier in the traditional temperature-difference hydrothermal kettle, it solves the defects of small effective nucleation area, drop of grown grains, too strong convection, and hindered transportation. The crystallization efficiency is greatly increased, and the crystal grains are further grown, and the crystal yield is also further improved.
附图说明Description of drawings
图1为本发明所述的含有泡沫金属结晶部件的高温高压水热釜一种实施方式的结构示意图;Fig. 1 is a schematic structural view of an embodiment of a high-temperature and high-pressure hydrothermal kettle containing foamed metal crystalline parts according to the present invention;
图2为悬挂于衬套管中的几种泡沫金属结晶部件的结构示意图,其中(a)为螺旋结构的结晶部件的结构示意图,(b)为平面片状间隔堆叠结构的结晶部件的结构示意图,(c)为盘形结构的结晶部件的结构示意图;(d)为齿状结构的结晶部件的结构示意图;(e)为空心柱状结构的结晶部件的结构示意图;(f)为直线结构的结晶部件的结构示意图;Figure 2 is a schematic diagram of the structure of several metal foam crystal parts suspended in the bushing tube, in which (a) is a structural schematic diagram of a helical structure crystal part, and (b) is a structural schematic diagram of a planar sheet-like spaced stacked crystal part , (c) is a schematic diagram of the crystal structure of the disk-shaped structure; (d) is a schematic diagram of the crystal structure of the tooth-shaped structure; (e) is a schematic diagram of the crystal structure of the hollow columnar structure; (f) is a linear structure Schematic diagram of the structure of the crystallization part;
图3为采用本发明所述含有泡沫金属结晶部件的高温高压水热釜,按实施例2所述方法生长得到的晶体的图片;Fig. 3 adopts the high-temperature and high-pressure hydrothermal kettle containing foamed metal crystalline parts of the present invention, the picture of the crystal that grows according to the method described in Example 2;
图4为采用本发明所述含有泡沫金属结晶部件的高温高压水热釜,按实施例2所述方法生长得到的晶体的XRD图谱;Fig. 4 is the XRD spectrum of the crystal grown by the method described in Example 2 by adopting the high-temperature and high-pressure hydrothermal kettle containing foamed metal crystalline parts of the present invention;
图5为采用本发明所述含有泡沫金属结晶部件的高温高压水热釜,按实施例3所述方法生长得到的晶体的图片;Fig. 5 adopts the high-temperature and high-pressure hydrothermal kettle containing foamed metal crystalline parts of the present invention, the picture of the crystal that grows according to the method described in Example 3;
图6为采用本发明所述含有泡沫金属结晶部件的高温高压水热釜,按实施例3所述方法生长得到的晶体的透过率图谱;Fig. 6 is the transmittance spectrum of the crystal grown by the method described in Example 3 using the high-temperature and high-pressure hydrothermal kettle containing the metal foam crystal part of the present invention;
图7为采用本发明所述含有泡沫金属结晶部件的高温高压水热釜,按实施例4所述方法生长得到的晶体的图片。Fig. 7 is a picture of crystals grown according to the method described in Example 4 by using the high-temperature and high-pressure hydrothermal kettle containing foamed metal crystal parts according to the present invention.
图中标号为:The labels in the figure are:
1自紧式密封釜塞;2紧固螺栓;3釜盖;4釜体;5衬套管;6挡板;7结晶区;8结晶部件;9溶解区;10吊篮。1 Self-tightening sealing kettle plug; 2 Fastening bolts; 3 Kettle cover; 4 Kettle body; 5 Bushing pipe; 6 Baffle plate; 7 Crystallization area;
具体实施方式detailed description
下面以具体实施例对本发明作进一步说明,但本发明并不局限于这些实施例。The present invention will be further described below with specific examples, but the present invention is not limited to these examples.
