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CN117599953A - A precision classification device and classification method for magnetic carbon black powder - Google Patents

A precision classification device and classification method for magnetic carbon black powder Download PDF

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Publication number
CN117599953A
CN117599953A CN202410096584.0A CN202410096584A CN117599953A CN 117599953 A CN117599953 A CN 117599953A CN 202410096584 A CN202410096584 A CN 202410096584A CN 117599953 A CN117599953 A CN 117599953A
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carbon black
black powder
magnetic carbon
valve
gas separation
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薛亚磊
史文仓
朱连超
王晓妮
陈先瑞
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Shanxi Anlun Chemical Co ltd
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Shanxi Anlun Chemical Co ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C1/00Magnetic separation
    • B03C1/02Magnetic separation acting directly on the substance being separated
    • B03C1/30Combinations with other devices, not otherwise provided for

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Abstract

The embodiment of the application provides a magnetic carbon black powder precise classification device and a classification method, wherein the precise classification device comprises: the feeding assembly comprises a feed bin and a stirring part, a first discharge hole is formed in the bottom of the feed bin, and the stirring end of the stirring part stretches into the feed bin to stir materials; the separation assembly comprises a gas separation tube, an electromagnetic coil and an induced draft fan, wherein the electromagnetic coil is sleeved on the outer wall of the middle part of the gas separation tube, and an air outlet of the induced draft fan is communicated with the lower part of the gas separation tube; the grading sedimentation assembly comprises a sedimentation pipe, one end of the sedimentation pipe is provided with a second feeding port, the second feeding port is communicated with the upper part of the gas separation pipe, the other end of the sedimentation pipe is provided with a recycling air outlet, and the bottom of the sedimentation pipe is sequentially communicated with at least two third discharging ports along the length direction; the magnetic carbon black powder separator has the beneficial effects of simple structure, capability of separating magnetic carbon black powder from non-magnetic carbon black powder and precisely classifying the magnetic carbon black powder; is suitable for the technical field of classification of magnetic carbon black.

Description

一种磁性炭黑粉体精密分级装置和分级方法A kind of magnetic carbon black powder precision classification device and classification method

技术领域Technical field

本申请涉及磁性炭黑的分级的技术领域,具体涉及一种磁性炭黑粉体精密分级装置和分级方法。The present application relates to the technical field of magnetic carbon black classification, and specifically relates to a magnetic carbon black powder precision classification device and classification method.

背景技术Background technique

磁性炭黑具有良好的化学稳定性,不易被氧化、还原和分解,不仅可以在空气中长期保存,也可以在高温环境中长时间稳定地存在,不会被燃烧或分解。因此磁性炭黑在医药、化工、环保等方面具有广泛的应用前景,磁性炭黑作为药物载体时可以控制药物释放速率,并吸附药物的毒性;作为催化剂载体以及重金属吸附剂时可以方便地从悬浮液中快速回收。磁性炭黑的粒径及分布直接影响到其使用性能,将磁性炭黑进行精密分级能够更好地发挥不同粒径磁性炭黑的使用效果。Magnetic carbon black has good chemical stability and is not easily oxidized, reduced and decomposed. Not only can it be stored in the air for a long time, it can also exist stably in a high temperature environment for a long time without being burned or decomposed. Therefore, magnetic carbon black has broad application prospects in medicine, chemical industry, environmental protection, etc. When used as a drug carrier, magnetic carbon black can control the drug release rate and adsorb the toxicity of the drug; when used as a catalyst carrier and heavy metal adsorbent, it can be easily suspended from suspension. Rapid recovery from liquid. The particle size and distribution of magnetic carbon black directly affect its performance. Precise classification of magnetic carbon black can better exert the use effect of magnetic carbon black with different particle sizes.

为了解决上述问题,公开号为CN211887805U的专利公开了一种炭黑高效筛选分级装置,包括筛选分级底座、筛选分级外壳和筛选分级室等,通过电机工作带动转动杆与转轴在转轴座上转动,匀料组件在随转动杆转动过程,刷毛不停与炭黑粒子接触,并推动炭黑粒子使炭黑粒子在相应的筛网处下落至相应的盛接盒内,筛选分级底座呈圆柱形,筛选分级底座的内部为空腔结构,筛选分级底座的空腔内沿半径方向均匀设置有隔板,隔板将筛选分级底座的空腔内分隔出多个隔室,多个隔室的上端均设置有筛网,此种设置方式使筛网呈环形排列。In order to solve the above problems, the patent with publication number CN211887805U discloses a high-efficiency screening and grading device for carbon black, including a screening and grading base, a screening and grading shell, a screening and grading chamber, etc., and the rotating rod and the rotating shaft are driven to rotate on the rotating shaft seat through the work of the motor. When the screed component rotates with the rotating rod, the bristles are constantly in contact with the carbon black particles, and push the carbon black particles to make the carbon black particles fall at the corresponding screen into the corresponding receiving box. The screening and grading base is cylindrical. The interior of the screening and grading base is a cavity structure. There are partitions evenly arranged along the radius direction in the cavity of the screening and grading base. The partitions separate the cavity of the screening and grading base into multiple compartments. The upper ends of the multiple compartments are evenly spaced. A screen is provided, and this arrangement makes the screen arranged in a ring.

公开号为CN218282599U的专利公开了一种炭黑造粒分级装置,包括搅拌锅主体,在挤压桶底部安装有排料管,搅拌锅主体下方设有固定座,固定座上表面开设有存储槽,插槽中均设有第一收纳盒,固定座右端处开设有凹槽,凹槽中设有第二收纳盒,固定座上方设有筛板,筛板上与存储槽对应处均设有筛网,筛板下表面靠近左端处设有振动电机,插柱圆周外壁上套设有弹簧,该炭黑造粒分级装置,通过设置带有阀门的排料管,便于手动控制生产出来的炭黑颗粒进入到筛板上,在多个筛网的配合下进行分级存储,振动电机驱动筛板振动,便于筛板上的炭黑颗粒依次落下,且插柱与弹簧配合使筛板在固定座上下晃动,引导炭黑颗粒持续进行分级作业。The patent with publication number CN218282599U discloses a carbon black granulation and classification device, which includes a mixing pot main body, a discharge pipe installed at the bottom of the extrusion barrel, a fixed seat below the mixing pot main body, and a storage tank on the upper surface of the fixed seat. , there is a first storage box in the slot, a groove is provided at the right end of the fixed base, and a second storage box is provided in the groove. There is a sieve plate above the fixed base, and there are sieve plates on the sieve plate corresponding to the storage slot. The screen, the lower surface of the screen plate is equipped with a vibration motor near the left end, and the outer wall of the insert column is equipped with a spring. This carbon black granulation and classification device facilitates manual control of the produced carbon by setting a discharge pipe with a valve. The black particles enter the sieve plate and are classified and stored with the cooperation of multiple screens. The vibration motor drives the sieve plate to vibrate, so that the carbon black particles on the sieve plate fall one after another, and the inserts and springs cooperate to keep the sieve plate in the fixed seat. Shake up and down to guide the carbon black particles to continue grading operations.

