CN110834090A - Metal powder shaping, refining and purifying device and method - Google Patents
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- 239000000843 powder Substances 0.000 title claims abstract description 231
- 229910052751 metal Inorganic materials 0.000 title claims abstract description 133
- 239000002184 metal Substances 0.000 title claims abstract description 133
- 238000000034 method Methods 0.000 title claims abstract description 25
- 238000007493 shaping process Methods 0.000 title claims abstract description 20
- 238000007670 refining Methods 0.000 title claims abstract description 17
- 239000007789 gas Substances 0.000 claims abstract description 153
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims abstract description 62
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 62
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 41
- 239000001301 oxygen Substances 0.000 claims abstract description 41
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 41
- 229910052786 argon Inorganic materials 0.000 claims abstract description 31
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 31
- 238000003860 storage Methods 0.000 claims abstract description 30
- 238000004140 cleaning Methods 0.000 claims abstract description 20
- 239000012535 impurity Substances 0.000 claims abstract description 9
- 238000005086 pumping Methods 0.000 claims abstract description 7
- 238000000746 purification Methods 0.000 claims description 37
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 17
- 238000005273 aeration Methods 0.000 claims description 11
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- 239000003513 alkali Substances 0.000 claims description 6
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- 238000010521 absorption reaction Methods 0.000 claims description 5
- 238000001514 detection method Methods 0.000 claims description 5
- 239000002994 raw material Substances 0.000 claims description 5
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 4
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 claims description 3
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 claims description 3
- MPCRDALPQLDDFX-UHFFFAOYSA-L Magnesium perchlorate Chemical compound [Mg+2].[O-]Cl(=O)(=O)=O.[O-]Cl(=O)(=O)=O MPCRDALPQLDDFX-UHFFFAOYSA-L 0.000 claims description 3
- 239000003063 flame retardant Substances 0.000 claims description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 2
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- 229910001220 stainless steel Inorganic materials 0.000 claims description 2
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- 238000004663 powder metallurgy Methods 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract 1
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- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
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- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
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- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 description 1
- 238000009688 liquid atomisation Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000002923 metal particle Substances 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 229910000601 superalloy Inorganic materials 0.000 description 1
- 210000003437 trachea Anatomy 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 238000009692 water atomization Methods 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F1/00—Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
- B22F1/14—Treatment of metallic powder
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F1/00—Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
- B22F1/06—Metallic powder characterised by the shape of the particles
- B22F1/065—Spherical particles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F2202/00—Treatment under specific physical conditions
- B22F2202/13—Use of plasma
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Nanotechnology (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
Abstract
一种金属粉末整形细化及净化装置及方法,它涉及粉末整形细化及净化设备和方法。它是要解决现有的金属粉末制法球形度低、纯度差的技术问题。本装置包括等离子体发生器、送粉机、金属粉末净化室器、收集器、换热器、尾气循环过滤器、气体氧氮净化器、r气体压缩机、气体存储装置、抽真空装置和粉末自动刮除器;等离子体发生器和送粉器安装在净化室器顶端;净化室器下部出气管依次经过换热器、循环过滤器、氧氮净化器和压缩机与气体存储装置连接。方法:整个系统抽真空后充入氩气,再开启等离子体发生器产生等离子体炬,送入金属粉末处理,氩气净化后循环。处理后粉末球形度≥90%,含氧量≤980ppm,杂质去除率≥90%,用于粉末冶金领域。
A metal powder shaping, refining and purifying device and method relate to a powder shaping, refining and purifying device and method. It is to solve the technical problems of low sphericity and poor purity in the existing metal powder manufacturing method. The device includes plasma generator, powder feeder, metal powder cleaning chamber, collector, heat exchanger, exhaust gas circulation filter, gas oxygen and nitrogen purifier, r gas compressor, gas storage device, vacuum pumping device and powder The automatic scraper; the plasma generator and the powder feeder are installed on the top of the clean room device; the lower air outlet pipe of the clean room device is connected to the gas storage device through the heat exchanger, the circulating filter, the oxygen and nitrogen purifier and the compressor in sequence. Method: The whole system is evacuated and filled with argon gas, and then the plasma generator is turned on to generate a plasma torch, which is sent to the metal powder for treatment, and the argon gas is purified and circulated. After treatment, the powder sphericity is ≥90%, the oxygen content is ≤980ppm, and the impurity removal rate is ≥90%. It is used in the field of powder metallurgy.
