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CN116477568A - A kind of hydrogenation metal powder dehydrogenation method - Google Patents

A kind of hydrogenation metal powder dehydrogenation method Download PDF

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Publication number
CN116477568A
CN116477568A CN202310487241.2A CN202310487241A CN116477568A CN 116477568 A CN116477568 A CN 116477568A CN 202310487241 A CN202310487241 A CN 202310487241A CN 116477568 A CN116477568 A CN 116477568A
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dehydrogenation
temperature
furnace
metal powder
stirring
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郭瑞
桂群峰
郑磊
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Zhejiang Taineng New Materials Co ltd
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/0005Reversible uptake of hydrogen by an appropriate medium, i.e. based on physical or chemical sorption phenomena or on reversible chemical reactions, e.g. for hydrogen storage purposes ; Reversible gettering of hydrogen; Reversible uptake of hydrogen by electrodes
    • C01B3/001Reversible uptake of hydrogen by an appropriate medium, i.e. based on physical or chemical sorption phenomena or on reversible chemical reactions, e.g. for hydrogen storage purposes ; Reversible gettering of hydrogen; Reversible uptake of hydrogen by electrodes characterised by the uptaking medium; Treatment thereof
    • C01B3/0026Reversible uptake of hydrogen by an appropriate medium, i.e. based on physical or chemical sorption phenomena or on reversible chemical reactions, e.g. for hydrogen storage purposes ; Reversible gettering of hydrogen; Reversible uptake of hydrogen by electrodes characterised by the uptaking medium; Treatment thereof of one single metal or a rare earth metal; Treatment thereof

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  • Manufacture Of Metal Powder And Suspensions Thereof (AREA)

Abstract

本发明公开了一种氢化金属粉脱氢方法,涉及金属粉制备领域,工艺步骤如下:A 将粒氢化金属粉装入特制的脱氢装置中,并设计有搅拌粉体装置;B 将炉内真空,并开始缓慢升温至100℃,同时开启搅拌,烘干粉体物料;C 待物料烘干后,继续将炉温升至300℃,此时开始缓慢发生脱氢反应;D继续将炉温升至600℃保温4h,此时开始大量释放氢气;E 最后,将炉温升至850℃,保温2h后开始降温,直至降至常温完成脱氢过程。与现有技术相比,本申请方法改变了现有脱氢处理时金属粉物平铺固定进行脱氢的工艺,改为搅拌运动式脱氢,不仅炉体容积利用率高,产能增强,脱氢处理速度以及脱氢效果也极为优越,所得金属粉氢含量降低至<0.003%,脱氢效率提升30%,有效的解决了现有技术中脱氢效率低、脱氢不完全的问题。

The invention discloses a hydrogenated metal powder dehydrogenation method, which relates to the field of metal powder preparation. The process steps are as follows: A. Put hydrogenated metal powder into a special dehydrogenation device, and design a stirring powder device; B. Vacuum the furnace, and start to slowly heat up to 100°C, and start stirring at the same time, and dry the powder material; C. After the materials are dried, continue to raise the furnace temperature to 300°C, and then the dehydrogenation reaction begins to slowly occur; D. Continue to raise the furnace temperature to 600°C for 4 hours, and then start to release a large amount of hydrogen ; E Finally, raise the temperature of the furnace to 850°C, keep it warm for 2 hours, and then start to cool down until it drops to room temperature to complete the dehydrogenation process. Compared with the prior art, the method of the present application changes the existing dehydrogenation process of metal powder flat and fixed during the dehydrogenation treatment, and changes it to a stirring motion type dehydrogenation, which not only has high furnace volume utilization rate, enhanced production capacity, dehydrogenation treatment speed and dehydrogenation effect are also extremely superior, the hydrogen content of the obtained metal powder is reduced to <0.003%, and the dehydrogenation efficiency is increased by 30%.

