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CN102909383B - The preparation method of extra-fine nickel powder or cobalt powder - Google Patents

The preparation method of extra-fine nickel powder or cobalt powder Download PDF

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CN102909383B
CN102909383B CN201110221409.2A CN201110221409A CN102909383B CN 102909383 B CN102909383 B CN 102909383B CN 201110221409 A CN201110221409 A CN 201110221409A CN 102909383 B CN102909383 B CN 102909383B
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cobalt
nickel
cobalt powder
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CN102909383A (en
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苏陶贵
杨柳
谭翠丽
何显达
刘沙
郭苗苗
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GEM Co Ltd China
Jingmen GEM New Material Co Ltd
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Shenzhen Gem High Tech Co Ltd
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Abstract

本发明适用于金属微粒制备领域,提供了一种超细镍粉或钴粉的制备方法,包括球磨;第一次气流破碎、分级处理;还原处理及第二次气流破碎、分级处理。本发明的超细镍粉或钴粉的制备方法,通过将球磨和气流破碎结合使用,使得镍粉前驱体或钴粉前驱体中的硬团聚体和软团聚体均被破碎、分散,有效的防止了球磨后的镍粉前驱体或钴粉前驱体的再次团聚;通过还原处理后进行再次气流破碎,使得镍粉或钴粉中的团聚体得到再次破碎分散,有效的防止了还原处理后的镍粉或钴粉的团聚,实现了超细镍粉或钴粉的粒径均一。本发明的制备方法,操作简单、成本低廉,非常适于工业化生产。

The invention is applicable to the field of metal particle preparation, and provides a preparation method of ultrafine nickel powder or cobalt powder, including ball milling; first airflow crushing and classification treatment; reduction treatment and second airflow crushing and classification treatment. The preparation method of ultrafine nickel powder or cobalt powder of the present invention uses ball milling and airflow crushing in combination, so that the hard aggregates and soft aggregates in the nickel powder precursor or cobalt powder precursor are broken and dispersed, effectively It prevents the re-agglomeration of the nickel powder precursor or cobalt powder precursor after ball milling; after the reduction treatment, the airflow crushing is carried out again, so that the agglomerates in the nickel powder or cobalt powder are broken and dispersed again, effectively preventing the re-agglomeration after the reduction treatment. The agglomeration of nickel powder or cobalt powder realizes the uniform particle size of ultrafine nickel powder or cobalt powder. The preparation method of the invention has simple operation and low cost, and is very suitable for industrial production.

Description

超细镍粉或钴粉的制备方法The preparation method of superfine nickel powder or cobalt powder

技术领域 technical field

本发明属于金属微粒制备技术领域,尤其涉及一种超细镍粉或钴粉的制备方法。The invention belongs to the technical field of metal particle preparation, and in particular relates to a preparation method of ultrafine nickel powder or cobalt powder.

背景技术 Background technique

目前,制备超细钴粉采用碳酸钴或草酸钴为原料,加入一定比例的分散剂,在氩气保护环境下经真空球磨,以及在氢气气氛中还原制得,但这种方法需要将球磨罐抽真空,且需要通往氩气保护,球磨时间长,因此生产成本较高;同时,所制备生产的镍粉或钴粉的粒径大小不一,不均匀,无法满足生产的需要。At present, cobalt carbonate or cobalt oxalate is used as raw material to prepare ultrafine cobalt powder, adding a certain proportion of dispersant, vacuum ball milling under argon protection environment, and reduction in hydrogen atmosphere, but this method requires a ball mill tank Vacuuming and argon protection are required, and the ball milling time is long, so the production cost is high; at the same time, the particle size of the prepared nickel powder or cobalt powder is different and uneven, which cannot meet the needs of production.