Description
技术领域technical field
本发明涉及粉末整形细化及净化设备和方法,属于粉末冶金工业技术领域。The invention relates to powder shaping, refining and purification equipment and method, belonging to the technical field of powder metallurgy industry.
背景技术Background technique
金属粉末是指尺寸小于1mm的金属颗粒群,包括单一金属粉末、合金粉末以及具有金属性质的某些难熔化合物粉末,是粉末冶金的主要原材料。金属粉末的制备方法主要有机械研磨破碎法、雾化法等。Metal powder refers to a group of metal particles with a size of less than 1 mm, including single metal powder, alloy powder and some refractory compound powder with metallic properties, and is the main raw material for powder metallurgy. The preparation methods of metal powder mainly include mechanical grinding and crushing method, atomization method, etc.
机械粉碎法主要是通过压碎、击碎和磨削等作用将固态金属碎化成粉末。该方法效率低,能耗大,粉末颗粒出现不规则尖角,降低了粉末流动性、松装密度和振实密度等;同时由于与不同材质的研磨介质接触,会引入杂质元素,影响粉末的纯度及后续所制备金属构件的综合性能。The mechanical crushing method mainly crushes solid metal into powder by crushing, crushing and grinding. This method has low efficiency, high energy consumption, irregular sharp corners of powder particles, which reduces powder fluidity, bulk density and tap density. Purity and comprehensive properties of the subsequently prepared metal components.
雾化法是指将大块固体金属通过高温加热变成,熔融金属并通过冷却介质液态金属雾化成细小液滴,在冷却介质中凝固成粉末。主要有气体雾化法和液体雾化法两种。也有利用旋转盘粉碎和熔体自身(自耗电极和坩埚)旋转的离心雾化法,以及其他雾化方法如溶氢真空雾化、超声波雾化等。气雾化粉末一般近球形,水雾化可制得不规则形状。但此方法所用的设备昂贵,能耗高,同时产品中易产生或混入杂质,影响粉末的纯度及后续所制备金属构件的综合性能。The atomization method refers to the process of heating a large solid metal into a molten metal and atomizing it into fine droplets through the cooling medium liquid metal, and solidifying it into powder in the cooling medium. There are mainly two kinds of gas atomization method and liquid atomization method. There are also centrifugal atomization methods that utilize rotating disk pulverization and the rotation of the melt itself (consumable electrodes and crucibles), as well as other atomization methods such as dissolved hydrogen vacuum atomization, ultrasonic atomization, and the like. Gas atomized powder is generally nearly spherical, and water atomization can produce irregular shapes. However, the equipment used in this method is expensive, and the energy consumption is high. At the same time, impurities are easily generated or mixed in the product, which affects the purity of the powder and the comprehensive performance of the subsequently prepared metal components.
发明内容SUMMARY OF THE INVENTION
本发明是要解决现有的金属粉末的制备方法球形度低、纯度差的技术问题,而提供一种金属粉末整形细化及净化装置和方法。The invention aims to solve the technical problems of low sphericity and poor purity of the existing metal powder preparation method, and provides a metal powder shaping, refining and purifying device and method.