Description

一种氢化金属粉脱氢方法A kind of hydrogenation metal powder dehydrogenation method

技术领域technical field

本发明涉及金属粉制备领域,特别涉及氢化金属粉脱氢制备金属粉的方法。The invention relates to the field of metal powder preparation, in particular to a method for preparing metal powder by dehydrogenating metal powder.

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溶化合物粉末,是粉末冶金的主要原材料。金属粉末的制备方法有还原法、雾化法、电解法、机械粉碎法、羟基法等,机械粉碎法最为简单,但是大部分金属具有延展性和硬度,给机械粉碎带来困难,因此,工艺上采用改变金属性质,使其变脆然后再进行机械粉碎,最常见的方法是氢化法,该方法利用某些金属如钛、钽、铌、锆等金属具有吸氢后变脆特性,变为氢化金属后再进行机械粉碎,与此同时,粉碎后氢化金属颗粒需进行脱氢处理,得到所需金属粉。Metal powder refers to a group of metal particles whose size is less than 1 mm. Including single metal powder, alloy powder and some insoluble compound powder with metal properties, it is the main raw material of powder metallurgy. Metal powder preparation methods include reduction method, atomization method, electrolysis method, mechanical pulverization method, hydroxyl method, etc. Mechanical pulverization method is the simplest, but most metals have ductility and hardness, which brings difficulties to mechanical pulverization. Therefore, in the process, the properties of metals are changed to make them brittle and then mechanical pulverization. The most common method is hydrogenation method. Get the required metal powder.

传统氢化脱氢工艺一般是将氢化金属粉装入料盘中,铺料厚度不超过10cm,然后在真空脱氢炉内进行真空高温脱氢,该工艺由于物料固定铺设一定厚度,脱出氢气不易快速扩散,导致脱氢效果和效率降低,并且由于铺设金属粉物料厚度有限,所以炉体的有效利用体积减少,产能减少。The traditional hydrodehydrogenation process generally puts hydrogenated metal powder into the material tray, the thickness of the material is not more than 10cm, and then carries out vacuum high-temperature dehydrogenation in the vacuum dehydrogenation furnace. In this process, because the material is fixed to a certain thickness, the dehydrogenated hydrogen is not easy to diffuse quickly, resulting in a reduction in the dehydrogenation effect and efficiency. In addition, due to the limited thickness of the metal powder material, the effective use volume of the furnace body is reduced and the production capacity is reduced.

发明内容Contents of the invention

本发明针对现有技术中的不足,提供了一种氢化金属粉脱氢方法,本方法改变了现有脱氢处理时金属粉物平铺固定进行脱氢的工艺,改为搅拌运动式脱氢,不仅炉体容积利用率高,产能增强,脱氢处理速度以及脱氢效果也极为优越,氢含量<0.003%,脱氢效率提升30%,解决了现有技术中脱氢效率低的问题。Aiming at the deficiencies in the prior art, the present invention provides a hydrogenation metal powder dehydrogenation method. This method changes the existing dehydrogenation process of the metal powder in flat and fixed dehydrogenation during the dehydrogenation treatment, and changes it to a stirring motion type dehydrogenation. Not only the furnace volume utilization rate is high, the production capacity is enhanced, the dehydrogenation treatment speed and dehydrogenation effect are also extremely superior, the hydrogen content is <0.003%, and the dehydrogenation efficiency is increased by 30%, which solves the problem of low dehydrogenation efficiency in the prior art.