实施例1:用于水热法生长晶体的含有泡沫金属结晶部件的高温高压水热釜Embodiment 1: High-temperature and high-pressure hydrothermal kettle containing foamed metal crystallization parts for hydrothermal growth of crystals
如图1所示,本发明所述的含有泡沫金属结晶部件的高温高压水热釜,包括釜体4和釜盖3,釜盖3上设有与釜体4内腔开口相互配合的自紧式密封釜塞1,所述釜体4和釜盖3通过紧固螺栓2连接;在高压釜釜体4内腔置有一衬套管5,所述衬套管5的中下部放置有一个在中心和边缘开孔的挡板6(开孔率为7~10%),该挡板6将衬套管5内部的空间分隔为下部的溶解区9和上部的结晶区7。在结晶区7内,由泡沫金属制成的结晶部件8通过贵金属丝悬挂于衬套管5的顶部(如衬套管5的管盖上);培养料置于衬套管5的底部(即置于溶解区9内),并在衬套管5内填充矿化剂。在高压釜和衬套管5的夹层中填充一定量的去离子水或蒸馏水,以维持衬套管5内外压力平衡,防止衬套管5破裂或压瘪。如果采用的衬套管5的口径较大,需要在衬套管5内加设吊篮10,将培养料置于吊篮10中。As shown in Figure 1, the high-temperature and high-pressure hydrothermal kettle containing foamed metal crystal parts according to the present invention includes a kettle body 4 and a kettle cover 3, and the kettle cover 3 is provided with a self-tightening mechanism that cooperates with the opening of the inner cavity of the kettle body 4. Sealed kettle plug 1, the kettle body 4 and kettle cover 3 are connected by fastening bolts 2; a bushing pipe 5 is placed in the inner cavity of the autoclave body 4, and a middle and lower part of the bushing pipe 5 is placed Baffles 6 with openings in the center and edges (the opening ratio is 7-10%). The baffles 6 divide the space inside the liner pipe 5 into a lower dissolution zone 9 and an upper crystallization zone 7 . In the crystallization zone 7, the crystallization part 8 made of foam metal is suspended on the top of the liner pipe 5 (such as on the pipe cover of the liner pipe 5) by precious metal wire; placed in the dissolution zone 9), and fill the liner tube 5 with a mineralizer. A certain amount of deionized water or distilled water is filled in the interlayer between the autoclave and the liner tube 5 to maintain the pressure balance inside and outside the liner tube 5 and prevent the liner tube 5 from breaking or being crushed. If the caliber of the liner pipe 5 adopted is relatively large, it is necessary to add a hanging basket 10 in the liner pipe 5 , and place the compost in the hanging basket 10 .
上述实施方式中,培养料和矿化剂根据要培养的晶体按现有常规技术进行选择。所述的衬套管5可以是黄金衬套管5、银衬套管5或者是铂金衬套管5,所述的贵金属丝可以是金丝、银丝或铂丝。所述的结晶部件8可以是由泡沫金属制成的具有各种形状或结构,空心或实心的部件,具体地,结晶部件8可以是由泡沫金属制作的呈现出直线结构(如图2(f)、平面片状间隔堆叠结构(如图2(b)所示)、盘形结构(如图2(c)、齿状结构(如图2(d)所示)、空心柱状结构(如图2(e)所示)、螺旋结构(如图2(a)所示)或锥状结构等其它任意形状。所述的泡沫金属优选具有下述结构参数:孔径为0.01~10mm,孔隙率为50%~98%,通孔率≥90%,体积密度为0.05~1g/cm3,具体的可以是具有上述结构参数的泡沫铝、泡沫铜、泡沫镍、泡沫铁、泡沫银、泡沫金、泡沫铂或泡沫合金,所述的泡沫合金具体可以是铜锡泡沫合金、铜锌泡沫合金、钛镍泡沫合金或铝镁泡沫合金等。In the above embodiment, the culture material and the mineralizer are selected according to the existing conventional technology according to the crystal to be cultured. The bushing tube 5 may be a gold bushing tube 5 , a silver bushing tube 5 or a platinum bushing tube 5 , and the precious metal wire may be a gold wire, a silver wire or a platinum wire. Described crystalline part 8 can be made of foamed metal with various shapes or structures, hollow or solid parts, specifically, crystalline part 8 can be made of foamed metal and presents a linear structure (as shown in Fig. 2(f) ), planar sheet-like spaced stacking structure (as shown in Figure 2(b)), disk-shaped structure (as shown in Figure 2(c), tooth-shaped structure (as shown in Figure 2(d)), hollow columnar structure (as shown in Figure 2(d) 2 (e)), helical structure (as shown in Figure 2 (a)) or other arbitrary shapes such as cone structure. The metal foam preferably has the following structural parameters: the aperture is 0.01~10mm, and the porosity is 50%-98%, porosity ≥ 90%, bulk density 0.05-1g/cm 3 , specifically aluminum foam, copper foam, nickel foam, iron foam, silver foam, gold foam, Platinum foam or foam alloy, the foam alloy may specifically be copper-tin foam alloy, copper-zinc foam alloy, titanium-nickel foam alloy or aluminum-magnesium foam alloy.
