CN111730060A - An atomizing spray disc, a method for preparing a narrow particle size alloy powder for additive manufacturing by gas atomization - Google Patents

An atomizing spray disc, a method for preparing a narrow particle size alloy powder for additive manufacturing by gas atomization Download PDF

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CN111730060A
CN111730060A CN202010358061.0A CN202010358061A CN111730060A CN 111730060 A CN111730060 A CN 111730060A CN 202010358061 A CN202010358061 A CN 202010358061A CN 111730060 A CN111730060 A CN 111730060A
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alloy powder
spray disk
spray
alloy
atomizing
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CN111730060B (en
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于月光
杜开平
沈婕
皮自强
郑兆然
马尧
胡宇
陆在平
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Bgrimm Advanced Materials Science & Technology Co ltd
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BGRIMM Technology Group Co Ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F9/00Making metallic powder or suspensions thereof
    • B22F9/02Making metallic powder or suspensions thereof using physical processes
    • B22F9/06Making metallic powder or suspensions thereof using physical processes starting from liquid material
    • B22F9/08Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying
    • B22F9/082Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying atomising using a fluid
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F1/00Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
    • B22F1/05Metallic powder characterised by the size or surface area of the particles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B33ADDITIVE MANUFACTURING TECHNOLOGY
    • B33YADDITIVE MANUFACTURING, i.e. MANUFACTURING OF THREE-DIMENSIONAL [3D] OBJECTS BY ADDITIVE DEPOSITION, ADDITIVE AGGLOMERATION OR ADDITIVE LAYERING, e.g. BY 3D PRINTING, STEREOLITHOGRAPHY OR SELECTIVE LASER SINTERING
    • B33Y70/00Materials specially adapted for additive manufacturing
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C19/00Alloys based on nickel or cobalt
    • C22C19/03Alloys based on nickel or cobalt based on nickel
    • C22C19/05Alloys based on nickel or cobalt based on nickel with chromium
    • C22C19/058Alloys based on nickel or cobalt based on nickel with chromium without Mo and W
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C38/00Ferrous alloys, e.g. steel alloys
    • C22C38/18Ferrous alloys, e.g. steel alloys containing chromium
    • C22C38/40Ferrous alloys, e.g. steel alloys containing chromium with nickel
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F9/00Making metallic powder or suspensions thereof
    • B22F9/02Making metallic powder or suspensions thereof using physical processes
    • B22F9/06Making metallic powder or suspensions thereof using physical processes starting from liquid material
    • B22F9/08Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying
    • B22F9/082Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying atomising using a fluid
    • B22F2009/0824Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying atomising using a fluid with a specific atomising fluid
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F9/00Making metallic powder or suspensions thereof
    • B22F9/02Making metallic powder or suspensions thereof using physical processes
    • B22F9/06Making metallic powder or suspensions thereof using physical processes starting from liquid material
    • B22F9/08Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying
    • B22F9/082Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying atomising using a fluid
    • B22F2009/0888Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying atomising using a fluid casting construction of the melt process, apparatus, intermediate reservoir, e.g. tundish, devices for temperature control

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  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • Manufacture Of Metal Powder And Suspensions Thereof (AREA)

Abstract

本发明公开了一种雾化喷盘、一种气雾化制备增材制造用窄粒径合金粉末的方法,属于粉末制备的领域,解决了制备窄粒径合金粉末的收得率低的技术问题。雾化喷盘包括喷盘主体、喷盘上连接体和喷盘下连接体,喷盘下连接体和喷盘上连接体之间形成环缝或在喷盘上连接体上开设环孔。一种气雾化制备增材制造用窄粒径合金粉末的方法,包括以下步骤:S1针对中值粒径为60μm以下的细粒径合金粉末制备,采用环缝喷盘制备;针对中值粒径为60μm以上的粗粒径合金粉末制备,采用环孔喷盘制备;S2确定喷盘的参数;S3确定雾化工艺参数。本发明的方法中使用本发明的雾化喷盘,具有低成本、高效制备高收得率窄粒径合金粉末的优势。

Figure 202010358061

The invention discloses an atomizing spray disc and a method for preparing narrow particle size alloy powder for additive manufacturing by gas atomization, which belongs to the field of powder preparation and solves the technology of preparing narrow particle size alloy powder with low yield question. The atomizing spray disc includes a spray disc main body, a spray disc upper connecting body and a spray disc lower connecting body. A ring seam is formed between the spray disc lower connecting body and the spray disc upper connecting body or an annular hole is formed on the spray disc upper connecting body. A method for preparing a narrow particle size alloy powder for additive manufacturing by gas atomization, comprising the following steps: S1, for the preparation of fine particle size alloy powder with a median particle size of less than 60 μm, using a ring-slit spray disc; Coarse-grained alloy powder with a diameter of more than 60 μm is prepared by using a ring-hole spray disc; S2 determines the parameters of the spray disc; S3 determines the atomization process parameters. Using the atomizing spray disc of the present invention in the method of the present invention has the advantages of low cost and high efficiency for preparing high yield and narrow particle size alloy powder.

Figure 202010358061

Description

一种雾化喷盘、一种气雾化制备增材制造用窄粒径合金粉末 的方法An atomizing spray disc, a gas atomization preparation of narrow particle size alloy powder for additive manufacturing Methods

技术领域technical field

本发明涉及粉末制备的技术领域,更具体地说,它涉及一种雾化喷盘、一种气雾化制备增材制造用窄粒径合金粉末的方法。The invention relates to the technical field of powder preparation, and more particularly, to an atomizing spray disc and a method for preparing narrow particle size alloy powder for additive manufacturing by gas atomization.

背景技术Background technique

随着激光工程化净成形、选区激光熔化、冷喷涂、激光熔覆等增材制造工艺在煤矿、汽车、船舶、航空航天等领域的不断应用,高质量合金粉末材料的需求日益增长。作为合金粉末制备的主流工艺,气雾化工艺的粉末制备量已达到世界粉末总产量的80%,部分发达国家和地区所占比例更为巨大。气雾化制粉技术是利用高压、高速气体冲击金属熔融液流,将熔融液流破碎成细小液滴并冷凝成粉末颗粒的非平衡快速过程,具有环境污染小、粉末球形度高、氧含量低以及冷却速率快等优点。但是由于制备得到的合金粉末的粒度分布范围广,而所需要的相对较窄的粒度分布区间内的合金粉末的收得率较低,即目标的窄粒径区间内的合金粉末的收得率较低(以下将窄粒度区间内的合金粉末简称为窄粒径合金粉末)。例如,选区激光熔化用中值粒径为30μm、粒度分布范围为15~53μm的GH4169镍基合金的合金粉末收得率仅为25%左右;激光熔覆技术用的中值粒径为95μm、粒度分布范围为53~150μm的FeNiCr不锈钢合金粉末收得率仅约为35%。With the continuous application of additive manufacturing processes such as laser engineered net shaping, selective laser melting, cold spraying, and laser cladding in coal mines, automobiles, ships, aerospace and other fields, the demand for high-quality alloy powder materials is increasing. As the mainstream process of alloy powder preparation, the powder preparation volume of gas atomization process has reached 80% of the world's total powder production, and the proportion of some developed countries and regions is even greater. Gas atomization pulverizing technology is a non-equilibrium and fast process that uses high-pressure and high-speed gas to impinge on the molten metal flow, breaking the molten liquid into fine droplets and condensing them into powder particles. It has less environmental pollution, high powder sphericity, and oxygen content. low and fast cooling rates. However, due to the wide range of particle size distribution of the prepared alloy powder, the yield of the alloy powder within the relatively narrow particle size distribution range required is relatively low, that is, the yield of the alloy powder within the target narrow particle size range is low. Lower (hereinafter, the alloy powder in the narrow particle size range is simply referred to as the narrow particle size alloy powder). For example, the yield of GH4169 nickel-based alloy with a median particle size of 30 μm and a particle size distribution range of 15 to 53 μm for selective laser melting is only about 25%; the median particle size for laser cladding technology is 95 μm, The yield of FeNiCr stainless steel alloy powder with a particle size distribution ranging from 53 to 150 μm is only about 35%.

为提高气雾化工艺的粉末成品率,合金粉末粒度的分布区间应尽可能多的集中在目标粒度范围内,即实现高收得率的窄粒径合金粉末的制备,因此如何实现目标气雾化粉末粒度的调控,是气雾化制粉技术降低生产成本、提高生产效率的关键,更是本领域技术人员渴望解决的技术难题。目前在这方面研究较多的是采用某种合金原料并通对气雾化工艺的优化来制备满足生产要求的合金粉末,以获得更多的目标粒度范围的合金粉末。In order to improve the powder yield of the gas atomization process, the distribution range of the particle size of the alloy powder should be concentrated in the target particle size range as much as possible, that is, the preparation of narrow particle size alloy powder with high yield, so how to achieve the target aerosol The regulation of the particle size of the chemical powder is the key to reducing the production cost and improving the production efficiency of the gas atomization pulverizing technology, and it is also a technical problem that those skilled in the art are eager to solve. At present, most of the research in this area is to use a certain alloy raw material and optimize the gas atomization process to prepare the alloy powder that meets the production requirements, so as to obtain more alloy powder with the target particle size range.

授权公告号为CN106399863B的发明专利公开了一种激光增材24CrNiMoRE合金钢粉末及制备方法,其方法利用真空坩埚感应熔炼气雾化方法,通过调控气雾化工艺参数,制备出具有球形、流动性良好、粒径范围可控、空心球率低、组织强韧性化的粉末。The invention patent with the authorization announcement number CN106399863B discloses a laser additive 24CrNiMoRE alloy steel powder and a preparation method. The method utilizes the vacuum crucible induction melting gas atomization method, and by adjusting the gas atomization process parameters, prepares a spherical, fluid Good powder with controllable particle size range, low hollow sphere rate, strong and tough structure.

但是该方法仅仅讨论了合金粉末制备中气雾化过程中的工艺参数对制备结果的影响,但影响目标粒度范围内的合金粉末收得率的因素还有很多;且现有技术中并未出现针对不同中值粒径合金粉末的高收得率的制备提出相关的方法和指导,从而使得目标中值粒径的粒度范围内的合金粉末的收得率不高。However, this method only discusses the influence of the process parameters in the gas atomization process in the preparation of alloy powder on the preparation result, but there are many factors affecting the yield of alloy powder within the target particle size range; Relevant methods and guidance are proposed for the preparation of high yields of alloy powders with different median diameters, so that the yields of alloy powders within the particle size range of the target median diameter are not high.

