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CN107008910A - A kind of lead-power machine - Google Patents

A kind of lead-power machine Download PDF

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Publication number
CN107008910A
CN107008910A CN201710288727.8A CN201710288727A CN107008910A CN 107008910 A CN107008910 A CN 107008910A CN 201710288727 A CN201710288727 A CN 201710288727A CN 107008910 A CN107008910 A CN 107008910A
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China
Prior art keywords
lead
lead powder
spiral case
power machine
turbine
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CN201710288727.8A
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CN107008910B (en
Inventor
郭志刚
李海彪
刘玉
李桂发
邓成智
马铭泽
崔海涛
孔鹤鹏
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Tianneng Battery Group Co Ltd
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Tianneng Battery 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
    • B22F9/04Making metallic powder or suspensions thereof using physical processes starting from solid material, e.g. by crushing, grinding or milling
    • 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
    • B22F9/04Making metallic powder or suspensions thereof using physical processes starting from solid material, e.g. by crushing, grinding or milling
    • B22F2009/045Making metallic powder or suspensions thereof using physical processes starting from solid material, e.g. by crushing, grinding or milling by other means than ball or jet milling
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

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  • Battery Electrode And Active Subsutance (AREA)

Abstract

本发明公开了一种铅粉机,包括主机和出料管,所述出料管上安装有筛选装置,所述筛选装置包括具有进风口和出风口的蜗壳,蜗壳内设有由电机驱动的涡轮,所述涡轮呈环形,中心具有与出风口衔接的进风通道,周侧设有环绕进风通道设置的叶片,相邻叶片之间具有连通进风通道的间隙。本发明铅粉机通过在主机的出料管上安装有筛选装置,将大颗粒的铅粉筛选出来重新进入主机进行粉碎,符合规格的小颗粒铅粉则收集起来,从而生产获得粒度更细且分布跨度更小的铅粉,从而提高极板固化效果的一致性和电池的一致性,延长整个电池的使用寿命。

The invention discloses a lead powder machine, which includes a main machine and a discharge pipe. A screening device is installed on the discharge pipe. The screening device includes a volute with an air inlet and an air outlet. The driven turbine is ring-shaped, with an air inlet channel connected to the air outlet in the center, blades arranged around the air inlet channel on the periphery, and gaps communicating with the air inlet channel between adjacent blades. The lead powder machine of the present invention is equipped with a screening device on the discharge pipe of the main machine, and the large-particle lead powder is screened out and re-enters the main machine for crushing, and the small-particle lead powder that meets the specifications is collected, thereby producing a finer particle size and Distribute lead powder with a smaller span, thereby improving the consistency of the plate curing effect and the consistency of the battery, and extending the service life of the entire battery.

Description

一种铅粉机A lead powder machine

技术领域technical field

本发明涉及铅蓄电池生产设备技术领域,特别是涉及一种铅粉机。The invention relates to the technical field of lead storage battery production equipment, in particular to a lead powder machine.

背景技术Background technique

铅粉是生产铅蓄电池最重要的原材料之一。铅粉的性能参数一般有氧化度、视密度、吸酸值、吸水值和粒度及其分布等。其中铅粉粒径及其分布对极板和电池性能有着很大的影响,粒径较细的铅粉,制成的未化成极板的孔隙度越大、极化时容易转化为活性物质PbO2、初始容量较大、做成的电池充电接受性好。Lead powder is one of the most important raw materials for the production of lead-acid batteries. The performance parameters of lead powder generally include oxidation degree, apparent density, acid absorption value, water absorption value, particle size and its distribution. Among them, the particle size and distribution of lead powder have a great influence on the performance of the plate and battery. The finer the lead powder, the greater the porosity of the unformed plate, and it is easy to convert into the active substance PbO during polarization. 2. The initial capacity is large, and the finished battery has good charge acceptance.