实施例2:采用本发明所述装置水热法生长钪掺杂氧化锌单晶Example 2: Using the device of the present invention to grow scandium-doped zinc oxide single crystal by hydrothermal method
采用具有下述结构参数的泡沫镍制作结晶部件:孔径为0.1~0.5mm,孔隙率为>90%,通孔率为95%,体积密度0.85g/cm3。The crystalline part is made of nickel foam with the following structural parameters: 0.1-0.5mm pore diameter, >90% porosity, 95% through-porosity, and 0.85g/cm 3 volume density.
本实施例中用具有上述结构参数的泡沫镍制成的结晶部件8呈连续齿状结构,将制作好的结晶部件8在超声条件下用无水乙醇清洗5min,然后用0.1mol/L的盐酸溶液清洗20s,再在4mol/L的KOH溶液中清洗20s,之后真空干燥。之后按图1所示装置的结构构建本实施例所用的高压釜,其中衬套管5采用Φ22(衬套管5内径为22mm)的黄金衬套管5,贵金属丝采用金丝,将干燥的结晶部件8用金丝悬挂于黄金衬套管5的顶部(即黄金衬套管5的管盖上),如图2(d)所示,其余结构同实施例1。测得衬套管5无填充容积为57ml,填装原料(即培养料)为高纯氧化锌颗粒22.24g,钪掺杂量≤0.003g,矿化剂为4mol/L的KOH,内填充度为75%,填充完毕后将衬套管5管盖与衬套管5密封焊接;将密封好的衬套管5放入高压釜釜体4中,在衬套管5和高压釜的夹层之间填充70%体积的去离子水。将密封后的高压釜放入两段加热的电阻炉内。设定溶解区9平均温度为380℃,结晶区7平均温度为360℃,保持5天后随炉冷却至室温。开启高压釜及衬套管5,在泡沫镍制成的结晶部件8上得到自发成核晶体约12g,最大晶体尺寸达8.57mm×3.73mm×3.86mm,如附图3所示。图4为所得晶体的XRD图谱。实验结果表明增加结晶部件8后高压釜的结晶效果良好。In this embodiment, the crystalline part 8 made of nickel foam with the above structural parameters has a continuous tooth-like structure, and the crystalline part 8 is cleaned with absolute ethanol for 5 minutes under ultrasonic conditions, and then washed with 0.1 mol/L hydrochloric acid The solution was washed for 20s, and then washed in 4mol/L KOH solution for 20s, and then vacuum-dried. Build the used autoclave of present embodiment afterwards by the structure of device shown in Fig. 1, wherein liner pipe 5 adopts the gold liner pipe 5 of Φ 22 (liner pipe 5 internal diameters are 22mm), and precious metal wire adopts gold wire, will dry The crystal part 8 is suspended on the top of the gold bushing tube 5 (ie on the cap of the gold bushing tube 5 ) with a gold wire, as shown in FIG. It is measured that the unfilled volume of the liner tube 5 is 57ml, the filling raw material (ie compost) is 22.24g of high-purity zinc oxide particles, the doping amount of scandium is ≤0.003g, the mineralizer is KOH of 4mol/L, and the inner filling degree After filling, seal and weld the cover of the liner tube 5 and the liner tube 5; put the sealed liner tube 5 into the autoclave body 4, between the liner tube 5 and the interlayer of the autoclave Fill with 70% deionized water by volume. The sealed autoclave was placed in a two-stage heating resistance furnace. Set the average temperature of the dissolution zone 9 to 380°C, and the average temperature of the crystallization zone 7 to 360°C, keep it for 5 days and then cool to room temperature with the furnace. The autoclave and the liner tube 5 were turned on, and about 12 g of spontaneous nucleated crystals were obtained on the crystallization part 8 made of nickel foam, with a maximum crystal size of 8.57mm×3.73mm×3.86mm, as shown in Figure 3. Figure 4 is the XRD pattern of the obtained crystals. Experimental results show that the crystallization effect of the autoclave is good after the crystallization part 8 is added.