上述分级方法中均为对普通炭黑粉体进行分级的方法,且刷毛或筛板等部件与炭黑粒子直接接触,容易使磁性炭黑材料发生失磁,影响磁性炭黑的使用效果,因此并不适用于磁性炭黑粉体;而且磁性炭黑粉体在生产过程中极易发生磁聚并凝并成较大颗粒,尤其会粘附大量非磁性炭黑,因此采用常规的筛分、离心沉降等方法均难以实现高效精密分级。The above classification methods are all methods for classifying ordinary carbon black powder, and parts such as bristles or sieve plates are in direct contact with the carbon black particles, which can easily cause the magnetic carbon black material to lose magnetism and affect the use effect of the magnetic carbon black. Therefore, It is not suitable for magnetic carbon black powder; and magnetic carbon black powder is very prone to magnetic aggregation and agglomeration into larger particles during the production process, especially a large amount of non-magnetic carbon black, so conventional screening, Methods such as centrifugal sedimentation are difficult to achieve efficient and precise classification.

发明内容Contents of the invention

为了解决上述技术缺陷之一,本申请实施例中提供了一种磁性炭黑粉体精密分级装置和分级方法。In order to solve one of the above technical deficiencies, embodiments of the present application provide a precision classification device and classification method for magnetic carbon black powder.

根据本申请实施例的第一个方面,提供了一种磁性炭黑粉体精密分级装置,包括:进料组件,包括料仓和搅拌部件,所述料仓的底部设置有第一出料口,所述搅拌部件的搅拌端伸入所述料仓内对物料进行搅拌;According to the first aspect of the embodiment of the present application, a magnetic carbon black powder precision classification device is provided, including: a feeding assembly, including a bin and a stirring component, and a first outlet is provided at the bottom of the bin , the stirring end of the stirring component extends into the silo to stir the material;

分离组件,包括气体分离管、电磁线圈和引风机;所述电磁线圈套设于所述气体分离管中部外壁上,所述引风机的出风口与所述气体分离管的下部相连通;所述气体分离管的顶部和底部分别设置有第一进料口和第二出料口,所述第一进料口与所述第一出料口之间通过第一阀门相连通;The separation component includes a gas separation pipe, an electromagnetic coil and an induced draft fan; the electromagnetic coil is set on the outer wall of the middle part of the gas separation pipe, and the air outlet of the induced draft fan is connected with the lower part of the gas separation pipe; The top and bottom of the gas separation pipe are respectively provided with a first feed port and a second discharge port, and the first feed port and the first discharge port are connected through a first valve;

分级沉降组件,包括沉降管,所述沉降管的一端设置有第二进料口,所述第二进料口与所述气体分离管的上部相连通,所述沉降管的另一端设置有回收出气口,所述沉降管的底部沿长度方向依次连通有至少两个第三出料口。A graded settling assembly, including a settling tube. One end of the settling tube is provided with a second feed port. The second feed port is connected to the upper part of the gas separation tube. The other end of the settling tube is provided with a recovery device. The bottom of the settling tube is connected with at least two third discharge ports in sequence along the length direction.

优选地,所述气体分离管的内部靠近所述第一进料口的地方设置有超声振荡器;所述超声振荡器包括振荡器主机和振荡器探头,所述振荡器探头的一端插设于所述振荡器主机的插口中,所述振荡器探头的另一端位于所述第一出料口的正下方。Preferably, an ultrasonic oscillator is provided inside the gas separation tube near the first feed inlet; the ultrasonic oscillator includes an oscillator host and an oscillator probe, and one end of the oscillator probe is inserted into In the socket of the oscillator host, the other end of the oscillator probe is located directly below the first outlet.

优选地,所述引风机的出风口处连通有第一连通管,所述第一连通管上远离所述引风机的一端设置有第二阀门,所述第一连通管的中部依次通过流量计和压力表与所述气体分离管的下部相连通。Preferably, a first communication pipe is connected to the air outlet of the induced draft fan, and a second valve is provided on one end of the first communication pipe away from the induced draft fan. The middle part of the first communication pipe passes through the flow meter in turn. The pressure gauge is connected to the lower part of the gas separation pipe.

更优选地,所述回收出气口处连通有第二连通管,所述第二连通管上远离所述回收出气口的一端设置有第三阀门,所述第二连通管的中部与所述引风机的进风口之间通过第四阀门相连通。More preferably, a second communication pipe is connected to the recovery air outlet, a third valve is provided on an end of the second communication pipe away from the recovery air outlet, and the middle part of the second communication pipe is connected to the guide pipe. The air inlets of the fans are connected through a fourth valve.

优选地,所述气体分离管的顶部与所述料仓之间连通有压力平衡管,所述压力平衡管上设置有第五阀门。Preferably, a pressure balance pipe is connected between the top of the gas separation pipe and the silo, and a fifth valve is provided on the pressure balance pipe.

更优选地,所述第三出料口的个数为四个。More preferably, the number of the third discharge openings is four.

根据本申请实施例的第二个方面,提供了一种磁性炭黑粉体精密分级装置的分级方法,包括以下步骤:According to the second aspect of the embodiment of the present application, a classification method of a magnetic carbon black powder precision classification device is provided, including the following steps:

S10,向料仓内投入混合炭黑粉体,通过搅拌部件对混合炭黑粉体进行搅拌,得到粗打散混合炭黑粉体;S10, put the mixed carbon black powder into the silo, stir the mixed carbon black powder through the stirring component, and obtain roughly dispersed mixed carbon black powder;

S20,调节阀门;S20, regulating valve;

关闭第一阀门、第四阀门和第五阀门,开启第二阀门和第三阀门;Close the first valve, the fourth valve and the fifth valve, and open the second valve and the third valve;

启动引风机,然后逐渐关闭第二阀门,逐渐打开第四阀门;逐渐关闭第三阀门,逐渐打开第一阀门和第五阀门;Start the induced draft fan, then gradually close the second valve, and gradually open the fourth valve; gradually close the third valve, and gradually open the first valve and the fifth valve;

启动超声振荡器主机,并为电磁线圈通电;Start the ultrasonic oscillator host and energize the electromagnetic coil;