发明内容 Contents of the invention

有鉴于此,本发明实施例提供一种超细镍粉或钴粉的制备方法,解决现有技术中制备超细镍粉或钴粉成本高、镍粉或钴粉粒径不均匀的技术问题。In view of this, the embodiment of the present invention provides a method for preparing ultrafine nickel powder or cobalt powder, which solves the technical problems of high cost of preparing ultrafine nickel powder or cobalt powder and uneven particle size of nickel powder or cobalt powder in the prior art .

本发明是这样实现的,The present invention is achieved like this,

一种超细镍粉或钴粉的制备方法,包括如下步骤:A preparation method of superfine nickel powder or cobalt powder, comprising the steps of:

将镍粉前驱体或钴粉前驱体球磨3-20小时;Ball mill the nickel powder precursor or cobalt powder precursor for 3-20 hours;

将球磨后的镍粉前驱体或钴粉前驱体进行气流破碎、分级处理,通过破碎和分级叶轮频率,收集目标粒径的镍粉前驱体或钴粉前驱体;The ball-milled nickel powder precursor or cobalt powder precursor is subjected to airflow crushing and grading treatment, and the nickel powder precursor or cobalt powder precursor of the target particle size is collected through crushing and grading impeller frequency;

将该镍粉前驱体或钴粉前驱体在还原气氛及温度为300-450℃条件下焙烧处理,得到镍粉或钴粉;Roasting the nickel powder precursor or cobalt powder precursor in a reducing atmosphere at a temperature of 300-450°C to obtain nickel powder or cobalt powder;

将该镍粉或钴粉进行气流破碎、分级处理,通过破碎和分级叶轮频率,得到超细镍粉或钴粉。The nickel powder or cobalt powder is subjected to airflow crushing and classification treatment, and the ultrafine nickel powder or cobalt powder is obtained by crushing and classifying the frequency of the impeller.

本发明实施例的超细镍粉或钴粉的制备方法,通过将球磨和气流破碎结合使用,使得镍粉前驱体或钴粉前驱体中的硬团聚体和软团聚体均被破碎、分散,有效的防止了球磨后的镍粉前驱体或钴粉前驱体的再次团聚;通过还原处理后进行再次气流破碎,使得镍粉或钴粉中的软团聚体得到再次破碎分散,有效的防止了还原处理后的镍粉或钴粉的团聚,实现了超细镍粉或钴粉的粒径均一。本发明实施例的制备方法,操作简单,成本低廉,非常适于工业化生产。The preparation method of ultra-fine nickel powder or cobalt powder in the embodiment of the present invention uses ball milling and airflow crushing in combination, so that both hard aggregates and soft aggregates in the nickel powder precursor or cobalt powder precursor are broken and dispersed, Effectively prevent the re-agglomeration of the nickel powder precursor or cobalt powder precursor after ball milling; after the reduction treatment, the air-flow crushing is performed again, so that the soft aggregates in the nickel powder or cobalt powder can be broken and dispersed again, effectively preventing the reduction The agglomeration of the treated nickel powder or cobalt powder realizes the uniform particle size of the superfine nickel powder or cobalt powder. The preparation method of the embodiment of the present invention has simple operation and low cost, and is very suitable for industrial production.

附图说明 Description of drawings

图1是本发明实施例超细镍粉或钴粉的制备方法的流程图;Fig. 1 is the flow chart of the preparation method of superfine nickel powder or cobalt powder of the embodiment of the present invention;

图2是本发明实施例一超细镍粉或钴粉的制备方法的流程图;Fig. 2 is the flow chart of the preparation method of the embodiment of the present invention one superfine nickel powder or cobalt powder;

图3是本发明实施例三所制备的超细钴粉电镜扫描照片。Fig. 3 is an electron microscope scanning photo of the ultrafine cobalt powder prepared in Example 3 of the present invention.

具体实施方式 Detailed ways

为了使本发明的目的、技术方案及优点更加清楚明白,以下结合附图及实施例,对本发明进行进一步详细说明。应当理解,此处所描述的具体实施例仅仅用以解释本发明,并不用于限定本发明。In order to make the object, technical solution and advantages of the present invention clearer, the present invention will be further described in detail below in conjunction with the accompanying drawings and embodiments. It should be understood that the specific embodiments described here are only used to explain the present invention, not to limit the present invention.