发明内容SUMMARY OF THE INVENTION

针对现有技术存在的不足,本发明的第一个目的在于提供一种雾化喷盘,其具有通过喷盘上连接体和喷盘下连接体的安装转换实现环缝雾化喷盘和环孔雾化喷盘之间的快速转换,具有使得制备窄粒径合金粉末的设备成本低、制备过程更加高效且设备适用于不同粒度范围的窄粒径合金粉末的制备的优势。Aiming at the deficiencies of the prior art, the first object of the present invention is to provide an atomizing spray disc, which has the ability to realize the annular seam atomization spray disc and the ring through the installation and conversion of the upper connecting body of the spray disc and the lower connecting body of the spray disc. The fast switching between the orifice atomizing spray discs has the advantages of low cost of equipment for preparing narrow particle size alloy powder, more efficient preparation process, and the equipment is suitable for the preparation of narrow particle size alloy powder with different particle size ranges.

本发明的第二个目的在于提供一种气雾化制备增材制造用窄粒径合金粉末的方法,其具有针对不同制备目,综合考虑雾化喷盘的影响因素,使得制备得到的目标粒度范围内的窄粒径合金粉末的收得率高的优点。The second object of the present invention is to provide a method for preparing narrow particle size alloy powder for additive manufacturing by gas atomization. The advantage of high yield of narrow particle size alloy powder in the range.

为实现上述第一个目的,本发明提供了如下技术方案:包括环状喷盘主体以及插设在喷盘主体中并封闭喷盘主体的上、下两端的喷盘上连接体、喷盘下连接体,所述喷盘上连接体、喷盘下连接体均和喷盘主体可拆卸密封连接,所述喷盘上连接体包括具有一中心孔的进料筒,所述喷盘下连接体套设在喷盘上连接体的进料筒下部外周面,所述喷盘主体、喷盘上连接体、喷盘下连接体之间形成气腔,所述喷盘主体的周面开设有进气口;所述进料筒下部外周面和喷盘下连接体之间形成连通所述气腔的环缝,即为环缝雾化喷盘;或者,所述喷盘下连接体与喷盘上连接体的进料筒下部密封套设,喷盘上连接体上的进料筒下端面自下而上开设有若干连通所述气腔的通孔,所述通孔环绕中心孔呈环形均匀排布,即为环孔雾化喷盘。In order to achieve the above-mentioned first purpose, the present invention provides the following technical scheme: comprising an annular spray disc body and a spray disc upper connecting body inserted in the spray disc body and closing the upper and lower ends of the spray disc body, a spray disc lower body A connecting body, the upper connecting body of the spray disc and the lower connecting body of the spraying disc are detachably and sealingly connected to the main body of the spraying disc, the upper connecting body of the spraying disc includes a feeding cylinder with a central hole, and the lower connecting body of the spraying disc is The outer peripheral surface of the lower part of the feed cylinder sleeved on the connecting body of the spray disc, an air cavity is formed between the main body of the spray disc, the upper connecting body of the spraying disc, and the lower connecting body of the spraying disc, and the peripheral surface of the spraying disc main body is provided with an inlet. Air port; an annular seam connecting the air cavity is formed between the outer peripheral surface of the lower part of the feeding cylinder and the lower connecting body of the spray disc, that is, the annular seam atomizing spray disc; or, the lower connecting body of the spray disc and the spray disc The lower part of the feeding cylinder of the upper connecting body is sealed and sleeved, and the lower end face of the feeding cylinder on the upper connecting body of the spray disc is provided with a plurality of through holes connecting the air cavity from bottom to top, and the through holes are annular and uniform around the central hole. Arrangement, that is, the ring hole atomizing spray disc.

通过采用上述技术方案,首先,针对不同粒度范围内的合金粉末的制备目的,上述的雾化喷盘提供给了一种可使用的喷盘;其次,现有的气雾化设备在使用的过程中喷盘上连接体和喷盘下连接体形成的喷嘴处(即环缝和环孔处)损坏后就无法实现高收得率的合金粉末的制备,因此要将喷盘整体更换,但是现有的雾化喷盘的价格比较贵,所以将喷盘做成可拆卸的,即喷盘上连接体和喷盘下连接体的配合使用之后,喷嘴的损坏只要更换不同的喷盘上连接体和喷盘下连接体即可。而相对的,喷盘上连接体和喷盘下连接体的体积较小,制备喷盘上连接体和喷盘下连接体的成本和制备雾化喷盘的成本相比低很多,因此实现环缝雾化喷盘和环孔喷盘共用同一个喷盘主体,也在很大程度上减少了生产过程中的设备成本。By adopting the above technical solution, firstly, for the purpose of preparing alloy powders in different particle size ranges, the above-mentioned atomizing spray disc provides a usable spray disc; secondly, the process of using the existing gas atomization equipment The preparation of alloy powder with high yield cannot be achieved after the nozzle formed by the connecting body on the middle spray disc and the connecting body under the spray disc (that is, at the annular seam and the annular hole) is damaged. The price of some atomizing spray discs is relatively expensive, so the spray disc is made detachable, that is, after the connecting body on the spray disc and the connecting body under the spray disc are used together, the damage to the nozzle only needs to replace the connecting body on the different spray disc. It can be connected with the connecting body under the spray disc. In contrast, the volume of the connecting body on the spray disc and the connecting body under the spray disc is small, and the cost of preparing the connecting body on the spray disc and the connecting body under the spray disc is much lower than the cost of preparing the atomizing spray disc. The slot atomizing spray disk and the annular spray disk share the same spray disk body, which also greatly reduces the equipment cost in the production process.

进一步地,所述喷盘上连接体的纵剖面为类“T”字形,所述进料筒为倒置的锥筒状,进料筒上部边缘沿径向凸设有圆环状的第一上水平连接部;所述喷盘下连接体包括倒置的锥筒状的第二筒体,所述第二筒体设置在进料筒外且进料筒外壁和第二筒体内壁之间形成环缝。Further, the longitudinal section of the connecting body on the spray disc is a "T"-like shape, the feeding cylinder is an inverted cone-shaped cylinder, and the upper edge of the feeding cylinder is radially protruded with an annular first upper a horizontal connection part; the lower connection body of the spray disc includes an inverted cone-shaped second cylinder, the second cylinder is arranged outside the feeding cylinder and a ring is formed between the outer wall of the feeding cylinder and the inner wall of the second cylinder sew.

通过采用上述技术方案,通过喷盘上连接体和喷盘下连接体以及喷盘主体之间的可拆卸实现了喷盘的更换,简单方便且密封性好,能够满足实际生产过程中不同中值粒径的细粒径合金粉末的生产要求。By adopting the above technical solution, the replacement of the spray disc is realized through the detachment between the upper connecting body of the spraying disc, the lower connecting body of the spraying disc and the main body of the spraying disc, which is simple and convenient and has good sealing performance, and can meet the different median values in the actual production process. Production requirements for fine particle size alloy powders.

进一步地,所述环缝的宽度d1为0.1~1.0mm,所述环缝下端的孔心距L1为5~40mm,所述环缝喷盘的喷射顶角α1为15~60°。Further, the width d 1 of the annular seam is 0.1-1.0 mm, the center-to-center distance L 1 of the lower end of the annular seam is 5-40 mm, and the spray tip angle α 1 of the annular seam spray disc is 15-60° .

通过采用上述技术方案,在上述的参数调节下,使得获得的中值粒径在60μm以下的细粒径合金粉末的收得率更高;而上述的环缝调节参数为工业生产提供了较大的调节范围,使得其适用于不同工业生产要求,实用性更强。By adopting the above technical scheme, under the adjustment of the above parameters, the yield of the obtained fine-grained alloy powder with a median diameter of less than 60 μm is higher; and the above-mentioned adjustment parameters of the annular seam provide a larger value for industrial production. The adjustment range makes it suitable for different industrial production requirements and has stronger practicability.

进一步地,所述喷盘上连接体的纵剖面为类“工”字形,所述进料筒为倒置的锥筒状,进料筒上部边缘沿径向凸设有圆环状的第二上水平连接部,进料筒下部外表面套设有环状的第二下水平连接部;所述第二上水平连接部的最大轴截面大于第二下水平连接部的最大轴截面,所述第二上水平连接部和喷盘主体可拆卸连接;所述喷盘下连接体为筒状且可拆卸连接在喷盘主体和第二下水平连接部之间;所述通孔开设在所述第二下水平连接部的靠近其与进料筒的套接处;其中,所述喷盘下连接体和第二下水平连接部之间设置有密封件。Further, the longitudinal section of the connecting body on the spray disc is an "I"-like shape, the feeding cylinder is in the shape of an inverted cone, and the upper edge of the feeding cylinder is radially provided with an annular second upper The horizontal connecting part, the outer surface of the lower part of the feeding cylinder is sleeved with an annular second lower horizontal connecting part; the maximum axial cross section of the second upper horizontal connecting part is larger than the largest axial cross section of the second lower horizontal connecting part, the The two upper horizontal connecting parts are detachably connected to the main body of the spray disc; the lower connecting body of the spray disc is cylindrical and is detachably connected between the main body of the spray disc and the second lower horizontal connecting part; the through hole is opened in the third The two lower horizontal connecting parts are close to the sleeve joints with the feeding cylinder; wherein, a sealing member is arranged between the lower connecting body of the spray disc and the second lower horizontal connecting part.