本发明的金属粉末整形细化及净化装置包括等离子体发生器1、送粉机2、金属粉末净化室器3、第一金属粉末收集器4、第一换热器5、尾气循环过滤器6、第二金属粉末收集器7、气体氧氮净化器8、第二换热器9、气体压缩机10、气体存储装置11、抽真空装置12和粉末自动刮除器13;The metal powder shaping, refining and purification device of the present invention includes a plasma generator 1, a
其中金属粉末净化室器3顶端安装有等离子体发生器1和送粉机2,底部安装有第一金属粉末收集器4;金属粉末净化室器3内部安装粉末自动刮除器13;The top of the metal powder
尾气循环过滤器6的底部安装有第二金属粉末收集器7;尾气循环过滤器6内设置阻燃过滤袋,用于过滤粉尘;A second
气体氧氮净化器8的内部设置吸收层,吸收层由下至上由铜粉层、碱石棉层、高氯酸镁层和碱石棉层组成,用于去除水蒸气和氧气;An absorption layer is arranged inside the gas oxygen and
气体存储装置11的出气口分别与等离子体发生器1、送粉机2连接;金属粉末净化室器3的下部的出气管依次经过第一换热器5、尾气循环过滤器6、气体氧氮净化器8、第二换热器9、气体压缩机10,与气体存储装置11进气口连接;The gas outlet of the
抽真空装置12分别与金属粉末净化室器3、尾气循环过滤器6和气体氧氮净化器8联通。The
更进一步地,所述送粉机2为双通道活塞式给料器或者盘式给料器;需要整形细化及净化处理的金属粉末能够实现连续不间断通过给料器进入金属粉末净化室器3;Further, the
更进一步地,金属粉末净化室器3的壳体外壁设有夹套,夹套底部设置进水口3-1;上部设置出水口3-2;夹套为冷却循环水路,冷却水由底部进水口3-1流入,由顶部出水口3-2流出。Further, the outer wall of the metal powder purifying
更进一步地,尾气循环过滤器6的壳体外壁设有夹套,夹套底部设置进水口,上部设置出水口;夹套为冷却循环水路,冷却水由底部流入,由顶部流出。Further, the outer wall of the shell of the exhaust
更进一步地,气体氧氮净化器8的壳体外壁设有夹套,夹套底部设置进水口;上部设置出水口;夹套为冷却循环水路,冷却水由底部流入,由顶部流出。Further, the outer wall of the gas oxygen and
更进一步地,气体存储装置11内的气体为高纯氩气。Furthermore, the gas in the
更进一步地,粉末自动刮除器13由环形刮刀13-1、驱动装置13-2和垂直杆13-3,环形刮刀13-1固定在垂直杆13-3底部,垂直杆13-3的上部与驱动装置13-2连接;驱动装置13-2带动垂直杆13-3上、下移动,从而使环形刮刀13-1刮去沉积在净化室内壁上的粉末。Further, the powder
更进一步地,本发明的金属粉末整形细化及净化装置还包括检测及自动控制仪14,它显示设备工作状态下的功率、电流、电压、真空度、气体流量、气体压力、气体氧含量及露点、冷却循环水温度和/或流量;具有实时在线监测及调整设备工作参数的功能。Further, the metal powder shaping, refining and purifying device of the present invention also includes a detection and
更进一步地,金属粉末净化室器3上还设置观察窗15;观察窗15处设置气管并与气体存储装置11连接,气管通气体是为了吹掉沉积在观察窗15上的粉末,利于观察。Further, an
更进一步地,金属粉末净化室器3的下部还设有进气管与气体存储装置11连接;用于直接将气体存储装置11内的气体直接输入到金属粉末净化室器3、尾气循环过滤器6 和气体氧氮净化器8中使整个系统充满气体,也可以进行气体循环,通过气体氧氮净化器 8净化进行,提高气体存储装置11内气体的纯度。Further, the lower part of the metal powder
更进一步地,等离子体发生器1为直流电弧等离子体发生器。Further, the plasma generator 1 is a DC arc plasma generator.
更进一步地,第一金属粉末收集器4和第二金属粉末收集器7均带有密封阀,能够确保它们与设备分离时仍保持密封。Furthermore, both the first metal powder collector 4 and the second
更进一步地,金属粉末净化室器3内还设置有曝气头,曝气头与气体存储装置11连接;曝气头的上表面为弧形,上表面设置出气孔,通过出气孔向金属粉末净化室器3内吹气体,可以降低金属粉末的下降的速度并提高液态金属的冷却速度,从而提高球形度;上表面为弧形也防止积粉。Furthermore, the metal powder
利用上述的装置进行金属粉末整形细化及净化的方法,按以下步骤进行:Utilize the above-mentioned device to carry out the method of metal powder shaping refinement and purification, carry out according to the following steps:
一、向送粉机2中装入待处理的金属粉末;1. Load the metal powder to be processed into the
二、启动抽真空装置12,将金属粉末净化室器3、尾气循环过滤器6和气体氧氮净化器8的真空度抽到1×10-3Pa以上,关闭抽真空装置12;2. Start the
三、通过气体存储装置11向金属粉末净化室器3、尾气循环过滤器6和气体氧氮净化器8的内部充入高纯氩气使压力达到0.2Pa~0.5Pa;开启等离子体发生器1,调整等离子体发生器1的电压为90~120V、电流为150~300A;调整通入等离子体发生器1内部的氩气流速为1.5~2.0L/h,产生等离子体炬;3. Fill the metal
四、开启送粉机2,调整通入送粉器3的氩气流量使得送粉器3的送粉速度达到 0.5~1kg/h,将金属粉末送入金属粉末净化室器3中;金属粉末经等离子体发生器1产生的高温等离子体炬处理后,落入第一金属粉末收集器4中;同时用于产生等离子体炬的氩气以及用于输送原料粉末的氩气经金属粉末净化室器3底部的出气口经第一换热器5进入尾气循环过滤器6中,经过滤下来的金属粉末落入第二金属粉末收集器7中收集,氩气再进入气体氧氮净化器8去除杂质,再经第二换热器9冷却、经气体压缩机10压缩后,返回至气体存储装置11中;第一金属粉末收集器4中的球形粉末为产品。4. Turn on the
更进一步地,步骤一中的金属粉末的粒径为75~100μm。Further, the particle size of the metal powder in step 1 is 75-100 μm.