S30,粗打散混合炭黑粉体在分离组件中分离为磁性炭黑粉体和非磁性炭黑粉体;S30, the roughly dispersed mixed carbon black powder is separated into magnetic carbon black powder and non-magnetic carbon black powder in the separation component;

气体分离管的第一进料口承接料仓的第一出料口处排出的粗打散混合炭黑粉体;The first feed port of the gas separation pipe receives the coarsely dispersed mixed carbon black powder discharged from the first discharge port of the silo;

然后通过设置于气体分离管内部的超声振荡器进行进一步打散,得到分散混合炭黑粉体;同时通过引风机为气体分离管的内部提供风力;Then it is further dispersed by an ultrasonic oscillator installed inside the gas separation tube to obtain dispersed and mixed carbon black powder; at the same time, an induced draft fan is used to provide wind power to the inside of the gas separation tube;

分散混合炭黑粉体中的磁性炭黑粉体在电磁线圈的作用下产生向上的作用力,磁性炭黑粉体随气流通过第二进料口输送至分级沉降组件中;The magnetic carbon black powder in the dispersed mixed carbon black powder generates an upward force under the action of the electromagnetic coil, and the magnetic carbon black powder is transported to the graded settling assembly through the second feed port with the air flow;

分散混合炭黑粉体中的非磁性炭黑粉体由于重力作用由第二出料口排出;The non-magnetic carbon black powder in the dispersed mixed carbon black powder is discharged from the second discharge port due to gravity;

S40,在分级沉降组件内对磁性炭黑粉体进行分级沉降;S40, perform graded settling of magnetic carbon black powder in the graded settling assembly;

第二进料口承接气流和磁性炭黑粉体后,通过沉降管底部设置的至少两个第三出料口对磁性炭黑粉体进行分级;其中越靠近第二进料口处的第三出料口中沉降的磁性炭黑粉体的粒径越大,越靠近回收出气口处的第三出料口中沉降的磁性炭黑粉体的粒径越小。After the second feed port receives the air flow and the magnetic carbon black powder, the magnetic carbon black powder is classified through at least two third discharge ports provided at the bottom of the settling tube; the closer to the third feed port at the second feed port, The larger the particle size of the magnetic carbon black powder settled in the discharge port is, the smaller the particle size of the magnetic carbon black powder settled in the third discharge port is closer to the recycling outlet.

优选地,还包括以下步骤:Preferably, the following steps are also included:

S50,磁性炭黑粉体分级沉降后,气流依次经过回收出气口、引风机后返回气体分离管中,重复步骤S30对气流进行循环使用。S50, after the magnetic carbon black powder is classified and settled, the air flow passes through the recovery air outlet and the induced draft fan in sequence and then returns to the gas separation tube. Step S30 is repeated to recycle the air flow.

本申请提供的磁性炭黑粉体精密分级装置结构简单、能够实现对混合炭黑粉体中磁性炭黑粉体和非磁性炭黑粉体的分离,以及对磁性炭黑粉体的进一步精密分级,使磁性炭黑粉体按照粒径大小进行精密分级,进而能够根据不同粒径大小选择磁性炭黑粉体适用的环境,使用效果更好。本申请中通过搅拌部件将料仓中的混合炭黑粉体进行搅拌,得到粗打散混合炭黑粉体,粗打散混合炭黑粉体进入气体分离管后通过引风机和电磁线圈的共同作用使磁性炭黑粉体和非磁性炭黑粉体进行分离,其中非磁性炭黑粉体由于重力作用通过第二出料口排出,磁性炭黑粉体则由于电磁线圈的作用产生向上的作用力而通过第二进料口输送至沉降管中,在沉降管中由于重力作用,磁性炭黑粉体按照粒径由大到小的顺序依次沉降在不同的第三出料口中,最后风力通过回收出气口进行排出或回收。The magnetic carbon black powder precision classification device provided by this application has a simple structure and can realize the separation of magnetic carbon black powder and non-magnetic carbon black powder in the mixed carbon black powder, as well as further precise classification of the magnetic carbon black powder. , so that the magnetic carbon black powder can be precisely classified according to the particle size, and then the suitable environment for the magnetic carbon black powder can be selected according to different particle sizes, and the use effect will be better. In this application, the mixed carbon black powder in the silo is stirred by the stirring component to obtain a coarsely dispersed mixed carbon black powder. After the coarsely dispersed mixed carbon black powder enters the gas separation tube, it passes through the combined force of the induced draft fan and the electromagnetic coil. The effect separates the magnetic carbon black powder and the non-magnetic carbon black powder. The non-magnetic carbon black powder is discharged through the second discharge port due to gravity, and the magnetic carbon black powder exerts an upward effect due to the action of the electromagnetic coil. The magnetic carbon black powder is transported to the settling tube through the second feed port by force. Due to the effect of gravity in the settling tube, the magnetic carbon black powder settles in different third discharge ports in order from large to small particle size. Finally, the wind force passes through Recycle the air outlet for discharge or recycling.

本申请的其它特征和优点将在随后的说明书中进行阐述,并且,部分地从说明书中变得显而易见,或者通过实施本申请而了解。本申请的目的和其他优点可通过在所写的说明书、权利要求书、以及附图中所指出的内容来实现和获得。Additional features and advantages of the application will be set forth in the description which follows, and in part will be apparent from the description, or may be learned by practice of the application. The objectives and other advantages of the application may be realized and attained by the written description, claims, and drawings.

附图说明Description of drawings

此处所说明的附图用来提供对本申请的进一步理解,构成本申请的一部分,本申请的示意性实施例及其说明用于解释本申请,并不构成对本申请的不当限定。在附图中:The drawings described here are used to provide a further understanding of the present application and constitute a part of the present application. The illustrative embodiments of the present application and their descriptions are used to explain the present application and do not constitute an improper limitation of the present application. In the attached picture:

图1为本申请实施例提供的一种磁性炭黑粉体精密分级装置的结构示意图;Figure 1 is a schematic structural diagram of a magnetic carbon black powder precision classification device provided by an embodiment of the present application;

图2为本申请实施例提供的分级前混合炭黑粉体的粒径分布图;Figure 2 is a particle size distribution diagram of the mixed carbon black powder before classification provided by the embodiment of the present application;

图3为本申请实施例提供的分级后磁性炭黑粉体的粒径分布图;Figure 3 is a particle size distribution diagram of the classified magnetic carbon black powder provided by the embodiment of the present application;

图中:In the picture:

10为进料组件,101为料仓,102为搅拌部件,103为第一阀门;10 is the feeding component, 101 is the silo, 102 is the stirring component, and 103 is the first valve;

20为分离组件,201为气体分离管,202为电磁线圈,203为引风机,204为超声振荡器,205为流量计,206为压力表,2011为第二出料口,2031为第二阀门;20 is a separation component, 201 is a gas separation tube, 202 is an electromagnetic coil, 203 is an induced draft fan, 204 is an ultrasonic oscillator, 205 is a flow meter, 206 is a pressure gauge, 2011 is the second outlet, and 2031 is the second valve ;

30为分级沉降组件,301为沉降管,3011为第二进料口,3012为回收出气口,3013为第三出料口,3014为第三阀门,3015为第四阀门;30 is a graded settling component, 301 is a settling tube, 3011 is a second feed port, 3012 is a recovery gas outlet, 3013 is a third outlet, 3014 is a third valve, and 3015 is a fourth valve;

40为压力平衡管,401为第五阀门。40 is a pressure balance pipe, and 401 is a fifth valve.