为了解决上述技术问题,本发明通过下述技术方案得以解决:一种氢化金属粉脱氢方法,包括以下几个步骤:步骤A:将粒径小于1mm的氢化金属粉装入真空脱氢装置中;步骤B:将炉内真空抽至小于7×10-4Pa,并开始缓慢升温至100℃,保温1h,烘干粉体物料;步骤C:待物料烘干后,继续将炉温升至250℃-350℃,保温1-6h,此时开始缓慢发生脱氢反应,然后,继续将炉温升至500℃-700℃保温1-6h,此时开始大量释放氢气;步骤D:最后,将炉温升至800℃以上,保温1-6h后开始缓慢降温,每降100℃保温至少1h,直至降至常温完成脱氢过程。In order to solve the above-mentioned technical problems, the present invention is solved by the following technical proposal: a method for dehydrogenating metal hydrogenation powder, comprising the following steps: Step A: loading metal hydrogenation powder with a particle size of less than 1mm into a vacuum dehydrogenation device; Step B: vacuuming the furnace to less than 7×10-4Pa, and start to slowly raise the temperature to 100°C, keep it warm for 1 hour, and dry the powder material; Step C: After the material is dried, continue to raise the furnace temperature to 250°C-350°C and keep it warm for 1-6h. ℃ for at least 1h, until the dehydrogenation process is completed at room temperature.

优选的,上述技术方案中,在步骤A中,真空脱氢装置内设置有搅拌装置。Preferably, in the above technical solution, in step A, a stirring device is provided in the vacuum dehydrogenation device.

优选的,上述技术方案中,在步骤B中,脱氢时开启搅拌,搅拌速度小于100转/min。Preferably, in the above technical solution, in step B, stirring is started during dehydrogenation, and the stirring speed is less than 100 rpm.

优选的,上述技术方案中,搅拌装置为耙式搅拌,搅拌速率10-100转/min。Preferably, in the above technical solution, the stirring device is rake stirring, and the stirring rate is 10-100 revolutions/min.

优选的,上述技术方案中,在步骤A中,真空脱氢装置内真空度小于10-4Pa。Preferably, in the above technical solution, in step A, the vacuum degree in the vacuum dehydrogenation device is less than 10 -4 Pa.

优选的,上述技术方案中,在步骤A中,真空脱氢装置真空口处装有孔径小于50微米的316L不锈钢滤网。Preferably, in the above technical solution, in step A, a 316L stainless steel filter with a pore size of less than 50 microns is installed at the vacuum port of the vacuum dehydrogenation device.

优选的,上述技术方案中,在步骤C中,待物料烘干后,继续将炉温升至300℃,保温2h,此时开始缓慢发生脱氢反应,然后,继续将炉温升至600℃保温4h。Preferably, in the above technical solution, in step C, after the materials are dried, continue to raise the furnace temperature to 300°C and keep it warm for 2 hours. At this time, the dehydrogenation reaction begins to slowly occur, and then continue to raise the furnace temperature to 600°C and keep it warm for 4 hours.

优选的,上述技术方案中,在步骤D中,将炉温升至850℃,保温2h后开始缓慢降温。Preferably, in the above technical solution, in step D, the temperature of the furnace is raised to 850° C., and the temperature is slowly lowered after keeping the temperature for 2 hours.

本申请方法相比传统脱氢方法主要在脱氢过程中做出了重大改进。传统的脱氢方法中金属粉物需要平铺固定在炉体内,一旦金属粉物厚度过厚则脱氢效果大打折扣,每次进行脱氢处理时,炉体内空间利用率低。因此本申请采用旋转搅拌的形式进行脱氢,即在脱氢处理时,炉体内不停的进行搅拌,让金属粉物一直在炉体内运动,这种设置不仅让金属粉物受热均匀,还能让氢气快速排出,不会聚集。更优越的是,采用旋转搅拌的方法一次性可以投入比平铺放置3倍以上的量,且在炉体内的脱氢时间远少与平铺放置进行脱氢的时间。Compared with the traditional dehydrogenation method, the method of the present application mainly makes significant improvements in the dehydrogenation process. In the traditional dehydrogenation method, the metal powder needs to be laid flat and fixed in the furnace body. Once the thickness of the metal powder is too thick, the dehydrogenation effect will be greatly reduced. Every time the dehydrogenation process is performed, the space utilization rate in the furnace body is low. Therefore, this application adopts the form of rotary stirring for dehydrogenation, that is, during the dehydrogenation process, the furnace body is continuously stirred to keep the metal powder moving in the furnace body. This setting not only allows the metal powder to be heated evenly, but also allows the hydrogen to be discharged quickly without accumulation. What's more, the method of rotating and stirring can be used to put in more than 3 times the amount of tiles at one time, and the dehydrogenation time in the furnace is much less than the time of tiles for dehydrogenation.