目前,行业内大部分采用滚筒式铅粉机(又称岛津式铅粉机)系统进行制粉。滚筒式铅粉机(又称岛津式铅粉机)是铅块生产铅粉最常用的机器。滚筒式铅粉机,一般包括外面的罩壳、罩壳内部可旋传的滚筒、送风装置、冷却喷淋装置、铅粉收集装置等,其中滚筒用来使铅粒翻滚摩擦碰撞,送风装置用来提供铅粉氧化所需空气和分离铅粉和铅粒,冷却喷淋装置用来给滚筒降温,铅粉收集装置用来收集滚筒产出的铅粉。一般滚筒以两端中空轴经轴承安装在机座上,两端中空轴分别作为风、铅粒的入口和风、铅粉的出口。At present, most of the industry adopts the drum type lead powder machine (also known as Shimadzu type lead powder machine) system for powder making. Drum type lead powder machine (also known as Shimadzu type lead powder machine) is the most commonly used machine for producing lead powder from lead blocks. The drum-type lead powder machine generally includes an outer casing, a rotating drum inside the casing, an air supply device, a cooling spray device, a lead powder collection device, etc., and the drum is used to make the lead particles tumble, rub and collide, and supply air. The device is used to provide the air required for the oxidation of lead powder and to separate the lead powder and lead particles. The cooling spray device is used to cool down the drum, and the lead powder collection device is used to collect the lead powder produced by the drum. Generally, the drum is installed on the machine base with the hollow shafts at both ends through bearings, and the hollow shafts at both ends are respectively used as the inlet of wind and lead particles and the outlet of wind and lead powder.

一般,铅粉机制粉过程如下:In general, the powder process of lead powder mechanism is as follows:

将铅块由铅粒储存仓按负载量送入铅粉机滚筒,同时通过风机给铅粉机内输入定量的新鲜空气。铅粉机滚筒由传动机构带动,以一定的转速旋转,铅粉机内的铅块不断的摩擦、撞击、晶体变形位移、氧化,铅块表面被氧化的部分逐渐从块体上脱落下来,续而进一步磨碎、研细而形成了覆盖一层PbO的细颗粒状铅粉。这些细小微粒通过滚筒旋转作用和滚筒内壁刮板作用扬起,通过气流带出铅粉机滚筒,进入出口弯管,再进入集粉器,通过集粉器内布袋的作用将气流中的铅粉进行收集,然后输送至粉仓进行储存。在出粉弯管处,过大颗粒会沉降下来通过反推螺旋装置推回铅粉机滚筒进行进一步研磨。Send the lead lumps from the lead particle storage bin to the lead powder machine drum according to the load, and at the same time, input a certain amount of fresh air into the lead powder machine through the fan. The lead powder machine drum is driven by the transmission mechanism and rotates at a certain speed. The lead blocks in the lead powder machine are constantly rubbed, impacted, crystal deformation, displacement, and oxidized. The oxidized part of the lead block surface gradually falls off from the block. Continued And further pulverized, pulverized and formed the fine granular lead powder that covers a layer of PbO. These fine particles are raised by the rotation of the drum and the scraper on the inner wall of the drum, and are taken out of the drum of the lead powder machine by the air flow, enter the outlet elbow, and then enter the powder collector, and the lead powder in the air flow is removed by the function of the bag in the powder collector. It is collected and then transported to the powder bin for storage. At the powder outlet elbow, the oversized particles will settle down and be pushed back to the drum of the lead powder machine through the reverse screw device for further grinding.

使用上述生产工艺生产的铅粉,经粒度分析发现,其铅粉粒度分布跨度过广,在0μm~120μm之间。铅粉粒度分布跨度过广,均匀性较差,造成极板固化效果差异性较大,最终影响电池的使用寿命。The particle size analysis of the lead powder produced by the above production process shows that the particle size distribution of the lead powder is too wide, ranging from 0 μm to 120 μm. The particle size distribution of the lead powder is too wide and the uniformity is poor, resulting in a large difference in the curing effect of the plate, which ultimately affects the service life of the battery.

发明内容Contents of the invention

本发明针对现有铅粉机制备的铅粉粒度分布跨度过广的问题,提供了一种铅粉机,利用本发明铅粉机制备的铅粉粒度更细且分布跨度更小,铅粉更细、均匀性更好。The present invention aims at the problem that the particle size distribution span of the lead powder prepared by the existing lead powder machine is too wide, and provides a lead powder machine. Fine, better uniformity.