通过采用上述技术方案,和现有技术中的环孔喷盘的结构不同的是,现有技术中的环孔雾化喷盘的上连接体和下连接体一体成型,而本发明中的喷盘上连接体和喷盘下连接体以及喷盘主体之间为可拆卸连接。这样设置的优势在于:首先实现了喷盘的更换,简单方便且密封性好;其次喷嘴处损坏之后不必直接更换昂贵的喷盘,只要更换喷盘上连接体和喷盘下连接体即可,降低成本;除此以外,能够根据实际生产过程中不同中值粒径的粗粒径合金粉末的生产要求适配适合的喷盘上连接体和喷盘下连接体,使得设备的实用性更高。By adopting the above technical solution, the structure of the annular hole spray disc in the prior art is different from the structure of the annular hole spray disc in the prior art. The upper connecting body and the lower connecting body of the annular hole atomizing spray disc in the prior art The upper connecting body of the disc, the lower connecting body of the spraying disc and the main body of the spraying disc are detachably connected. The advantages of this arrangement are: first, the replacement of the spray disc is simple, convenient and has good sealing performance; secondly, after the nozzle is damaged, it is not necessary to directly replace the expensive spray disc, but only the upper connecting body of the spray disc and the lower connecting body of the spray disc can be replaced. Reduce costs; in addition, according to the production requirements of coarse-grained alloy powders with different median diameters in the actual production process, suitable upper and lower connectors of the spray disc can be adapted, which makes the equipment more practical. .

进一步地,所述通孔的内径d2为0.1~2.0mm,所述环孔喷盘的喷射顶角α2为15~60°,所述通孔下端的孔心距L2为5~40mm,通孔数量n为4~40个。Further, the inner diameter d 2 of the through hole is 0.1-2.0 mm, the spray apex angle α 2 of the annular spray disc is 15-60°, and the hole center distance L 2 at the lower end of the through hole is 5-40 mm , the number n of through holes is 4 to 40.

通过采用上述技术方案,在上述的参数调节下,使得获得的中值粒径在60μm以上的粗粒径合金粉末的收得率更高。同时,操作简单,易实现工业,且适用于不同的工业要求。By adopting the above technical solution, under the above parameter adjustment, the obtained coarse-grained alloy powder with a median diameter of 60 μm or more has a higher yield. At the same time, the operation is simple, easy to realize industrial, and suitable for different industrial requirements.

为实现上述第二个目的,本发明提供了如下技术方案:For realizing the above-mentioned second purpose, the present invention provides the following technical solutions:

S1根据待制备的窄粒径合金粉末的不同目标中值粒径的制备要求,选择所要使用的雾化喷盘类型,其中,针对中值粒径为60μm以下的细粒径合金粉末的制备,采用环缝雾化喷盘;针对中值粒径为60μm以上的粗粒径合金粉末的制备,采用环孔雾化喷盘;S1 According to the preparation requirements of different target median particle diameters of the narrow particle diameter alloy powder to be prepared, the type of atomizing spray disc to be used is selected, wherein, for the preparation of fine particle diameter alloy powder with a median particle diameter of 60 μm or less, A ring-slit atomizing spray disc is used; for the preparation of coarse-grained alloy powders with a median particle size of more than 60 μm, a ring-hole atomizing spray disc is used;

S2使得高温金属熔液通过中心孔进入雾化喷盘,同时自进气口通入惰性气体,调节气雾化参数后,惰性气体通过环缝或通孔后生成合金粉末;S2 makes the high-temperature molten metal enter the atomizing spray disc through the central hole, and at the same time, the inert gas is introduced from the air inlet. After adjusting the gas atomization parameters, the inert gas passes through the annular seam or through hole to generate alloy powder;

其中,所述环缝雾化喷盘为权利要求1-3任一所述的环缝雾化喷盘,所述环孔雾化喷盘为权利要求1、4-5任一所述的环孔雾化喷盘;所述合金选自GH4169、GH3625、NiCrAlY、316L以及FeNiCr型合金中的一种,其中NiCrAlY型合金的具体合金成分为:Cr 21%~26.5%,Al4%~11%,Y 0.3%~1.3%,余量为Ni;FeNiCr型合金的具体合金成分为:Ni 0.5%~6%,Cr 14%~18%,余量为Fe;NiCoCrAlY合金的具体成分为:Co 20%~24%,Cr 15%~20%,Al 11%~13%,Y 0.3%~0.8%,余量为Ni。Wherein, the annular slot atomizing spray disc is the annular slot atomizing spray disc described in any one of claims 1-3, and the annular hole atomizing spray disc is the annular slot atomizing spray disc described in any one of claims 1, 4-5 Hole atomizing spray disc; the alloy is selected from one of GH4169, GH3625, NiCrAlY, 316L and FeNiCr type alloys, wherein the specific alloy composition of NiCrAlY type alloy is: Cr 21%~26.5%, Al4%~11%, Y 0.3%~1.3%, the balance is Ni; the specific alloy composition of FeNiCr alloy is: Ni 0.5%~6%, Cr 14%~18%, the balance is Fe; the specific composition of NiCoCrAlY alloy is: Co 20% ~ 24%, Cr 15% ~ 20%, Al 11% ~ 13%, Y 0.3% ~ 0.8%, the balance is Ni.

通过采用上述技术方案,在同样的气压之下,通过环缝雾化喷盘后获得的合金粉末的粒径比通过环孔雾化喷盘后获得的合金粉末的粒径要小,而对于不同合金粉末的制备要求,本发明首先是根据所要获得的目标合金粉末的粒度范围,选择不同的雾化喷盘:以合金粉末的目标中值粒径为判断标准,中值粒径为60μm以上的合金粉末和中值粒径为60μm以下的合金粉末的制备所选择的喷盘不同;其次再对具体某一种喷盘的设备参数进行选择;最后考虑的是对气雾化过程中的工艺参数进行筛选优化。采用上述的方式实现了对中值粒径为60μm以上的粗粒径合金粉末和中值粒径为60μm以下的细粒径合金粉末的较窄粒度区间内的合金粉末的高收得率的制备。而且通过对上述的相关参数的优化,有效提高了目标的窄粒径合金粉末的收得率。By adopting the above technical solution, under the same air pressure, the particle size of the alloy powder obtained after passing through the annular slot atomized spray disc is smaller than that of the alloy powder obtained after passing through the annular hole atomized spray disc. According to the preparation requirements of alloy powder, the present invention first selects different atomizing spray discs according to the particle size range of the target alloy powder to be obtained: the target median particle size of the alloy powder is used as the judgment standard, and the median particle size is more than 60 μm. The spray discs selected for the preparation of alloy powder and alloy powder with a median particle size of less than 60 μm are different; secondly, the equipment parameters of a specific spray disc are selected; the last consideration is the process parameters in the gas atomization process. Filter optimization. The above-mentioned method achieves the preparation of alloy powder with high yield in a narrow particle size range of coarse-grained alloy powder with a median particle size of 60 μm or more and fine-grained alloy powder with a median particle size of 60 μm or less . Moreover, by optimizing the above-mentioned relevant parameters, the yield of the target narrow particle size alloy powder is effectively improved.

进一步地,所述步骤S2中雾化气体压力为0.5~4.0MPa,雾化气体温度为10~300℃,高温金属熔液的过热度为50~300℃,高温金属熔液的流量为0.5~20kg/min。Further, in the step S2, the pressure of the atomizing gas is 0.5-4.0 MPa, the temperature of the atomizing gas is 10-300 °C, the superheat degree of the high-temperature molten metal is 50-300 °C, and the flow rate of the high-temperature molten metal is 0.5-300 °C. 20kg/min.

通过采用上述技术方案,通过与操作目标相适应的工业操作条件,使得更有利于获得高收得率的目标粒度区间的合金粉末。By adopting the above-mentioned technical solution, it is more favorable to obtain alloy powder with a high yield and a target particle size range through industrial operation conditions suitable for the operation target.

进一步地,当采用316L合金制备中值粒径为30μm、目标粒度范围为15~53μm的细粒径合金粉末时,采用环缝喷盘进行合金粉末的制备,所述环缝的宽度d1的选择范围为0.2~1.0mm,所述环缝下端的孔心距L1的选择范围为5~40mm,所述喷射顶角α1为15~60°,雾化气体压力为3.0~4.0MPa,雾化气体温度为20~300℃,高温金属熔液的过热度为200~300℃,高温金属熔液的流量为0.5~20kg/min;Further, when using 316L alloy to prepare fine-grained alloy powder with a median particle size of 30 μm and a target particle size range of 15-53 μm, a ring-slit spray disc is used to prepare the alloy powder. The selection range is 0.2-1.0 mm, the selection range of the hole center distance L 1 at the lower end of the annular seam is 5-40 mm, the spray top angle α 1 is 15-60°, and the atomizing gas pressure is 3.0-4.0 MPa, The atomizing gas temperature is 20~300℃, the superheat degree of the high temperature metal melt is 200~300℃, and the flow rate of the high temperature metal melt is 0.5~20kg/min;

当采用GH4169合金制备中值粒径为30μm、目标粒度范围为15~53μm的细粒径合金粉末时,采用环缝喷盘进行合金粉末的制备,所述环缝的宽度d1为0.8mm,所述环缝下端的孔心距L1为14mm,所述喷射顶角α1为30°,雾化气体压力为3.0MPa,雾化气体温度为20℃,高温金属熔液的过热度为200℃,高温金属熔液的流量为10kg/min;When the GH4169 alloy is used to prepare fine-grained alloy powder with a median particle size of 30 μm and a target particle size range of 15-53 μm, a ring-slit spray disc is used to prepare the alloy powder, and the width d1 of the ring-slit is 0.8 mm, The hole-to-center distance L1 at the lower end of the annular seam is 14 mm, the spray apex angle α1 is 30 °, the atomizing gas pressure is 3.0 MPa, the atomizing gas temperature is 20°C, and the superheat degree of the high-temperature metal melt is 200°C. ℃, the flow rate of high temperature molten metal is 10kg/min;

当采用GH3625合金制备中值粒径为30μm、目标粒度范围为15~53μm的细粒径合金粉末时,采用环缝喷盘进行合金粉末的制备,所述环缝的宽度d1为0.8mm,所述环缝下端的孔心距L1为12mm,所述喷射顶角α1为34°,雾化气体压力为3.5MPa,雾化气体温度为20℃,高温金属熔液的过热度为200℃,高温金属熔液的流量为10kg/min;When the GH3625 alloy is used to prepare fine-grained alloy powder with a median particle size of 30 μm and a target particle size range of 15 to 53 μm, a ring-slit spray disc is used to prepare the alloy powder, and the width d 1 of the annular slit is 0.8 mm, The hole-to-center distance L1 at the lower end of the annular seam is 12 mm, the spray apex angle α1 is 34°, the atomizing gas pressure is 3.5MPa, the atomizing gas temperature is 20°C, and the superheat degree of the high-temperature metal melt is 200°C. ℃, the flow rate of high temperature molten metal is 10kg/min;