具体实施方式Detailed ways

为了使本申请实施例中的技术方案及优点更加清楚明白,以下结合附图对本申请的示例性实施例进行进一步详细的说明,显然,所描述的实施例仅是本申请的一部分实施例,而不是所有实施例的穷举。需要说明的是,在不冲突的情况下,本申请中的实施例及实施例中的特征可以相互组合。In order to make the technical solutions and advantages in the embodiments of the present application clearer, the exemplary embodiments of the present application are further described in detail below in conjunction with the accompanying drawings. Obviously, the described embodiments are only part of the embodiments of the present application. This is not an exhaustive list of all embodiments. It should be noted that, as long as there is no conflict, the embodiments and features in the embodiments of this application can be combined with each other.

图1为本申请实施例提供的一种磁性炭黑粉体精密分级装置的结构示意图,如图1所示,针对上述问题,本申请实施例中提供了一种磁性炭黑粉体精密分级装置,包括:进料组件10,包括料仓101和搅拌部件102,料仓101的底部设置有第一出料口,搅拌部件102的搅拌端伸入料仓101内对物料进行搅拌;Figure 1 is a schematic structural diagram of a magnetic carbon black powder precision classification device provided by an embodiment of the present application. As shown in Figure 1, to address the above problems, an embodiment of the present application provides a magnetic carbon black powder precision classification device. , including: a feed assembly 10, including a bin 101 and a stirring component 102. The bottom of the bin 101 is provided with a first outlet, and the stirring end of the stirring component 102 extends into the bin 101 to stir the material;

分离组件20,包括气体分离管201、电磁线圈202和引风机203;电磁线圈202套设于气体分离管201中部外壁上,引风机203的出风口与气体分离管201的下部相连通;气体分离管201的顶部和底部分别设置有第一进料口和第二出料口2011,第一进料口与第一出料口之间通过第一阀门103相连通;The separation assembly 20 includes a gas separation tube 201, an electromagnetic coil 202 and an induced draft fan 203; the electromagnetic coil 202 is set on the outer wall of the middle part of the gas separation tube 201, and the air outlet of the induced draft fan 203 is connected with the lower part of the gas separation tube 201; gas separation The top and bottom of the tube 201 are respectively provided with a first feed port and a second discharge port 2011, and the first feed port and the first discharge port are connected through the first valve 103;

分级沉降组件30,包括沉降管301,沉降管301的一端设置有第二进料口3011,第二进料口3011与气体分离管201的上部相连通,沉降管301的另一端设置有回收出气口3012,沉降管301的底部沿长度方向依次连通有至少两个第三出料口3013。具体地,沉降管301为中空方管,第三出料口3013为方锥管。The graded settling assembly 30 includes a settling tube 301. One end of the settling tube 301 is provided with a second feed port 3011. The second feed port 3011 is connected to the upper part of the gas separation tube 201. The other end of the settling tube 301 is provided with a recovery outlet. The gas port 3012 and the bottom of the settling tube 301 are connected with at least two third discharge ports 3013 in sequence along the length direction. Specifically, the settling tube 301 is a hollow square tube, and the third discharge port 3013 is a square tapered tube.

本申请提供的磁性炭黑粉体精密分级装置结构简单、能够实现对混合炭黑粉体中磁性炭黑粉体和非磁性炭黑粉体的分离,以及对磁性炭黑粉体的进一步精密分级,使磁性炭黑粉体按照粒径大小进行精密分级,进而能够根据不同粒径大小选择磁性炭黑粉体适用的环境,使用效果更好。本申请中通过搅拌部件102将料仓中的混合炭黑粉体进行搅拌,得到粗打散混合炭黑粉体,粗打散混合炭黑粉体进入气体分离管201后通过引风机203和电磁线圈202的共同作用使磁性炭黑粉体和非磁性炭黑粉体进行分离,其中非磁性炭黑粉体由于重力作用通过第二出料口2011排出,磁性炭黑粉体则由于电磁线圈202的作用产生向上的作用力而通过第二进料口3011输送至沉降管301中,在沉降管301中由于重力作用,磁性炭黑粉体按照粒径由大到小的顺序依次沉降在不同的第三出料口3013中,最后风力通过回收出气口3012进行排出或回收。The magnetic carbon black powder precision classification device provided by this application has a simple structure and can realize the separation of magnetic carbon black powder and non-magnetic carbon black powder in the mixed carbon black powder, as well as further precise classification of the magnetic carbon black powder. , so that the magnetic carbon black powder can be precisely classified according to the particle size, and then the suitable environment for the magnetic carbon black powder can be selected according to different particle sizes, and the use effect will be better. In this application, the mixed carbon black powder in the silo is stirred by the stirring component 102 to obtain coarsely dispersed mixed carbon black powder. The coarsely dispersed mixed carbon black powder enters the gas separation pipe 201 and passes through the induced draft fan 203 and electromagnetic The joint action of the coil 202 separates the magnetic carbon black powder and the non-magnetic carbon black powder. The non-magnetic carbon black powder is discharged through the second discharge port 2011 due to gravity, and the magnetic carbon black powder is discharged due to the electromagnetic coil 202. The action of the magnetic carbon black powder generates an upward force and is transported to the settling tube 301 through the second feed port 3011. In the settling tube 301, due to the effect of gravity, the magnetic carbon black powder settles in different particles in order from large to small in particle size. In the third outlet 3013, the final wind force is discharged or recovered through the recovery outlet 3012.