更进一步地,步骤一中的金属粉末为铁粉、不锈钢粉、有色金属粉末或特种金属粉末;Further, the metal powder in step 1 is iron powder, stainless steel powder, non-ferrous metal powder or special metal powder;
更进一步地,有色金属粉末为铜粉、铅粉、锌粉、锰粉、铬粉、钛粉、铝粉、镁粉、钨粉或钼粉;Further, the non-ferrous metal powder is copper powder, lead powder, zinc powder, manganese powder, chromium powder, titanium powder, aluminum powder, magnesium powder, tungsten powder or molybdenum powder;
更进一步地,特种金属粉末为高温合金粉或硬质合金粉。Further, the special metal powder is superalloy powder or cemented carbide powder.
本发明的装置利用等离子体炬对金属粉末进行整形细化,消除表面不规则尖角,使粒径分布更加均匀,进而提高粉末的流动性,同时在对粉末进行整形细化的同时,该设备还能降低金属粉末含氧量及其他非金属夹杂,提高纯度。经发明的装置处理的金属粉末与原始粉末相比,粉末表面不规则尖角消失,球形度可达到90%以上;同时粉末含氧量可降低到980ppm以下,杂质去除率到达90%以上。The device of the invention uses a plasma torch to shape and refine the metal powder, eliminates irregular sharp corners on the surface, makes the particle size distribution more uniform, and further improves the fluidity of the powder. It can also reduce the oxygen content of metal powder and other non-metallic inclusions, and improve the purity. Compared with the original powder, the metal powder treated by the invented device has the irregular sharp corners on the powder surface disappear, and the sphericity can reach more than 90%; meanwhile, the oxygen content of the powder can be reduced to less than 980ppm, and the impurity removal rate can reach more than 90%.
本发明的装置和方法可用于处理金属粉末,工序简单、效率高。The device and method of the present invention can be used for processing metal powder, and the process is simple and the efficiency is high.
附图说明Description of drawings
图1是本发明的装置的结构示意图;Fig. 1 is the structural representation of the device of the present invention;
图2是金属粉末净化室器3及其中的粉末自动刮除器13的结构示意图;FIG. 2 is a schematic structural diagram of the metal powder
图中,1为等离子体发生器,2为送粉机,3为金属粉末净化室器,4为第一金属粉末收集器4,5为第一换热器,6为尾气循环过滤器,7为第二金属粉末收集器,8为气体氧氮净化器,9为第二换热器,10为气体压缩机,11为气体存储装置,12为抽真空装置, 13为粉末自动刮除器,14为检测及自动控制仪,15为观察窗;In the figure, 1 is the plasma generator, 2 is the powder feeder, 3 is the metal powder cleaning chamber, 4 is the first metal powder collector 4, 5 is the first heat exchanger, 6 is the exhaust gas circulation filter, 7 is the second metal powder collector, 8 is the gas oxygen and nitrogen purifier, 9 is the second heat exchanger, 10 is the gas compressor, 11 is the gas storage device, 12 is the vacuuming device, 13 is the powder automatic scraper, 14 is the detection and automatic controller, and 15 is the observation window;