一种铅粉机,包括主机和出料管,所述出料管上安装有筛选装置,所述筛选装置包括具有进风口和出风口的蜗壳,蜗壳内设有由电机驱动的涡轮,所述涡轮呈环形,中心具有与出风口衔接的进风通道,周侧设有环绕进风通道设置的叶片,相邻叶片之间具有连通进风通道的间隙。A lead powder machine, comprising a main engine and a discharge pipe, a screening device is installed on the discharge pipe, the screening device includes a volute with an air inlet and an air outlet, and a turbine driven by a motor is arranged in the volute, The turbine is ring-shaped, with an air inlet channel connected to the air outlet in the center, blades arranged around the air inlet channel on the periphery, and gaps connecting the air inlet channel between adjacent blades.

所述蜗壳呈筒状,底部径向缩小呈锥形,底端设有回料口,所述进风口设于蜗壳的侧面,出风口设于蜗壳的顶端端面。The volute is in the shape of a tube, the bottom is tapered in radial direction, and the bottom end is provided with a material return port, the air inlet is provided on the side of the volute, and the air outlet is provided on the top end surface of the volute.

所述涡轮的顶端端面与蜗壳内壁相配合。The top end surface of the turbine matches the inner wall of the volute.

所述涡轮上具有穿过出风口伸出蜗壳外的转轴,所述蜗壳外部设有包围转轴的保护罩,保护罩连接所述出料管。The turbine has a rotating shaft extending out of the volute through the air outlet, and a protective cover surrounding the rotating shaft is provided outside the volute, and the protective cover is connected to the discharge pipe.

所述进风通道靠近出风口的端部设有连接转轴的十字架。The end of the air inlet passage near the air outlet is provided with a cross connected to the rotating shaft.

所述主机的出料口安装有回料绞龙,所述出料管的进料端以及蜗壳的底部均连接回料绞龙。A return auger is installed at the discharge port of the main engine, and the feed end of the discharge pipe and the bottom of the volute are both connected to the return auger.

所述蜗壳底部通过下料阀连接回料绞龙。The bottom of the volute is connected to the return auger through the feeding valve.

所述涡轮两端设有固定叶片的端盖,端盖中心具有通孔。Both ends of the turbine are provided with end covers for fixing the blades, and the center of the end covers has a through hole.

本发明铅粉机通过在主机的出料管上安装有筛选装置,筛选装置包括蜗壳,蜗壳内的涡轮在电极驱动下转动,从主机中出来的铅粉进入涡轮中心的进风通道时,涡轮转动使铅粉颗粒形成离心力,大颗粒离心力较大从涡轮叶片间的间隙甩出,最后重新进入主机进行粉碎,符合规格的小颗粒铅粉则不能被甩出,从蜗壳的出风口进入后续收集铅粉的布袋中,从而生产获得粒度更细且分布跨度更小的铅粉,从而提高极板固化效果的一致性和电池的一致性,延长整个电池的使用寿命。The lead powder machine of the present invention is equipped with a screening device on the discharge pipe of the main engine. The screening device includes a volute, and the turbine in the volute rotates under the drive of the electrode. , the rotation of the turbine makes the lead powder particles form a centrifugal force, and the large particles are thrown out from the gap between the turbine blades with a large centrifugal force, and finally re-enter the main engine for crushing. Enter the cloth bag for subsequent collection of lead powder, so as to produce lead powder with finer particle size and smaller distribution span, so as to improve the consistency of plate curing effect and battery consistency, and prolong the service life of the entire battery.

附图说明Description of drawings

图1为本发明铅粉机的结构示意图。Fig. 1 is the structural representation of lead powder machine of the present invention.

图2为本发明铅粉机筛选装置的结构示意图。Fig. 2 is the structural representation of the screening device of the lead powder machine of the present invention.

图3为本发明涡轮的结构示意图。Fig. 3 is a structural schematic diagram of the turbine of the present invention.

图4为图3中沿A-A方向的剖视图。Fig. 4 is a cross-sectional view along A-A direction in Fig. 3 .

图5为涡轮的俯视结构示意图。Fig. 5 is a top structural schematic diagram of the turbine.