请参阅图1,图1显示本发明实施例的一种超细镍粉或钴粉的制备方法的流程图,包括如下步骤:Please refer to Fig. 1, Fig. 1 shows the flow chart of the preparation method of a kind of superfine nickel powder or cobalt powder of the embodiment of the present invention, comprises the steps:

步骤S01,球磨Step S01, ball milling

将镍粉前驱体或钴粉前驱体球磨3-20小时;Ball mill the nickel powder precursor or cobalt powder precursor for 3-20 hours;

步骤S02,第一次气流破碎、分级处理Step S02, the first air flow crushing and grading treatment

将球磨后的镍粉前驱体或钴粉前驱体进行气流破碎、分级处理,收集镍粉前驱或钴粉前驱体;Perform air crushing and classification treatment on the nickel powder precursor or cobalt powder precursor after ball milling, and collect the nickel powder precursor or cobalt powder precursor;

步骤S03,还原Step S03, restore

将该镍粉前躯体或钴粉前躯体在还原气氛及温度为300-450℃条件下焙烧处理,得到镍粉或钴粉;Roasting the nickel powder precursor or cobalt powder precursor in a reducing atmosphere at a temperature of 300-450°C to obtain nickel powder or cobalt powder;

步骤S04,第二次气流破碎、分级处理Step S04, the second air flow crushing and grading treatment

将该镍粉或钴粉进行气流破碎、分级处理,收集镍粉或钴粉,得到超细镍粉或钴粉。The nickel powder or cobalt powder is subjected to airflow crushing and classification treatment, and the nickel powder or cobalt powder is collected to obtain superfine nickel powder or cobalt powder.

具体地,该镍粉前驱体选自碳酸镍、草酸镍、氧化镍、氧化亚镍或氢氧化镍中的一种或以上;该钴粉前躯体选自碳酸钴、草酸钴、氧化钴、氧化亚钴或氢氧化钴中的一种或以上。Specifically, the nickel powder precursor is selected from one or more of nickel carbonate, nickel oxalate, nickel oxide, nickelous oxide or nickel hydroxide; the cobalt powder precursor is selected from cobalt carbonate, cobalt oxalate, cobalt oxide, oxide One or more of sub-cobalt or cobalt hydroxide.

具体地,步骤S01中,该球磨所使用的设备没有限制,例如,行星动力球磨机、高能搅拌球磨机等;球磨时间为3-20小时,优选为10-20小时;球磨步骤中,球磨设备的转速为100-300转/分。通过球磨处理,将镍粉前驱体或钴粉前驱体进行破碎分散,特别是对镍钴粉前驱体中的一些硬团聚体,起到了特别有效的破碎分散作用。Specifically, in step S01, the equipment used for the ball milling is not limited, for example, a planetary power ball mill, a high-energy stirring ball mill, etc.; the ball milling time is 3-20 hours, preferably 10-20 hours; in the ball milling step, the speed of the ball milling equipment 100-300 rpm. Through ball milling, the nickel powder precursor or cobalt powder precursor is crushed and dispersed, especially for some hard aggregates in the nickel-cobalt powder precursor, which plays a particularly effective role in crushing and dispersing.