进一步地,气体分离管201的内部靠近第一进料口的地方设置有超声振荡器204;超声振荡器204包括振荡器主机和振荡器探头,振荡器探头的一端插设于振荡器主机的插口中,振荡器探头的另一端位于第一出料口的正下方。具体地,气体分离管201的上部设置有第四出料口,通过第四出料口实现第二进料口3011与气体分离管201的上部相连通。更具体地,所述第四出料口设置于超声振荡器204的下方。Further, an ultrasonic oscillator 204 is provided inside the gas separation tube 201 near the first feed inlet; the ultrasonic oscillator 204 includes an oscillator host and an oscillator probe, and one end of the oscillator probe is inserted into the socket of the oscillator host. , the other end of the oscillator probe is located directly below the first discharge port. Specifically, a fourth outlet is provided on the upper part of the gas separation tube 201, and the second feed port 3011 is connected to the upper part of the gas separation tube 201 through the fourth outlet. More specifically, the fourth outlet is provided below the ultrasonic oscillator 204 .

本申请中由于在料仓101中粗打散混合炭黑粉体中还存在团聚体,因此需要对其进行进一步打散,其中振荡器探头设置在第一出料口的正下方,当粗打散混合炭黑粉体进入气体分离管201后即可通过振荡器探头进行打散,振荡器主机为振荡器探头提供打散动力,在气体分离管201中靠近第一进料口的地方立即对团聚体进行打散,使进入气体分离管201中部和下部的均为分散混合炭黑粉体,便于后续的分级筛选。第四出料口设置于超声振荡器204的下方,使分散混合炭黑粉体中的磁性炭黑粉体能够顺利通过第四出料口、第二进料口3011后进入沉降管301中进行沉降。In this application, since there are still agglomerates in the roughly dispersed mixed carbon black powder in the silo 101, it needs to be further dispersed. The oscillator probe is set directly below the first discharge port. After the loosely mixed carbon black powder enters the gas separation tube 201, it can be dispersed by the oscillator probe. The oscillator host provides the dispersion power for the oscillator probe, and is immediately dispersed in the gas separation tube 201 near the first feed port. The agglomerates are broken up, so that what enters the middle and lower parts of the gas separation tube 201 is dispersed mixed carbon black powder, which facilitates subsequent classification and screening. The fourth outlet is provided below the ultrasonic oscillator 204, so that the magnetic carbon black powder in the dispersed and mixed carbon black powder can smoothly pass through the fourth outlet and the second inlet 3011 and then enter the settling tube 301 for processing. settlement.

进一步地,引风机203的出风口处连通有第一连通管,第一连通管上远离引风机203的一端设置有第二阀门2031,第一连通管的中部依次通过流量计205和压力表206与气体分离管201的下部相连通。Further, a first communication pipe is connected to the air outlet of the induced draft fan 203. A second valve 2031 is provided on the end of the first communication pipe away from the induced draft fan 203. The middle part of the first communication pipe passes through the flow meter 205 and the pressure gauge 206 in sequence. It is connected with the lower part of the gas separation pipe 201.

更进一步地,回收出气口3012处连通有第二连通管,第二连通管上远离回收出气口3012的一端设置有第三阀门3014,第二连通管的中部与引风机203的进风口之间通过第四阀门3015相连通。Furthermore, a second communication pipe is connected to the recovery air outlet 3012. A third valve 3014 is provided on the end of the second communication pipe away from the recovery air outlet 3012. The middle part of the second communication pipe is between the air inlet of the induced draft fan 203. connected through the fourth valve 3015.

本申请中流量计205和压力表206的设置能够实时监测精密分级装置内部的气体流量和气压,防止压力过大或过小造成分级效果不好、甚至存在安全隐患的问题发生;第一阀门103、第二阀门2031、第三阀门3014、第四阀门3015的设置使分级操作前便于调节分级装置的内部气压,使分级效果更好;第二连通管的中部与引风机203的进风口之间相连通,进而使回收出气口3012处的气流能够通过引风机203的进风口进行回收循环利用,有效节约了资源,防止对环境的污染。The settings of the flow meter 205 and the pressure gauge 206 in this application can monitor the gas flow and pressure inside the precision classification device in real time, preventing problems such as poor classification effect or even safety hazard caused by excessive or too small pressure; the first valve 103 The settings of the second valve 2031, the third valve 3014, and the fourth valve 3015 make it easy to adjust the internal air pressure of the classification device before the classification operation, so that the classification effect is better; between the middle part of the second communication pipe and the air inlet of the induced draft fan 203 are connected, so that the air flow at the recovery air outlet 3012 can be recovered and recycled through the air inlet of the induced draft fan 203, effectively saving resources and preventing environmental pollution.

进一步地,气体分离管201的顶部与料仓101之间连通有压力平衡管40,压力平衡管40上设置有第五阀门401。本申请中分级装置的分级过程为封闭进行的,其中进料组件10和分离组件20之间通过压力平衡管40和第五阀门401实现安全封闭运行。Further, a pressure balance pipe 40 is connected between the top of the gas separation pipe 201 and the silo 101, and a fifth valve 401 is provided on the pressure balance pipe 40. The classification process of the classification device in this application is carried out in a closed manner, in which a safe closed operation is achieved between the feed component 10 and the separation component 20 through the pressure balance pipe 40 and the fifth valve 401 .

更进一步地,第三出料口3013的个数为四个。第三出料口3013处沉积的磁性炭黑粉体沿第二进料口3011至回收出气口3012方向依次为:磁性炭黑粉体a,磁性炭黑粉体b,磁性炭黑粉体c,磁性炭黑粉体d。Furthermore, the number of third discharge ports 3013 is four. The magnetic carbon black powder deposited at the third outlet 3013 along the direction from the second inlet 3011 to the recovery outlet 3012 is: magnetic carbon black powder a, magnetic carbon black powder b, magnetic carbon black powder c , magnetic carbon black powder d.

本申请中通过四个第三出料口3013对磁性炭黑粉体进行精密分级,其中磁性炭黑粉体a的粒径>磁性炭黑粉体b的粒径>磁性炭黑粉体c的粒径>磁性炭黑粉体d的粒径。经过四个第三出料口3013即可实现全部磁性炭黑粉体的沉降分级,分级效果好。In this application, the magnetic carbon black powder is precisely classified through four third discharge ports 3013, where the particle size of magnetic carbon black powder a > the particle size of magnetic carbon black powder b > the particle size of magnetic carbon black powder c Particle size>Particle size of magnetic carbon black powder d. All the magnetic carbon black powder can be settled and classified through the four third discharge ports 3013, and the classification effect is good.