图6为使用现有技术铅粉机生产的铅粉粒度分析结果图。Fig. 6 is a graph showing particle size analysis results of lead powder produced by a prior art lead powder machine.

图7为使用本发明铅粉机生产的铅粉粒度分析结果图。Fig. 7 is the particle size analysis result diagram of the lead powder produced by the lead powder machine of the present invention.

具体实施方式detailed description

实施例1Example 1

如图1~5所示,一种铅粉机,包括主机1,主机1内具有可自转的滚筒101,主机1的进料口连接有铅粒储存仓2,出料口连接出料管,出料管上安装有筛选装置5,筛选装置5包括蜗壳501,蜗壳501具有进风口502和出风口503,出料管被筛选装置5分成两段,分别为与进风口502相连的出料管3和与出风口503相连的出料管4。出料管4另一端连接集粉器6,集粉器6包括用于将铅粉和气流分离的布袋601、为主机1中铅粉进入集粉器6提供动力的负压风机602以及将铅粉从集粉器6的出粉口输出至后段工序进行储存的绞龙603。As shown in Figures 1 to 5, a lead powder machine includes a main machine 1, which has a rotating drum 101 inside the main machine 1. The feed port of the main machine 1 is connected with a lead particle storage bin 2, and the discharge port is connected with a discharge pipe. A screening device 5 is installed on the discharge pipe, and the screening device 5 includes a volute 501. The volute 501 has an air inlet 502 and an air outlet 503. The discharge pipe is divided into two sections by the screening device 5, which are respectively connected to the air inlet 502 The feed pipe 3 and the discharge pipe 4 connected with the air outlet 503 . The other end of the discharge pipe 4 is connected to the powder collector 6, and the powder collector 6 includes a cloth bag 601 for separating the lead powder from the air flow, a negative pressure blower 602 that provides power for the lead powder in the main engine 1 to enter the powder collector 6, and the lead powder The powder is output from the powder outlet of the powder collector 6 to the auger 603 for storage in the subsequent process.

蜗壳501呈筒状,底部径向缩小呈锥形,底端设有回料口510,进风口502设于蜗壳501的侧面,出风口503设于蜗壳501的顶端端面。蜗壳501内设有涡轮504,涡轮504呈环形,中心具有与出风口503衔接的进风通道505,周侧设有环绕进风通道505设置的叶片506,相邻叶片506之间具有连通进风通道505的间隙512。涡轮504的顶端端面与蜗壳501内壁相配合,两者之间在涡轮504转动过程中保持密封配合。涡轮504上具有穿过出风口503伸出蜗壳501外的转轴507,进风通道505靠近出风口503的端部设有连接转轴507的十字架513。蜗壳501外部设有包围转轴507的保护罩508,保护罩508连接出料管4。转轴507一端连接有驱动涡轮504转动的电机509。The volute 501 is in the shape of a cylinder, the bottom of which is tapered radially, and the bottom end is provided with a material return port 510 , the air inlet 502 is provided on the side of the volute 501 , and the air outlet 503 is provided on the top end surface of the volute 501 . The volute 501 is provided with a turbine 504, the turbine 504 is annular, the center has an air inlet channel 505 connected with the air outlet 503, and the surrounding side is provided with blades 506 arranged around the air inlet channel 505, and there are connecting inlets between adjacent blades 506. The gap 512 of the wind channel 505 . The top end surface of the worm gear 504 fits with the inner wall of the volute 501 , and the two keep a tight fit during the rotation of the worm gear 504 . The turbine 504 has a rotating shaft 507 extending out of the volute 501 through the air outlet 503 , and the end of the air inlet channel 505 near the air outlet 503 is provided with a cross 513 connected to the rotating shaft 507 . A protective cover 508 surrounding the rotating shaft 507 is provided outside the volute 501 , and the protective cover 508 is connected to the discharge pipe 4 . One end of the rotating shaft 507 is connected with a motor 509 for driving the turbine 504 to rotate.