具体地,步骤S02中,该气流破碎、分级处理是指,经过超声气流破碎分级机的破碎、筛选,得到目标粒径的粉末。本步骤中气流破碎、分级处理所使用的设备为流化床气流粉碎机,流化床气流粉碎机是一种用高速气流来实现干式物料超微粉碎的设备,它由粉碎喷嘴、分级转子、螺旋加料器等组成,物料通过螺旋加料器进入粉碎室,压速空气通过特殊配置的超音速喷嘴向粉碎室高速喷射,物料在超音速喷嘴射流中加速,并在喷嘴交汇处反复冲击、碰撞,达到粉碎。被粉碎物料随上升气流进入分级室,由于分级转自高速旋转,粒子既受到分级转子产生的离心力,又受到气流粘性作用产生的向心力,当粒子受到离心力大于向心力,即分级径以上的粗粒子返回粉碎室继续冲击粉碎,分级径以下的细粒子随气流进入旋风分离器、捕集器收集,气体由引风机排出。气流破碎步骤中,该超声气流破碎分级机的频率为30-70HZ/分;该气流破碎的气氛没有限制,例如空气、惰性气氛(例如氮气气氛、氩气气氛等),还原气氛(氢气气氛、一氧化碳气氛等)等。由于步骤S01的球磨过程会产生大量的热,使镍粉前驱体或钴粉前驱体中的水分蒸发,形成水蒸汽,同时球磨过程中因粉末细化,表面能增大,粉末易再次形成团聚体,经过将步骤S02的气流破碎处理后,能够有效的将该团聚体分散,使得镍粉前驱体或钴粉前驱体得到有效的破碎;本步骤S02得到的镍粉前驱体或钴粉前驱体的粒径在200目以上。Specifically, in step S02, the airflow crushing and grading process refers to crushing and screening by an ultrasonic airflow crushing and classifying machine to obtain powder with a target particle size. The equipment used in the airflow crushing and grading treatment in this step is a fluidized bed airflow mill. The fluidized bed airflow mill is a kind of equipment that uses high-speed airflow to realize ultrafine crushing of dry materials. It consists of a crushing nozzle and a grading rotor. , screw feeder, etc., the material enters the crushing chamber through the screw feeder, and the pressure-velocity air is sprayed into the crushing chamber at high speed through a specially configured supersonic nozzle. The material accelerates in the supersonic nozzle jet, and repeatedly impacts and collides at the nozzle intersection. , to achieve crushing. The crushed material enters the classification chamber with the updraft. Since the classifier rotates at high speed, the particles are subjected to both the centrifugal force generated by the classifying rotor and the centripetal force generated by the viscosity of the air flow. The chamber continues to impact and crush, and the fine particles below the classification diameter enter the cyclone separator and collector with the airflow to collect, and the gas is discharged by the induced draft fan. In the air flow crushing step, the frequency of the ultrasonic air flow crushing classifier is 30-70HZ/min; the atmosphere of the air flow crushing is not limited, such as air, inert atmosphere (such as nitrogen atmosphere, argon atmosphere, etc.), reducing atmosphere (hydrogen atmosphere, carbon monoxide atmosphere, etc.), etc. Since the ball milling process in step S01 will generate a large amount of heat, the moisture in the nickel powder precursor or cobalt powder precursor will evaporate to form water vapor. At the same time, due to the powder refinement in the ball milling process, the surface energy will increase, and the powder will easily form agglomeration again. body, after the air flow crushing treatment in step S02, the agglomerates can be effectively dispersed, so that the nickel powder precursor or cobalt powder precursor is effectively broken; the nickel powder precursor or cobalt powder precursor obtained in this step S02 The particle size is above 200 mesh.

本步骤S02中,超声气流破碎分级机,通过破碎频率来控制破碎与分级效果,当粉末粒径达到要求后被分离出来,末达到粒径要求返回破碎腔继续破碎,收集目标粉末,进入下一步处理中;In this step S02, the ultrasonic airflow crushing and classifying machine controls the crushing and grading effect through the crushing frequency. When the particle size of the powder reaches the requirement, it is separated, and the particle size is not reached. Return to the crushing chamber to continue crushing, collect the target powder, and enter the next step Processing;