当采用NiCrAlY合金制备中值粒径为20μm、目标粒度范围为小于38μm的细粒径合金粉末时,采用环缝喷盘进行合金粉末的制备,所述环缝的宽度d1为0.6mm,所述环缝下端的孔心距L1为14mm,所述喷射顶角α1为30°,雾化气体压力为3.5MPa,雾化气体温度为20℃,高温金属熔液的过热度为200℃,高温金属熔液的流量为10kg/min;When NiCrAlY alloy is used to prepare fine-grained alloy powder with a median particle size of 20 μm and a target particle size range of less than 38 μm, a ring-slit spray disc is used to prepare the alloy powder. The hole-to-center distance L1 at the lower end of the annular seam is 14mm, the spray top angle α1 is 30 °, the atomizing gas pressure is 3.5MPa, the atomizing gas temperature is 20°C, and the superheat degree of the high-temperature metal melt is 200°C , the flow rate of high temperature metal melt is 10kg/min;

当采用NiCoCrAlY合金制备中值粒径为56μm、目标粒度范围为38~75μm的细粒径合金粉末时,采用环缝喷盘进行合金粉末的制备,所述环缝的宽度d1为0.6mm,所述环缝下端的孔心距L1为14mm,所述喷射顶角α1为30°,雾化气体压力为3.0MPa,雾化气体温度为20℃,高温金属熔液的过热度为200℃,高温金属熔液的流量为10kg/min;When the NiCoCrAlY alloy is used to prepare fine-grained alloy powder with a median particle size of 56 μm and a target particle size range of 38 to 75 μm, a ring-slit spray disc is used to prepare the alloy powder, and the width d 1 of the annular slit is 0.6 mm, The hole-to-center distance L1 at the lower end of the annular seam is 14 mm, the spray apex angle α1 is 30 °, the atomizing gas pressure is 3.0 MPa, the atomizing gas temperature is 20°C, and the superheat degree of the high-temperature metal melt is 200°C. ℃, the flow rate of high temperature molten metal is 10kg/min;

当采用NiCrAlY合金制备中值粒径为67μm、目标粒度范围为45~90μm的粗粒径合金粉末时,采用环孔喷盘进行合金粉末的制备,所述环孔宽度d2为0.5mm,所述环孔下端的孔心距L2为20mm,所述喷射顶角α2为28°,所述环孔数量为30,雾化气体压力为3.5MPa,雾化气体温度为20℃,高温金属熔液的过热度为200℃,高温金属熔液的流量为10kg/min;When NiCrAlY alloy is used to prepare coarse-grained alloy powder with a median particle size of 67 μm and a target particle size range of 45 to 90 μm, a ring-hole spray disc is used to prepare the alloy powder. The ring-hole width d 2 is 0.5 mm, so The hole-to - center distance L2 at the lower end of the ring hole is 20mm, the spray top angle α2 is 28°, the number of the ring holes is 30, the atomizing gas pressure is 3.5MPa, the atomizing gas temperature is 20°C, and the high temperature metal The superheat degree of the melt is 200℃, and the flow rate of the high temperature metal melt is 10kg/min;

当采用FeNiCr合金制备中值粒径为95μm、目标粒度范围为53~150μm的粗粒径合金粉末时,采用环孔喷盘进行合金粉末的制备,所述环孔宽度d2为0.5mm,所述环孔下端的孔心距L2为20mm,所述喷射顶角α2为28°,所述环孔数量为30,雾化气体压力为2.5MPa,雾化气体温度为20℃,高温金属熔液的过热度为200℃,高温金属熔液的流量为15kg/min。When FeNiCr alloy is used to prepare coarse-grained alloy powder with a median particle size of 95 μm and a target particle size range of 53 to 150 μm, a ring-hole spray disc is used to prepare the alloy powder. The ring-hole width d 2 is 0.5 mm, so The hole-to - center distance L2 at the lower end of the ring hole is 20mm, the spray top angle α2 is 28°, the number of the ring holes is 30, the atomizing gas pressure is 2.5MPa, the atomizing gas temperature is 20°C, and the high temperature metal The superheat degree of the molten metal was 200°C, and the flow rate of the high-temperature molten metal was 15 kg/min.

通过采用上述技术方案,在进行合金粉末的制备之前,首先根据制备目的,选择所要使用的喷盘,随后选择优化的喷盘参数,最后对气雾化工艺进行优选。在上述的工艺条件下制备得到的目标的窄粒径合金粉末的收得率较高。By adopting the above technical solution, before preparing the alloy powder, firstly select the spray disc to be used according to the preparation purpose, then select the optimized spray disc parameters, and finally optimize the gas atomization process. The yield of the target narrow particle size alloy powder prepared under the above-mentioned process conditions is relatively high.

进一步地,当采用316L合金制备中值粒径为30μm、目标粒度范围为15~53μm的细粒径合金粉末时,采用环缝喷盘进行合金粉末的制备,所述环缝的宽度d1为0.2mm,所述环缝下端的孔心距L1为16mm,所述喷射顶角α1为30°,雾化气体压力为3.0MPa,雾化气体温度为20℃,高温金属熔液的过热度为200℃,高温金属熔液的流量为10kg/min。Further, when the 316L alloy is used to prepare fine-grained alloy powder with a median particle size of 30 μm and a target particle size range of 15-53 μm, a ring-slit spray disc is used to prepare the alloy powder, and the width d1 of the ring-slit is 0.2 mm, the hole-center distance L 1 at the lower end of the annular seam is 16 mm, the spray apex angle α 1 is 30°, the atomizing gas pressure is 3.0 MPa, the atomizing gas temperature is 20° C. The heat was 200°C, and the flow rate of the high-temperature molten metal was 10kg/min.

进一步地,所述高温金属熔液通过将金属原材料和/或返料熔炼后获得,或者将母合金棒熔炼获得。Further, the high-temperature molten metal is obtained by smelting metal raw materials and/or return materials, or by smelting master alloy rods.

通过采用上述技术方案,简单高效的实现高温金属熔液的原料。By adopting the above technical solutions, the raw material of the high-temperature molten metal can be realized simply and efficiently.

综上所述,本发明具有以下有益效果:To sum up, the present invention has the following beneficial effects:

第一、本发明可针对不同合金粉末目标粒度要求,首先选择不同的雾化喷盘,并对雾化喷盘的参数筛选,以便针对不同的制备目的进行差异化破碎,使得制备得到的窄粒径合金粉末的收得率较高且满足增材制造技术对于粉末性能的特殊要求。First, according to the target particle size requirements of different alloy powders, the present invention can first select different atomizing spray discs, and screen the parameters of the atomizing spray discs, so as to carry out differential crushing for different preparation purposes, so that the narrow particles obtained can be obtained. The yield of diameter alloy powder is high and meets the special requirements of additive manufacturing technology for powder properties.

第二、本发明提供的一种雾化喷盘通过匹配不同的喷盘上连接体和喷盘下连接体,使得同一台雾化设备能够满足不同粒度区间的粉末制备目的;与此同时,对于喷盘的损坏更换更加便捷、设备成本降低。Second, the atomizing spray disc provided by the present invention enables the same atomizing equipment to meet the purpose of powder preparation in different particle size ranges by matching different upper connecting bodies of the spraying disc and lower connecting bodies of the spraying disc; at the same time, for Damaged and replaced spray discs are more convenient and equipment costs are reduced.

附图说明Description of drawings

图1为环缝雾化喷盘的剖视图;Fig. 1 is the sectional view of the circular seam atomizing spray disc;

图2为环孔雾化喷盘的剖视图;Fig. 2 is the sectional view of annular hole atomizing spray disc;

图3为实施例1制备得到的细粒径合金粉末的SEM电镜下的形貌图;Fig. 3 is the topography under the SEM electron microscope of the fine-grained alloy powder prepared in Example 1;

图4为实施例16制备得到的粗粒径合金粉末的SEM电镜下的形貌图。FIG. 4 is a morphological diagram under the SEM electron microscope of the coarse-grained alloy powder prepared in Example 16. FIG.

图中,1、喷盘主体;11、喷盘上连接体安装避让槽;12、喷盘下连接体安装避让槽;2、喷盘上连接体;21、第一上水平连接部;22、进料筒;23、第二上水平连接部;25、第二下水平连接部;251、第二下水平连接部安装避让槽;3、喷盘下连接体;31、第二筒体;4、中心孔;5、气腔;6、进气口;7、环缝;8、通孔。In the figure, 1, the main body of the spray disc; 11, the connecting body on the spray disc is installed with an avoidance groove; 12, the lower connecting body of the spray disc is installed with an avoidance groove; 2, the upper connecting body on the spray disc; 21, the first upper horizontal connection part; 22, Feeding cylinder; 23. The second upper horizontal connecting part; 25. The second lower horizontal connecting part; , central hole; 5, air cavity; 6, air inlet; 7, annular seam; 8, through hole.

具体实施方式Detailed ways

以下结合附图和实施例对本发明作进一步详细说明。The present invention will be described in further detail below with reference to the accompanying drawings and embodiments.

粉末粒度分级设备分别为振动筛分机和气流分级机,振动筛分机购自新乡市宏升机械有限公司,设备型号为:¢800mm;气流分级机购自四川巨子超微科技有限公司,设备型号为JZF-200;气雾化设备购自邯郸市旭瑞合金材料有限公司,设备型号为:XR-PF(Q-2k)5。The powder particle size classification equipment is a vibrating screen and an air classifier. The vibrating screen is purchased from Xinxiang Hongsheng Machinery Co., Ltd., and the equipment model is: ¢800mm; the air classifier is purchased from Sichuan Juzi Supermicro Technology Co., Ltd., and the equipment model is JZF-200; gas atomization equipment was purchased from Handan Xurui Alloy Materials Co., Ltd., and the equipment model is: XR-PF(Q-2k)5.