本申请还提供了一种磁性炭黑粉体精密分级装置的分级方法,包括以下步骤:This application also provides a classification method of a magnetic carbon black powder precision classification device, which includes the following steps:

S10,向料仓101内投入混合炭黑粉体,通过搅拌部件102对混合炭黑粉体进行搅拌,得到粗打散混合炭黑粉体;S10, put the mixed carbon black powder into the silo 101, stir the mixed carbon black powder through the stirring component 102, and obtain roughly dispersed mixed carbon black powder;

S20,调节阀门;S20, regulating valve;

关闭第一阀门103、第四阀门3015和第五阀门401,开启第二阀门2031和第三阀门3014;Close the first valve 103, the fourth valve 3015 and the fifth valve 401, and open the second valve 2031 and the third valve 3014;

启动引风机203,然后逐渐关闭第二阀门2031,逐渐打开第四阀门3015;逐渐关闭第三阀门3014,逐渐打开第一阀门103和第五阀门401;Start the induced draft fan 203, then gradually close the second valve 2031, and gradually open the fourth valve 3015; gradually close the third valve 3014, and gradually open the first valve 103 and the fifth valve 401;

启动超声振荡器主机,并为电磁线圈202通电;Start the ultrasonic oscillator host and energize the electromagnetic coil 202;

S30,粗打散混合炭黑粉体在分离组件20中分离为磁性炭黑粉体和非磁性炭黑粉体;S30, the roughly dispersed mixed carbon black powder is separated into magnetic carbon black powder and non-magnetic carbon black powder in the separation component 20;

气体分离管201的第一进料口承接料仓101的第一出料口处排出的粗打散混合炭黑粉体;The first feed port of the gas separation pipe 201 receives the roughly dispersed mixed carbon black powder discharged from the first discharge port of the silo 101;

然后通过设置于气体分离管201内部的超声振荡器204进行进一步打散,得到分散混合炭黑粉体;同时通过引风机203为气体分离管201的内部提供风力;Then, the ultrasonic oscillator 204 installed inside the gas separation tube 201 is further dispersed to obtain dispersed and mixed carbon black powder; at the same time, the induced draft fan 203 is used to provide wind force to the inside of the gas separation tube 201;

分散混合炭黑粉体中的磁性炭黑粉体在电磁线圈202的作用下产生向上的作用力,磁性炭黑粉体随气流通过第二进料口3011输送至分级沉降组件30中;The magnetic carbon black powder in the dispersed mixed carbon black powder generates an upward force under the action of the electromagnetic coil 202, and the magnetic carbon black powder is transported to the graded settling assembly 30 through the second feed port 3011 along with the air flow;

分散混合炭黑粉体中的非磁性炭黑粉体由于重力作用由第二出料口2011排出;The non-magnetic carbon black powder in the dispersed mixed carbon black powder is discharged from the second discharge port 2011 due to gravity;

S40,在分级沉降组件30内对磁性炭黑粉体进行分级沉降;S40, perform graded settling of the magnetic carbon black powder in the graded settling assembly 30;

第二进料口3011承接气流和磁性炭黑粉体后,通过沉降管301底部设置的至少两个第三出料口3013对磁性炭黑粉体进行分级;其中越靠近第二进料口3011处的第三出料口3013中沉降的磁性炭黑粉体的粒径越大,越靠近回收出气口3012处的第三出料口3013中沉降的磁性炭黑粉体的粒径越小。After the second feed port 3011 receives the air flow and the magnetic carbon black powder, the magnetic carbon black powder is classified through at least two third discharge ports 3013 provided at the bottom of the settling tube 301; the closer to the second feed port 3011 The particle size of the magnetic carbon black powder settled in the third outlet 3013 is larger, and the particle size of the magnetic carbon black powder settled in the third outlet 3013 closer to the recovery outlet 3012 is smaller.

由于本申请提供的精密分级方法中包括了上述精密分级装置,因此可以认为精密分级方法中也包括上述精密分级装置的有益效果,在此不再赘述。Since the precision classification method provided by this application includes the above-mentioned precision classification device, it can be considered that the precision classification method also includes the beneficial effects of the above-mentioned precision classification device, which will not be described again here.

进一步地,还包括以下步骤:S50,磁性炭黑粉体分级沉降后,气流依次经过回收出气口3012、引风机203后返回气体分离管201中,重复步骤S30对气流进行循环使用。Further, the following steps are included: S50, after the magnetic carbon black powder is classified and settled, the air flow passes through the recovery air outlet 3012 and the induced draft fan 203 in sequence and then returns to the gas separation pipe 201, and repeats step S30 to recycle the air flow.

本申请中对气流的循环利用不仅节约资源、符合绿色环保理念,还能够实现对混合炭黑粉体的连续筛选和分级,效率更高。The recycling of air flow in this application not only saves resources and conforms to the concept of green environmental protection, but also enables continuous screening and classification of mixed carbon black powder, with higher efficiency.

为了证明本申请提供的分级方法和分级装置对磁性炭黑粉体的分级效果,对分级前混合炭黑粉体的粒径、分级后各个第三出料口3013中磁性炭黑粉体的粒径均进行了检测。图2为本申请实施例提供的分级前混合炭黑粉体的粒径分布图,由图2可知,分级前混合炭黑粉体的粒径分布范围较宽,在0.15~0.6μm之间。经过本申请提供的分级方法和分级装置进行分级后,多个第三出料口3013中的磁性炭黑粉体的粒径分布较为精细,越靠近第二进料口3011处的第三出料口3013中沉降的磁性炭黑粉体的粒径越大,越靠近回收出气口3012处的第三出料口3013中沉降的磁性炭黑粉体的粒径越小;图3为本申请实施例提供的分级后磁性炭黑粉体的粒径分布图,如图3所示,沿第二进料口3011至回收出气口3012方向,第三出料口3013中沉积的磁性炭黑粉体的粒径逐渐减小,即磁性炭黑粉体a的粒径>磁性炭黑粉体b的粒径>磁性炭黑粉体c的粒径>磁性炭黑粉体d的粒径。In order to prove the classification effect of the classification method and classification device provided in this application on magnetic carbon black powder, the particle size of the mixed carbon black powder before classification and the particle size of the magnetic carbon black powder in each third outlet 3013 after classification were compared. diameters were tested. Figure 2 is a particle size distribution diagram of the mixed carbon black powder before classification provided by the embodiment of the present application. It can be seen from Figure 2 that the particle size distribution range of the mixed carbon black powder before classification is wide, between 0.15 and 0.6 μm. After being classified by the classification method and classification device provided by this application, the particle size distribution of the magnetic carbon black powder in the plurality of third discharge ports 3013 is relatively fine. The closer the third discharge port is to the second feed port 3011 The larger the particle size of the magnetic carbon black powder settled in the port 3013 is, the smaller the particle size of the magnetic carbon black powder settled in the third discharge port 3013 is closer to the recycling outlet 3012; Figure 3 shows the implementation of the present application. The particle size distribution diagram of the classified magnetic carbon black powder provided in the example is shown in Figure 3. The magnetic carbon black powder deposited in the third outlet 3013 is along the direction from the second inlet 3011 to the recovery outlet 3012. The particle size gradually decreases, that is, the particle size of magnetic carbon black powder a>the particle size of magnetic carbon black powder b>the particle size of magnetic carbon black powder c>the particle size of magnetic carbon black powder d.