具体地,步骤S03中,将步骤S02中收集的镍粉前驱体或钴粉前驱体进行还原处理,还原处理的温度为300-450℃,优选为360-420℃;还原处理的时间为2-6小时;该还原气氛没有限制,有还原性气体和惰性气体组成,该还原性气体例如,氢气、一氧化碳;该惰性气氛例如,氮气、氦气、氩气等;该还原性气氛中,还原性气体和惰性气体的体积比为1∶0.1-2.5。经过本步骤的还原处理,使步骤S02中收集的镍粉前驱体或钴粉前驱体被还原成镍粉或钴粉。Specifically, in step S03, the nickel powder precursor or cobalt powder precursor collected in step S02 is subjected to reduction treatment, the temperature of the reduction treatment is 300-450°C, preferably 360-420°C; the time of the reduction treatment is 2- 6 hours; the reducing atmosphere is not limited, and consists of reducing gas and inert gas, such as hydrogen, carbon monoxide; the inert atmosphere, such as nitrogen, helium, argon, etc.; in the reducing atmosphere, reducing The volume ratio of gas and inert gas is 1:0.1-2.5. After the reduction treatment in this step, the nickel powder precursor or cobalt powder precursor collected in step S02 is reduced into nickel powder or cobalt powder.

具体地,步骤S04中,该超声气流破碎分级处理和前述的原理相同,在此不重复阐述。其中,本步骤S04中,气流破碎的气氛为惰性气氛,该惰性气氛和前述的相同,在此不重复阐述;该超声气流破碎分级机的频率为30-70HZ/分。由于步骤S03的还原处理中,会产生水蒸汽,使得本步骤中的镍粉或钴粉长大并再次团聚,使得所制备的镍粉或钴粉粒径大小不一,不具有均匀性,不能满足生产的需要;步骤S03中所制备得到的镍粉或钴粉经过步骤S04的超声气流破碎分级处理,使得镍粉或钴粉中的团聚体进行破碎分散;通过调整破碎频率,得到粒径小、分布窄超细镍粉或钴粉。经过步骤S04处理,所得到的超细镍粉或钴粉的费氏粒径为FSSS0.5-1.0微米,氧含量为0.4-0.8%。Specifically, in step S04 , the classification process of ultrasonic airflow crushing is the same as the aforementioned principle, which will not be repeated here. Wherein, in this step S04, the atmosphere of the jet crushing is an inert atmosphere, which is the same as the above, and will not be repeated here; the frequency of the ultrasonic jet crushing classifier is 30-70HZ/min. Because in the reduction treatment of step S03, water vapor can be produced, making the nickel powder or cobalt powder in this step grow up and agglomerate again, so that the prepared nickel powder or cobalt powder have different particle sizes, do not have uniformity, cannot meet the needs of production; the nickel powder or cobalt powder prepared in step S03 is subjected to the ultrasonic air flow crushing and classification treatment of step S04, so that the agglomerates in the nickel powder or cobalt powder are broken and dispersed; by adjusting the crushing frequency, a particle size small , narrow distribution of ultra-fine nickel powder or cobalt powder. After the treatment in step S04, the obtained ultrafine nickel powder or cobalt powder has a Fischer particle size of 0.5-1.0 micron FSSS and an oxygen content of 0.4-0.8%.

本发明实施例的超细镍粉或钴粉的制备方法,通过将球磨和气流破碎结合使用,使得镍粉前驱体或钴粉前驱体中的硬团聚体和软团聚体均被破碎、分散,有效的防止了球磨后的镍粉前驱体或钴粉前驱体的再次团聚;通过还原处理后进行再次气流破碎,使得镍粉或钴粉中的软团聚体得到再次破碎分散,有效的防止了还原处理后的镍粉或钴粉的再次团聚,实现了超细镍粉或钴粉的粒径均一。The preparation method of ultra-fine nickel powder or cobalt powder in the embodiment of the present invention uses ball milling and airflow crushing in combination, so that both hard aggregates and soft aggregates in the nickel powder precursor or cobalt powder precursor are broken and dispersed, Effectively prevent the re-agglomeration of the nickel powder precursor or cobalt powder precursor after ball milling; after the reduction treatment, the air-flow crushing is performed again, so that the soft aggregates in the nickel powder or cobalt powder can be broken and dispersed again, effectively preventing the reduction The re-agglomeration of the treated nickel powder or cobalt powder realizes the uniform particle size of the ultrafine nickel powder or cobalt powder.