如图1和图2所示,本发明提供的雾化喷盘包括环状的喷盘主体1以及插设在喷盘主体1中并封闭喷盘主体1的上、下两端的喷盘上连接体2、喷盘下连接体3,喷盘上连接体2、喷盘下连接体3分别和喷盘主体1可拆卸密封连接,进一步的,喷盘上连接体2、喷盘下连接体3分别和喷盘主体1螺纹连接。喷盘上连接体2包括中心开设有一个中心孔4的进料筒22,使得高温金属熔液通过进料筒22的中心孔4进入雾化喷盘。喷盘主体1、喷盘上连接体2、喷盘下连接体3之间形成气腔5,喷盘主体1的周面沿其径向开设有进气口6。进料筒22和喷盘下连接体3之间形成连通气腔5和中心孔4的环缝7(见图1)或进料筒22的下端面自下而上开设有若干连通气腔5和的通孔8(见图2);喷盘上连接体2和喷盘主体1间以及喷盘下连接体3和喷盘主体1间均设置有密封件。As shown in FIG. 1 and FIG. 2 , the atomizing spray disc provided by the present invention includes an annular spray disc body 1 and a spray disc upper connection inserted in the spray disc body 1 and closing the upper and lower ends of the spray disc body 1 Body 2, lower connecting body 3 of spray disc, upper connecting body 2 of spray disc, lower connecting body 3 of spray disc are respectively detachable and sealing connection with the main body 1 of spray disc, further, connecting body 2 of spraying disc, connecting body 3 lower of spraying disc They are respectively connected with the main body 1 of the spray disc threadedly. The connecting body 2 on the spray disc includes a feeding cylinder 22 with a central hole 4 in the center, so that the high-temperature molten metal enters the atomizing spray disc through the central hole 4 of the feeding cylinder 22 . An air cavity 5 is formed between the spray disc main body 1 , the spray disc upper connecting body 2 and the spray disc lower connecting body 3 , and an air inlet 6 is opened on the peripheral surface of the spray disc body 1 along its radial direction. Between the feeding cylinder 22 and the lower connecting body 3 of the spray disc, a circular seam 7 (see FIG. 1 ) connecting the air cavity 5 and the central hole 4 is formed, or the lower end surface of the feeding cylinder 22 is provided with several communicating air cavities 5 from bottom to top. and through holes 8 (see FIG. 2 ); seals are provided between the upper connecting body 2 of the spray disc and the spray disc main body 1 and between the spray disc lower connecting body 3 and the spray disc body 1 .

具体地,如图1所示,雾化喷盘为环缝雾化喷盘,喷盘主体1为筒体,喷盘上连接体2的纵剖面为类“T”字形,进料筒22为倒置的锥筒状,进料筒22上部边缘沿径向凸设有圆环状的第一上水平连接部21,进料筒22和第一上水平连接部21同轴设置且一体成型。Specifically, as shown in FIG. 1 , the atomizing spray disc is a circular seam atomizing spray disc, the spray disc main body 1 is a cylindrical body, the longitudinal section of the connecting body 2 on the spray disc is a "T"-like shape, and the feeding cylinder 22 is Inverted cone-shaped, the upper edge of the feeding cylinder 22 is radially protruded with an annular first upper horizontal connecting part 21 , the feeding cylinder 22 and the first upper horizontal connecting part 21 are coaxially arranged and integrally formed.

优选地,自筒状的喷盘主体1的上端面靠近其内部的位置开设有一个环形的喷盘上连接体安装避让槽11,喷盘上连接体安装避让槽11自喷盘主体1上表面向下延伸后开设而成并连通喷盘主体1内部。第一上水平连接部21和喷盘主体1螺纹连接,此时第一上水平连接部21的外沿位于喷盘上连接体安装避让槽11内。进一步优选地,在喷盘上连接体安装避让槽11的和喷盘主体1之间安装有密封圈,将喷盘主体1和喷盘上连接体2的连接处密封,并在二者的连接处设置有螺栓,进一步将二者连接(图中未示出密封圈和螺栓)。Preferably, a ring-shaped connecting body mounting avoidance groove 11 on the spray disk is provided from the upper end surface of the cylindrical spray disk main body 1 near the inside thereof. After extending downward, it is opened and communicated with the inside of the spray disc main body 1 . The first upper horizontal connecting portion 21 is screwed to the spray pan body 1 , and at this time, the outer edge of the first upper horizontal connecting portion 21 is located in the mounting and avoiding groove 11 of the connecting body on the spray pan. Further preferably, a sealing ring is installed between the installation avoidance groove 11 of the connecting body on the spray disc and the spray disc main body 1 to seal the connection between the spray disc main body 1 and the connecting body 2 on the spray disc, and at the connection between the two. There are bolts at the place to further connect the two (the sealing ring and the bolts are not shown in the figure).

所述喷盘下连接体3包括倒置的锥筒状的第二筒体31,第二筒体31套设在进料筒22下端外部,从而在进料筒22的外壁和第二筒体31的内壁之间形成上述环缝7。进一步地,环缝7的宽度d1为0.1~1.0mm,环缝7下端的孔心距L1为5~40mm,环缝喷盘的喷射顶角α1为15~60°。The lower connecting body 3 of the spray disc includes an inverted cone-shaped second cylinder 31, and the second cylinder 31 is sleeved outside the lower end of the feeding cylinder 22, so that the outer wall of the feeding cylinder 22 and the second cylinder 31 The above-mentioned annular seam 7 is formed between the inner walls of the Further, the width d1 of the annular seam 7 is 0.1-1.0 mm, the center-to-center distance L1 of the lower end of the annular seam 7 is 5-40 mm, and the spray tip angle α1 of the annular seam spray disc is 15-60°.

和喷盘上连接体安装避让槽11的结构类似的,在喷盘主体1下表面开设有一个环形的喷盘下连接体安装避让槽12,喷盘下连接体安装避让槽12自喷盘主体1的下表面向上延伸后开设而成并连通喷盘主体1内部。喷盘下连接体安装避让槽12的远离喷盘主体1内侧面的一侧开设有内螺纹,喷盘下连接体3的外周面开设有外螺纹,喷盘下连接体3和喷盘主题1螺纹连接,此时喷盘下连接体3的外沿位于喷盘下连接体安装避让槽12内,并通过密封圈和螺栓将喷盘下连接体3和喷盘主体1密封连接(图中未示出密封圈和螺栓)。Similar to the structure of the connecting body installation avoidance groove 11 on the spray disc, there is an annular spray disc lower connection body installation avoidance groove 12 on the lower surface of the spray disc main body 1. The lower surface of 1 extends upward and is opened to communicate with the interior of the spray disc main body 1 . The side of the installation avoidance groove 12 of the lower connecting body of the spray disc is provided with an inner thread, and the outer peripheral surface of the lower connecting body 3 of the spray disc is provided with an external thread. threaded connection, at this time the outer edge of the lower connecting body 3 of the spray disc is located in the installation avoidance groove 12 of the lower connecting body of the spray disc, and the lower connecting body 3 of the spray disc and the main body 1 of the spray disc are sealed and connected by the sealing ring and the bolt (not shown in the figure). seals and bolts shown).

如图2所示,雾化喷盘为环孔雾化喷盘,其喷盘上连接体2的纵剖面为类“工”字形,进料筒22为倒置的锥筒状,进料筒22的上部边缘沿径向凸设有圆环状的第二上水平连接部23,进料筒22的下部边缘沿径向凸设有圆环状的第二下水平连接部25,第二上水平连接部23、进料筒22以及第二下水平连接部25同轴设置且一体成型。第二上水平连接部23的最大轴截面大于第二下水平连接部25的最大轴截面,第二上水平连接部23和喷盘主体1螺纹连接。喷盘下连接体3为圆筒状且可拆卸连接在喷盘主体1和第二下水平连接部25之间。具体地,喷盘下连接体3的内周面和外周面均开设有螺纹,第二下水平连接部25和喷盘下连接体3的连接端的外周面开设有外螺纹,喷盘下连接体3和第二下水平连接部25螺纹连接,喷盘下连接体3和喷盘主体1螺纹连接。As shown in Fig. 2, the atomizing spray disc is an annular atomizing spray disc, the longitudinal section of the connecting body 2 on the spray disc is an "I"-like shape, the feeding cylinder 22 is an inverted cone-shaped cylinder, and the feeding cylinder 22 The upper edge of the feed cylinder 22 is radially protruded with an annular second upper horizontal connecting portion 23, and the lower edge of the feeding cylinder 22 is radially protruded with an annular second lower horizontal connecting portion 25. The connecting portion 23 , the feeding cylinder 22 and the second lower horizontal connecting portion 25 are coaxially disposed and integrally formed. The maximum axial cross-section of the second upper horizontal connecting portion 23 is larger than the maximum axial cross-section of the second lower horizontal connecting portion 25 , and the second upper horizontal connecting portion 23 is screwed with the spray disc main body 1 . The spray pan lower connecting body 3 is cylindrical and is detachably connected between the spray pan main body 1 and the second lower horizontal connecting part 25 . Specifically, the inner peripheral surface and the outer peripheral surface of the lower connecting body 3 of the spray disc are provided with threads, and the outer peripheral surface of the connecting end of the second lower horizontal connecting portion 25 and the lower connecting body 3 of the spray disc is provided with external threads, and the lower connecting body of the spray disc is provided with external threads. 3 and the second lower horizontal connecting part 25 are screwed together, and the lower connecting body 3 of the spray disc is screwed with the main body 1 of the spray disc.

进一步地,喷盘下连接体3上开设有第二下水平连接部安装避让槽251,第二下水平连接部安装避让槽251是自喷盘下连接体3的上表面向下延伸后开设而成并连通喷盘下连接体3的内部。喷盘下连接体3和第二下水平连接部25螺纹连接后,第二下水平连接部25的外沿位于第二下水平连接部安装避让槽251内。进一步优选地,第二下水平连接部25和喷盘下连接体3之间设置有将二者密封的密封圈,且通过螺栓将二者连接。Further, the lower connecting body 3 of the spray disc is provided with a second lower horizontal connecting part installation avoidance groove 251, and the second lower horizontal connecting part installation avoidance groove 251 extends downward from the upper surface of the lower connecting body 3 of the spray disc and opens. form and communicate with the interior of the lower connecting body 3 of the spray disc. After the lower connecting body 3 of the spray pan and the second lower horizontal connecting part 25 are screwed together, the outer edge of the second lower horizontal connecting part 25 is located in the installation and avoiding groove 251 of the second lower horizontal connecting part. Further preferably, a sealing ring is provided between the second lower horizontal connecting part 25 and the lower connecting body 3 of the spray disc for sealing the two, and the two are connected by bolts.