粉末自动刮除器13中13-1为环形刮刀,13-2为驱动装置,13-3为垂直杆13-3。In the powder
具体实施方式Detailed ways
用下面的实施例验证本发明的有益效果:Verify the beneficial effects of the present invention with the following examples:
实施例1:本实施例的金属粉末整形细化及净化装置由直流电弧等离子体发生器1、送粉机2、金属粉末净化室器3、第一金属粉末收集器4、第一换热器5、尾气循环过滤器 6、第二金属粉末收集器7、气体氧氮净化器8、第二换热器9、气体压缩机10、气体存储装置11、抽真空装置12、粉末自动刮除器13和检测及自动控制仪14组成;其中金属粉末净化室器3顶端安装有直流电弧等离子体发生器1和送粉机2,底部安装有第一金属粉末收集器4;金属粉末净化室器3内部安装气体曝气头13和粉末自动刮除器13;尾气循环过滤器6的底部安装有第二金属粉末收集器7;尾气循环过滤器6内设置阻燃过滤袋,用于过滤粉尘;气体氧氮净化器8的内部设置有吸收层,吸收层由下至上由铜粉层、碱石棉层、高氯酸镁层和碱石棉层组成,用于去除水蒸气和氧气;气体存储装置11的出气口分别与等离子体发生器1、送粉机2连接;金属粉末净化室器3的下部的出气管依次经过第一换热器5、尾气循环过滤器6、气体氧氮净化器8、第二换热器9和气体压缩机10与气体存储装置11进气口连接;抽真空装置12分别与金属粉末净化室器3、尾气循环过滤器6和气体氧氮净化器8联通;所述送粉机2为双通道活塞式给料器;金属粉末净化室器 3的壳体外壁设有夹套;夹套为冷却循环水路,冷却水由底部进水口3-1流入,由顶部出水口3-2流出;尾气循环过滤器6的壳体外壁设有夹套;夹套为冷却循环水路,冷却水由底部流入,由顶部流出;气体氧氮净化器8的壳体外壁设有夹套;夹套为冷却循环水路,冷却水由底部流入,由顶部流出;气体存储装置11内的气体为质量百分纯度为99.999%的高纯氩气;粉末自动刮除器13由环形刮刀13-1、驱动装置13-2和垂直杆13-3,环形刮刀13-1固定在垂直杆13-3底部,垂直杆13-3的上部与驱动装置13-2连接;驱动装置13-2 带动垂直杆13-3上、下移动,从而使环形刮刀13-1刮去沉积在净化室内壁上的粉末;金属粉末净化室器3的壁上还设置了观察窗15;观察窗15处设置气管并与气体存储装置11 连接,气管通气体是为了吹掉沉积在观察窗15上的粉末,利于观察;检测及自动控制仪 14显示设备工作状态下的功率、电流、电压、真空度、气体流量、气体压力、气体氧含量及露点、冷却循环水温度和流量;具有实时在线监测及调整设备工作参数的功能;第一金属粉末收集器4和第二金属粉末收集器7均带有密封阀,能够确保它们与设备分离时仍保持密封。Embodiment 1: The metal powder shaping, refining and purification device of this embodiment consists of a DC arc plasma generator 1, a
利用本实施例1的装置处理钛合金粉末的方法,按以下步骤进行:The method for processing titanium alloy powder using the device of this embodiment 1 is carried out according to the following steps:
一、向送粉机2中装入1kg平均粒径为75μm且形状不规则的钛合金TA1粉末;1. Load 1kg of titanium alloy TA1 powder with an average particle size of 75 μm and an irregular shape into the
二、启动抽真空装置12,将金属粉末净化室器3、尾气循环过滤器6和气体氧氮净化器8的真空度抽到1×10-3Pa,关闭抽真空装置12;2. Start the
三、通过气体存储装置11向金属粉末净化室器3、尾气循环过滤器6和气体氧氮净化器8的内部充入高纯氩气使压力达到0.2Pa;开启等离子体发生器1,调整等离子体发生器1的电压为90V、电流为150A;调整通入等离子体发生器1内部的氩气流速为1.5L/h,产生等离子体炬;3. Fill the metal