以下结合具体实施例对上述超细镍粉或钴粉的制备方法进行详细阐述。The preparation method of the above-mentioned ultrafine nickel powder or cobalt powder is described in detail below in conjunction with specific examples.

实施例一Embodiment one

请参阅图2,图2显示本发明实施例一超细钴粉制备方法具体流程,包括如下步骤:Please refer to Fig. 2, Fig. 2 shows the specific process of the preparation method of ultrafine cobalt powder according to the embodiment of the present invention, including the following steps:

将碳酸钴在转速为100转/分条件下球磨10小时;The cobalt carbonate was ball milled for 10 hours at a speed of 100 rpm;

将球磨后的碳酸钴进行气流破碎、分级处理,破碎频率为45HZ,得到钴粉前驱体超细粒子粉末;The cobalt carbonate after ball milling is subjected to airflow crushing and classification treatment, and the crushing frequency is 45HZ to obtain superfine particle powder of cobalt powder precursor;

将该钴粉前躯驱体粉末在氮气和氢气(氮气与氢气体积比2.5∶1)及温度为380℃条件下焙烧处理,得到钴粉;The cobalt powder precursor powder is roasted under the conditions of nitrogen and hydrogen (nitrogen to hydrogen volume ratio 2.5:1) and a temperature of 380° C. to obtain cobalt powder;

将该钴粉进行气流破碎、分级处理,气流破碎频率为40HZ,得到超细钴粉,钴粉FSSS0.75um,氧0.55%。The cobalt powder is subjected to airflow crushing and classification treatment, and the airflow crushing frequency is 40HZ to obtain ultrafine cobalt powder, cobalt powder FSSS0.75um, oxygen 0.55%.

实施例二Embodiment two

本发明实施例超细镍粉制备方法,包括如下步骤:The preparation method of the superfine nickel powder of the embodiment of the present invention comprises the following steps:

将草酸镍在转速为200转/分条件下球磨10小时;Nickel oxalate was ball milled for 10 hours at a speed of 200 rpm;

将球磨后的碳酸镍进行气流破碎、分级处理,破碎频率为50HZ得到镍粉前驱体。将该镍粉前驱体在一氧化碳和氮气混合气体(一氧化碳与氮气体积比1∶0.1)及温度为370℃条件下焙烧处理,得到镍粉;The ball-milled nickel carbonate is subjected to airflow crushing and classification treatment, and the crushing frequency is 50HZ to obtain a nickel powder precursor. The nickel powder precursor is calcined under the conditions of carbon monoxide and nitrogen gas mixture (volume ratio of carbon monoxide and nitrogen: 1:0.1) and a temperature of 370° C. to obtain nickel powder;

将该镍粉或镍粉进行气流破碎、分级处理,气流破碎频率为30HZ得到超细镍粉,镍粉FSSS0.65um,氧含量0.61%。The nickel powder or nickel powder is subjected to airflow crushing and classification treatment, and the airflow crushing frequency is 30HZ to obtain superfine nickel powder, nickel powder FSSS0.65um, oxygen content 0.61%.

实施例三Embodiment three

本发明实施例超细钴粉制备方法,包括如下步骤:The preparation method of ultrafine cobalt powder in the embodiment of the present invention comprises the following steps:

将氢氧化钴在转速为300转/分条件下球磨20小时;Cobalt hydroxide was ball milled for 20 hours at a speed of 300 rpm;