主机1的出料口安装有回料绞龙8,出料管3的进料端以及蜗壳501的底部均连接回料绞龙8。蜗壳501底部通过下料阀511连接回料绞龙8。下料阀511为标准件,也称旋转下料阀,具有锁风密闭、下粉的功能,既能保证大粒径的铅粉顺利输送至回料绞龙8处,又要保证蜗壳501底部不能有风通过,避免风将沉降下来的大粒径的铅粉再次扬起。为了保证出料管内铅粉不堆积、避免铅粉堵塞出料管,在出料管3和出料管4上分别安装有振动电机301和振动电机401。The discharge port of the main engine 1 is equipped with a return auger 8 , and the feed end of the discharge pipe 3 and the bottom of the volute 501 are connected to the return auger 8 . The bottom of the volute 501 is connected to the return auger 8 through the feed valve 511 . The feeding valve 511 is a standard part, also known as the rotary feeding valve, which has the function of airtight sealing and powder feeding, which can not only ensure the smooth delivery of large particle size lead powder to the return auger 8, but also ensure that the volute 501 No wind can pass through the bottom, so as to prevent the wind from raising the settled large-size lead powder again. In order to ensure that the lead powder in the discharge pipe does not accumulate and prevent the lead powder from blocking the discharge pipe, a vibration motor 301 and a vibration motor 401 are installed on the discharge pipe 3 and the discharge pipe 4 respectively.

出料管4上设有二次进风口,二次进风口处安装有进风管402,进风管402上设有流量调节阀,铅粉和通过滚筒101的气流从主机1出来后温度很高,从二次进风口进入的新鲜风温度低,能够对铅粉和气流进行降温。而环境温度一年四季相差较大,可以通过二次进风口上流量调节阀根据实际需要调节进入的风量。The discharge pipe 4 is provided with a secondary air inlet, and an air inlet pipe 402 is installed at the secondary air inlet. The air inlet pipe 402 is provided with a flow regulating valve. High, the temperature of fresh air entering from the secondary air inlet is low, which can cool down the lead powder and airflow. The ambient temperature varies greatly throughout the year, and the air volume can be adjusted according to actual needs through the flow regulating valve on the secondary air inlet.

生产时,铅粒从铅粒储存仓2按主机1的负荷情况连续进入主机1的滚筒101内,在滚筒101内铅粒碰撞、研磨、氧化,产生铅粉。滚筒101内铅粉在滚筒101旋转作用和扬粉机构的作用下被扬起,在负压风机602产生的风力作用下被吸入出料管3内,再进入筛选装置5内进行粒径分离、筛选。筛选装置5的电机509工作,由转轴507带动涡轮504转动,含有铅粉的气流进入蜗壳501内部后,进入涡轮504内部的进风通道505,在涡轮504转动所产生的离心力作用下,气流中粒径足够大的铅粉沿径向运动,通过叶片506之间的间隙512被甩出涡轮501,在蜗壳501内壁或接近蜗壳501内壁的位置开始沉降,最后收集到蜗壳501的底部,经下料阀511由回料绞龙8送入主机1的滚筒101内进一步进行研磨加工;而粒径较小的铅粉由离心力较小,在气流带动下从进风通道505的上端出出风口503,然后进入出料管4并进入集粉器6,在布袋601的作用下将气流与铅粉分离,铅粉由绞龙603驱动,通过集粉器6的出粉口输出至后段工序进行储存。从而生产获得粒度更细且分布跨度更小的铅粉。During production, lead grains enter the drum 101 of the main machine 1 continuously from the lead grain storage bin 2 according to the load of the main machine 1, and the lead grains collide, grind and oxidize in the drum 101 to produce lead powder. The lead powder in the drum 101 is lifted up under the action of the rotation of the drum 101 and the action of the powder lifting mechanism, and is sucked into the discharge pipe 3 under the action of the wind force generated by the negative pressure fan 602, and then enters the screening device 5 for particle size separation, filter. The motor 509 of the screening device 5 works, and the rotating shaft 507 drives the turbine 504 to rotate. After the airflow containing lead powder enters the inside of the volute 501, it enters the air inlet channel 505 inside the turbine 504. Under the action of the centrifugal force generated by the rotation of the turbine 504, the airflow The lead powder with a sufficiently large medium particle size moves radially, is thrown out of the turbine 501 through the gap 512 between the blades 506, begins to settle at or near the inner wall of the volute 501, and is finally collected in the volute 501. The bottom is fed into the drum 101 of the main machine 1 by the feeding auger 8 through the feeding valve 511 for further grinding; while the lead powder with a smaller particle size is driven by the airflow from the upper end of the air inlet channel 505 due to the smaller centrifugal force. Out of the air outlet 503, then into the discharge pipe 4 and into the powder collector 6, the air flow is separated from the lead powder under the action of the cloth bag 601, and the lead powder is driven by the auger 603, and is output to the powder outlet through the powder collector 6. Storage in the later stage of the process. Thereby producing lead powder with finer particle size and smaller distribution span.