在本申请的描述中,需要理解的是,术语 “长度”、“上”、“下”、“顶”、“底”、“内”、“外”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本申请和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本申请的限制。In the description of this application, it should be understood that the terms "length", "upper", "lower", "top", "bottom", "inner", "outer", etc. indicate an orientation or positional relationship based on the attached The orientation or positional relationship shown in the figures is only for the convenience of describing the present application and simplifying the description. It does not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and therefore cannot be understood as limiting the present application. Application restrictions.

此外,术语“第一”、“第二”仅用于描述目的,而不能理解为指示或暗示相对重要性或者隐含指明所指示的技术特征的数量。由此,限定有“第一”、“第二”的特征可以明示或者隐含地包括一个或者更多个该特征。在本申请的描述中,“多个”的含义是至少两个,例如两个,三个等,除非另有明确具体的限定。In addition, the terms “first” and “second” are used for descriptive purposes only and cannot be understood as indicating or implying relative importance or implicitly indicating the quantity of indicated technical features. Therefore, features defined as "first" and "second" may explicitly or implicitly include one or more of these features. In the description of this application, "plurality" means at least two, such as two, three, etc., unless otherwise expressly and specifically limited.

在本申请中,除非另有明确的规定和限定,术语“安装”、“相连”、“连接”、“固定”等术语应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或成一体;可以是机械连接,也可以是电连接或可以互相通讯;可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通或两个元件的相互作用关系。对于本领域的普通技术人员而言,可以根据具体情况理解上述术语在本申请中的具体含义。In this application, unless otherwise clearly stated and limited, the terms "installation", "connection", "connection", "fixing" and other terms should be understood in a broad sense. For example, it can be a fixed connection or a detachable connection. , or integrated; it can be mechanical connection, electrical connection or mutual communication; it can be directly connected, or it can be indirectly connected through an intermediate medium, it can be the internal connection of two elements or the interaction between two elements. For those of ordinary skill in the art, the specific meanings of the above terms in this application can be understood according to specific circumstances.

尽管已描述了本申请的优选实施例,但本领域内的技术人员一旦得知了基本创造性概念,则可对这些实施例作出另外的变更和修改。所以,所附权利要求意欲解释为包括优选实施例以及落入本申请范围的所有变更和修改。Although the preferred embodiments of the present application have been described, those skilled in the art will be able to make additional changes and modifications to these embodiments once the basic inventive concepts are apparent. Therefore, it is intended that the appended claims be construed to include the preferred embodiments and all changes and modifications that fall within the scope of this application.

显然,本领域的技术人员可以对本申请进行各种改动和变型而不脱离本申请的精神和范围。这样,倘若本申请的这些修改和变型属于本申请权利要求及其等同技术的范围之内,则本申请也意图包含这些改动和变型在内。Obviously, those skilled in the art can make various changes and modifications to the present application without departing from the spirit and scope of the present application. In this way, if these modifications and variations of the present application fall within the scope of the claims of the present application and equivalent technologies, the present application is also intended to include these modifications and variations.

Claims (8)