通孔8开设在第二下水平连接部25的靠近进料筒22处,该通孔8沿着进料筒22的周面自下而上均匀开设多个,通孔8和气腔5连通。通孔8的内径d2为0.1~2.0mm,环孔喷盘的喷射顶角α2为15~60°,通孔8下端的孔心距L2为5~40mm,通孔8的数量n为4~40个,且通孔8绕着进料筒22的周面一圈排布。The through holes 8 are opened in the second lower horizontal connecting part 25 near the feeding cylinder 22 . The through holes 8 are evenly opened from bottom to top along the peripheral surface of the feeding cylinder 22 , and the through holes 8 communicate with the air cavity 5 . The inner diameter d 2 of the through hole 8 is 0.1 to 2.0 mm, the spray apex angle α 2 of the annular spray disc is 15 to 60°, the center distance L 2 of the lower end of the through hole 8 is 5 to 40 mm, and the number n of the through holes 8 There are 4 to 40 through holes, and the through holes 8 are arranged in a circle around the peripheral surface of the feeding cylinder 22 .

实施例1Example 1

一种基于降熵调控的增材制造用窄粒径合金粉末制备方法,包括如下步骤:A method for preparing narrow particle size alloy powder for additive manufacturing based on entropy reduction regulation, comprising the following steps:

(1)合金熔炼:将GH4169镍基合金棒料置于熔炼室进行真空电极感应熔炼,熔炼温度为1520℃,通过控制感应线圈的加热,棒料下端逐渐熔化形成连续稳定的金属熔液,合金熔液过热度200℃、合金熔液流量6kg/min。(1) Alloy smelting: The GH4169 nickel-based alloy bar is placed in the smelting chamber for vacuum electrode induction melting, and the melting temperature is 1520 ° C. By controlling the heating of the induction coil, the lower end of the bar gradually melts to form a continuous and stable metal melt. The melt superheat degree is 200℃, and the alloy melt flow rate is 6kg/min.

(2)雾化制粉:根据选区激光熔化技术用中值粒径为30μm、粒度分布范围为15~53μm的合金粉末目标粒度要求,选择环缝雾化喷盘,环缝宽度d1为0.8mm,喷射顶角α1为30°,环缝下端的孔心距L1为14mm;(2) Atomization powder production: According to the target particle size requirements of the alloy powder with a median particle size of 30 μm and a particle size distribution range of 15 to 53 μm for the selective laser melting technology, the annular slot atomization spray disc is selected, and the annular slot width d 1 is 0.8 mm, the spray top angle α 1 is 30°, and the hole center distance L 1 at the lower end of the annular seam is 14 mm;

(3)使高温金属熔液通过中心孔4进入环缝雾化喷盘,同时自进气口6通入惰性气体,使得惰性气体进入气腔5,调节气雾化参数:雾化气体为高纯氩气,其纯度为99.999%;雾化破碎压力为3.0MPa,雾化气体温度为20℃;合金熔液自环缝7喷出,在高纯氩气的破碎及冷却作用下,得到GH4169镍基合金粉末。(3) The high-temperature molten metal enters the annular seam atomizing spray disc through the central hole 4, and at the same time, the inert gas is introduced from the air inlet 6, so that the inert gas enters the air cavity 5, and the gas atomization parameters are adjusted: the atomizing gas is high Pure argon gas, its purity is 99.999%; the atomization crushing pressure is 3.0MPa, and the atomization gas temperature is 20 ℃; the alloy melt is sprayed from the annular gap 7, and under the crushing and cooling action of high-purity argon gas, GH4169 is obtained Nickel-based alloy powder.

实施例2-19Example 2-19

实施例2-19与实施例1的区别在于进行合金粉末制备时所选用的合金原料不同、喷盘不同、喷盘结构参数不同以及雾化工艺参数不同,具体见表1。The difference between Examples 2-19 and Example 1 lies in the different alloy raw materials, different spray discs, different spray disc structural parameters and different atomization process parameters when preparing the alloy powder, as shown in Table 1 for details.

表1实施例1-19的制备合金粉末的设备、工艺条件Table 1 Equipment and process conditions for preparing alloy powder of Examples 1-19

Figure BDA0002474149730000101
Figure BDA0002474149730000101

其中,实施例1-2、实施例4-15所采用的合金为市售;其高温合金熔液的获得是通过将母合金棒熔炼获得。实施例3和实施例17中的NiCrAlY合金的具体成分及比例为:Ni为余量,Cr:23%,Al:8%,Y:0.8%;实施例16的FeNiCr合金是将金属铁、镍、铬、铌等原材料按照合金配比加入熔炼坩埚中进行熔炼,获得FeNiCr不锈钢合金熔液,合金成分比例为:Ni:3%,Cr:16%,Fe为余量;实施例18中的NiCoCrAlY的具体成分为:Co:23%,Cr:18%,Al:12%,Y:0.6%,余量为Ni。Among them, the alloys used in Examples 1-2 and 4-15 are commercially available; the superalloy melt is obtained by smelting the master alloy rod. The specific components and proportions of the NiCrAlY alloy in Example 3 and Example 17 are: Ni is the balance, Cr: 23%, Al: 8%, Y: 0.8%; , chromium, niobium and other raw materials are added into the smelting crucible according to the alloy ratio for smelting to obtain FeNiCr stainless steel alloy melt. The alloy composition ratio is: Ni: 3%, Cr: 16%, and Fe is the balance; NiCoCrAlY in Example 18 The specific components are: Co: 23%, Cr: 18%, Al: 12%, Y: 0.6%, and the balance is Ni.

对比例1-6Comparative Examples 1-6

对比例1-6与实施例1的区别在于进行合金粉末制备时所选用的合金原料不同、喷盘不同、喷盘结构参数不同以及雾化工艺参数不同,具体见表2。The difference between Comparative Examples 1-6 and Example 1 lies in the different alloy raw materials, different spray discs, different spray disc structural parameters and different atomization process parameters when preparing the alloy powder, as shown in Table 2 for details.

表2对比例1-6的制备合金粉末的设备、工艺条件Table 2 Equipment and process conditions for preparing alloy powder of Comparative Examples 1-6

Figure BDA0002474149730000111
Figure BDA0002474149730000111

其中,对比例1、对比例5-6的合金为市售获得,对比例2的FeNiCr合金的具体成分同实施例16,对比例3的NiCrAlY合金的具体成分同实施例17,对比例4的NiCoCrAlY合金的具体成分同实施例18。Wherein, the alloys of Comparative Example 1 and Comparative Examples 5-6 are commercially available, the specific composition of the FeNiCr alloy of Comparative Example 2 is the same as that of Example 16, the specific composition of the NiCrAlY alloy of Comparative Example 3 is the same as that of The specific composition of the NiCoCrAlY alloy is the same as that of Example 18.

(一)合金粉末收得率检测(1) Detection of the yield of alloy powder

对实施例1-1-2、实施例4-15和对比例5-6、对比例1中雾化收集的合金粉末分别采用气流分级的方法进行粒度分级,从而获得选区激光熔化技术用的粒度分布范围为15~53μm的合金粉末,其合金粉末的收得率结果见表3。对实施例16和对比例2中雾化收集的合金粉末采用振动筛分的方法进行粒度分级,从而获得激光熔覆技术用的粒度分布范围为53~150μm的合金粉末,其合金粉末的收得率结果见表3。对实施例3的合金粉末采用振动筛分的方法进行粒度分级,从而获得低压等离子喷涂技术用的粒度分布范围为小于38μm的合金粉末,其合金粉末的收得率结果见表3。对实施例17-18和对比例3-4的收集的合金粉末分别采用振动筛分的方法进行粒度分级,从而获得大气等离子喷涂技术用的对应粒度分布范围的合金粉末,其合金粉末的收得率结果见表3。The particle size classification of the alloy powders collected by atomization in Example 1-1-2, Example 4-15, Comparative Example 5-6, and Comparative Example 1 was carried out by air classification, so as to obtain the particle size for selective laser melting technology. For the alloy powder with a distribution range of 15-53 μm, the yield results of the alloy powder are shown in Table 3. The particle size classification of the alloy powder collected by atomization in Example 16 and Comparative Example 2 was carried out by vibrating sieving method to obtain an alloy powder with a particle size distribution range of 53-150 μm for laser cladding technology. The results are shown in Table 3. The alloy powder of Example 3 was subjected to particle size classification by vibrating sieving, thereby obtaining alloy powder with a particle size distribution range of less than 38 μm for low-pressure plasma spraying technology. The collected alloy powders of Examples 17-18 and Comparative Examples 3-4 were respectively subjected to particle size classification by vibrating sieving, thereby obtaining alloy powders with corresponding particle size distribution ranges for atmospheric plasma spraying technology. The results are shown in Table 3.

表3实施例1-18和对比例1-6制备得到的合金粉末的相应粒度范围内的粉末合金的收得率Table 3 Yields of powder alloys within the corresponding particle size ranges of the alloy powders prepared in Examples 1-18 and Comparative Examples 1-6

Figure BDA0002474149730000121
Figure BDA0002474149730000121

Figure BDA0002474149730000131
Figure BDA0002474149730000131

从表3的结果表明,通过对比实施例4-15和对比例1(或者比较实施例18和对比例4)的数据表明,选择相同的合金制备目标中值粒径的目标粒度范围的合金粉末,当目标中值粒径小于60μm时,应首先选择环缝喷盘,随后筛选得到环缝喷盘的较优参数以及气雾化的较优参数,采用这样的方法使得制备得到的目标中值粒径下的目标粒度范围的合金粉末收得率较高:以316L合金为原料制备中值粒径在30μm左右、粉末粒度为15~53μm的合金粉末,采用环缝喷盘制备得到的该粒度范围内的合金粉末的收得率为31~45%;若是首先选择环孔喷盘,以316L合金为原料制备中值粒径在30μm左右、粉末粒度为15~53μm的合金粉末,其合金粉末的收得率为25%。From the results in Table 3, it is shown by the data of Comparative Examples 4-15 and Comparative Example 1 (or Comparative Example 18 and Comparative Example 4) that the same alloy is selected to prepare alloy powders with a target particle size range of the target median particle size. , when the target median particle size is less than 60 μm, the annular slot spray disc should be selected first, and then the optimal parameters of the annular slot spray disc and the optimal parameters of aerosolization should be obtained by screening. The yield of alloy powder in the target particle size range under the particle size is relatively high: the 316L alloy is used as the raw material to prepare alloy powder with a median particle size of about 30 μm and a powder particle size of 15 to 53 μm. The yield of alloy powder within the range is 31-45%; if the ring-hole spray disc is selected first, the 316L alloy is used as the raw material to prepare alloy powder with a median particle size of about 30 μm and a powder particle size of 15-53 μm. The yield was 25%.