涡轮504的转速通过电机509变频可调,其他条件不变的情况下,不同的转速会导致不同粒径的铅粉通过筛选装置5,转速越高,通过筛选装置5的铅粉粒径越小,反之越大。The rotating speed of the turbine 504 is adjustable through the frequency conversion of the motor 509. Under other conditions remaining unchanged, different rotating speeds will cause lead powders of different particle sizes to pass through the screening device 5. The higher the rotating speed, the smaller the particle size of the lead powder passing through the screening device 5. , and vice versa.

实施例2Example 2

将实施例1中安装有筛选装置的铅粉机生产的铅粉与现有技术中没有安装筛选装置的铅粉机(两者其余结果相同)生产的铅粉分别进行铅粉粒度分析,粒度分析使用激光粒度分析仪(winner2000ZD),分析步骤如下:The lead powder produced by the lead powder machine that the screening device is installed in embodiment 1 and the lead powder produced by the lead powder machine (both other results are the same) that do not install the screening device in the prior art carry out lead powder particle size analysis respectively, particle size analysis Using a laser particle size analyzer (winner2000ZD), the analysis steps are as follows:

1、在相同环境条件下(24℃,35%相对湿度)测试改进前后的两种样品,称量相同质量的两种样品;1. Under the same environmental conditions (24°C, 35% relative humidity), test the two samples before and after improvement, and weigh the two samples with the same mass;

2、先进水到达水位线,然后进行超声,搅拌,对样品颗粒进行充分的分散,待充分分散后进行正式循环+超声测试,待数据,谱线稳定后保存数据,导出结果,最后对仪器进行冲洗,实验完毕。2. The advanced water reaches the water level line, and then perform ultrasonication and stirring to fully disperse the sample particles. After the full dispersion, perform a formal circulation + ultrasonic test. After the data and spectral lines are stable, save the data, export the results, and finally perform a test on the instrument. Rinse, the experiment is over.

试验中选择分散剂和分散介质都是水。测量范围0.6~120μm,搅拌档位6,超声时间都是60s。The dispersant and dispersion medium selected in the test are both water. The measuring range is 0.6-120μm, the stirring position is 6, and the ultrasonic time is 60s.

结果如表1~3以及图6和7所示,表1和图6为使用现有技术(没有安装筛选装置)生产的铅粉粒径分布情况;表2和图7为使用本发明铅粉机生产的铅粉粒径分布情况;表3为两者的一些数据对比,D10、D50、D80、D90、D99分别指铅粉累积体积(即粒径不大于特定值的所有铅粉的总体积)达到10%、50%、80%、90%、99%时粒径的大小,S/V表示铅粉的比表面积,Dav表示平均粒径。使用现有技术(没有安装筛选装置)生产的铅粉粒径明显分布跨度较广,分布并不均匀,小颗粒与大颗粒铅粉体积比例差距较大。而使用本发明铅粉机生产的铅粉粒径较为稳定的分布在小颗粒尺寸范围,粒径跨度小,分布区间稳定,粒径分布能达到均匀一致性,大颗粒体积含量基本为零。Result is shown in Table 1~3 and Fig. 6 and 7, and table 1 and Fig. 6 are the particle size distribution situation of the lead powder that uses prior art (not installing screening device) to produce; Table 2 and Fig. 7 use lead powder of the present invention The particle size distribution of the lead powder produced by the machine; Table 3 is some data comparison between the two, D10, D50, D80, D90, D99 respectively refer to the cumulative volume of lead powder (that is, the total volume of all lead powders whose particle size is not greater than a specific value ) reaches 10%, 50%, 80%, 90%, and 99% of the particle size, S/V represents the specific surface area of the lead powder, and Dav represents the average particle size. The particle size distribution of the lead powder produced by the existing technology (without installing a screening device) is obviously wider and uneven, and the volume ratio of small particles and large particles of lead powder has a large gap. The particle size of the lead powder produced by the lead powder machine of the present invention is relatively stable in the small particle size range, the particle size span is small, the distribution interval is stable, the particle size distribution can reach uniformity, and the volume content of large particles is basically zero.