与现有技术相比,本申请方法改变了现有脱氢处理时金属粉物平铺固定进行脱氢的工艺,改为搅拌运动式脱氢,不仅炉体容积利用率高,产能增强,脱氢处理速度以及脱氢效果也极为优越,金属粉脱氢后氢含量<0.003%,脱氢效率可提升30%,有效的解决了现有技术中脱氢效率低的问题。Compared with the existing technology, the method of the present application changes the existing dehydrogenation process of metal powder flat and fixed during dehydrogenation treatment, and changes it to stirring motion dehydrogenation. Not only the furnace volume utilization rate is high, the production capacity is enhanced, the dehydrogenation treatment speed and dehydrogenation effect are also extremely superior. After the metal powder is dehydrogenated, the hydrogen content is <0.003%, and the dehydrogenation efficiency can be increased by 30%, which effectively solves the problem of low dehydrogenation efficiency in the prior art.

附图说明Description of drawings

图1为本申请中脱氢装置示意图。Figure 1 is a schematic diagram of the dehydrogenation device in this application.

图2为本申请方法流程图。Fig. 2 is a flow chart of the method of the present application.

具体实施方式Detailed ways

如图1和图2所示。As shown in Figure 1 and Figure 2.

实施例1:称取1公斤氢化钛粉,装入特制的脱氢炉中,开启炉内耙式搅拌,设定搅拌速率30转/min,将炉内真空抽至7×10-4Pa,并开始缓慢升温至100℃,并保温1h,继续将炉内温度升至300℃,并保温3h,接着升温至650℃,开始大量析出氢气,真空表压力显示有所上升,达到10-3Pa,继续升温至750℃,并保温3h,最后升温至850℃,保温2h后,开始缓慢降温,每降100℃保温1h,直至降至常温完成脱氢,放出脱氢后钛粉,检测氢含量为0.0024%。Example 1: Weigh 1 kg of titanium hydride powder, put it into a special dehydrogenation furnace, start the rake stirring in the furnace, set the stirring rate to 30 rpm, and vacuum the furnace to 7×10-4Pa, and began to slowly raise the temperature to 100°C, and keep it warm for 1h, continue to raise the temperature in the furnace to 300°C, and keep it warm for 3h, then raise the temperature to 650°C, a large amount of hydrogen gas begins to be precipitated, and the vacuum gauge pressure shows a rise, reaching 10-3Pa, continue to raise the temperature to 750°C and keep it warm for 3 hours, and finally raise the temperature to 850°C. After holding the heat for 2 hours, start to cool down slowly, and keep it for 1 hour every time the temperature drops by 100°C, until it drops to room temperature to complete the dehydrogenation, release the dehydrogenated titanium powder, and the hydrogen content is 0.0024%.

实施例2:称取3公斤氢化钛粉,装入特制的脱氢炉中,开启炉内耙式搅拌,设定搅拌速率50转/min,将炉内真空抽至8×10-4Pa,并开始缓慢升温至100℃,并保温1h,继续将炉内温度升至300℃,并保温3h,接着升温至650℃,开始大量析出氢气,真空表压力显示有所上升,达到10-1Pa,继续升温至750℃,并保温3h,最后升温至900℃,保温2h后,开始缓慢降温,每降100℃保温1h,直至降至常温完成脱氢,放出脱氢后钛粉,检测氢含量为0.0021%。Example 2: Weigh 3 kg of titanium hydride powder, put it into a special dehydrogenation furnace, start the rake stirring in the furnace, set the stirring rate to 50 rpm, and vacuum the furnace to 8×10-4Pa, and began to slowly raise the temperature to 100°C, and keep it warm for 1h, continue to raise the temperature in the furnace to 300°C, and keep it warm for 3h, then raise the temperature to 650°C, a large amount of hydrogen gas begins to be precipitated, and the vacuum gauge pressure shows a rise, reaching 10-1Pa, continue to raise the temperature to 750°C, keep it warm for 3 hours, and finally raise the temperature to 900°C, keep it warm for 2 hours, then start to lower the temperature slowly, and keep it warm for 1 hour every time it drops by 100°C, until it drops to room temperature to complete the dehydrogenation, release the dehydrogenated titanium powder, and the hydrogen content is 0.0021%.