以NiCoCrAlY合金为原料制备中值粒径在56μm左右、粉末粒度为38~75μm的合金粉末,采用环缝喷盘制备得到的该粒度范围内的合金粉末的收得率为43%;若是首先选择环孔喷盘,以NiCoCrAlY合金为原料制备中值粒径在57μm左右、粉末粒度为38~75μm的合金粉末,其合金粉末的收得率为35%。Using NiCoCrAlY alloy as raw material to prepare alloy powder with a median particle size of about 56 μm and a powder particle size of 38 to 75 μm, the yield of alloy powder within this particle size range prepared by using a ring-slit spray disc is 43%; The ring-hole spray disc uses NiCoCrAlY alloy as raw material to prepare alloy powder with a median particle size of about 57 μm and a powder particle size of 38-75 μm, and the yield of the alloy powder is 35%.

通过对比实施例16和对比例2(或者比较实施例17和对比例3)的数据表明,选择相同的合金制备目标中值粒径的目标粒度范围的合金粉末,当目标中值粒径大于60μm时,应首先选择环孔喷盘,随后筛选得到环孔喷盘的较优参数以及气雾化的较优参数,采用这样的方法使得制备得到的目标中值粒径下的目标粒度范围的合金粉末收得率较高:以FeNiCr合金为原料制备中值粒径在95μm左右、粉末粒度为53~150μm的合金粉末,采用环孔喷盘制备得到的该粒度范围内的合金粉末的收得率为66%;若是首先选择环缝喷盘,以FeNiCr合金为原料制备中值粒径在95μm左右、粉末粒度为53~150μm的合金粉末,其合金粉末的收得率为42%。The data of comparative example 16 and comparative example 2 (or comparative example 17 and comparative example 3) show that the same alloy is selected to prepare alloy powder with the target particle size range of the target median particle size, when the target median particle size is greater than 60 μm When , the ring-hole spray disc should be selected first, and then the optimal parameters of the ring-hole spray disc and the optimal parameters of gas atomization should be obtained by screening. Using this method, the alloy with the target particle size range under the target median particle size can be prepared. High powder yield: FeNiCr alloy is used as raw material to prepare alloy powder with a median particle size of about 95 μm and a powder particle size of 53 to 150 μm, and the yield of alloy powder within this particle size range prepared by ring-hole spray disc If the ring-slit spray disc is selected first, and FeNiCr alloy is used as raw material to prepare alloy powder with a median particle size of about 95 μm and a powder particle size of 53-150 μm, the yield of alloy powder is 42%.

以NiCrAlY合金为原料制备中值粒径在67μm左右、粉末粒度为53~150μm的合金粉末,采用环孔喷盘制备得到的该粒度范围内的合金粉末的收得率为49%;若是首先选择环缝喷盘,以NiCrAlY合金为原料制备中值粒径在68μm左右、粉末粒度为53~150μm的合金粉末,其合金粉末的收得率为32%。Using NiCrAlY alloy as raw material to prepare alloy powder with a median particle size of about 67 μm and a powder particle size of 53 to 150 μm, the yield of alloy powder in this particle size range prepared by using a ring-hole spray disc is 49%; The ring-slit spray disc uses NiCrAlY alloy as raw material to prepare alloy powder with a median particle size of about 68 μm and a powder particle size of 53-150 μm, and the yield of the alloy powder is 32%.

因此,在制备合金粉末之前,首先选择要使用的喷盘是非常重要的。Therefore, it is very important to first select the spray disc to be used before preparing the alloy powder.

(二)合金粉末其它性能检测(2) Testing of other properties of alloy powder

对实施例1-2和实施例4、对比例1制备得到的用于选区激光熔化的合金粉末的其它性能进行检测,其中,对于合金粉末的松装密度的检测依据国家标准GB/T 1479.1-2011进行;对于合金粉末流动性的检测依据国家标准GB/T1482-2010进行;对于合金粉末的安息角的检测依据国家标准GB/T16913-2008进行;选区激光熔化制品的拉伸强度、屈服强度和断后延伸率的检测依据国家标准GB/T 228-2002进行,其结果如表4所示。Other properties of the alloy powders for selective laser melting prepared in Examples 1-2, Example 4 and Comparative Example 1 were tested, wherein the detection of the bulk density of the alloy powders was based on the national standard GB/T 1479.1- 2011; the fluidity of alloy powders was tested according to the national standard GB/T1482-2010; the angle of repose of alloy powders was tested according to the national standard GB/T16913-2008; the tensile strength, yield strength and The detection of elongation after fracture is carried out according to the national standard GB/T 228-2002, and the results are shown in Table 4.

表4实施例1-2、实施例4和对比例1制备得到的合金粉末的性能检测Table 4 Performance testing of alloy powders prepared in Examples 1-2, Example 4 and Comparative Example 1

Figure BDA0002474149730000141
Figure BDA0002474149730000141

结合表4的结果可知,将实施例1-2、实施例4的合金粉末用于选区激光熔化技术制备成形的制品组织均匀、结构致密、力学性能优良。Combining the results in Table 4, it can be seen that the alloy powders of Examples 1-2 and 4 are used in the selective laser melting technology to prepare and form products with uniform structure, compact structure and excellent mechanical properties.

对实施例16和对比例2制备得到的用于激光熔覆的合金粉末的其它性能进行检测,其中,对于合金粉末的松装密度的检测依据国家标准GB/T1479.1-2011进行;对于合金粉末流动性的检测依据国家标准GB/T1482-2010进行;激光熔覆涂层的熔覆层硬度的检测依据国家标准YS/T 541-2006进行;激光熔覆涂层的熔覆层厚度的检测依据国家标准GB/T6463-2005进行;激光熔覆涂层的中性盐雾腐蚀检测依据国家标准GB/T 2423.17-2008进行,其结果如表5所示。Other properties of the alloy powders for laser cladding prepared in Example 16 and Comparative Example 2 were tested, wherein the detection of the bulk density of the alloy powders was carried out according to the national standard GB/T1479.1-2011; The testing of powder fluidity is carried out according to the national standard GB/T1482-2010; the testing of the hardness of the cladding layer of the laser cladding coating is carried out according to the national standard YS/T 541-2006; the detection of the thickness of the cladding layer of the laser cladding coating According to the national standard GB/T6463-2005; the neutral salt spray corrosion test of the laser cladding coating is carried out according to the national standard GB/T 2423.17-2008, and the results are shown in Table 5.

表5实施例16和对比例2制备得到的合金粉末的性能检测Table 5 Performance testing of alloy powders prepared in Example 16 and Comparative Example 2

Figure BDA0002474149730000151
Figure BDA0002474149730000151

结合表5的数据可知,本实施例制备得到的FeNiCr不锈钢合金粉末满足激光熔覆技术对于粉末粒度的特殊要求,通过激光熔覆技术制备的成形件制品组织均匀、结构致密、力学性能优良。Combined with the data in Table 5, it can be seen that the FeNiCr stainless steel alloy powder prepared in this example meets the special requirements of laser cladding technology for powder particle size.

对实施例17-18和对比例3-4制备得到的用于大气等离子喷涂的合金粉末的其它性能进行检测,其中,对于合金粉末的松装密度的检测依据国家标准GB/T1479.1-2011进行;对于合金粉末流动性的检测依据国家标准GB/T1482-2010进行,其结果如表6所示。Other properties of the alloy powders for atmospheric plasma spraying prepared in Examples 17-18 and Comparative Examples 3-4 were tested, wherein the detection of the bulk density of the alloy powders was based on the national standard GB/T1479.1-2011 The detection of the fluidity of the alloy powder was carried out according to the national standard GB/T1482-2010, and the results are shown in Table 6.

表6实施例17-18制备得到的合金粉末的性能检测Table 6 Performance testing of alloy powders prepared in Examples 17-18

检测项目Test items 松装密度(g/cm<sup>3</sup>)Bulk density (g/cm<sup>3</sup>) 流动性(s/50g)Mobility (s/50g) 球形度Sphericity 实施例17Example 17 3.843.84 13.7513.75 9595 实施例18Example 18 3.873.87 15.9315.93 9494 对比例3Comparative Example 3 3.923.92 13.9213.92 9797 对比例4Comparative Example 4 3.833.83 15.8715.87 9393

同时,图1提供了实施例1制备得到的细粒径合金粉末的SEM图,图2提供了实施例16制备得到的粗粒径合金粉末的SEM图。图中显示的合金粉末球形度好。Meanwhile, FIG. 1 provides the SEM image of the fine-grained alloy powder prepared in Example 1, and FIG. 2 provides the SEM image of the coarse-grained alloy powder prepared in Example 16. The alloy powder shown in the figure has good sphericity.

本具体实施例仅仅是对本发明的解释,其并不是对本发明的限制,本领域技术人员在阅读完本说明书后可以根据需要对本实施例做出没有创造性贡献的修改,但只要在本发明的权利要求范围内都受到专利法的保护。This specific embodiment is only an explanation of the present invention, and it does not limit the present invention. Those skilled in the art can make modifications without creative contribution to the present embodiment as required after reading this specification, but as long as the rights of the present invention are used All claims are protected by patent law.