将球磨后的氢氧化钴进行气流破碎、分级处理,破碎频率为70HZ得到钴粉前驱体。将该钴粉前驱体在氢气和氮气混合气体(氢气与氮气体积比1∶1.25)及温度为450℃条件下焙烧处理,得到钴粉;The ball-milled cobalt hydroxide is subjected to airflow crushing and classification treatment, and the crushing frequency is 70HZ to obtain a cobalt powder precursor. The cobalt powder precursor is calcined under the conditions of hydrogen and nitrogen mixed gas (hydrogen and nitrogen volume ratio 1:1.25) and a temperature of 450° C. to obtain cobalt powder;

将该钴粉进行气流破碎、分级处理,气流破碎频率为40HZ得到超细钴粉。钴粉FSSS0.55um,氧含量0.65%。请参阅图3,图3显示本发明实施例三所制备的超细钴粉电镜扫描照片,从图3中可以看出,该钴粉粒径小且均匀。The cobalt powder is subjected to airflow crushing and classification treatment, and the airflow crushing frequency is 40HZ to obtain superfine cobalt powder. Cobalt powder FSSS0.55um, oxygen content 0.65%. Please refer to Fig. 3, Fig. 3 shows the electron microscope scanning photo of the ultrafine cobalt powder prepared in Example 3 of the present invention. It can be seen from Fig. 3 that the particle size of the cobalt powder is small and uniform.

以上所述仅为本发明的较佳实施例而已,并不用以限制本发明,凡在本发明的精神和原则之内所作的任何修改、等同替换和改进等,均应包含在本发明的保护范围之内。The above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention. Any modifications, equivalent replacements and improvements made within the spirit and principles of the present invention should be included in the protection of the present invention. within range.

Claims (9)

1. a preparation method for extra-fine nickel powder or cobalt powder, comprises the steps:
By nickel powder precursor or cobalt powder precursor ball milling 3-20 hour;
Powdered nickel precursor body after ball milling or cobalt powder presoma are carried out airflow crash, classification process, collects powdered nickel precursor body or cobalt powder presoma; It is characterized in that, also comprise the steps:
The calcination process under reducing atmosphere and temperature are 300-450 DEG C of condition by described powdered nickel precursor body or cobalt powder presoma, obtains nickel powder or cobalt powder;
Described nickel powder or cobalt powder are carried out airflow crash, classification process, collects extra-fine nickel powder or cobalt powder;
Described powdered nickel precursor body be selected from nickelous carbonate, nickel oxalate, nickel oxide, nickel protoxide or nickel hydroxide one or more; Described cobalt powder presoma be selected from cobalt carbonate, cobalt oxalate, cobalt oxide, cobalt protoxide or cobalt hydroxide one or more.
2. the preparation method of extra-fine nickel powder as claimed in claim 1 or cobalt powder, it is characterized in that, rotating speed during described ball milling is 100-300 rev/min.
3. the preparation method of extra-fine nickel powder as claimed in claim 1 or cobalt powder, it is characterized in that, the time of described ball milling is 10-20 hour.
4. the preparation method of extra-fine nickel powder as claimed in claim 1 or cobalt powder, it is characterized in that, described milling atmosphere is air atmosphere.
5. the preparation method of extra-fine nickel powder as claimed in claim 1 or cobalt powder, it is characterized in that, the frequency of described air current classifying fragmentation is that 30-70HZ/ divides.
6. the preparation method of extra-fine nickel powder as claimed in claim 1 or cobalt powder, is characterized in that, described reducing atmosphere is the mixed atmosphere of reducibility gas and inert gas composition.
7. the preparation method of extra-fine nickel powder as claimed in claim 1 or cobalt powder, it is characterized in that, the time of described calcination process is 2-6 hour.
8. the preparation method of extra-fine nickel powder as claimed in claim 1 or cobalt powder, it is characterized in that, described nickel powder or cobalt powder are carried out in airflow crash, classification treatment step, the atmosphere of airflow crash is inert atmosphere.
9. the preparation method of extra-fine nickel powder as claimed in claim 1 or cobalt powder, it is characterized in that, described nickel powder or cobalt powder oxygen content are 0.4-0.8%.
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