实施例3:称取10公斤氢化钛粉,装入特制的脱氢炉中,开启炉内耙式搅拌,设定搅拌速率60转/min,将炉内真空抽至9×10-4Pa,并开始缓慢升温至100℃,并保温1h,继续将炉内温度升至300℃,并保温3h,接着升温至650℃,开始大量析出氢气,真空表压力显示有所上升,达到10-1Pa,继续升温至750℃,并保温3h,最后升温至900℃,保温2h后,开始缓慢降温,每降100℃保温1h,直至降至常温完成脱氢,放出脱氢后钛粉,检测氢含量为0.0022%。Example 3: Weigh 10 kg of titanium hydride powder, put it into a special dehydrogenation furnace, start the rake stirring in the furnace, set the stirring rate at 60 rpm, and vacuum the furnace to 9×10-4Pa, and began to slowly raise the temperature to 100°C, and keep it warm for 1h, continue to raise the temperature in the furnace to 300°C, and keep it warm for 3h, then raise the temperature to 650°C, a large amount of hydrogen gas begins to be precipitated, and the vacuum gauge pressure shows a rise, reaching 10-1Pa, continue to raise the temperature to 750°C, keep it warm for 3 hours, and finally raise the temperature to 900°C. After holding it for 2 hours, start to cool down slowly, and keep it for 1 hour every time it drops by 100°C, until it drops to room temperature to complete the dehydrogenation, release the dehydrogenated titanium powder, and the hydrogen content is 0.0022%.

实施例4:称取1公斤氢化钛粉,装入特制的脱氢炉中,开启炉内耙式搅拌,设定搅拌速率50转/min,将炉内真空抽至7×10-4Pa,并开始缓慢升温至120℃,并保温1h,继续将炉内温度升至300℃,并保温2.5h,接着升温至700℃,开始大量析出氢气,真空表压力显示有所上升,达到10-3Pa,继续升温至800℃,并保温2h,最后升温至900℃,保温1.5h后,开始缓慢降温,每降100℃保温1h,直至降至常温完成脱氢,放出脱氢后钛粉,检测氢含量为0.0026%。Example 4: Weigh 1 kg of titanium hydride powder, put it into a special dehydrogenation furnace, start the rake stirring in the furnace, set the stirring rate to 50 rpm, and vacuum the furnace to 7×10-4Pa, and began to slowly raise the temperature to 120°C, and keep it warm for 1h, continue to raise the temperature in the furnace to 300°C, and keep it warm for 2.5h, then raise the temperature to 700°C, a large amount of hydrogen gas begins to be precipitated, and the vacuum gauge pressure shows a rise, reaching 10-3Pa, continue to raise the temperature to 800°C, keep it warm for 2 hours, and finally raise the temperature to 900°C, keep it warm for 1.5 hours, then start to cool down slowly, and keep it warm for 1 hour every time it drops by 100°C, until it drops to room temperature to complete the dehydrogenation, release the dehydrogenated titanium powder, and the hydrogen content is 0.0026%.