Claims (10)

1. An atomizing spray disk comprises an annular spray disk main body (1), and a spray disk upper connecting body (2) and a spray disk lower connecting body (3) which are inserted into the spray disk main body (1) and seal the upper end and the lower end of the spray disk main body (1), wherein the spray disk upper connecting body (2) and the spray disk lower connecting body (3) are detachably and hermetically connected with the spray disk main body (1), the spray disk upper connecting body (2) comprises a feeding cylinder (22) with a central hole (4), the spray disk lower connecting body (3) is sleeved on the outer peripheral surface of the lower part of the feeding cylinder (22) of the spray disk upper connecting body (2), an air cavity (5) is formed among the spray disk main body (1), the spray disk upper connecting body (2) and the spray disk lower connecting body (3), and an air inlet (6) is formed on the peripheral surface of the spray disk main body (1); the device is characterized in that a circular seam (7) communicated with the air cavity (5) is formed between the peripheral surface of the lower part of the feeding cylinder (22) and the lower connecting body (3) of the spray disk, namely the circular seam atomization spray disk; or the lower connecting body (3) of the spray disk and the lower part of the feeding cylinder (22) of the upper connecting body (2) of the spray disk are sleeved in a sealing way, the lower end surface of the feeding cylinder (22) on the upper connecting body (2) of the spray disk is provided with a plurality of through holes (8) communicated with the air cavity (5) from bottom to top, and the through holes (8) are uniformly distributed in an annular shape around the central hole (4), namely the annular atomizing spray disk.
2. The atomizing spray disk of claim 1, characterized in that the longitudinal section of the upper connecting body (2) of the spray disk is similar to a T shape, the feeding cylinder (22) is in an inverted cone shape, and the upper edge of the feeding cylinder (22) is provided with a circular first upper horizontal connecting part (21) in a protruding way along the radial direction; the lower spray disk connecting body (3) comprises an inverted conical second cylinder body (31), the second cylinder body (31) is arranged outside the feeding cylinder (22), and a circular seam (7) is formed between the outer wall of the feeding cylinder (22) and the inner wall of the second cylinder body (31).
3. Atomizing spray disk according to claim 2, characterized in that the width d of the circumferential slot (7)10.1-1.0 mm, and the hole center distance L of the lower end of the circular seam (7)1Is 5-40 mm, and the jet vertex angle α of the circular seam spray disk1Is 15 to 60 degrees.
4. The atomizing spray disk of claim 1, wherein the longitudinal section of the upper connecting body (2) of the spray disk is in an I shape like the Chinese character 'er', the feeding cylinder (22) is in an inverted conical cylinder shape, the edge of the upper part of the feeding cylinder (22) is provided with a circular second upper horizontal connecting part (23) in a protruding mode along the radial direction, and the outer surface of the lower part of the feeding cylinder (22) is sleeved with a circular second lower horizontal connecting part (25); the maximum axial section of the second upper horizontal connecting part (23) is larger than that of the second lower horizontal connecting part (25), and the second upper horizontal connecting part (23) is detachably connected with the spray disc main body (1); the spray plate lower connecting body (3) is cylindrical and is detachably connected between the spray plate main body (1) and the second lower horizontal connecting part (25); the through hole (8) is formed in the second lower horizontal connecting part (25) close to the sleeving joint of the second lower horizontal connecting part and the feeding cylinder (22); and a sealing element is arranged between the spray disk lower connecting body (3) and the second lower horizontal connecting part (25).
5. Atomizing spray disk according to claim 4, characterized in that the inner diameter d of the through-opening (8)2Is 0.1-2.0 mm, and the spray vertex angle α of the annular hole spray disk2Is 15-60 degrees, and the hole center distance L of the lower end of the through hole (8)25-40 mm, and 4-40 through holes (8).
6. A method for preparing alloy powder with narrow particle size for additive manufacturing by gas atomization is characterized by comprising the following steps:
s1, selecting the type of the atomizing spray disk to be used according to the preparation requirements of different target median diameters of the narrow-particle-diameter alloy powder to be prepared, wherein the circular seam atomizing spray disk is adopted for the preparation of the fine-particle-diameter alloy powder with the median diameter of less than 60 mu m; aiming at the preparation of coarse-grain alloy powder with the median grain diameter of more than 60 mu m, an annular hole atomizing spray disk is adopted;
s2, enabling the high-temperature molten metal to enter the atomizing spray disk through the central hole (4), simultaneously introducing inert gas from the gas inlet (6), and after gas atomization parameters are adjusted, enabling the inert gas to pass through the circular seam (7) or the through hole (8) to generate alloy powder;
wherein, the annular seam atomizing spray disk is the annular seam atomizing spray disk of any one of claims 1 to 3, and the annular hole atomizing spray disk is the annular hole atomizing spray disk of any one of claims 1 and 4 to 5; the alloy is selected from one of GH4169, GH3625, NiCrAlY, 316L and FeNiCr type alloy, wherein the specific alloy components of the NiCrAlY type alloy are as follows: 21-26.5% of Cr, 4-11% of Al, 0.3-1.3% of Y and the balance of Ni; the FeNiCr type alloy comprises the following specific alloy components: 0.5-6% of Ni, 14-18% of Cr and the balance of Fe; the NiCoCrAlY alloy comprises the following specific components: 20-24% of Co, 15-20% of Cr, 11-13% of Al, 0.3-0.8% of Y and the balance of Ni.
7. The method for preparing alloy powder with narrow particle size for additive manufacturing according to claim 6, wherein the atomizing gas pressure in step S2 is 0.5-4.0 MPa, the atomizing gas temperature is 10-300 ℃, the superheat degree of the high-temperature molten metal is 50-300 ℃, and the flow rate of the high-temperature molten metal is 0.5-20 kg/min.
8. The method for preparing alloy powder with narrow particle size for additive manufacturing by gas atomization according to claim 6,
when 316L alloy is adopted to prepare fine-grain-size alloy powder with the median grain size of 30 mu m and the target grain size range of 15-53 mu m, a circular seam spray disk is adopted to prepare the alloy powder, and the width d of the circular seam1The selection range of (1) is 0.2-1.0 mm, and the hole center distance L of the lower end of the circular seam1The selection range of (A) is 5-40 mm, and the jet vertex angle is α115-60 degrees, the pressure of atomizing gas is 3.0-4.0 MPa, the temperature of atomizing gas is 20-300 ℃, the superheat degree of high-temperature molten metal is 200-300 ℃, and the flow rate of the high-temperature molten metal is 0.5-20 kg/min;
when GH4169 alloy is adopted to prepare fine-grain-size alloy powder with the median grain size of 30 mu m and the target grain size range of 15-53 mu m, a circular seam spray disk is adopted to prepare the alloy powder, and the width d of the circular seam1Is 0.8mm, and the hole center distance L of the lower end of the circular seam1At 14mm, the spray apex angle α1At 30 degrees, the pressure of atomizing gas is 3.0MPa, and the atomization is carried outThe gas temperature is 20 ℃, the superheat degree of the high-temperature molten metal is 200 ℃, and the flow rate of the high-temperature molten metal is 10 kg/min;
when GH3625 alloy is used for preparing fine-grain-size alloy powder with the median grain size of 30 mu m and the target grain size range of 15-53 mu m, a circular seam spray disk is used for preparing the alloy powder, and the width d of the circular seam1Is 0.8mm, and the hole center distance L of the lower end of the circular seam112mm, the spray apex angle α1At 34 degrees, the pressure of atomizing gas is 3.5MPa, the temperature of atomizing gas is 20 ℃, the superheat degree of high-temperature molten metal is 200 ℃, and the flow rate of the high-temperature molten metal is 10 kg/min;
when NiCrAlY alloy is used for preparing fine-grain alloy powder with the median grain diameter of 20 mu m and the target grain size range of less than 38 mu m, a circular seam spray disk is used for preparing the alloy powder, and the width d of the circular seam1Is 0.6mm, and the hole center distance L of the lower end of the circular seam1At 14mm, the spray apex angle α1At 30 degrees, the pressure of atomizing gas is 3.5MPa, the temperature of atomizing gas is 20 ℃, the superheat degree of high-temperature molten metal is 200 ℃, and the flow rate of the high-temperature molten metal is 10 kg/min;
when NiCoCrAlY alloy is adopted to prepare fine-grain alloy powder with the median grain diameter of 56 mu m and the target grain size range of 38-75 mu m, a circular seam spray disk is adopted to prepare the alloy powder, and the width d of the circular seam1Is 0.6mm, and the hole center distance L of the lower end of the circular seam1At 14mm, the spray apex angle α1At 30 degrees, the pressure of atomizing gas is 3.0MPa, the temperature of atomizing gas is 20 ℃, the superheat degree of high-temperature molten metal is 200 ℃, and the flow rate of the high-temperature molten metal is 10 kg/min;
when NiCrAlY alloy is adopted to prepare coarse-grain-size alloy powder with the median grain size of 67 mu m and the target grain size range of 45-90 mu m, an annular hole spray disk is adopted to prepare the alloy powder, and the width d of the annular hole2Is 0.5mm, and the hole center distance L of the lower end of the annular hole2Is 20mm, and the jet vertex angle is α2At 28 degrees, the number of the annular holes is 30, the pressure of atomizing gas is 3.5MPa, the temperature of the atomizing gas is 20 ℃, the superheat degree of high-temperature molten metal is 200 ℃, and the flow rate of the high-temperature molten metal is 10kg/min;
When FeNiCr alloy is adopted to prepare coarse-grain-size alloy powder with the median grain size of 95 microns and the target grain size range of 53-150 microns, an annular hole spraying disc is adopted to prepare the alloy powder, and the width d of the annular hole2Is 0.5mm, and the hole center distance L of the lower end of the annular hole2Is 20mm, and the jet vertex angle is α2The temperature is 28 degrees, the number of the annular holes is 30, the pressure of atomizing gas is 2.5MPa, the temperature of the atomizing gas is 20 ℃, the superheat degree of high-temperature molten metal is 200 ℃, and the flow rate of the high-temperature molten metal is 15 kg/min.
9. The method for preparing alloy powder with narrow particle size for additive manufacturing through gas atomization according to claim 8, wherein when 316L alloy is used for preparing alloy powder with fine particle size, the median particle size of which is 30 μm and the target particle size range of which is 15-53 μm, the preparation of the alloy powder is carried out through a circular seam spray disk, and the width d of the circular seam is1Is 0.2mm, and the hole center distance L of the lower end of the circular seam116mm, the spray apex angle α1The temperature is 30 degrees, the pressure of atomizing gas is 3.0MPa, the temperature of atomizing gas is 20 ℃, the superheat degree of high-temperature molten metal is 200 ℃, and the flow rate of the high-temperature molten metal is 10 kg/min.
10. The method for preparing alloy powder with narrow particle size for additive manufacturing through gas atomization according to claim 1, wherein the high-temperature molten metal is obtained after smelting a metal raw material and/or a return material, or is obtained by smelting a master alloy rod.
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