1.一种磁性炭黑粉体精密分级装置,其特征在于,包括:1. A magnetic carbon black powder precision classification device, which is characterized in that it includes: 进料组件(10),包括料仓(101)和搅拌部件(102),所述料仓(101)的底部设置有第一出料口,所述搅拌部件(102)的搅拌端伸入所述料仓(101)内对物料进行搅拌;The feeding assembly (10) includes a silo (101) and a stirring component (102). The bottom of the silo (101) is provided with a first outlet, and the stirring end of the stirring component (102) extends into the The materials are stirred in the silo (101); 分离组件(20),包括气体分离管(201)、电磁线圈(202)和引风机(203);所述电磁线圈(202)套设于所述气体分离管(201)中部外壁上,所述引风机(203)的出风口与所述气体分离管(201)的下部相连通;所述气体分离管(201)的顶部和底部分别设置有第一进料口和第二出料口(2011),所述第一进料口与所述第一出料口之间通过第一阀门(103)相连通;The separation component (20) includes a gas separation tube (201), an electromagnetic coil (202) and an induced draft fan (203); the electromagnetic coil (202) is set on the outer wall of the middle part of the gas separation tube (201), and the The air outlet of the induced draft fan (203) is connected with the lower part of the gas separation pipe (201); the top and bottom of the gas separation pipe (201) are respectively provided with a first feed port and a second discharge port (2011 ), the first feed port and the first discharge port are connected through a first valve (103); 分级沉降组件(30),包括沉降管(301),所述沉降管(301)的一端设置有第二进料口(3011),所述第二进料口(3011)与所述气体分离管(201)的上部相连通,所述沉降管(301)的另一端设置有回收出气口(3012),所述沉降管(301)的底部沿长度方向依次连通有至少两个第三出料口(3013)。The graded settling assembly (30) includes a settling tube (301). One end of the settling tube (301) is provided with a second feed port (3011). The second feed port (3011) is connected to the gas separation tube. The upper part of the settling pipe (201) is connected, the other end of the settling pipe (301) is provided with a recovery air outlet (3012), and the bottom of the settling pipe (301) is connected with at least two third outlets in sequence along the length direction. (3013). 2.根据权利要求1所述的磁性炭黑粉体精密分级装置,其特征在于,所述气体分离管(201)的内部靠近所述第一进料口的地方设置有超声振荡器(204);2. The magnetic carbon black powder precision classification device according to claim 1, characterized in that an ultrasonic oscillator (204) is provided inside the gas separation tube (201) near the first feed port. ; 所述超声振荡器(204)包括振荡器主机和振荡器探头,所述振荡器探头的一端插设于所述振荡器主机的插口中,所述振荡器探头的另一端位于所述第一出料口的正下方。The ultrasonic oscillator (204) includes an oscillator host and an oscillator probe. One end of the oscillator probe is inserted into the socket of the oscillator host, and the other end of the oscillator probe is located at the first outlet. Right below the material opening. 3.根据权利要求1所述的磁性炭黑粉体精密分级装置,其特征在于,所述引风机(203)的出风口处连通有第一连通管,所述第一连通管上远离所述引风机(203)的一端设置有第二阀门(2031),所述第一连通管的中部依次通过流量计(205)和压力表(206)与所述气体分离管(201)的下部相连通。3. The magnetic carbon black powder precision classification device according to claim 1, characterized in that the air outlet of the induced draft fan (203) is connected with a first communication pipe, and the first communication pipe is away from the A second valve (2031) is provided at one end of the induced draft fan (203), and the middle part of the first communication pipe is connected to the lower part of the gas separation pipe (201) through a flow meter (205) and a pressure gauge (206). . 4.根据权利要求1~3中任一项所述的磁性炭黑粉体精密分级装置,其特征在于,所述回收出气口(3012)处连通有第二连通管,所述第二连通管上远离所述回收出气口(3012)的一端设置有第三阀门(3014),所述第二连通管的中部与所述引风机(203)的进风口之间通过第四阀门(3015)相连通。4. The magnetic carbon black powder precision classification device according to any one of claims 1 to 3, characterized in that the recovery air outlet (3012) is connected with a second communication pipe, and the second communication pipe A third valve (3014) is provided at one end of the top away from the recovery air outlet (3012). The middle part of the second communication pipe is connected to the air inlet of the induced draft fan (203) through a fourth valve (3015). Pass. 5.根据权利要求4所述的磁性炭黑粉体精密分级装置,其特征在于,所述气体分离管(201)的顶部与所述料仓(101)之间连通有压力平衡管(40),所述压力平衡管(40)上设置有第五阀门(401)。5. The magnetic carbon black powder precision classification device according to claim 4, characterized in that a pressure balance pipe (40) is connected between the top of the gas separation pipe (201) and the silo (101). , the pressure balance pipe (40) is provided with a fifth valve (401). 6.根据权利要求5所述的磁性炭黑粉体精密分级装置,其特征在于,所述第三出料口(3013)的个数为四个。6. The magnetic carbon black powder precision classification device according to claim 5, characterized in that the number of the third discharge ports (3013) is four. 7.一种如权利要求6所述的磁性炭黑粉体精密分级装置的分级方法,其特征在于,包括以下步骤:7. A classification method of the magnetic carbon black powder precision classification device according to claim 6, characterized in that it includes the following steps: S10,向料仓(101)内投入混合炭黑粉体,通过搅拌部件(102)对混合炭黑粉体进行搅拌,得到粗打散混合炭黑粉体;S10, put the mixed carbon black powder into the silo (101), stir the mixed carbon black powder through the stirring component (102), and obtain a roughly dispersed mixed carbon black powder; S20,调节阀门;S20, regulating valve; 关闭第一阀门(103)、第四阀门(3015)和第五阀门(401),开启第二阀门(2031)和第三阀门(3014);Close the first valve (103), the fourth valve (3015) and the fifth valve (401), and open the second valve (2031) and the third valve (3014); 启动引风机(203),然后逐渐关闭第二阀门(2031),逐渐打开第四阀门(3015);逐渐关闭第三阀门(3014),逐渐打开第一阀门(103)和第五阀门(401);Start the induced draft fan (203), then gradually close the second valve (2031), and gradually open the fourth valve (3015); gradually close the third valve (3014), and gradually open the first valve (103) and the fifth valve (401) ; 启动超声振荡器主机,并为电磁线圈(202)通电;Start the ultrasonic oscillator host and energize the electromagnetic coil (202); S30,粗打散混合炭黑粉体在分离组件(20)中分离为磁性炭黑粉体和非磁性炭黑粉体;S30, the coarsely broken mixed carbon black powder is separated into magnetic carbon black powder and non-magnetic carbon black powder in the separation component (20); 气体分离管(201)的第一进料口承接料仓(101)的第一出料口处排出的粗打散混合炭黑粉体;The first feed port of the gas separation pipe (201) receives the roughly dispersed mixed carbon black powder discharged from the first discharge port of the silo (101); 然后通过设置于气体分离管(201)内部的超声振荡器(204)进行进一步打散,得到分散混合炭黑粉体;同时通过引风机(203)为气体分离管(201)的内部提供风力;Then, the ultrasonic oscillator (204) installed inside the gas separation tube (201) is further dispersed to obtain dispersed and mixed carbon black powder; at the same time, the induced draft fan (203) is used to provide wind force for the inside of the gas separation tube (201); 分散混合炭黑粉体中的磁性炭黑粉体在电磁线圈(202)的作用下产生向上的作用力,磁性炭黑粉体随气流通过第二进料口(3011)输送至分级沉降组件(30)中;The magnetic carbon black powder in the dispersed mixed carbon black powder generates an upward force under the action of the electromagnetic coil (202), and the magnetic carbon black powder is transported to the graded settling assembly (3011) through the second feed port (3011) with the air flow. 30) in; 分散混合炭黑粉体中的非磁性炭黑粉体由于重力作用由第二出料口(2011)排出;The non-magnetic carbon black powder in the dispersed mixed carbon black powder is discharged from the second discharge port (2011) due to gravity; S40,在分级沉降组件(30)内对磁性炭黑粉体进行分级沉降;S40, perform graded settling of the magnetic carbon black powder in the graded settling assembly (30); 第二进料口(3011)承接气流和磁性炭黑粉体后,通过沉降管(301)底部设置的至少两个第三出料口(3013)对磁性炭黑粉体进行分级;其中越靠近第二进料口(3011)处的第三出料口(3013)中沉降的磁性炭黑粉体的粒径越大,越靠近回收出气口(3012)处的第三出料口(3013)中沉降的磁性炭黑粉体的粒径越小。After the second feed port (3011) receives the air flow and magnetic carbon black powder, the magnetic carbon black powder is classified through at least two third discharge ports (3013) provided at the bottom of the settling tube (301); the closer the The larger the particle size of the magnetic carbon black powder settled in the third outlet (3013) at the second inlet (3011) is, the closer it is to the third outlet (3013) at the recovery outlet (3012). The particle size of the magnetic carbon black powder that settles in the medium is smaller. 8.根据权利要求7所述的磁性炭黑粉体精密分级装置的分级方法,其特征在于,还包括以下步骤:8. The classification method of the magnetic carbon black powder precision classification device according to claim 7, characterized in that it also includes the following steps: S50,磁性炭黑粉体分级沉降后,气流依次经过回收出气口(3012)、引风机(203)后返回气体分离管(201)中,重复步骤S30对气流进行循环使用。S50, after the magnetic carbon black powder is classified and settled, the air flow passes through the recovery outlet (3012) and the induced draft fan (203) in sequence and then returns to the gas separation tube (201). Step S30 is repeated to recycle the air flow.
CN202410096584.0A 2024-01-24 2024-01-24 A precision classification device and classification method for magnetic carbon black powder Pending CN117599953A (en)

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Application publication date: 20240227