实施例5:称取1公斤氢化钛粉,装入特制的脱氢炉中,开启炉内耙式搅拌,设定搅拌速率40转/min,将炉内真空抽至7×10-4Pa,并开始缓慢升温至100℃,并保温1.5h,继续将炉内温度升至300℃,并保温2.5h,接着升温至700℃,开始大量析出氢气,真空表压力显示有所上升,达到10-3Pa,继续升温至800℃,并保温1.5h,最后升温至900℃,保温2h后,开始缓慢降温,每降100℃保温1h,直至降至常温完成脱氢,放出脱氢后钛粉,检测氢含量为0.0027%。Example 5: Weigh 1 kg of titanium hydride powder, put it into a special dehydrogenation furnace, start the rake stirring in the furnace, set the stirring rate to 40 rpm, and vacuum the furnace to 7×10-4Pa, and began to slowly raise the temperature to 100°C, and keep it warm for 1.5h, continue to raise the temperature in the furnace to 300°C, and keep it warm for 2.5h, then raise the temperature to 700°C, a large amount of hydrogen gas begins to be precipitated, and the vacuum gauge pressure shows a rise, reaching 10-3Pa, continue to raise the temperature to 800°C, keep it warm for 1.5h, and finally raise the temperature to 900°C, keep it warm for 2h, then start to cool down slowly, and keep it warm for 1h every time it drops by 100°C, until it drops to room temperature to complete the dehydrogenation, release the dehydrogenated titanium powder, and the hydrogen content is 0.0027%.

Claims (8)

1. The dehydrogenation method of the hydrogenated metal powder is characterized by comprising the following steps of:
step A: loading hydrogenated metal powder with the particle size smaller than 1mm into a vacuum dehydrogenation device;
and (B) step (B): vacuum in the furnace to less than 7X10 -4 Pa, starting to slowly heat up to 100 ℃, preserving heat for 1h, and drying the powder material;
step C: after the materials are dried, continuously heating the furnace to 250-350 ℃, preserving heat for 1-6 hours, at the moment, starting to slowly perform dehydrogenation reaction, then continuously heating the furnace to 500-700 ℃ and preserving heat for 1-6 hours, at the moment, starting to release a large amount of hydrogen;
step D: and finally, raising the furnace temperature to above 800 ℃, keeping the temperature for 1-6 hours, then starting to slowly cool, keeping the temperature for at least 1 hour when the temperature is lowered by 100 ℃, and finishing the dehydrogenation process until the temperature is lowered to normal temperature.
2. The method for dehydrogenating a hydrogenated metal powder according to claim 1, wherein in the step A, a stirring device is provided in the vacuum dehydrogenating device.
3. The method for dehydrogenating a hydrogenated metal powder according to claim 2, wherein in the step B, stirring is started at a stirring speed of less than 100 rpm.
4. A method for dehydrogenating a hydrogenated metal powder according to claim 2 or 3, wherein the stirring means is a rake stirring at a stirring rate of 10 to 100 rpm.
5. The method for dehydrogenating a hydrogenated metal powder according to claim 1, wherein in the step A, the vacuum degree in the vacuum dehydrogenating apparatus is less than 10 -4 Pa。
6. The method for dehydrogenating metal hydride powder as claimed in claim 1, wherein in the step A, a 316L stainless steel filter screen with a pore size of less than 50 μm is installed at the vacuum port of the vacuum dehydrogenation unit.
7. The method for dehydrogenating metal hydride powder according to claim 1, wherein in the step C, after the material is dried, the furnace temperature is continuously raised to 300 ℃ for 2 hours, at which time the dehydrogenation reaction is slowly started, and then the furnace temperature is continuously raised to 600 ℃ for 4 hours.
8. The method for dehydrogenating a hydrogenated metal powder according to claim 1, wherein in the step D, the furnace temperature is raised to 850℃and the temperature is kept for 2 hours and then the temperature is slowly lowered.
CN202310487241.2A 2023-05-04 2023-05-04 A kind of hydrogenation metal powder dehydrogenation method Pending CN116477568A (en)

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