表1使用现有技术生产的铅粉粒径分布情况。Table 1 uses the particle size distribution of the lead powder produced by the prior art.

粒径μmParticle size μm 体积%volume% 累积%accumulation% 粒径μmParticle size μm 体积%volume% 累积%accumulation% 粒径μmParticle size μm 体积%volume% 累积%accumulation% 0.120.12 0.000.00 0.000.00 1.831.83 10.1810.18 27.2327.23 27.6327.63 1.981.98 93.5293.52 0.150.15 0.000.00 0.000.00 2.222.22 12.9812.98 40.2140.21 33.5433.54 2.062.06 95.5895.58 0.180.18 0.000.00 0.000.00 2.702.70 12.8712.87 53.0853.08 40.7240.72 1.901.90 97.4897.48 0.220.22 0.000.00 0.000.00 3.283.28 8.268.26 61.3461.34 49.4349.43 1.401.40 98.8798.87 0.260.26 0.000.00 0.000.00 3.983.98 4.594.59 65.9265.92 60.0060.00 0.660.66 99.5499.54 0.320.32 0.000.00 0.000.00 4.834.83 3.133.13 69.0669.06 72.8472.84 0.240.24 99.7899.78 0.390.39 0.000.00 0.000.00 5.865.86 2.492.49 71.5571.55 88.4288.42 0.120.12 99.9199.91 0.470.47 0.000.00 0.000.00 7.117.11 2.392.39 73.9473.94 107.33107.33 0.090.09 100.00100.00 0.570.57 0.000.00 0.000.00 8.648.64 2.782.78 76.7276.72 120.00120.00 0.000.00 100.00100.00 0.690.69 1.671.67 1.671.67 10.4810.48 3.273.27 79.9979.99 158.17158.17 0.000.00 100.00100.00 0.840.84 2.482.48 4.154.15 12.7312.73 3.483.48 83.4783.47 192.00192.00 0.000.00 100.00100.00 1.021.02 3.213.21 7.367.36 15.4515.45 3.193.19 86.6686.66 233.07233.07 0.000.00 100.00100.00 1.241.24 4.204.20 11.5711.57 18.7518.75 2.672.67 89.3489.34 282.93282.93 0.000.00 100.00100.00 1.511.51 5.485.48 17.0517.05 22.7622.76 2.212.21 91.5491.54 300.00300.00 0.000.00 100.00100.00

表2使用本发明铅粉机生产的铅粉粒径分布情况。Table 2 uses the particle size distribution of the lead powder produced by the lead powder machine of the present invention.