对比例comparative example
作为实施例2的对比实验,仅是在结晶区7悬挂金丝以替代实施例2中由泡沫镍制成的结晶部件8,其它工艺、条件均与实施例2相同。实验结果显示晶核并未在金丝及管壁上附着,仅仅在黄金衬套管5底部及黄金衬套管5管口焊缝处收集到直径≤2mm的晶粒,晶粒的总重量约为3g。As a comparative experiment of Example 2, only a gold wire is suspended in the crystallization area 7 to replace the crystallization part 8 made of nickel foam in Example 2, and other processes and conditions are the same as in Example 2. The experimental results show that the crystal nuclei are not attached to the gold wire and the tube wall, and only crystal grains with a diameter of ≤2 mm are collected at the bottom of the gold bushing tube 5 and the welding seam of the nozzle of the gold bushing tube 5. The total weight of the crystal grains is about for 3g.
实施例3:采用本发明所述装置水热法生长KTP(磷酸钛氧钾)单晶Embodiment 3: Adopt the device hydrothermal method of the present invention to grow KTP (potassium titanyl phosphate) single crystal
采用具有下述结构参数的泡沫银制作结晶部件:孔隙率≥85%,孔数:80~110PPI,厚度:(0.2~2.5)±0.05mm,比表面积≥10㎡/g。The crystalline parts are made of silver foam with the following structural parameters: porosity ≥ 85%, number of pores: 80-110PPI, thickness: (0.2-2.5) ± 0.05mm, specific surface area ≥ 10㎡/g.
本实施例中用具有上述结构参数的泡沫银制成的结晶部件8呈盘形结构,具体是从圆心开始向外螺旋盘排成盘形,将制作好的结晶部件8在超声条件下用无水乙醇清洗5min,然后用0.1mol/L的盐酸溶液清洗20s,再在4mol/L的KOH溶液中清洗20s,之后真空干燥。之后按图1所示装置的结构构建本实施例所用的高压釜,其中衬套管5采用Φ22(衬套管5内径为22mm)的黄金衬套管5,贵金属丝采用金丝,将干燥的结晶部件8用金丝悬挂于黄金衬套管5的顶部(即黄金衬套管5的管盖上),如图2(c)所示,其余结构同实施例1。测得衬套管5无填充容积为56.5ml,填装原料为磷酸钛氧钾原料22g,矿化剂为0.25mol/L的磷酸二氢钾与2.5mol/L的磷酸氢二钾混合溶液,内填充度为70%,填充完毕后将衬套管5管盖与衬套管5密封焊接;将密封好的衬套管5放入高压釜釜体4中,在衬套管5和高压釜的夹层之间填充65%体积的去离子水。将密封后的高压釜放入两段加热的电阻炉内。设定溶解区9平均温度510℃,结晶区7平均温度为450℃,保持10天后随炉冷却至室温。开启高压釜及衬套管5,在泡沫银结晶部件8上得到自发成核晶体约15g,最大晶体尺寸达10.06mm×8.27mm×3.71mm,如图5所示。对所得的晶体进行透过率测试,其透过率图谱如图6所示,与KTP标准图谱完全一致,可见上述所得的晶体光学质量十分优异。In the present embodiment, the crystalline part 8 made of foamed silver with the above structural parameters is in a disc-shaped structure, specifically, it is arranged in a disc shape from the center of the circle to the outer spiral disk, and the crystalline part 8 made under ultrasonic conditions is used without Wash with water and ethanol for 5 minutes, then wash with 0.1mol/L hydrochloric acid solution for 20s, then wash with 4mol/L KOH solution for 20s, and then vacuum dry. Build the used autoclave of present embodiment afterwards by the structure of device shown in Fig. 1, wherein liner pipe 5 adopts the gold liner pipe 5 of Φ 22 (liner pipe 5 internal diameters are 22mm), and precious metal wire adopts gold wire, will dry The crystallization part 8 is suspended on the top of the gold bushing tube 5 (i.e. on the cap of the gold bushing tube 5) with a gold wire, as shown in Figure 2(c), and all the other structures are the same as in Embodiment 1. It is measured that the liner pipe 5 has a non-filling volume of 56.5ml, and the filling material is 22g of potassium titanyl phosphate raw material, and the mineralizer is a mixed solution of potassium dihydrogen phosphate of 0.25mol/L and dipotassium hydrogen phosphate of 2.5mol/L. The inner filling degree is 70%. After the filling is completed, seal and weld the cover of the liner tube 5 and the liner tube 5; put the sealed liner tube 5 into the autoclave body 4, 65% volume of deionized water is filled between the interlayers. The sealed autoclave was placed in a two-stage heating resistance furnace. Set the average temperature of the dissolution zone 9 to 510°C, and the average temperature of the crystallization zone 7 to 450°C, keep it for 10 days and then cool to room temperature with the furnace. The autoclave and the liner tube 5 were turned on, and about 15 g of spontaneous nucleated crystals were obtained on the foamed silver crystallization part 8, with a maximum crystal size of 10.06mm×8.27mm×3.71mm, as shown in FIG. 5 . The transmittance of the obtained crystal was tested, and its transmittance spectrum is shown in Figure 6, which is completely consistent with the KTP standard spectrum. It can be seen that the optical quality of the crystal obtained above is very excellent.