四、开启送粉机2,调整通入送粉机2的氩气流量为0.6L/h使得送粉机2的送粉速度达到0.5kg/h,将TA1粉末送入金属粉末净化室器3中;TA1粉末在等离子体发生器1 产生的高温等离子体炬中加热熔化,表面不规则尖角消失,由于表面张力而形成球状熔融液滴,并在重力作用下不断下降冷却,到达金属粉末净化室器3底部,形成球形粉末落入第一金属粉末收集器4中;同时用于产生等离子体炬的氩气以及用于输送原料粉末的氩气经金属粉末净化室器3底部的出气口经第一换热器5进入尾气循环过滤器6中,经过滤下来的细小的金属粉末落入第二金属粉末收集器7中收集,氩气再进入气体氧氮净化器8 去除杂质气体,再经第二换热器9冷却,经气体压缩机10压缩,返回至气体存储装置11 中;第一金属粉末收集器4中的球形TA1粉末为产品。4. Turn on the
本实施例的TA1粉末产品与原始粉末相比,粉末表面不规则尖角消失,球形度达到90%;平均粒径为30μm,细化率达到50%;同时TA1粉末含氧量由原始粉末的10000ppm 降低到980ppm,杂质去除率达到90%。Compared with the original powder, the TA1 powder product of this embodiment has the disappearance of irregular sharp corners on the powder surface, and the sphericity reaches 90%; the average particle size is 30 μm, and the refinement rate reaches 50%; at the same time, the oxygen content of the TA1 powder is determined by the original powder. 10000ppm is reduced to 980ppm, and the impurity removal rate reaches 90%.
实施例2:本实施例的金属粉末整形细化及净化装置与实施例1不同的是金属粉末净化室器3内还设置有曝气头,曝气头与气体存储装置11连接;曝气头为的上表面为弧形,上表面设置出气孔,通过出气孔向金属粉末净化室器3内吹氩气。其它与实施例1相同。Embodiment 2: The difference between the metal powder shaping, refining and purification device of this embodiment is that the metal powder
利用本实施例2的装置处理钛合金粉末的方法,按以下步骤进行:Utilize the method of the device of this
一、向送粉机2中装入1kg平均粒径为75μm且形状不规则的钛合金TA1粉末;1. Load 1kg of titanium alloy TA1 powder with an average particle size of 75 μm and an irregular shape into the
二、启动抽真空装置12,将金属粉末净化室器3、尾气循环过滤器6和气体氧氮净化器8的真空度抽到9×10-4Pa,关闭抽真空装置12;2. Start the
三、通过气体存储装置11向金属粉末净化室器3、尾气循环过滤器6和气体氧氮净化器8的内部充入高纯氩气使压力达到0.3Pa;开启等离子体发生器1,调整等离子体发生器1的电压为110V、电流为200A;调整通入等离子体发生器1内部的氩气流速为1.5L/h,产生等离子体炬;3. Fill the metal
四、开启送粉机2,调整通入送粉机2的氩气流量为0.6L/h使得送粉机2的送粉速度达到0.5kg/h,将TA1粉末送入金属粉末净化室器3中,同时通过曝气头向金属粉末净化室器3内通入氩气;TA1粉末在等离子体发生器1产生的高温等离子体炬中加热熔化,表面不规则尖角消失,由于表面张力而形成球状熔融液滴,并在重力作用下不断下降冷却,到达金属粉末净化室器3底部,形成球形粉末落入第一金属粉末收集器4中;用于产生等离子体炬的氩气以及用于输送原料粉末的氩气经金属粉末净化室器3底部的出气口经第一换热器5进入尾气循环过滤器6中,经过滤下来的细小的金属粉末落入第二金属粉末收集器7中收集,氩气再进入气体氧氮净化器8去除杂质气体,再经第二换热器9冷却,经气体压缩机10压缩,返回至气体存储装置11中;第一金属粉末收集器4中的球形TA1 粉末为产品。4. Turn on the
本实施例的曝气头,从曝气头的出气孔向金属粉末净化室器3内吹入的氩气,可以提高液态金属的冷却速度,减小熔融液滴下降过程中的变形,从而提高球形度;上表面为弧形也防止积粉。本实施例的TA1粉末产品与原始粉末相比,粉末表面不规则尖角消失,球形度达到95%;平均粒径为30μm,细化率达到52%;同时TA1粉末含氧量由原始粉末的10000ppm降低到965ppm,杂质去除率达到93%。In the aeration head of this embodiment, the argon gas blown into the metal powder
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