粒径μmParticle size μm 体积%volume% 累积%accumulation% 粒径μmParticle size μm 体积%volume% 累积%accumulation% 粒径μmParticle size μm 体积%volume% 累积%accumulation% 0.120.12 0.000.00 0.000.00 1.831.83 26.4926.49 53.4353.43 27.6327.63 0.000.00 100.00100.00 0.150.15 0.000.00 0.000.00 2.222.22 24.9824.98 78.4178.41 33.5433.54 0.000.00 100.00100.00 0.180.18 0.000.00 0.000.00 2.702.70 16.6216.62 95.0395.03 40.7240.72 0.000.00 100.00100.00 0.220.22 0.000.00 0.000.00 3.283.28 4.674.67 99.7099.70 49.4349.43 0.000.00 100.00100.00 0.260.26 0.000.00 0.000.00 3.983.98 0.240.24 99.9499.94 60.0060.00 0.000.00 100.00100.00 0.320.32 0.000.00 0.000.00 4.834.83 0.060.06 100.00100.00 72.8472.84 0.000.00 100.00100.00 0.390.39 0.000.00 0.000.00 5.865.86 0.000.00 100.00100.00 88.4288.42 0.000.00 100.00100.00 0.470.47 0.000.00 0.000.00 7.117.11 0.000.00 100.00100.00 107.33107.33 0.000.00 100.00100.00 0.570.57 0.000.00 0.000.00 8.648.64 0.000.00 100.00100.00 120.00120.00 0.000.00 100.00100.00 0.690.69 0.980.98 0.980.98 10.4810.48 0.000.00 100.00100.00 158.17158.17 0.000.00 100.00100.00 0.840.84 1.471.47 2.452.45 12.7312.73 0.000.00 100.00100.00 192.00192.00 0.000.00 100.00100.00 1.021.02 1.901.90 4.354.35 15.4515.45 0.000.00 100.00100.00 233.07233.07 0.000.00 100.00100.00 1.241.24 7.347.34 11.6911.69 18.7518.75 0.000.00 100.00100.00 282.93282.93 0.000.00 100.00100.00 1.511.51 15.2515.25 26.9426.94 22.7622.76 0.000.00 100.00100.00 300.00300.00 0.000.00 100.00100.00

表3两种铅粉数据比较。Table 3 Comparison of two kinds of lead powder data.

现有技术生产铅粉Production of lead powder by prior art 本发明铅粉机生产铅粉Lead powder machine of the present invention produces lead powder D10D10 1.16μm1.16μm 1.19μm1.19μm D50D50 2.59μm2.59μm 1.79μm1.79μm D80D80 -- 2.27μm2.27μm D90D90 19.96μm19.96μm 2.55μm2.55μm D99D99 51.44μm51.44μm 3.19μm3.19μm S/VS/V 25334.97cm2/cm3 25334.97cm 2 /cm 3 35947.22cm2/cm3 35947.22cm 2 /cm 3 DavDavid 7.22μm7.22μm 1.83μm1.83μm

Claims (8)

1. a kind of lead-power machine, including main frame and discharge nozzle, it is characterised in that screening plant is provided with the discharge nozzle, described Screening plant includes being provided with the spiral case with air inlet and air outlet, spiral case by motor-driven turbine, and the turbine is in ring Shape, center has the air intake passage being connected with air outlet, and the week side of boss is provided around between the blade of air intake passage setting, adjacent blades Gap with connection air intake passage.
2. lead-power machine as claimed in claim 1, it is characterised in that the spiral case is cylindrical in shape, bottom radially reduces tapered, bottom End is provided with feedback outlet, and the air inlet is located at the side of spiral case, and air outlet is located at the top end face of spiral case.
3. lead-power machine as claimed in claim 2, it is characterised in that the top end face of the turbine is engaged with spiral case inwall.
4. lead-power machine as claimed in claim 1, it is characterised in that have on the turbine through air outlet and stretch out outside spiral case Rotating shaft, the scroll outer connects the discharge nozzle provided with the protective cover for surrounding rotating shaft, protective cover.
5. lead-power machine as claimed in claim 4, it is characterised in that the air intake passage is close to the end of air outlet provided with connection The cross of rotating shaft.
6. lead-power machine as claimed in claim 1, it is characterised in that the discharging opening of the main frame is provided with return material packing auger, described The feed end of discharge nozzle and the bottom of spiral case are all connected with return material packing auger.
7. lead-power machine as claimed in claim 6, it is characterised in that the spiral case bottom connects return material packing auger by baiting valve.
8. lead-power machine as claimed in claim 1, it is characterised in that the turbine two ends are provided with the end cap of fixed blade, end cap Center has through hole.
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CN107684975A (en) * 2017-09-19 2018-02-13 长兴新源机械设备科技有限公司 A kind of lead powder selecting system, refiner and method for concentrating
CN109244358A (en) * 2018-10-31 2019-01-18 江苏华兴电气科技有限公司 A kind of ultralow partial size lead powder extraction element
CN116851763A (en) * 2023-07-23 2023-10-10 郴州市耐普电源有限公司 Lead powder machine capable of recycling hot air

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JP2008149257A (en) * 2006-12-18 2008-07-03 Kurimoto Ltd Crushing and classifying apparatus
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