申请经过大量试验得知,在高压釜内增加由泡沫金属制成的结晶部件8可以创造大量的成核位点,并直接获得大尺寸的晶体,与传统使用金丝、金片及金架无籽晶状态获得KTP晶体的方法(单次生长获得晶体质量<10g,最大晶体粒径≤5mm)相比,使用本发明所述的高压釜可有效增加自发成核体积和质量。After applying for a lot of tests, it is known that adding crystallization parts 8 made of metal foam in the autoclave can create a large number of nucleation sites, and directly obtain large-sized crystals, which is different from the traditional use of gold wires, gold sheets and gold frames. Compared with the method of obtaining KTP crystals in the seed crystal state (the crystal quality obtained in a single growth is <10g, and the maximum crystal particle size is ≤5mm), the autoclave of the present invention can effectively increase the volume and quality of spontaneous nucleation.
实施例4:采用本发明所述装置水热法生长磷酸亚铁锂单晶Embodiment 4: Using the device of the present invention to grow lithium iron phosphate single crystal by hydrothermal method
采用具有下述结构参数的泡沫铜制作结晶部件:孔径为0.6mm,孔隙率为>92%,通孔率为98%,体积密度0.6g/cm3。The crystalline part is made of copper foam with the following structural parameters: 0.6mm pore diameter, >92% porosity, 98% through-porosity, and 0.6g/cm 3 bulk density.
本实施例中用具有上述结构参数的泡沫铜制成的结晶部件8呈空心柱状结构,其中圆柱结构柱高150mm,内径为30mm,厚度为2.5mm。将制作好的结晶部件8在超声条件下用无水乙醇清洗5min,然后用0.1mol/L的盐酸溶液清洗20s,再在4mol/L的KOH溶液中清洗20s,之后真空干燥。之后按图1所示装置的结构构建本实施例所用的高压釜,其中衬套管5采用Φ42(衬套管5内径为38mm)的黄金衬套管5,贵金属丝采用金丝,将干燥的结晶部件8用金丝悬挂于黄金衬套管5的顶部(即黄金衬套管5的管盖上),如图2(e)所示,其余结构同实施例1。测得衬套管5无填充容积为710ml,填装原料为碳包覆磷酸亚铁锂粉末(桂林九一新能源材料公司)20g,矿化剂为饱和磷酸二氢锂溶液,内填充度为75%,填充完毕后将衬套管5管盖与衬套管5密封焊接;将密封好的衬套管5放入高压釜釜体4中,在衬套管5和高压釜的夹层之间填充70%体积的去离子水。将密封后的高压釜放入两段加热的电阻炉内。设定溶解区9平均温度480℃,结晶区7平均温度为450℃,保持5天后随炉冷却至室温。开启高压釜及衬套管5,在泡沫铜制成的结晶部件8上得到自发成核晶体约5g,最大晶体尺寸为280*150*80μm3,如图7所示。由本实施例所得的结晶产物为六棱柱形态的磷酸铁锂单晶,对单晶进行x-射线单晶衍射的分析,获得晶胞结构为D162h,Pbnm空间群,其中 α=β=γ=90°。样品的X-射线单晶衍射数据测得的晶胞参数(在SHELXL-97(Sheldrick,1997)软件程序中对结构进行解析、精修和数据输出。R1=0.0234,wR2(I>2σ)=0.0581;R1=0.0225,wR2(all)=0.0589)。由测试数据计算晶体密度为3.6061g/cm3,较之文献(YuriJanssen,DhamodaranSanthanagopalan,etal.ReciprocalSaltFluxGrowthofLiFePO4SingleCrystalswithControlledDefectConcentrations[J].Chem.Mater.2013,25,4574-4584)报道和ICSD数据库数据都有提高。In this embodiment, the crystalline part 8 made of foamed copper having the above structural parameters has a hollow columnar structure, wherein the column height of the cylindrical structure is 150mm, the inner diameter is 30mm, and the thickness is 2.5mm. The prepared crystal part 8 was cleaned with absolute ethanol for 5 minutes under ultrasonic conditions, then washed with 0.1 mol/L hydrochloric acid solution for 20 seconds, and then washed with 4 mol/L KOH solution for 20 seconds, and then vacuum-dried. Build the used autoclave of the present embodiment by the structure of device shown in Figure 1 afterwards, wherein liner pipe 5 adopts the gold liner pipe 5 of Φ 42 (liner pipe 5 inner diameters are 38mm), and precious metal wire adopts gold wire, will dry The crystal part 8 is suspended on the top of the gold bushing tube 5 (ie on the cap of the gold bushing tube 5 ) with a gold wire, as shown in Figure 2(e), and all the other structures are the same as in Embodiment 1. The measured liner tube 5 has a non-filling volume of 710ml, and the filling material is 20g of carbon-coated lithium iron phosphate powder (Guilin Jiuyi New Energy Materials Co., Ltd.), the mineralizer is saturated lithium dihydrogen phosphate solution, and the inner filling degree is 75%, after filling, seal and weld the cover of the liner tube 5 and the liner tube 5; put the sealed liner tube 5 into the autoclave body 4, between the liner tube 5 and the interlayer of the autoclave Fill to 70% volume with deionized water. The sealed autoclave was placed in a two-stage heating resistance furnace. Set the average temperature in the dissolution zone 9 to 480°C, and set the average temperature in the crystallization zone 7 to 450°C, keep it for 5 days and then cool to room temperature with the furnace. The autoclave and the liner tube 5 were turned on, and about 5 g of spontaneously nucleated crystals were obtained on the crystallization part 8 made of foamed copper, with a maximum crystal size of 280*150*80 μm 3 , as shown in FIG. 7 . The crystallized product obtained in this example is a lithium iron phosphate single crystal in the form of a hexagonal prism, and the single crystal is analyzed by x-ray single crystal diffraction, and the unit cell structure is obtained as D162h, Pbnm space group, wherein α=β=γ=90°. The unit cell parameters measured by the X-ray single crystal diffraction data of the sample (the structure is analyzed, refined and data output in the SHELXL-97 (Sheldrick, 1997) software program. R1=0.0234, wR 2 (I>2σ) = 0.0581; R1 = 0.0225, wR 2 (all) = 0.0589). The crystal density calculated from the test data is 3.6061g/cm 3 , which is higher than that reported in the literature (Yuri Janssen, Dhamodaran Santhanagopalan, et al. ReciprocalSaltFluxGrowthofLiFePO4SingleCrystalswithControlledDefectConcentrations[J]. Chem. Mater. 2013, 25, 4574-4584) and ICSD database data.
上述试验证明,增加泡沫金属制成的结晶部件8的高压釜特别适用于无籽晶、难生长的新型晶体的研发。The above test proves that the autoclave with crystal part 8 made of metal foam is especially suitable for the research and development of seedless and difficult-to-grow new crystals.
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| CN1445387A (en) * | 2003-04-25 | 2003-10-01 | 郎丽红 | Autoclave for artificial quartz crystal |
| CN2680347Y (en) * | 2004-03-19 | 2005-02-23 | 桂林矿产地质研究院 | Autoclave with thermal barrier |
| CN101103143A (en) * | 2005-01-12 | 2008-01-09 | 溶剂热结晶成长技术研究组合 | Pressure vessel for growing single crystals |
| CN101643937A (en) * | 2009-08-28 | 2010-02-10 | 桂林矿产地质研究院 | A kind of method of growing bismuth silicate single crystal by hydrothermal method |
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| CN202450181U (en) * | 2011-12-09 | 2012-09-26 | 中山兆龙光电科技有限公司 | Novel device for large-size crystal growth |
| CN204058646U (en) * | 2014-09-04 | 2014-12-31 | 中国有色桂林矿产地质研究院有限公司 | A kind of High Temperature High Pressure hydro-thermal still containing foamed metal crystallization parts |
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